National Emission Standards for Hazardous Air Pollutants for Clay Ceramics Manufacturing, 58601-58623 [2019-22812]

Download as PDF Federal Register / Vol. 84, No. 212 / Friday, November 1, 2019 / Rules and Regulations The Rule This amendment to Title 14 Code of Federal Regulations (14 CFR) part 71 modifies Class E airspace extending upward from 700 feet above the surface at Wray Municipal Airport, Wray, CO, to within 1 mile each side of the 180° bearing extending from the 6.5 mile radius to 11 miles south of the airport and 2 miles each side of the 360° bearing extending from the 6.5 mile radius to 10.8 miles north of the airport. Additionally, this action removes Class E airspace extending upward from 1,200 feet above the surface at Wray Municipal Airport, Wray, CO. This airspace is wholly contained within the Denver en route airspace area and duplication is not necessary. Regulatory Notices and Analyses The FAA has determined that this regulation only involves an established body of technical regulations for which frequent and routine amendments are necessary to keep them operationally current, is non-controversial and unlikely to result in adverse or negative comments. It, therefore: (1) Is not a ‘‘significant regulatory action’’ under Executive Order 12866; (2) is not a ‘‘significant rule’’ under DOT Regulatory Policies and Procedures (44 FR 11034; February 26, 1979); and (3) does not warrant preparation of a regulatory evaluation as the anticipated impact is so minimal. Since this is a routine matter that will only affect air traffic procedures and air navigation, it is certified that this rule, when promulgated, would not have a significant economic impact on a substantial number of small entities under the criteria of the Regulatory Flexibility Act. Environmental Review The FAA has determined that this action qualifies for categorical exclusion under the National Environmental Policy Act in accordance with FAA Order 1050.1F, ‘‘Environmental Impacts: Policies and Procedures,’’ paragraph 5–6.5a. This airspace action is not expected to cause any potentially significant environmental impacts, and no extraordinary circumstances exist that warrant preparation of an environmental assessment. List of Subjects in 14 CFR Part 71 Adoption of the Amendment In consideration of the foregoing, the Federal Aviation Administration amends 14 CFR part 71 as follows: 16:01 Oct 31, 2019 Jkt 250001 1. The authority citation for 14 CFR part 71 continues to read as follows: ■ Authority: 49 U.S.C. 106(f), 106(g), 40103, 40113, 40120; E.O. 10854, 24 FR 9565, 3 CFR, 1959–1963 Comp., p. 389. § 71.1 [Amended] 2. The incorporation by reference in 14 CFR 71.1 of FAA Order 7400.11D, Airspace Designations and Reporting Points, dated August 8, 2019, and effective September 15, 2019, is amended as follows: ■ Paragraph 6005 Class E Airspace Areas Extending Upward From 700 Feet or More Above the Surface of the Earth. * * * * * ANM CO E5 Wray, CO Wray Municipal Airport (Lat. 40°06′01″ N, long. 102°14′28″ W) That airspace extending upward from 700 feet above the surface within a 6.5 mile radius of the airport, and within 1 mile each side of the 180° bearing extending from the 6.5 mile radius to 11 miles south of the airport, and within 2 miles each side of the 360° bearing extending from the 6.5 mile radius to 10.8 miles north of the Wray Municipal Airport. Issued in Seattle, Washington, on October 18, 2019. Shawn M. Kozica, Group Manager, Operations Support Group, Western Service Center. [FR Doc. 2019–23318 Filed 10–31–19; 8:45 am] BILLING CODE 4910–13–P ENVIRONMENTAL PROTECTION AGENCY 40 CFR Part 63 [EPA–HQ–OAR–2013–0290; FRL–10001–21– OAR] RIN 2060–AT25 National Emission Standards for Hazardous Air Pollutants for Clay Ceramics Manufacturing Environmental Protection Agency (EPA). ACTION: Final rule. AGENCY: This action finalizes certain amendments to the National Emission Standards for Hazardous Air Pollutants (NESHAP): Clay Ceramics Manufacturing source category. The final amendments are being issued in response to a petition for reconsideration filed by an affected SUMMARY: Airspace, Incorporation by reference, Navigation (air). VerDate Sep<11>2014 PART 71—DESIGNATION OF CLASS A, B, C, D, AND E AIRSPACE AREAS; AIR TRAFFIC SERVICE ROUTES; AND REPORTING POINTS PO 00000 Frm 00003 Fmt 4700 Sfmt 4700 58601 industry (Kohler Company) on the final rule promulgated on October 26, 2015, as well as our review of the 2015 rule with respect to certain other issues raised by Kohler. This action revises the temperature monitoring methodology used to demonstrate continuous compliance with the dioxin/furan (D/F) emissions limit of the final rule. In addition, we are addressing concerns raised by Kohler regarding visible emissions (VE) monitoring of tunnel kiln stacks for continuous compliance with particulate matter (PM) and mercury (Hg) emission limitations. This action also amends the requirements for weekly visual inspections of system ductwork and control device equipment for water curtain spray booths. Lastly, this action amends the NESHAP to include provisions for emissions averaging, makes technical corrections, and adds certain definitions. DATES: This final rule is effective on November 1, 2019. ADDRESSES: The U.S. Environmental Protection agency (EPA) has established a docket for this rulemaking under Docket ID No. EPA–HQ–OAR–2013– 0290. All documents in the docket are listed on the https:// www.regulations.gov/ website. Although listed, some information is not publicly available, e.g., confidential business information (CBI) or other information whose disclosure is restricted by statute. Certain other material, such as copyrighted material, is not placed on the internet and will be publicly available only in hard copy form. Publicly available docket materials are available either electronically through https://www.regulations.gov/, or in hard copy form at the EPA Docket Center, Room 3334, WJC West Building, 1301 Constitution Avenue NW, Washington, DC. The Public Reading Room is open from 8:30 a.m. to 4:30 p.m., Monday through Friday, excluding legal holidays. The telephone number for the Public Reading Room is (202) 566–1744, and the telephone number for the EPA Docket Center is (202) 566–1742. FOR FURTHER INFORMATION CONTACT: For questions about this final action, contact Mr. Brian Storey, Sector Policies and Programs Division (D243–04), Office of Air Quality Planning and Standards, U.S. Environmental Protection Agency, Research Triangle Park, North Carolina 27711; telephone number: (919) 541– 1103; fax number: (919) 541–4991; and email address: storey.brian@epa.gov. SUPPLEMENTARY INFORMATION: Preamble acronyms and abbreviations. We use multiple acronyms and terms in this preamble. While this list may not be exhaustive, to E:\FR\FM\01NOR1.SGM 01NOR1 58602 Federal Register / Vol. 84, No. 212 / Friday, November 1, 2019 / Rules and Regulations ease the reading of this preamble and for reference purposes, the EPA defines the following terms and acronyms here: BSCP brick and structural clay products CAA Clean Air Act CBI Confidential Business Information CFR Code of Federal Regulations D/F dioxins/furans EJ environmental justice EPA U.S. Environmental Protection Agency HAP hazardous air pollutant(s) Hg mercury HON Hazardous Organic NESHAP lb pounds NAICS North American Industry Classification System NESHAP national emission standards for hazardous air pollutants No. number NTTAA National Technology Transfer and Advancement Act OMB Office of Management and Budget PM particulate matter POC products of combustion PRA Paperwork Reduction Act RFA Regulatory Flexibility Act UMRA Unfunded Mandates Reform Act U.S. United States U.S.C. United States Code v. versus VE visible emissions Background information. On August 20, 2018, the EPA proposed revisions to the Clay Ceramics Manufacturing NESHAP. In this action, we are finalizing revisions to the rule. The EPA briefly summarizes the more significant comments we received regarding the proposed rule that have resulted in changes to the final rule, and we provide our responses in this preamble. A more comprehensive summary of the public comments on the proposal and the EPA’s responses to those comments is available in the National Emission Standards for Hazardous Air Pollutants for Clay Ceramics Manufacturing; Amendments—Background Information for Final Rule: Summary of Public Comments and Responses. A ‘‘track changes’’ version of the regulatory language that incorporates the changes in this action is available in the docket. Organization of this document. The information in this preamble is organized as follows: Table of Contents I. General Information A. Does this action apply to me? B. Where can I get a copy of this document and other related information? C. Judicial Review and Administrative Reconsideration II. Background A. What is the statutory authority for this action? B. What actions preceded these final amendments? III. Summary of the Final Amendments IV. Rationale for Changes to the Proposed Amendments A. Visible Emissions Monitoring of Tunnel Kiln Exhaust B. Weekly Visual Inspections of Water Curtain Spray Booths C. Emissions Averaging V. Summary of Cost, Environmental, and Economic Impacts VI. Statutory and Executive Order Reviews A. Executive Order 12866: Regulatory Planning and Review and Executive Order 13563: Improving Regulation and Regulatory Review B. Executive Order 13771: Reducing Regulations and Controlling Regulatory Costs C. Paperwork Reduction Act (PRA) D. Regulatory Flexibility Act (RFA) E. Unfunded Mandates Reform Act (UMRA) F. Executive Order 13132: Federalism G. Executive Order 13175: Consultation and Coordination With Indian Tribal Governments H. Executive Order 13045: Protection of Children From Environmental Health Risks and Safety Risks I. Executive Order 13211: Actions Concerning Regulations That Significantly Affect Energy Supply, Distribution, or Use J. National Technology Transfer and Advancement Act (NTTAA) K. Executive Order 12898: Federal Actions To Address Environmental Justice in Minority Populations and Low-Income Populations L. Congressional Review Act (CRA) I. General Information A. Does this action apply to me? Table 1 of this preamble lists the NESHAP and associated regulated industrial source categories that are the subject of this final action. Table 1 is not intended to be exhaustive but rather provides a guide for readers regarding the entities that this final action is likely to affect. The final amendments will be directly applicable to the affected sources. Federal, state, local and tribal government entities would not be affected by this final action. As defined in the Initial List of Categories of Sources Under Section 112(c)(1) of the Clean Air Act Amendments of 1990 (see 57 FR 31576, July 16, 1992) and Documentation for Developing the Initial Source Category List (see EPA– 450/3–91–030), the Clay Products Manufacturing source category as originally listed included any facility engaged in manufacturing of clay products such as brick, vitrified clay pipe, structural clay tile, and clay refractories. The Clay Products Manufacturing source category has since been replaced by the Brick and Structural Clay Products (BSCP) Manufacturing source category and the Clay Ceramics Manufacturing source category (see 67 FR 47894, July 22, 2002). TABLE 1—NESHAP AND INDUSTRIAL SOURCE CATEGORIES AFFECTED BY THIS FINAL ACTION NAICS code 1 Category Industry ..................................................... 327120 327110 Federal government .................................. State/local/tribal government .................... 1 North ........................ ........................ Examples of potentially regulated entities Ceramic wall and floor tile manufacturing facilities (Clay Ceramics Manufacturing NESHAP). Vitreous plumbing fixtures (sanitaryware) manufacturing facilities (Clay Ceramics Manufacturing NESHAP). Not affected. Not affected. American Industry Classification System. B. Where can I get a copy of this document and other related information? In addition to being available in the docket, an electronic copy of this final action is available on the internet. Following signature by the EPA Administrator, the EPA will post a copy of this final action at https:// VerDate Sep<11>2014 16:01 Oct 31, 2019 Jkt 250001 www.epa.gov/stationary-sources-airpollution/brick-and-structural-clayproducts-national-emission-standards. Following publication in the Federal Register, the EPA will post the Federal Register version of the final amendments and key technical documents at this same website. PO 00000 Frm 00004 Fmt 4700 Sfmt 4700 A redline version of the regulatory language that incorporates the changes in this final action is available in the docket for this action (Docket ID No. EPA–HQ–OAR–2013–0290). E:\FR\FM\01NOR1.SGM 01NOR1 Federal Register / Vol. 84, No. 212 / Friday, November 1, 2019 / Rules and Regulations C. Judicial Review and Administrative Reconsideration Under Clean Air Act (CAA) section 307(b)(1), judicial review of this final action is available only by filing a petition for review in the United States Court of Appeals for the District of Columbia Circuit by December 31, 2019. Under CAA section 307(b)(2), the requirements established by this final rule may not be challenged separately in any civil or criminal proceedings brought by the EPA to enforce the requirements. Section 307(d)(7)(B) of the CAA further provides that only an objection to a rule or procedure which was raised with reasonable specificity during the period for public comment (including any public hearing) may be raised during judicial review. This section also provides a mechanism for the EPA to reconsider the rule if the person raising an objection can demonstrate to the Administrator that it was impracticable to raise such objection within the period for public comment or if the grounds for such objection arose after the period for public comment (but within the time specified for judicial review) and if such objection is of central relevance to the outcome of the rule. Any person seeking to make such a demonstration should submit a Petition for Reconsideration to the Office of the Administrator, U.S. EPA, Room 3000, WJC South Building, 1200 Pennsylvania Ave. NW, Washington, DC 20460, with a copy to both the person listed in the preceding FOR FURTHER INFORMATION CONTACT section, and the Associate General Counsel for the Air and Radiation Law Office, Office of General Counsel (Mail Code 2344A), U.S. EPA, 1200 Pennsylvania Ave. NW, Washington, DC 20460. II. Background A. What is the statutory authority for this action? The statutory authority for this action is provided by sections 112 and 307(d)(7)(B) of the CAA as amended (42 U.S.C. 7412 and 7607(d)(7)(B)). B. What actions preceded these final amendments? The initial NESHAP for Clay Ceramics Manufacturing was published in the Federal Register on May 16, 2003 (68 FR 26690), and codified at 40 CFR part 63, subpart KKKKK, pursuant to section 112 of the CAA. These standards were challenged and subsequently vacated by the United States Court of Appeals for the District of Columbia Circuit in 2007. See Sierra Club v. EPA, 479 F.3d 875, 876 (D.C. Cir. 2007). Following the 2007 vacatur of the 2003 rule, the EPA collected additional data and information to support new standards for the clay ceramics industry. This information is contained in the docket at https://www.regulations.gov/ (see Docket ID No. EPA–HQ–OAR–2013– 0290). On December 18, 2014, the EPA proposed the new NESHAP for Clay Ceramics Manufacturing (79 FR 75622). The EPA received additional data and comments during the public comment period. These data and comments were considered and analyzed and, where appropriate, revisions to the NESHAP were made. The NESHAP for Clay Ceramics Manufacturing was finalized on October 26, 2015 (80 FR 65470). On December 23, 2015, Kohler Company (Kohler) petitioned the EPA for reconsideration of the final rule for Clay Ceramics Manufacturing (Docket ID No. EPA–HQ–OAR–2013–0290– 0316). On August 20, 2018, we proposed revisions to the Clay Ceramics Manufacturing NESHAP based on the information provided by Kohler in their petition and information collected by the EPA (83 FR 42066). Public comments were received on the proposal requesting some changes to the proposed revisions. This action finalizes the revisions to the NESHAP and, where deemed appropriate, incorporates the requested changes. The intent of these amendments is to provide flexibility to the clay ceramics manufacturing industry, while maintaining the emissions and operational standards of the NESHAP. III. Summary of the Final Amendments The EPA is issuing the following amendments to 40 CFR part 63, subpart KKKKK, in response to Kohler’s petition for reconsideration on the October 26, 2015, final rule (80 FR 65470): • Revise the temperature monitoring methodology used to demonstrate continuous compliance with the D/F emissions limits from sanitaryware firstfire tunnel kilns; 58603 • Provide an alternative to the monitoring provisions for VE from tunnel kiln exhaust stacks; • Amend the requirements for weekly visual inspections of system ductwork and control device equipment for water curtain spray booths; • Define cooling stacks in the rule and differentiate cooling stacks from kiln exhaust stacks for compliance purposes; and • Include provisions to allow emissions averaging for emissions from existing tunnel kilns and glaze spray booths and make associated revisions to the definition of affected source and recordkeeping and reporting requirements. We are finalizing all the amendments listed above as proposed except for the provisions to allow emissions averaging. A description of the changes made to the emissions averaging provisions since proposal along with the rationale for those changes is provided in section IV of this preamble. This final rule achieves meaningful burden reduction by providing regulated facilities with the ability to use existing monitoring equipment and removing the requirements for periodic inspections that we have determined are not necessary to demonstrate compliance. We also more clearly identify which stacks are cooling stacks; thus, avoiding the possibility that a source might be required to perform an emission test on a stack that emits only cooling air. Finally, this action provides additional compliance flexibility for sources to meet certain emissions limits by averaging; thereby, simplifying compliance. All of these actions should reduce the overall burden to the regulated sources. This action is limited to the specific issues raised in the petition for reconsideration, plus some minor technical corrections. There are no changes to emission limits as a result of these final amendments. Technical corrections are being issued as proposed to correct inaccuracies that were promulgated in the final rule, replace text that might be considered confusing, and correct outdated information. These changes are described in Table 2 of this preamble. TABLE 2—TECHNICAL CORRECTIONS TO 40 CFR PART 63, SUBPART KKKKK Table to subpart KKKKK Description of correction 40 CFR 63.8635(g)(1) .............................................................................. Table 2, item 3 ......................................................................................... Update the addresses for EPA websites. To avoid confusion, revise the description of the operating limit for carbon flow rate. VerDate Sep<11>2014 16:01 Oct 31, 2019 Jkt 250001 PO 00000 Frm 00005 Fmt 4700 Sfmt 4700 E:\FR\FM\01NOR1.SGM 01NOR1 58604 Federal Register / Vol. 84, No. 212 / Friday, November 1, 2019 / Rules and Regulations TABLE 2—TECHNICAL CORRECTIONS TO 40 CFR PART 63, SUBPART KKKKK—Continued Table to subpart KKKKK Description of correction Table 2, items 10 and 11 ......................................................................... Revise the block period for average operating temperature for spray dryers and floor tile press dryers from 3-hour to 4-hour to align with the test run length for EPA Method 23. In the measurement of carbon flow rate data, include data from the Hg and D/F performance test data for tunnel or roller kilns equipped with an activated carbon injection system. Revise the block average for operating temperature for spray dryers and floor tile press dryers from 3-hour to 4-hour to align with the test run length for EPA Method 23. To avoid confusion, remove mention of the specific block period and simply refer to ‘‘the period of the initial performance test.’’ Table 4, item 8 ......................................................................................... Table 4, items 11 and 12 ......................................................................... Table 6, items 2.a.ii, 2.b.ii, 2.c.ii, 3.a.ii, 3.b.ii, 3.c.ii, 4.a.ii, 4.b.ii, 4.c.ii, 5.a.ii, 5.b.ii, 6.a.ii, 7.a.ii, 8.a.ii, 9.a.ii, 10.a.ii, 11.a.ii, 12.a.ii, 12.b.ii, 12.c.ii, 13.a.ii, 13.b.ii, 13.c.ii, 14.a.ii, 14.b.ii, 14.c.ii, 15.a.ii, 15.b.ii, 16.a.ii, 17.a.ii, 18.a.ii, 19.a.ii, 20.a.ii, and 21.a.ii. Table 7, items 10 and 11 ......................................................................... IV. Rationale for Changes to the Proposed Amendments A. Visible Emissions Monitoring of Tunnel Kiln Exhaust In its petition for reconsideration, Kohler stated that the EPA failed to adequately respond to Kohler’s public comments regarding VE monitoring in the Agency’s response to comments document and in the preamble for the final rule. In their comments on the December 18, 2014, proposal, Kohler had argued that VE monitoring is not a useful parameter to assess kiln operation nor to assess hazardous air pollutant (HAP) emissions. Kohler requested that the EPA open a new public comment period to reconsider and respond to Kohler’s concerns. In response to the petition, we proposed amendments to 40 CFR 63.8620 in the Clay Ceramics Manufacturing NESHAP, adding a new paragraph (e)(2) which provided an alternative to VE testing that allowed sources to demonstrate compliance by maintaining the kiln temperature profile within acceptable parameters and, for any incidence where the kiln exceeds its temperature profile, monitor VE at each kiln stack as specified. In public comments on the proposed amendments, a commenter questioned Kohler’s assertion about VE monitoring and recommended that the EPA define what a ‘‘temperature profile’’ is and clarify what it means to ‘‘maintain’’ it v. ‘‘exceed’’ it. In response to this comment, we are finalizing amendments to 40 CFR 63.8620(e)(2), the operating limits table (Table 2), and the continuous compliance table (Table 7) to clarify that the owner or operator will be required to maintain their kiln operating temperature within the range of acceptable temperatures (i.e., a temperature profile) established for each VerDate Sep<11>2014 16:01 Oct 31, 2019 Jkt 250001 Revise the block average for operating temperature for spray dryers and floor tile press dryers from 3-hour to 4-hour to align with the test run length for EPA Method 23. kiln and product. For any incident where the kiln is operating outside of its acceptable temperature range (i.e., exceeding its temperature profile) for the product being fired, the owner or operator will be required to record the incident as a deviation, and perform corrective action in accordance with the facility’s operation, maintenance, and monitoring (OM&M) plan. B. Weekly Visual Inspections of Water Curtain Spray Booths In its petition for reconsideration, Kohler requested that the EPA reconsider the frequency of visual inspection requirements for system ductwork and control device equipment for water curtain spray booths. In response to the petition, we proposed amendments to the operating limits table (Table 2) and the continuous compliance table (Table 7) to remove the requirement to conduct weekly visual inspections of the system ductwork and control equipment for leaks for all glaze spray operations equipped with water curtains. In public comments on the proposal, one commenter stated that if the EPA is relying on operator observations of visible particulate on the product to determine when there is a leak in the spray booth ductwork, the rule should require operators to log such incidents and report them as deviations when they occur. We recognize the commenter’s concerns and agree that if there is an indication of particulate in the glaze of the product, then it is likely there is a failure in the ductwork requiring corrective action, and, therefore, this would be considered a deviation. We are finalizing amendments to Table 7 to require owners or operators to record as deviations any observations of particulates or other impurities getting PO 00000 Frm 00006 Fmt 4700 Sfmt 4700 into the glaze that has been sprayed onto a piece of ware and perform corrective action in accordance with the facility’s OM&M plan. C. Emissions Averaging In its petition for reconsideration, Kohler requested that the EPA allow the use of emissions averaging as a compliance option in the Clay Ceramics Manufacturing NESHAP for existing tunnel kilns and glaze spray booths. In response to the petition, we proposed amendments to 40 CFR 63.8595 in the Clay Ceramics Manufacturing NESHAP that included alternative emissions averaging limits for the following: • PM and Hg, in units of pounds per ton (lb/ton) of fired product for existing floor tile roller kilns; • PM and Hg in units of lb/ton of fired product for existing wall tile roller kilns; • PM and Hg, in units of lb/ton of greenware fired for existing first-fired sanitaryware tunnel kilns; • PM and Hg, in units of lb/ton of first-fired glaze sprayed (dry weight basis) for existing tile glaze lines with glaze spraying; and • PM, in units of lb/ton of first-fire glaze sprayed (dry weight basis), for existing sanitaryware manual, spray machine, or robot glaze applications. The proposed conditions required for emissions averaging included the following: (1) Emissions averaging would only be permitted between individual sources at a single existing affected source; (2) emissions averaging would only be permitted between individual sources subject to the Clay Ceramics Manufacturing NESHAP; (3) emissions averaging would not be permitted between two or more different affected sources; (4) emissions averaging would not be permitted between two or more sources in different subcategories; E:\FR\FM\01NOR1.SGM 01NOR1 Federal Register / Vol. 84, No. 212 / Friday, November 1, 2019 / Rules and Regulations (5) new sources could not use emissions averaging; and (6) averaged emissions could not exceed 90 percent of the applicable emission limit, which translates to a discount factor of 1.1 applied to actual emissions. The emissions averaging provisions that we proposed were based, in part, on the emissions averaging provisions in the Hazardous Organic NESHAP (HON). The legal basis and rationale for the HON emissions averaging provisions were provided in the preamble to the final HON (59 FR 19425, April 22, 1994). In public comments on the proposal, two commenters requested that the EPA remove the requirement that averaged emissions cannot exceed 90 percent of the applicable emission limit, and a third commenter stated that no justification was provided for the selection of 90 percent (instead of an alternate value, such as 80 or 99 percent). While averaging should only be permitted if it can be demonstrated that the total quantity of any HAP will not be greater than it could be if each individually affected unit complied separately with the applicable standard, one commenter stated this requirement can be demonstrated without the ‘‘90 percent of the limit’’ safety factor. The commenter noted that the EPA has allowed emissions averaging across similar emission units in other NESHAP, such as the Reinforced Plastics Composites NESHAP (40 CFR part 63, subpart WWWW), and stated that similar logic for averaging should be applied to this subpart to eliminate the unnecessary factor. In response to these comments, we have re-evaluated whether a discount factor is appropriate for the emissions averaging provisions in this subpart and have concluded that a discount factor is not necessary here. The issues faced in the HON, where a discount factor of 1.1 was applied to the emissions averaging calculation, included significant differences in toxicity of the various HAP and a situation where facilities were applying emissions controls. This is not the case here. All facilities are meeting the relevant standards in this subpart without added controls and are using pollution prevention where needed. Accordingly, a straight average, without any discount factor, is appropriate in this situation. This straight-average approach is consistent with other rules, such as the Reinforced Plastic Composites NESHAP. Therefore, the EPA has decided not to include a discount factor in 40 CFR 63.8595(h), Equation 9, and 40 CFR 63.8620, Equation 10 to calculate the average weighted emissions. VerDate Sep<11>2014 16:01 Oct 31, 2019 Jkt 250001 In addition, a commenter noted that the proposed emissions averaging provisions prohibited emissions averaging of new sources but did not prohibit emissions averaging of reconstructed sources. The commenter stated that reconstructed sources should not be allowed to use the emissions averaging provisions. We agree with the commenter, and in the final amendments the EPA has revised 40 CFR 63.8595(h)(1) to indicate that neither new nor reconstructed sources can be included in the emissions averaging. Finally, we note that Equations 9 through 11 were all proposed to be added to 40 CFR 63.8595(h). However, one commenter noted an apparent discrepancy between Equation 9 and Equation 10, and it appears that the commenter misunderstood that Equation 9 is intended to determine initial compliance based on an initial performance test, while Equation 10 is intended to determine ongoing compliance based on the latest performance test. Equation 11 is also used for ongoing compliance and is intended to determine the 12-month rolling average of the monthly weighted average emission rates. Therefore, in the final amendments, Equations 10 and 11 have been moved to 40 CFR 63.8620, the section that describes how to demonstrate continuous compliance. V. Summary of Cost, Environmental, and Economic Impacts This action will have no cost, environmental, energy, or economic impacts beyond those impacts presented in the October 26, 2015, final rule for Clay Ceramics Manufacturing and may result in a cost savings due to the changes in monitoring and testing requirements discussed in section III of this preamble. The technical corrections are cost neutral. VI. Statutory and Executive Order Reviews Additional information about these statutes and Executive Orders can be found at https://www.epa.gov/lawsregulations/laws-and-executive-orders. A. Executive Order 12866: Regulatory Planning and Review and Executive Order 13563: Improving Regulation and Regulatory Review This action is not a significant regulatory action and was, therefore, not submitted to the OMB for review. PO 00000 Frm 00007 Fmt 4700 Sfmt 4700 58605 B. Executive Order 13771: Reducing Regulations and Controlling Regulatory Costs This action is considered an Executive Order 13771 deregulatory action. This final rule provides meaningful burden reduction by providing additional regulatory flexibilities. C. Paperwork Reduction Act (PRA) This action does not impose any new information collection burden under the PRA. OMB has previously approved the information collection activities contained in the existing regulation (40 CFR part 63, subpart KKKKK) and has assigned OMB control number 2060– 0513. This action does not change the information collection requirements. D. Regulatory Flexibility Act (RFA) I certify that this action will not have a significant economic impact on a substantial number of small entities under the RFA. In making this determination, the impact of concern is any significant adverse economic impact on small entities. An agency may certify that a rule will not have a significant economic impact on a substantial number of small entities if the rule relieves regulatory burden, has no net burden, or otherwise has a positive economic effect on the small entities subject to the rule. This final rule will not impose any additional requirements on small entities, only alternatives to existing requirements. We have, therefore, concluded that this action will have no net regulatory burden for all directly regulated small entities. E. Unfunded Mandates Reform Act (UMRA) This action does not contain an unfunded mandate as described in UMRA, 2 U.S.C. 1531–1538, and does not significantly or uniquely affect small governments. The action imposes no enforceable duty on any state, local, or tribal governments or the private sector. F. Executive Order 13132: Federalism This action does not have federalism implications. It will not have substantial direct effects on the states, on the relationship between the national government and the states, or on the distribution of power and responsibilities among the various levels of government. G. Executive Order 13175: Consultation and Coordination With Indian Tribal Governments This action does not have tribal implications as specified in Executive E:\FR\FM\01NOR1.SGM 01NOR1 Federal Register / Vol. 84, No. 212 / Friday, November 1, 2019 / Rules and Regulations Order 13175. It will neither impose substantial direct compliance costs on federally recognized tribal governments, nor preempt tribal law. The final amendments impose no requirements on tribal governments. Thus, Executive Order 13175 does not apply to this action. H. Executive Order 13045: Protection of Children From Environmental Health Risks and Safety Risks The EPA interprets Executive Order 13045 as applying only to those regulatory actions that concern environmental health or safety risks that the EPA has reason to believe may disproportionately affect children, per the definition of ‘‘covered regulatory action’’ in section 2–202 of the Executive Order. This action is not subject to Executive Order 13045 because it does not concern an environmental health risk or safety risk. I. Executive Order 13211: Actions Concerning Regulations That Significantly Affect Energy Supply, Distribution, or Use This action is not subject to Executive Order 13211, because it is not a significant regulatory action under Executive Order 12866. J. National Technology Transfer and Advancement Act (NTTAA) This rulemaking does not involve technical standards. K. Executive Order 12898: Federal Actions To Address Environmental Justice in Minority Populations and Low-Income Populations The EPA believes that this action does not have disproportionately high and adverse human health or environmental effects on minority populations, lowincome populations, and/or indigenous peoples, as specified in Executive Order 12898 (59 FR 7629, February 16, 1994). The documentation for this decision is contained in the docket. (See EJ Screening Report for Clay Ceramics, Docket ID Item No. EPA–HQ–OAR– 2013–0290–0241.) L. Congressional Review Act (CRA) This action is subject to the CRA, and the EPA will submit a rule report to each House of the Congress and to the Comptroller General of the United States. This action is not a ‘‘major rule’’ as defined by 5 U.S.C. 804(2). List of Subjects in 40 CFR Part 63 Environmental protection, Administrative practices and procedures, Air pollution control, Hazardous substances, Intergovernmental relations, Reporting and recordkeeping requirements. Dated: October 10, 2019. Andrew R. Wheeler, Administrator. For the reasons set out in the preamble, 40 CFR part 63 is amended as follows: PART 63—NATIONAL EMISSION STANDARDS FOR HAZARDOUS AIR POLLUTANTS FOR SOURCE CATEGORIES 1. The authority citation for part 63 continues to read as follows: ■ Authority: 42 U.S.C. 7401 et seq. Subpart KKKKK—National Emission Standards for Hazardous Air Pollutants for Clay Ceramics Manufacturing 2. Section 63.8595 is amended by: a. Revising paragraph (c); b. Redesignating paragraph (h) as paragraph (i); ■ c. Adding a new paragraph (h); and ■ d. Revising newly redesignated paragraphs (i) introductory text and (i)(1) introductory text. The revisions and addition read as follows: ■ ■ ■ § 63.8595 How do I conduct performance tests and establish operating limits? * * * * * (c) Each performance test must be conducted according to the requirements in § 63.7 and under the specific conditions in Table 4 to this subpart. Stacks to be tested at sanitaryware manufacturing facilities shall be limited to products of combustion (POC) stacks and not include cooling stacks. * * * * * (h)(1) As an alternative to meeting the requirements of § 63.8555 for PM or Where: ERi = Average weighted emissions for PM or mercury, in units of kilograms (pounds) per megagram (ton) of fired product for VerDate Sep<11>2014 16:01 Oct 31, 2019 Jkt 250001 PO 00000 existing floor tile roller kilns and wall tile roller kilns, greenware fired for existing first-fired sanitaryware tunnel kilns, and first-fire glaze sprayed (dry Frm 00008 Fmt 4700 Sfmt 4700 mercury, if you have more than one existing source in any subcategories located at your facility, you may demonstrate compliance by emissions averaging, if your averaged emissions are no higher than the applicable emission limit, according to the procedures in this section. You may not include new or reconstructed sources in an emissions average. (2) For a group of two or more existing sources in the same subcategory that each vent to a separate stack, you may average PM or mercury emissions among existing units to demonstrate compliance with the limits in Table 1 to this subpart as specified in paragraph (h)(2)(i) through (iv) of this section, if you satisfy the requirements in paragraphs (h)(3) and (4) of this section. (i) You may average across existing sources in the same kiln type and size category (e.g., roller or tunnel kilns, large or small kilns) and the same subcategory (e.g., sanitaryware manual or spray machine or robot glaze application) where applicable; (ii) You may not include a unit in the emissions average if the unit shares a common stack with units in other subcategories; (iii) You may not include spray dryers or press dryers in the emissions average; and (iv) You may not average between different types of pollutants. (3) The averaged emissions rate from the existing sources participating in the emissions averaging option must not exceed the limits in Table 1 to this subpart at all times the affected units are subject to numeric emission limits following the compliance date specified in § 63.8545. (4)(i) You must demonstrate initial compliance using the maximum process rate and the results of the initial performance tests. (ii) You must use Equation 9 of this section to demonstrate that the PM or mercury emissions from all existing units participating in the emissions averaging option for that pollutant do not exceed the emission limits in Table 1 to this subpart. weight basis) for existing tile glaze lines with glaze spraying and average weighted emissions for PM, in units of kilograms (pounds) per megagram (ton) E:\FR\FM\01NOR1.SGM 01NOR1 ER01NO19.003</GPH> 58606 Federal Register / Vol. 84, No. 212 / Friday, November 1, 2019 / Rules and Regulations of first-fire glaze sprayed (dry weight basis) for existing sanitaryware manual, spray machine, or robot glaze applications. Ei = Emission rate (as determined during the initial compliance demonstration) of PM or mercury from unit i, in units of kilograms (pounds) per megagram (ton). Determine the emission rate for PM or mercury by performance testing according to Table 4 to this subpart using the applicable equation in paragraph (f) of this section. Pmax i = Maximum process rate for unit i, in units of megagrams per hour (tons per hour). n = Number of units participating in the emissions averaging option. (5) You must develop and submit upon request to the applicable Administrator for review and approval, an implementation plan for emissions averaging according to the following procedures and requirements in paragraphs (h)(5)(i) through (iv) of this section. (i) If requested, you must submit the implementation plan no later than 180 days before the date that the facility intends to demonstrate compliance using the emissions averaging option. (ii) You must include the information contained in paragraphs (h)(5)(ii)(A) through (D) of this section in your implementation plan for all emission sources included in an emissions average: (A) The identification of all existing sources in the averaging group, including for each either the applicable HAP emissions level or the control technology installed and the date on which you are requesting emissions averaging to commence; (B) The specific control technology or pollution prevention measure to be used for each source in the averaging group and the date of its installation or application. If the pollution prevention measure reduces or eliminates emissions from multiple sources, the owner or operator must identify each source; (C) The test plan for the measurement of emissions in accordance with the requirements in this section; and (D) The operating parameters to be monitored for each control system or device consistent with § 63.8555 and Table 2 to this subpart, and a description of how the operating limits will be determined. (iii) If submitted upon request, the Administrator shall review and approve or disapprove the plan according to the following criteria: VerDate Sep<11>2014 16:01 Oct 31, 2019 Jkt 250001 (A) Whether the content of the plan includes all of the information specified in paragraph (h)(5)(ii) of this section; and (B) Whether the plan presents sufficient information to determine that compliance will be achieved and maintained. (iv) The applicable Administrator shall not approve an emissions averaging implementation plan containing any of the following provisions: (A) Any averaging between emissions of differing pollutants or between differing sources; or (B) The inclusion of any emission source other than an existing unit in the same subcategories. (i) For each affected source that is subject to the emission limits specified in Table 1 to this subpart and is equipped with an APCD that is not addressed in Table 2 to this subpart or that is using process changes as a means of meeting the emission limits in Table 1 to this subpart, you must meet the requirements in § 63.8(f) and paragraphs (i)(1) and (2) of this section. (1) Submit a request for approval of alternative monitoring procedures to the Administrator no later than the notification of intent to conduct a performance test. The request must contain the information specified in paragraphs (i)(1)(i) through (iv) of this section. * * * * * ■ 3. Section 63.8620 is amended by: ■ a. Redesignating paragraphs (e) introductory text and (e)(1) through (3) as paragraphs (e)(1) introductory text and (e)(1)(i) through (iii), respectively; ■ b. Revising newly redesignated paragraph (e)(1) introductory text; and ■ c. Adding new paragraph (e)(2) and paragraphs (f) and (g). The revision and additions read as follows: § 63.8620 How do I demonstrate continuous compliance with the emission limitations and work practice standards? * * * * * (e)(1) Visible emissions testing. You must demonstrate continuous compliance with the operating limits in Table 2 to this subpart for visible emissions (VE) from tunnel or roller kilns that are uncontrolled or equipped with DIFF, DLS/FF, or other dry control device by monitoring VE at each kiln stack according to the requirements in paragraphs (e)(1)(i) through (iii) of this section. * * * * * PO 00000 Frm 00009 Fmt 4700 Sfmt 4700 58607 (2) Alternative to VE testing. You must demonstrate continuous compliance with the operating limits in Table 2 to this subpart for kiln temperature profile for tunnel or roller kilns that are uncontrolled or equipped with DIFF, DLS/FF, or other dry control device by maintaining the kiln operating temperature within the range of acceptable temperatures (i.e., temperature profile) established for each kiln and product. For any incidence where the kiln is operating outside of its acceptable temperature range (i.e., exceeds its temperature profile) for the product being fired, you must record the incident as a deviation, and perform the necessary corrective action in accordance with your OM&M plan to return the kiln to the acceptable operating temperature for the product being fired. To confirm the kiln has returned to the acceptable temperature range, you will monitor VE at the kiln stack according to the requirements in paragraphs (e)(2)(i) through (iii) of this section. (i) Perform VE observations at the stack of each kiln operating outside of its temperature profile according to the procedures of Method 22 of 40 CFR part 60, appendix A–7. The duration of each Method 22 test must be at least 15 minutes. (ii) If VE are observed during any test conducted using Method 22 of 40 CFR part 60, appendix A–7, you must continue to perform corrective action until VE are no longer observed. (iii) If VE are observed during any test conducted using Method 22 of 40 CFR part 60, appendix A–7, you must report these deviations by following the requirements in § 63.8635. (f) Following the compliance date, you must demonstrate compliance with the emissions averaging provision under this subpart on a continuous basis by meeting the requirements of paragraphs (f)(1) through (3) of this section. (1)(i) After the initial compliance demonstration described in § 63.8595(h)(4), you must demonstrate compliance on a monthly basis determined at the end of every month (12 times per year) according to paragraph (f)(1)(ii) of this section. The first monthly period begins on the compliance date specified in § 63.8545. (ii) For each calendar month, you must use Equation 10 of this section to calculate the average weighted emission rate for that month. E:\FR\FM\01NOR1.SGM 01NOR1 Federal Register / Vol. 84, No. 212 / Friday, November 1, 2019 / Rules and Regulations Where: ERi = Average weighted emissions for PM or mercury, in units of kilograms (pounds) per megagram (ton) of fired product for existing floor tile roller kilns and wall tile roller kilns, greenware fired for existing first-fired sanitaryware tunnel kilns, and first-fire glaze sprayed (dry weight basis) for existing tile glaze lines with glaze spraying and average weighted emissions for PM, in units of kilograms (pounds) per megagram (ton) of first-fire glaze sprayed (dry weight basis) for existing sanitaryware manual, spray machine, or robot glaze applications, for that calendar month. Ei = Emission rate (as determined during the most recent compliance demonstration) of PM or mercury from unit i, in units of kilograms (pounds) per megagram (ton). Determine the emission rate for PM or mercury by performance testing according to Table 4 to this subpart using the applicable equation in § 63.8595(f). Pmonth i = The process rate for that calendar month for unit i, in units of megagrams (tons). n = Number of units participating in the emissions averaging option. (2) Until 12 monthly weighted average emission rates have been accumulated, calculate and report only the average weighted emission rate determined under paragraph (f)(1)(ii) of this section for each calendar month. After 12 monthly weighted average emission rates have been accumulated, for each subsequent calendar month, use Equation 11 of this section to calculate the 12-month rolling average of the monthly weighted average emission rates for the current calendar month and the previous 11 calendar months. Where: Eavg = 12-month rolling average emission rate for PM or mercury, in units of kilograms (pounds) per megagram (ton) of fired product for existing floor tile roller kilns and wall tile roller kilns, greenware fired for existing first-fired sanitaryware tunnel kilns, and first-fire glaze sprayed (dry weight basis) for existing tile glaze lines with glaze spraying and average weighted emissions for PM, in units of kilograms (pounds) per megagram (ton) of first-fire glaze sprayed (dry weight basis) for existing sanitaryware manual, spray machine, or robot glaze applications. ERi = Monthly weighted average, for calendar month ‘‘i,’’ in units of kilograms (pounds) per megagram (ton), as calculated by paragraph (f)(1)(ii) of this section. requirements in paragraphs (f)(1) through (3) of this section is a deviation. technology employed on December 28, 2015. * * * * * ■ 5. Section 63.8635 is amended by: ■ a. Revising paragraphs (c) introductory text and (c)(4)(iii)(C); ■ b. Adding paragraph (c)(9); and ■ c. Revising paragraph (g)(1). The revisions and addition read as follows: Where: RM = Annual percentage of affected source uptime during which control device was offline for routine control device maintenance. DTp = Control device downtime claimed under the routine control device maintenance alternative standard for the previous semiannual compliance period. VerDate Sep<11>2014 16:01 Oct 31, 2019 Jkt 250001 § 63.8630 What notifications must I submit and when? * * * * * (c) If you are required to conduct a performance test or other initial compliance demonstration as specified in Tables 4 and 6 to this subpart, your Notification of Compliance Status as specified in Table 9 to this subpart must include the information in paragraphs (c)(1) through (4) of this section. * * * * * (4) Identification of whether you plan to demonstrate compliance by emissions averaging. If you plan to demonstrate compliance by emissions averaging, report the emissions level that was being achieved or the control DTc = Control device downtime claimed under the routine control device maintenance alternative standard for the current semiannual compliance period. SUp = Affected source uptime for the previous semiannual compliance period. SUc = Affected source uptime for the current semiannual compliance period. * PO 00000 * * Frm 00010 * Fmt 4700 * Sfmt 4700 § 63.8635 when? What reports must I submit and * * * * * (c) The compliance report must contain the information in paragraphs (c)(1) through (9) of this section. * * * * * (4) * * * (iii) * * * (C) Based on the information recorded under paragraphs (c)(4)(iii)(A) and (B) of this section, compute the annual percent of affected source operating uptime during which the control device was offline for routine maintenance using Equation 12 of this section. (9) If you plan to demonstrate compliance by emissions averaging, certify the emissions level achieved or the control technology employed is no less stringent than the level or control technology contained in the notification of compliance status in § 63.8630(c)(4), including all necessary documentation E:\FR\FM\01NOR1.SGM 01NOR1 ER01NO19.005</GPH> ER01NO19.006</GPH> (3) For each existing unit participating in the emissions averaging option, you must comply with the continuous compliance requirements in Table 7 to this subpart. (g) Any instance where you fail to comply with the continuous monitoring 4. Section 63.8630 is amended by revising paragraph (c) introductory text and adding paragraph (c)(4) to read as follows: ■ ER01NO19.004</GPH> 58608 Federal Register / Vol. 84, No. 212 / Friday, November 1, 2019 / Rules and Regulations to support this certification, such as inputs to Equations 9 through 11 of this subpart. * * * * * (g) * * * (1) For data collected using test methods supported by the EPA’s Electronic Reporting Tool (ERT) as listed on the EPA’s ERT website (https://www.epa.gov/ electronicreporting-air-emissions/ electronicreporting-tool-ert) at the time of the test, you must submit the results of the performance test to the EPA via the Compliance and Emissions Data Reporting Interface (CEDRI). (CEDRI can be accessed through the EPA’s Central Data Exchange (CDX) (https:// cdx.epa.gov/).) Performance test data must be submitted in a file format generated through the use of the EPA’s ERT or an alternate electronic file format consistent with the extensible markup language (XML) schema listed on the EPA’s ERT website. If you claim that some of the performance test information being submitted is confidential business information (CBI), you must submit a complete file generated through the use of the EPA’s ERT or an alternate electronic file consistent with the XML schema listed on the EPA’s ERT website, including information claimed to be CBI, on a compact disc, flash drive, or other commonly used electronic storage media to the EPA. The electronic media must be clearly marked as CBI and mailed to U.S. EPA/OAPQS/CORE CBI Office, Attention: Group Leader, Measurement Policy Group, MD C404– 02, 4930 Old Page Rd., Durham, NC 27703. The same ERT or alternate file with the CBI omitted must be submitted to the EPA via the EPA’s CDX as described earlier in this paragraph (g)(1). * * * * * ■ 6. Section 63.8640 is amended by revising paragraph (c) introductory text and adding paragraph (c)(11) to read as follows: § 63.8640 What records must I keep? * * * * * (c) You must also maintain the records listed in paragraphs (c)(1) through (11) of this section. * * * * * (11) If you elect to average emissions consistent with § 63.8595(h), you must additionally keep a copy of the emissions averaging implementation plan required in § 63.8595(h)(5), all calculations required under § 63.8595(h), including monthly records of process rate, as applicable, and monitoring records consistent with § 63.8620(f). ■ 7. Section 63.8665 is amended by adding definitions for ‘‘Cooling stack,’’ 58609 ‘‘Emissions averaging sources,’’ and ‘‘Products of combustion (POC) stack’’ in alphabetical order to read as follows: § 63.8665 subpart? What definitions apply to this * * * * * Cooling stack means a stack (release point) installed on the cooling zone of a tunnel kiln to release air used to cool down the fired product from its maximum temperature to room temperature. A cooling stack does not release any air from the firing zone of the tunnel kiln. * * * * * Emissions averaging sources means, for purposes of the emissions averaging provisions of § 63.8595(h), the collection of all existing ceramic tile roller kilns, sanitaryware tunnel kilns, ceramic tile glaze lines using glaze spraying, and sanitaryware glaze spray booths, within a kiln type and size category and within a subcategory. * * * * * Products of combustion (POC) stack means a stack (release point) installed on the front end of the firing zone of a tunnel kiln to release air used to heat the greenware from room temperature to its maximum temperature. * * * * * ■ 8. Table 1 to subpart KKKKK is revised to read as follows: TABLE 1 TO SUBPART KKKKK OF PART 63—EMISSION LIMITS As stated in § 63.8555, you must meet each emission limit in the following table that applies to you: For each . . . You must meet the following emission limits . . . 1. Collection of all tunnel or roller kilns at facility. 2. Existing floor tile roller kiln .......... HF and HCl emissions must not exceed 62 kilograms per hour (kg/hr) (140 pounds per hour (lb/hr)) HCl equivalent, under the health-based standard, as determined using Equations 4 and 5 of this subpart. a. PM emissions must not exceed 0.063 kilogram per megagram (kg/Mg) (0.13 pound per ton (lb/ton)) of fired product. b. Hg emissions must not exceed 6.3 E–05 kg/Mg (1.3 E–04 lb/ton) of fired product. c. Dioxin/furan emissions must not exceed 2.8 nanograms per kilogram (ng/kg) of fired product. a. PM emissions must not exceed 0.19 kg/Mg (0.37 lb/ton) of fired product. b. Hg emissions must not exceed 1.1 E–04 kg/Mg (2.1 E–04 lb/ton) of fired product. c. Dioxin/furan emissions must not exceed 0.22 ng/kg of fired product. a. PM emissions must not exceed 0.17 kg/Mg (0.34 lb/ton) of greenware fired. 3. Existing wall tile roller kiln .......... 4. Existing first-fire sanitaryware tunnel kiln. 5. Existing tile glaze line with glaze spraying. 6. Existing sanitaryware manual glaze application. 7. Existing sanitaryware spray machine glaze application. 8. Existing sanitaryware robot glaze application. 9. Existing floor tile spray dryer ...... 10. Existing wall tile spray dryer ..... 11. Existing floor tile press dryer .... 12. New or reconstructed floor tile roller kiln. b. Hg emissions must not exceed 1.3 E–04 kg/Mg (2.6 E–04 lb/ton) of greenware fired. c. Dioxin/furan emissions must not exceed 3.3 ng/kg of greenware fired. a. PM emissions must not exceed 0.93 kg/Mg (1.9 lb/ton) of first-fire glaze sprayed (dry weight basis). b. Hg emissions must not exceed 8.0 E–05 kg/Mg (1.6 E–04 lb/ton) of first-fire glaze sprayed (dry weight basis). PM emissions must not exceed 18 kg/Mg (35 lb/ton) of first-fire glaze sprayed (dry weight basis). PM emissions must not exceed 6.2 kg/Mg (13 lb/ton) of first-fire glaze sprayed (dry weight basis). PM emissions must not exceed 4.5 kg/Mg (8.9 lb/ton) of first-fire glaze sprayed (dry weight basis). Dioxin/furan emissions must not exceed 19 ng/kg of throughput processed. Dioxin/furan emissions must not exceed 0.058 ng/kg of throughput processed. Dioxin/furan emissions must not exceed 0.024 ng/kg of throughput processed. a. PM emissions must not exceed 0.019 kg/Mg (0.037 lb/ton) of fired product. b. Hg emissions must not exceed 2.0 E–05 kg/Mg (3.9 E–05 lb/ton) of fired product. c. Dioxin/furan emissions must not exceed 1.3 ng/kg of fired product. VerDate Sep<11>2014 16:01 Oct 31, 2019 Jkt 250001 PO 00000 Frm 00011 Fmt 4700 Sfmt 4700 E:\FR\FM\01NOR1.SGM 01NOR1 58610 Federal Register / Vol. 84, No. 212 / Friday, November 1, 2019 / Rules and Regulations TABLE 1 TO SUBPART KKKKK OF PART 63—EMISSION LIMITS—Continued As stated in § 63.8555, you must meet each emission limit in the following table that applies to you: For each . . . You must meet the following emission limits . . . 13. New or reconstructed wall tile roller kiln. a. PM emissions must not exceed 0.19 kg/Mg (0.37 lb/ton) of fired product. 14. New or reconstructed first-fire sanitaryware tunnel kiln. 15. New or reconstructed tile glaze line with glaze spraying. 16. New or reconstructed sanitaryware manual glaze application. 17. New or reconstructed sanitaryware spray machine glaze application. 18. New or reconstructed sanitaryware robot glaze application. 19. New or reconstructed floor tile spray dryer. 20. New or reconstructed wall tile spray dryer. 21. New or reconstructed floor tile press dryer. 22. Collection of emissions averaging sources. 23. Collection of emissions averaging sources. b. Hg emissions must not exceed 1.1 E–04 kg/Mg (2.1 E–04 lb/ton) of fired product. c. Dioxin/furan emissions must not exceed 0.22 ng/kg of fired product. a. PM emissions must not exceed 0.048 kg/Mg (0.095 lb/ton) of greenware fired. b. Hg emissions must not exceed 6.1 E–05 kg/Mg (1.3 E–04 lb/ton) of greenware fired. c. Dioxin/furan emissions must not exceed 0.99 ng/kg of greenware fired. a. PM emissions must not exceed 0.31 kg/Mg (0.61 lb/ton) of first-fire glaze sprayed (dry weight basis). b. Hg emissions must not exceed 8.0 E–05 kg/Mg (1.6 E–04 lb/ton) of first-fire glaze sprayed (dry weight basis). PM emissions must not exceed 2.0 kg/Mg (3.9 lb/ton) of first-fire glaze sprayed (dry weight basis). PM emissions must not exceed 1.6 kg/Mg (3.2 lb/ton) of first-fire glaze sprayed (dry weight basis). PM emissions must not exceed 1.2 kg/Mg (2.3 lb/ton) of first-fire glaze sprayed (dry weight basis). Dioxin/furan emissions must not exceed 0.071 ng/kg of throughput processed. Dioxin/furan emissions must not exceed 0.058 ng/kg of throughput processed. Dioxin/furan emissions must not exceed 0.024 ng/kg of throughput processed. PM emissions must not exceed the applicable emission limit, under the emissions averaging option, as determined using Equations 9 through 11 of this subpart. Hg emissions must not exceed the applicable emission limit, under the emissions averaging option, as determined using Equations 9 through 11 of this subpart. 9. Table 2 to subpart KKKKK is revised to read as follows: ■ TABLE 2 TO SUBPART KKKKK OF PART 63—OPERATING LIMITS As stated in § 63.8555, you must meet each operating limit in the following table that applies to you: For each . . . You must . . . Or you must . . . 1. Tunnel or roller kiln equipped with a DIFF or DLS/FF. a. If you use a bag leak detection system, initiate corrective action within 1 hour of a bag leak detection system alarm and complete corrective actions in accordance with your OM&M plan; operate and maintain the fabric filter such that the alarm is not engaged for more than 5 percent of the total operating time in a 6-month block reporting period; and b. Maintain free-flowing lime in the feed hopper or silo and to the APCD at all times for continuous injection systems; maintain the feeder setting (on a per ton of throughput basis) at or above the level established during the performance test for continuous injection systems in which compliance was demonstrated. a. Maintain the average scrubber liquid pH for each 3hour block period at or above the average scrubber liquid pH established during the HF/HCl performance test in which compliance was demonstrated; and b. Maintain the average scrubber liquid flow rate for each 3-hour block period at or above the highest average scrubber liquid flow rate established during the HF/HCl and PM performance tests in which compliance was demonstrated. Maintain the 3-hour block average carbon flow rate at or above the highest average carbon flow rate established during the Hg and dioxin/furan performance tests in which compliance was demonstrated. i. Maintain no VE from the DIFF or DLS/FF stack; or ii. Maintain your kiln operating temperature within the range of acceptable temperatures (i.e., temperature profile established for each kiln and product. 2. Tunnel or roller kiln equipped with a WS. 3. Tunnel or roller kiln equipped with an ACI system. VerDate Sep<11>2014 16:01 Oct 31, 2019 Jkt 250001 PO 00000 Frm 00012 Fmt 4700 Sfmt 4700 E:\FR\FM\01NOR1.SGM 01NOR1 Federal Register / Vol. 84, No. 212 / Friday, November 1, 2019 / Rules and Regulations 58611 TABLE 2 TO SUBPART KKKKK OF PART 63—OPERATING LIMITS—Continued As stated in § 63.8555, you must meet each operating limit in the following table that applies to you: For each . . . You must . . . Or you must . . . 4. Tunnel or roller kiln intending to comply with dioxin/furan emission limit without an ACI system. Maintain the average operating temperature for each 12-hour block period at or below the highest operating temperature established during the dioxin/furan performance test in which compliance was demonstrated. a. Maintain no VE from the stack; and i. Maintain your kiln operating temperature within the range of acceptable temperatures (i.e., temperature profile established for each kiln and product. 5. Tunnel or roller kiln with no add-on control. 6. Glaze spray operation equipped with a FF. 7. Glaze spray operation equipped with a WS. 8. Glaze spray operation equipped with a water curtain. 9. Glaze spray operation equipped with baffles. 10. Spray dryer .................... 11. Floor tile press dryer ...... b. Maintain the kiln process rate at or below the kiln process rate determined according to § 63.8595(g)(1) if your total facility maximum potential HCl-equivalent emissions are greater than the HCl-equivalent limit in Table 1 to this subpart; and c. Maintain the average operating temperature for each 12-hour block period at or below the highest operating temperature established during the dioxin/furan performance test in which compliance was demonstrated. a. If you use a bag leak detection system, initiate corrective action within 1 hour of a bag leak detection system alarm and complete corrective actions in accordance with your OM&M plan; operate and maintain the fabric filter such that the alarm is not engaged for more than 5 percent of the total operating time in a 6-month block reporting period. a. Maintain the average scrubber pressure drop for each 3-hour block period at or above the average pressure drop established during the PM performance test in which compliance was demonstrated; and b. Maintain the average scrubber liquid flow rate for each 3-hour block period at or above the average scrubber liquid flow rate established during the PM performance test in which compliance was demonstrated. a. Conduct daily inspections to verify the presence of water flow to the wet control system; and i. Maintain no VE from the FF stack. b. Conduct annual inspections of the interior of the control equipment (if applicable) to determine the structural integrity and condition of the control equipment. Conduct an annual visual inspection of the baffles to confirm the baffles are in place. Maintain the average operating temperature for each 4hour block period at or above the average temperature established during the dioxin/furan performance test in which compliance was demonstrated. Maintain the average operating temperature for each 4hour block period at or below the average temperature established during the dioxin/furan performance test in which compliance was demonstrated. 10. Table 4 to subpart KKKKK is revised to read as follows: ■ TABLE 4 TO SUBPART KKKKK OF PART 63—REQUIREMENTS FOR PERFORMANCE TESTS As stated in § 63.8595, you must conduct each performance test in the following table that applies to you: For each . . . You must . . . Using . . . According to the following requirements . . . 1. Tunnel or roller kiln ......... a. Select locations of sampling ports and the number of traverse points. b. Determine velocities and volumetric flow rate. Method 1 or 1A of 40 CFR part 60, appendix A–1. Sampling sites must be located at the outlet of the APCD and prior to any releases to the atmosphere for all affected sources. You may use Method 2A, 2C, 2D, or 2F of 40 CFR part 60, appendix A–1, or Method 2G of 40 CFR part 60, appendix A–2, as appropriate, as an alternative to using Method 2 of 40 CFR part 60, appendix A–1. VerDate Sep<11>2014 16:01 Oct 31, 2019 Jkt 250001 PO 00000 Method 2 of 40 CFR part 60, appendix A–1. Frm 00013 Fmt 4700 Sfmt 4700 E:\FR\FM\01NOR1.SGM 01NOR1 58612 Federal Register / Vol. 84, No. 212 / Friday, November 1, 2019 / Rules and Regulations TABLE 4 TO SUBPART KKKKK OF PART 63—REQUIREMENTS FOR PERFORMANCE TESTS—Continued As stated in § 63.8595, you must conduct each performance test in the following table that applies to you: For each . . . You must . . . Using . . . According to the following requirements . . . c. Conduct gas molecular weight analysis. Method 3 of 40 CFR part 60, appendix A–2. You may use Method 3A or 3B of 40 CFR part 60, appendix A–2, as appropriate, as an alternative to using Method 3 of 40 CFR part 60, appendix A–2. ANSI/ASME PTC 19.10–1981 (incorporated by reference, see § 63.14) may be used as an alternative to the manual procedures (but not the instrumental procedures) in Methods 3A and 3B. d. Measure moisture content of the stack gas. e. Measure HF and HCl emissions. Method 4 of 40 CFR part 60, appendix A–3. i. Method 26A of 40 CFR part 60, appendix A–8; or ii. Method 320 of appendix A of this part. f. Measure PM emissions .. g. Measure Hg emissions 2. Glaze spray operation ..... 3. Spray dryer or floor tile press dryer. VerDate Sep<11>2014 16:01 Oct 31, 2019 i. Method 5 of 40 CFR part 60, appendix A–3; or ii. Method 29 of 40 CFR part 60, appendix A–8. Method 29 of 40 CFR part 60, appendix A–8. h. Measure dioxin/furan emissions. a. Select locations of sampling ports and the number of traverse points. b. Determine velocities and volumetric flow rate. Method 23 of 40 CFR part 60, appendix A–7. Method 1 or 1A of 40 CFR part 60, appendix A–1. c. Conduct gas molecular weight analysis. Method 3 of 40 CFR part 60, appendix A–2. d. Measure moisture content of the stack gas. e. Measure PM emissions Method 4 of 40 CFR part 60, appendix A–3. Method 5 of 40 CFR part 60, appendix A–3. Method 29 of 40 CFR part 60, appendix A–8. f. Measure Hg emissions (tile glaze spray operations only). a. Select locations of sampling ports and the number of traverse points. b. Determine velocities and volumetric flow rate. Jkt 250001 PO 00000 Method 2 of 40 CFR part 60, appendix A–1. Method 1 or 1A of 40 CFR part 60, appendix A–1. Method 2 of 40 CFR part 60, appendix A–1. Frm 00014 Fmt 4700 Sfmt 4700 You may use Method 26 of 40 CFR part 60, appendix A–8, as an alternative to using Method 26A of 40 CFR part 60, appendix A–8, when no acid PM (e.g., HF or HCl dissolved in water droplets emitted by sources controlled by a WS) is present. ASTM D6735–01 (Reapproved 2009) (incorporated by reference, see § 63.14) may be used as an alternative to Methods 26 and 26A. When using Method 320 of appendix A of this part, you must follow the analyte spiking procedures of section 13 of Method 320 of appendix A of this part, unless you can demonstrate that the complete spiking procedure has been conducted at a similar source. ASTM D6348–03 (Reapproved 2010) (incorporated by reference, see § 63.14) may be used as an alternative to Method 320 if the test plan preparation and implementation in Annexes A1–A8 are mandatory and the %R in Annex A5 is determined for each target analyte. ASTM D6784–02 (Reapproved 2008) (incorporated by reference, see § 63.14) may be used as an alternative to Method 29 (portion for Hg only). Sampling sites must be located at the outlet of the APCD and prior to any releases to the atmosphere for all affected sources. You may use Method 2A, 2C, 2D, or 2F of 40 CFR part 60, appendix A–1, or Method 2G of 40 CFR part 60, appendix A–2, as appropriate, as an alternative to using Method 2 of 40 CFR part 60, appendix A–1. You may use Method 3A or 3B of 40 CFR part 60, appendix A–2, as appropriate, as an alternative to using Method 3 of 40 CFR part 60, appendix A–2. ANSI/ASME PTC 19.10–1981 (incorporated by reference, see § 63.14) may be used as an alternative to the manual procedures (but not the instrumental procedures) in Methods 3A and 3B. ASTM D6784–02 (Reapproved 2008) (incorporated by reference, see § 63.14) may be used as an alternative to Method 29 (portion for Hg only). Sampling sites must be located at the outlet of the APCD and prior to any releases to the atmosphere for all affected sources. You may use Method 2A, 2C, 2D, or 2F of 40 CFR part 60, appendix A–1, or Method 2G of 40 CFR part 60, appendix A–2, as appropriate, as an alternative to using Method 2 of 40 CFR part 60, appendix A–1. E:\FR\FM\01NOR1.SGM 01NOR1 Federal Register / Vol. 84, No. 212 / Friday, November 1, 2019 / Rules and Regulations 58613 TABLE 4 TO SUBPART KKKKK OF PART 63—REQUIREMENTS FOR PERFORMANCE TESTS—Continued As stated in § 63.8595, you must conduct each performance test in the following table that applies to you: For each . . . You must . . . Using . . . According to the following requirements . . . c. Conduct gas molecular weight analysis. Method 3 of 40 CFR part 60, appendix A–2. You may use Method 3A or 3B of 40 CFR part 60, appendix A–2, as appropriate, as an alternative to using Method 3 of 40 CFR part 60, appendix A–2. ANSI/ASME PTC 19.10–1981 (incorporated by reference, see § 63.14) may be used as an alternative to the manual procedures (but not the instrumental procedures) in Methods 3A and 3B. d. Measure moisture content of the stack gas. e. Measure dioxin/furan emissions. a. Establish the operating limit(s) for kiln process rate if the total facility maximum potential HClequivalent emissions are greater than the HClequivalent limit in Table 1 to this subpart. b. Establish the operating limit for kiln operating temperature. Method 4 of 40 CFR part 60, appendix A–3. Method 23 of 40 CFR part 60, appendix A–7. HCl-equivalent limit in Table 1 to this subpart and emissions and production data from the HF/HCl/Cl2 performance test. 5. Tunnel or roller kiln that is complying with PM and/or Hg production-based emission limits. Determine the production rate during each PM/Hg test run in order to determine compliance with PM and/or Hg production-based emission limits. 6. Tunnel or roller kiln equipped with a DIFF or DLS/FF. Establish the operating limit for the lime feeder setting. Production data collected during the PM/Hg performance tests (e.g., the number of ceramic pieces and weight per piece in the kiln during a test run divided by the amount of time to fire a piece). Data from the lime feeder during the HF/HCl performance test. 7. Tunnel or roller kiln equipped with a WS. a. Establish the operating limit for the average scrubber liquid pH. Data from the pH measurement device during the HF/HCl performance test. b. Establish the operating limit for the average scrubber liquid flow rate. Data from the flow rate measurement device during the HF/HCl and PM performance tests. 4. Tunnel or roller kiln with no add-on control. VerDate Sep<11>2014 16:01 Oct 31, 2019 Jkt 250001 PO 00000 i. Data from the kiln operating temperature measurement device during the dioxin/furan performance test. Frm 00015 Fmt 4700 Sfmt 4700 Using the procedures in § 63.8595(g)(1), you must determine the maximum process rate(s) for your kiln(s) that would ensure total facility maximum potential HCl-equivalent emissions remain at or below the HCl-equivalent limit in Table 1 to this subpart. The maximum process rate(s) would become your sitespecific process rate operating limit(s). (1) You must continuously measure the kiln operating temperature during three 4-hour test runs and, from a 12-hour block of time consisting of 1-hour increments, calculate the following two values: (a) The standard deviation of the 12 1-hour temperature measurements (refer to Note 1). (b) 1 percent of the 12-hour block average. (2) You must decide which of the two values would provide the greatest variability (i.e., the highest value), and then add this value to the 12-hour block average measured during the compliance testing. The result is the maximum temperature at which your kiln may operate during normal operations. You must measure and record the production rate, on a ton of throughput processed basis, of the affected kiln for each of the three test runs. For continuous lime injection systems, you must ensure that lime in the feed hopper or silo and to the APCD is free-flowing at all times during the performance test and record the feeder setting, on a per ton of throughput basis, for the three test runs. If the feed rate setting varies during the three test runs, determine and record the average feed rate from the three test runs. The average of the three test runs establishes your minimum site-specific feed rate operating limit. You must continuously measure the scrubber liquid pH, determine and record the block average pH values for the three test runs, and determine and record the 3-hour block average of the recorded pH measurements for the three test runs. The average of the three test runs establishes your minimum site-specific liquid pH operating limit. You must continuously measure the scrubber liquid flow rate, determine and record the block average flow rate values for the three test runs, and determine and record the 3-hour block average of the recorded flow rate measurements for the three test runs. The average of the three test runs establishes your minimum site-specific liquid flow rate operating level. If different average wet scrubber liquid flow rate values are measured during the HF/HCl and PM tests, the highest of the average values become your site-specific operating limit. E:\FR\FM\01NOR1.SGM 01NOR1 58614 Federal Register / Vol. 84, No. 212 / Friday, November 1, 2019 / Rules and Regulations TABLE 4 TO SUBPART KKKKK OF PART 63—REQUIREMENTS FOR PERFORMANCE TESTS—Continued As stated in § 63.8595, you must conduct each performance test in the following table that applies to you: For each . . . You must . . . Using . . . According to the following requirements . . . 8. Tunnel or roller kiln equipped with an ACI system. Establish the operating limit for the average carbon flow rate. Data from the carbon flow rate measurement conducted during the Hg and dioxin/furan performance tests. 9. Tunnel or roller kiln intending to comply with dioxin/furan emission limit without an ACI system. a. Establish the operating limit for kiln operating temperature. i. Data from the kiln operating temperature measurement device during the dioxin/furan performance test. 10. Glaze spray operation equipped with a WS. a. Establish the operating limit for the average scrubber pressure drop. Data from the pressure drop measurement device during the PM performance test. b. Establish the operating limit for the average scrubber liquid flow rate. Data from the flow rate measurement device during the PM performance test. 11. Spray dryer .................... Establish the operating limit for operating temperature. Data from the temperature measurement device during the dioxin/furan performance test. 12. Floor tile press dryer ..... Establish the operating limit for operating temperature. Data from the temperature measurement device during the dioxin/furan performance test. You must measure the carbon flow rate during each test run, determine and record the block average carbon flow rate values for the three test runs, and determine and record the 3-hour block average of the recorded carbon flow rate measurements for the three test runs. The average of the three test runs establishes your minimum site-specific activated carbon flow rate operating limit. (1) You must continuously measure the kiln operating temperature during three 4-hour test runs and, from a 12-hour block of time consisting of 1-hour increments, calculate the following two values: (a) The standard deviation of the 12 1-hour temperature measurements (refer to Note 1). (b) 1 percent of the 12-hour block average (2) You must decide which of the two values would provide the greatest variability (i.e., the highest value), and then add this value to the 12-hour block average measured during the compliance testing. The result is the maximum temperature at which your kiln may operate during normal operations. You must continuously measure the scrubber pressure drop, determine and record the block average pressure drop values for the three test runs, and determine and record the 3-hour block average of the recorded pressure drop measurements for the three test runs. The average of the three test runs establishes your minimum site-specific pressure drop operating limit. You must continuously measure the scrubber liquid flow rate, determine and record the block average flow rate values for the three test runs, and determine and record the 3-hour block average of the recorded flow rate measurements for the three test runs. The average of the three test runs establishes your minimum site-specific liquid flow rate operating limit. You must continuously measure the operating temperature, determine and record the block average temperature values for the three test runs, and determine and record the 4-hour block average of the recorded temperature measurements for the three test runs. The average of the three test runs establishes your minimum site-specific operating limit. You must continuously measure the operating temperature, determine and record the block average temperature values for the three test runs, and determine and record the 4-hour block average of the recorded temperature measurements for the three test runs. The average of the three test runs establishes your maximum site-specific operating limit. Note 1: The standard deviation of the 12 1-hour temperature measurements is calculated as follows: VerDate Sep<11>2014 16:01 Oct 31, 2019 xi = each 1-hour temperature measurement m = mean of all 12 1-hour measurements N = 12 measurements Jkt 250001 PO 00000 Frm 00016 Fmt 4700 Sfmt 4700 11. Table 6 to subpart KKKKK is revised to read as follows: ■ E:\FR\FM\01NOR1.SGM 01NOR1 ER01NO19.007</GPH> Where: s = standard deviation Federal Register / Vol. 84, No. 212 / Friday, November 1, 2019 / Rules and Regulations 58615 TABLE 6 TO SUBPART KKKKK OF PART 63—INITIAL COMPLIANCE WITH EMISSION LIMITATIONS AND WORK PRACTICE STANDARDS As stated in § 63.8605, you must demonstrate initial compliance with each emission limitation and work practice standard that applies to you according to the following table: For each . . . For the following . . . You have demonstrated initial compliance if . . . 1. Collection of all tunnel or roller kilns at the facility. a. HF, HCl, and Cl2 emissions must not exceed 62 kg/hr (140 lb/hr) HCl equivalent. 2. Existing floor tile roller kiln .......... a. PM emissions must not exceed 0.063 kg/Mg (0.13 lb/ton) of fired product. i. You measure HF and HCl emissions for each kiln using Method 26 or 26A of 40 CFR part 60, appendix A–8 or its alternative, ASTM D6735–01 (Reapproved 2009) (incorporated by reference, see § 63.14); or Method 320 of appendix A of this part or its alternative, ASTM D6348–03 (Reapproved 2010) (incorporated by reference, see § 63.14); and ii. You calculate the HCl-equivalent emissions for HF for each kiln using Equation 4 to this subpart; and iii. You sum the HCl-equivalent values for all kilns at the facility using Equation 5 to this subpart; and iv. The facility total HCl-equivalent does not exceed 62 kg/hr (140 lb/ hr). i. The PM emissions measured using Method 5 of 40 CFR part 60, appendix A–3 or Method 29 of 40 CFR part 60, appendix A–8, over the period of the initial performance test, according to the calculations in § 63.8595(f)(1), do not exceed 0.063 kg/Mg (0.13 lb/ ton) of fired product; and ii. You establish and have a record of the applicable operating limits listed in Table 2 to this subpart over the period of the initial performance test during which PM emissions did not exceed 0.063 kg/ Mg (0.13 lb/ton) of fired product. i. The Hg emissions measured using Method 29 of 40 CFR part 60, appendix A–8 or its alternative, ASTM D6784–02 (Reapproved 2008) (incorporated by reference, see § 63.14), over the period of the initial performance test, do not exceed 6.3 E–05 kg/Mg (1.3 E– 04 lb/ton) of fired product; and ii. You establish and have a record of the operating limits listed in Table 2 to this subpart over the period of the initial performance test during which Hg emissions did not exceed 6.3 E–05 kg/Mg (1.3 E–04 lb/ton) of fired product. i. The dioxin/furan emissions measured using Method 23 of 40 CFR part 60, appendix A–7, over the period of the initial performance test, do not exceed 2.8 ng/kg of fired product; and ii. You establish and have a record of the operating limits listed in Table 2 to this subpart over the period of the initial performance test during which dioxin/furan emissions did not exceed 2.8 ng/kg of fired product. i. The PM emissions measured using Method 5 of 40 CFR part 60, appendix A–3 or Method 29 of 40 CFR part 60, appendix A–8, over the period of the initial performance test, according to the calculations in § 63.8595(f)(1), do not exceed 0.19 kg/Mg (0.37 lb/ton) of fired product; and ii. You establish and have a record of the operating limits listed in Table 2 to this subpart over the period of the initial performance test during which PM emissions did not exceed 0.19 kg/Mg (0.37 lb/ton) of fired product. i. The Hg emissions measured using Method 29 of 40 CFR part 60, appendix A–8 or its alternative, ASTM D6784–02 (Reapproved 2008) (incorporated by reference, see § 63.14), over the period of the initial performance test, do not exceed 1.1 E–04 kg/Mg (2.1 E– 04 lb/ton) of fired product; and ii. You establish and have a record of the operating limits listed in Table 2 to this subpart over the period of the initial performance test during which Hg emissions did not exceed 1.1 E–04 kg/Mg (2.1 E–04 lb/ton) of fired product. i. The dioxin/furan emissions measured using Method 23 of 40 CFR part 60, appendix A–7, over the period of the initial performance test, do not exceed 0.22 ng/kg of fired product; and ii. You establish and have a record of the operating limits listed in Table 2 to this subpart over the period of the initial performance test during which dioxin/furan emissions did not exceed 0.22 ng/kg of fired product. i. The PM emissions measured using Method 5 of 40 CFR part 60, appendix A–3 or Method 29 of 40 CFR part 60, appendix A–8, over the period of the initial performance test, according to the calculations in § 63.8595(f)(1), do not exceed 0.17 kg/Mg (0.34 lb/ton) of greenware fired; and b. Hg emissions must not exceed 6.3 E–05 kg/Mg (1.3 E–04 lb/ ton) of fired product. c. Dioxin/furan emissions must not exceed 2.8 ng/kg of fired product. 3. Existing wall tile roller kiln ........... a. PM emissions must not exceed 0.19 kg/Mg (0.37 lb/ton) of fired product. b. Hg emissions must not exceed 1.1 E–04 kg/Mg (2.1 E–04 lb/ ton) of fired product. c. Dioxin/furan emissions must not exceed 0.22 ng/kg of fired product. 4. Existing first-fire sanitaryware tunnel kiln. VerDate Sep<11>2014 16:01 Oct 31, 2019 a. PM emissions must not exceed 0.17 kg/Mg (0.34 lb/ton) of greenware fired. Jkt 250001 PO 00000 Frm 00017 Fmt 4700 Sfmt 4700 E:\FR\FM\01NOR1.SGM 01NOR1 58616 Federal Register / Vol. 84, No. 212 / Friday, November 1, 2019 / Rules and Regulations TABLE 6 TO SUBPART KKKKK OF PART 63—INITIAL COMPLIANCE WITH EMISSION LIMITATIONS AND WORK PRACTICE STANDARDS—Continued As stated in § 63.8605, you must demonstrate initial compliance with each emission limitation and work practice standard that applies to you according to the following table: For each . . . For the following . . . 5. Existing tile glaze line with glaze spraying. 6. Existing sanitaryware manual glaze application. 7. Existing sanitaryware spray machine glaze application. 8. Existing sanitaryware robot glaze application. 9. Existing floor tile spray dryer ...... VerDate Sep<11>2014 16:01 Oct 31, 2019 You have demonstrated initial compliance if . . . ii. You establish and have a record of the operating limits listed in Table 2 to this subpart over the period of the initial performance test during which PM emissions did not exceed 0.17 kg/Mg (0.34 lb/ton) of greenware fired. b. Hg emissions must not exceed i. The Hg emissions measured using Method 29 of 40 CFR part 60, 1.3 E–04 kg/Mg (2.6 E–04 lb/ appendix A–8 or its alternative, ASTM D6784–02 (Reapproved ton) of greenware fired. 2008) (incorporated by reference, see § 63.14), over the period of the initial performance test, do not exceed 1.3 E–04 kg/Mg (2.6 E– 04 lb/ton) of greenware fired; and ii. You establish and have a record of the operating limits listed in Table 2 to this subpart over the period of the initial performance test during which Hg emissions did not exceed 1.3 E–04 kg/Mg (2.6 E–04 lb/ton) of greenware fired. c. Dioxin/furan emissions must not i. The dioxin/furan emissions measured using Method 23 of 40 CFR exceed 3.3 ng/kg of greenware part 60, appendix A–7, over the period of the initial performance fired. test, do not exceed 3.3 ng/kg of greenware fired; and ii. You establish and have a record of the operating limits listed in Table 2 to this subpart over the period of the initial performance test during which dioxin/furan emissions did not exceed 3.3 ng/kg of greenware fired. a. PM emissions must not exceed i. The PM emissions measured using Method 5 of 40 CFR part 60, 0.93 kg/Mg (1.9 lb/ton) of firstappendix A–3, over the period of the initial performance test, acfire glaze sprayed (dry weight cording to the calculations in § 63.8595(f)(2), do not exceed 0.93 basis). kg/Mg (1.9 lb/ton) of first-fire glaze sprayed (dry weight basis); and ii. You establish and have a record of the operating limits listed in Table 2 to this subpart over the period of the initial performance test during which PM emissions did not exceed 0.93 kg/Mg (1.9 lb/ ton) of first-fire glaze sprayed (dry weight basis). b. Hg emissions must not exceed i. The Hg emissions measured using Method 29 of 40 CFR part 60, 8.0 E–05 kg/Mg (1.6 E–04 lb/ appendix A–8 or its alternative, ASTM D6784–02 (Reapproved ton) of first-fire glaze sprayed 2008) (incorporated by reference, see § 63.14), over the period of (dry weight basis). the initial performance test, do not exceed 8.0 E–05 kg/Mg (1.6 E– 04 lb/ton) of first-fire glaze sprayed (dry weight basis); and ii. You establish and have a record of the operating limits listed in Table 2 to this subpart over the period of the initial performance test during which Hg emissions did not exceed 8.0 E–05 kg/Mg (1.6 E–04 lb/ton) of first-fire glaze sprayed (dry weight basis). a. PM emissions must not exceed i. The PM emissions measured using Method 5 of 40 CFR part 60, 18 kg/Mg (35 lb/ton) of first-fire appendix A–3, over the period of the initial performance test, acglaze sprayed (dry weight basis). cording to the calculations in § 63.8595(f)(2), do not exceed 18 kg/ Mg (35 lb/ton) of first-fire glaze sprayed (dry weight basis); and ii. You establish and have a record of the operating limits listed in Table 2 to this subpart over the period of the initial performance test during which PM emissions did not exceed 18 kg/Mg (35 lb/ ton) of first-fire glaze sprayed (dry weight basis). a. PM emissions must not exceed i. The PM emissions measured using Method 5 of 40 CFR part 60, 6.2 kg/Mg (13 lb/ton) of first-fire appendix A–3, over the period of the initial performance test, acglaze sprayed (dry weight basis). cording to the calculations in § 63.8595(f)(2), do not exceed 6.2 kg/ Mg (13 lb/ton) of first-fire glaze sprayed (dry weight basis); and ii. You establish and have a record of the operating limits listed in Table 2 to this subpart over the period of the initial performance test during which PM emissions did not exceed 6.2 kg/Mg (13 lb/ ton) of first-fire glaze sprayed (dry weight basis). a. PM emissions must not exceed i. The PM emissions measured using Method 5 of 40 CFR part 60, 4.5 kg/Mg (8.9 lb/ton) of first-fire appendix A–3, over the period of the initial performance test, acglaze sprayed (dry weight basis). cording to the calculations in § 63.8595(f)(2), do not exceed 4.5 kg/ Mg (8.9 lb/ton) of first-fire glaze sprayed (dry weight basis); and ii. You establish and have a record of the operating limits listed in Table 2 to this subpart over the period of the initial performance test during which PM emissions did not exceed 4.5 kg/Mg (8.9 lb/ ton) of first-fire glaze sprayed (dry weight basis). a. Dioxin/furan emissions must not i. The dioxin/furan emissions measured using Method 23 of 40 CFR exceed 19 ng/kg of throughput part 60, appendix A–7, over the period of the initial performance processed. test, do not exceed 19 ng/kg of throughput processed; and ii. You establish and have a record of the operating limits listed in Table 2 to this subpart over the period of the initial performance test during which dioxin/furan emissions did not exceed 19 ng/kg of throughput processed. Jkt 250001 PO 00000 Frm 00018 Fmt 4700 Sfmt 4700 E:\FR\FM\01NOR1.SGM 01NOR1 Federal Register / Vol. 84, No. 212 / Friday, November 1, 2019 / Rules and Regulations 58617 TABLE 6 TO SUBPART KKKKK OF PART 63—INITIAL COMPLIANCE WITH EMISSION LIMITATIONS AND WORK PRACTICE STANDARDS—Continued As stated in § 63.8605, you must demonstrate initial compliance with each emission limitation and work practice standard that applies to you according to the following table: For each . . . For the following . . . You have demonstrated initial compliance if . . . 10. Existing wall tile spray dryer ..... a. Dioxin/furan emissions must not exceed 0.058 ng/kg of throughput processed. 11. Existing floor tile press dryer .... a. Dioxin/furan emissions must not exceed 0.024 ng/kg of throughput processed. 12. New or reconstructed floor tile roller kiln. a. PM emissions must not exceed 0.019 kg/Mg (0.037 lb/ton) of fired product. i. The dioxin/furan emissions measured using Method 23 of 40 CFR part 60, appendix A–7, over the period of the initial performance test, do not exceed 0.058 ng/kg of throughput processed; and ii. You establish and have a record of the operating limits listed in Table 2 to this subpart over the period of the initial performance test during which dioxin/furan emissions did not exceed 0.058 ng/ kg of throughput processed. i. The dioxin/furan emissions measured using Method 23 of 40 CFR part 60, appendix A–7, over the period of the initial performance test, do not exceed 0.024 ng/kg of throughput processed; and ii. You establish and have a record of the operating limits listed in Table 2 to this subpart over the period of the initial performance test during which dioxin/furan emissions did not exceed 0.024 ng/ kg of throughput processed. i. The PM emissions measured using Method 5 of 40 CFR part 60, appendix A–3 or Method 29 of 40 CFR part 60, appendix A–8, over the period of the initial performance test, according to the calculations in § 63.8595(f)(1), do not exceed 0.019 kg/Mg (0.037 lb/ ton) of fired product; and ii. You establish and have a record of the operating limits listed in Table 2 to this subpart over the period of the initial performance test during which PM emissions did not exceed 0.019 kg/Mg (0.037 lb/ton) of fired product. i. The Hg emissions measured using Method 29 of 40 CFR part 60, appendix A–8 or its alternative, ASTM D6784–02 (Reapproved 2008) (incorporated by reference, see § 63.14), over the period of the initial performance test, do not exceed 2.0 E–05 kg/Mg (3.9 E– 05 lb/ton) of fired product; and ii. You establish and have a record of the operating limits listed in Table 2 to this subpart over the period of the initial performance test during which Hg emissions did not exceed 2.0 E–05 kg/Mg (3.9 E–05 lb/ton) of fired product. i. The dioxin/furan emissions measured using Method 23 of 40 CFR part 60, appendix A–7, over the period of the initial performance test, do not exceed 1.3 ng/kg of fired product; and ii. You establish and have a record of the operating limits listed in Table 2 to this subpart over the period of the initial performance test during which dioxin/furan emissions did not exceed 1.3 ng/kg of fired product. i. The PM emissions measured using Method 5 of 40 CFR part 60, appendix A–3 or Method 29 of 40 CFR part 60, appendix A–8, over the period of the initial performance test, according to the calculations in § 63.8595(f)(1), do not exceed 0.19 kg/Mg (0.37 lb/ton) of fired product; and ii. You establish and have a record of the operating limits listed in Table 2 to this subpart over the period of the initial performance test during which PM emissions did not exceed 0.19 kg/Mg (0.37 lb/ton) of fired product. i. The Hg emissions measured using Method 29 of 40 CFR part 60, appendix A–8 or its alternative, ASTM D6784–02 (Reapproved 2008) (incorporated by reference, see § 63.14), over the period of the initial performance test, do not exceed 1.1 E–04 kg/Mg (2.1 E– 04 lb/ton) of fired product; and ii. You establish and have a record of the operating limits listed in Table 2 to this subpart over the period of the initial performance test during which Hg emissions did not exceed 1.1 E–04 kg/Mg (2.1 E–04 lb/ton) of fired product. i. The dioxin/furan emissions measured using Method 23 of 40 CFR part 60, appendix A–7, over the period of the initial performance test, do not exceed 0.22 ng/kg of fired product; and ii. You establish and have a record of the operating limits listed in Table 2 to this subpart over the period of the initial performance test during which dioxin/furan emissions did not exceed 0.22 ng/kg of fired product. b. Hg emissions must not exceed 2.0 E–05 kg/Mg (3.9 E–05 lb/ ton) of fired product. c. Dioxin/furan emissions must not exceed 1.3 ng/kg of fired product. 13. New or reconstructed wall tile roller kiln. a. PM emissions must not exceed 0.19 kg/Mg (0.37 lb/ton) of fired product. b. Hg emissions must not exceed 1.1 E–04 kg/Mg (2.1 E–04 lb/ ton) of fired product. c. Dioxin/furan emissions must not exceed 0.22 ng/kg of fired product. VerDate Sep<11>2014 16:01 Oct 31, 2019 Jkt 250001 PO 00000 Frm 00019 Fmt 4700 Sfmt 4700 E:\FR\FM\01NOR1.SGM 01NOR1 58618 Federal Register / Vol. 84, No. 212 / Friday, November 1, 2019 / Rules and Regulations TABLE 6 TO SUBPART KKKKK OF PART 63—INITIAL COMPLIANCE WITH EMISSION LIMITATIONS AND WORK PRACTICE STANDARDS—Continued As stated in § 63.8605, you must demonstrate initial compliance with each emission limitation and work practice standard that applies to you according to the following table: For each . . . For the following . . . 14. New or reconstructed first-fire sanitaryware tunnel kiln. a. PM emissions must not exceed 0.048 kg/Mg (0.095 lb/ton) of greenware fired. 15. New or reconstructed tile glaze line with glaze spraying. 16. New or reconstructed sanitaryware manual glaze application. 17. New or reconstructed sanitaryware spray machine glaze application. 18. New or reconstructed sanitaryware robot glaze application. VerDate Sep<11>2014 16:01 Oct 31, 2019 You have demonstrated initial compliance if . . . i. The PM emissions measured using Method 5 of 40 CFR part 60, appendix A–3 or Method 29 of 40 CFR part 60, appendix A–8, over the period of the initial performance test, according to the calculations in § 63.8595(f)(1), do not exceed 0.048 kg/Mg (0.095 lb/ ton) of greenware fired; and ii. You establish and have a record of the operating limits listed in Table 2 to this subpart over the period of the initial performance test during which PM emissions did not exceed 0.048 kg/Mg (0.095 lb/ton) of greenware fired. b. Hg emissions must not exceed i. The Hg emissions measured using Method 29 of 40 CFR part 60, 6.1 E–05 kg/Mg (1.3 E–04 lb/ appendix A–8 or its alternative, ASTM D6784–02 (Reapproved ton) of greenware fired. 2008) (incorporated by reference, see § 63.14), over the period of the initial performance test, do not exceed 6.1 E–05 kg/Mg (1.3 E– 04 lb/ton) of greenware fired; and ii. You establish and have a record of the operating limits listed in Table 2 to this subpart over the period of the initial performance test during which Hg emissions did not exceed 6.1 E–05 kg/Mg (1.3 E–04 lb/ton) of greenware fired. c. Dioxin/furan emissions must not i. The dioxin/furan emissions measured using Method 23 of 40 CFR exceed 0.99 ng/kg of greenware part 60, appendix A–7, over the period of the initial performance fired. test, do not exceed 0.99 ng/kg of greenware fired; and ii. You establish and have a record of the operating limits listed in Table 2 to this subpart over the period of the initial performance test during which dioxin/furan emissions did not exceed 0.99 ng/kg of greenware fired. a. PM emissions must not exceed i. The PM emissions measured using Method 5 of 40 CFR part 60, 0.31 kg/Mg (0.61 lb/ton) of firstappendix A–3, over the period of the initial performance test, acfire glaze sprayed (dry weight cording to the calculations in § 63.8595(f)(2), do not exceed 0.31 basis). kg/Mg (0.61 lb/ton) of first-fire glaze sprayed (dry weight basis); and ii. You establish and have a record of the operating limits listed in Table 2 to this subpart over the period of the initial performance test during which PM emissions did not exceed 0.31 kg/Mg (0.61 lb/ton) of first-fire glaze sprayed (dry weight basis). b. Hg emissions must not exceed i. The Hg emissions measured using Method 29 of 40 CFR part 60, 8.0 E–05 kg/Mg (1.6 E–04 lb/ appendix A–8 or its alternative, ASTM D6784–02 (Reapproved ton) of first-fire glaze sprayed 2008) (incorporated by reference, see § 63.14), over the period of (dry weight basis). the initial performance test, do not exceed 8.0 E–05 kg/Mg (1.6 E– 04 lb/ton) of first-fire glaze sprayed (dry weight basis); and ii. You establish and have a record of the operating limits listed in Table 2 to this subpart over the period of the initial performance test during which Hg emissions did not exceed 8.0 E–05 kg/Mg (1.6 E–04 lb/ton) of first-fire glaze sprayed (dry weight basis). a. PM emissions must not exceed i. The PM emissions measured using Method 5 of 40 CFR part 60, 2.0 kg/Mg (3.9 lb/ton) of first-fire appendix A–3, over the period of the initial performance test, acglaze sprayed (dry weight basis). cording to the calculations in § 63.8595(f)(2), do not exceed 2.0 kg/ Mg (3.9 lb/ton) of first-fire glaze sprayed (dry weight basis); and ii. You establish and have a record of the operating limits listed in Table 2 to this subpart over the period of the initial performance test during which PM emissions did not exceed 2.0 kg/Mg (3.9 lb/ ton) of first-fire glaze sprayed (dry weight basis). a. PM emissions must not exceed i. The PM emissions measured using Method 5 of 40 CFR part 60, 1.6 kg/Mg (3.2 lb/ton) of first-fire appendix A–3, over the period of the initial performance test, acglaze sprayed (dry weight basis). cording to the calculations in § 63.8595(f)(2), do not exceed 1.6 kg/ Mg (3.2 lb/ton) of first-fire glaze sprayed (dry weight basis); and ii. You establish and have a record of the operating limits listed in Table 2 to this subpart over the period of the initial performance test during which PM emissions did not exceed 1.6 kg/Mg (3.2 lb/ ton) of first-fire glaze sprayed (dry weight basis). a. PM emissions must not exceed i. The PM emissions measured using Method 5 of 40 CFR part 60, 1.2 kg/Mg (2.3 lb/ton) of first-fire appendix A–3, over the period of the initial performance test, acglaze sprayed (dry weight basis). cording to the calculations in § 63.8595(f)(2), do not exceed 1.2 kg/ Mg (2.3 lb/ton) of first-fire glaze sprayed (dry weight basis); and ii. You establish and have a record of the operating limits listed in Table 2 to this subpart over the period of the initial performance test during which PM emissions did not exceed 1.2 kg/Mg (2.3 lb/ ton) of first-fire glaze sprayed (dry weight basis). Jkt 250001 PO 00000 Frm 00020 Fmt 4700 Sfmt 4700 E:\FR\FM\01NOR1.SGM 01NOR1 Federal Register / Vol. 84, No. 212 / Friday, November 1, 2019 / Rules and Regulations 58619 TABLE 6 TO SUBPART KKKKK OF PART 63—INITIAL COMPLIANCE WITH EMISSION LIMITATIONS AND WORK PRACTICE STANDARDS—Continued As stated in § 63.8605, you must demonstrate initial compliance with each emission limitation and work practice standard that applies to you according to the following table: For each . . . For the following . . . You have demonstrated initial compliance if . . . 19. New or reconstructed floor tile spray dryer. a. Dioxin/furan emissions must not exceed 0.071 ng/kg of throughput processed. 20. New or reconstructed wall tile spray dryer. a. Dioxin/furan emissions must not exceed 0.058 ng/kg of throughput processed. 21. New or reconstructed floor tile press dryer. a. Dioxin/furan emissions must not exceed 0.024 ng/kg of throughput processed. 22. Existing, new, or reconstructed sanitaryware shuttle kiln. a. Minimize HAP emissions ........... i. The dioxin/furan emissions measured using Method 23 of 40 CFR part 60, appendix A–7, over the period of the initial performance test, do not exceed 0.071 ng/kg of throughput processed; and ii. You establish and have a record of the operating limits listed in Table 2 to this subpart over the period of the initial performance test during which dioxin/furan emissions did not exceed 0.071 ng/ kg of throughput processed. i. The dioxin/furan emissions measured using Method 23 of 40 CFR part 60, appendix A–7, over the period of the initial performance test, do not exceed 0.058 ng/kg of throughput processed; and ii. You establish and have a record of the operating limits listed in Table 2 to this subpart over the period of the initial performance test during which dioxin/furan emissions did not exceed 0.058 ng/ kg of throughput processed. i. The dioxin/furan emissions measured using Method 23 of 40 CFR part 60, appendix A–7, over the period of the initial performance test, do not exceed 0.024 ng/kg of throughput processed; and ii. You establish and have a record of the operating limits listed in Table 2 to this subpart over the period of the initial performance test during which dioxin/furan emissions did not exceed 0.024 ng/ kg of throughput processed. i. Use natural gas, or equivalent, as the kiln fuel; and ii. Develop a designed firing time and temperature cycle for the sanitaryware shuttle kiln. You must either program the time and temperature cycle into your kiln or track each step on a log sheet; and iii. Label each sanitaryware shuttle kiln with the maximum load (in tons) of greenware that can be fired in the kiln during a single firing cycle; and iv. Develop maintenance procedures for each kiln that, at a minimum, specify the frequency of inspection and maintenance of temperature monitoring devices, controls that regulate air-to-fuel ratios, and controls that regulate firing cycles. 12. Table 7 to subpart KKKKK is revised to read as follows: ■ TABLE 7 TO SUBPART KKKKK OF PART 63—CONTINUOUS COMPLIANCE WITH EMISSION LIMITATIONS AND WORK PRACTICE STANDARDS As stated in § 63.8620, you must demonstrate continuous compliance with each emission limitation and work practice standard that applies to you according to the following table: For each . . . For the following . . . You must demonstrate continuous compliance by . . . Or by . . . 1. Tunnel or roller kiln equipped with a DIFF or DLS/FF. a. Each emission limit in Table 1 to this subpart and each operating limit in Item 1 of Table 2 to this subpart for kilns equipped with DIFF or DLS/FF. i. If you use a bag leak detection system, as prescribed in § 63.8450(e), initiating corrective action within 1 hour of a bag leak detection system alarm and completing corrective actions in accordance with your OM&M plan; operating and maintaining the fabric filter such that the alarm is not engaged for more than 5 percent of the total operating time in a 6-month block reporting period; in calculating this operating time fraction, if inspection of the fabric filter demonstrates that no corrective action is required, no alarm time is counted; if corrective action is required, each alarm is counted as a minimum of 1 hour; if you take longer than 1 hour to initiate corrective action, the alarm time is counted as the actual amount of time taken by you to initiate corrective action; and (1) Performing VE observations of the DIFF or DLS/FF stack at the frequency specified in § 63.8620(e) using Method 22 of 40 CFR part 60, appendix A–7; and maintaining no VE from the DIFF or DLS/FF stack; or (2) Maintaining your kiln operating temperature within the range of acceptable temperatures (i.e., temperature profile for each kiln and product; for any incidence where the kiln is operating outside of its acceptable temperature range (i.e., exceeds its temperature profile) for the product being fired, performing VE observations of the DIFF or DLS/FF stack as specified in § 63.8620(e) using Method 22 of 40 CFR part 60, appendix A–7; and observing no VE from the DIFF or DLS/FF stack. VerDate Sep<11>2014 16:01 Oct 31, 2019 Jkt 250001 PO 00000 Frm 00021 Fmt 4700 Sfmt 4700 E:\FR\FM\01NOR1.SGM 01NOR1 58620 Federal Register / Vol. 84, No. 212 / Friday, November 1, 2019 / Rules and Regulations TABLE 7 TO SUBPART KKKKK OF PART 63—CONTINUOUS COMPLIANCE WITH EMISSION LIMITATIONS AND WORK PRACTICE STANDARDS—Continued As stated in § 63.8620, you must demonstrate continuous compliance with each emission limitation and work practice standard that applies to you according to the following table: For each . . . For the following . . . 2. Tunnel or roller kiln equipped with a WS. a. Each emission limit in Table 1 to this subpart and each operating limit in Item 2 of Table 2 to this subpart for kilns equipped with WS. 3. Tunnel or roller kiln equipped with an ACI system. Each emission limit in Table 1 to this subpart and each operating limit in Item 3 of Table 2 to this subpart for kilns equipped with ACI system. 4. Tunnel or roller kiln intending to comply with dioxin/furan emission limit without an ACI system. Each emission limit in Table 1 to this subpart and each operating limit in Item 4 of Table 2 to this subpart for kilns intending to comply with dioxin/furan emission limit without an ACI system. a. Each emission limit in Table 1 to this subpart and each operating limit in Item 5 of Table 2 to this subpart for tunnel or roller kilns with no add-on control. 5. Tunnel or roller kiln with no add-on control. VerDate Sep<11>2014 16:01 Oct 31, 2019 Jkt 250001 You must demonstrate continuous compliance by . . . Or by . . . ii. Verifying that lime is free-flowing via a load cell, carrier gas/lime flow indicator, carrier gas pressure drop measurement system, or other system; recording all monitor or sensor output, and if lime is found not to be free flowing, promptly initiating and completing corrective actions in accordance with your OM&M plan; recording the feeder setting once each shift of operation to verify that the feeder setting is being maintained at or above the level established during the HF/HCl performance test in which compliance was demonstrated. i. Collecting the scrubber liquid pH data according to § 63.8600(a); reducing the scrubber liquid pH data to 3-hour block averages according to § 63.8600(a); maintaining the average scrubber liquid pH for each 3-hour block period at or above the average scrubber liquid pH established during the HF/HCl performance test in which compliance was demonstrated; and ii. Collecting the scrubber liquid flow rate data according to § 63.8600(a); reducing the scrubber liquid flow rate data to 3-hour block averages according to § 63.8600(a); maintaining the average scrubber liquid flow rate for each 3-hour block period at or above the highest average scrubber liquid flow rate established during the HF/HCl and PM performance tests in which compliance was demonstrated. Collecting the carbon flow rate data according to § 63.8600(a); reducing the carbon flow rate data to 3-hour block averages according to § 63.8600(a); maintaining the average carbon flow rate for each 3-hour block period at or above the highest average carbon flow rate established during the Hg and dioxin/furan performance tests in which compliance was demonstrated. Collecting the operating temperature data according to § 63.8600(a); and maintaining the operating temperature at or below the highest operating temperature established during the dioxin/furan performance test in which compliance was demonstrated. i. Performing VE observations of the stack at the frequency specified in § 63.8620(e) using Method 22 of 40 CFR part 60, appendix A–7; and maintaining no VE from the stack; and PO 00000 Frm 00022 Fmt 4700 Sfmt 4700 Collecting the operating temperature data according to § 63.8600(a); reducing the operating temperature data to a 12-hour block average; and maintaining the average operating temperature for each 12-hour block period at or below the highest operating temperature established during the dioxin/ furan performance test in which compliance was demonstrated. (1) Maintaining your kiln operating temperature within the range of acceptable temperatures (i.e., temperature profile established for each kiln and product for any incidence where the kiln is operating outside of its acceptable temperature range (i.e., exceeds its temperature profile) for the product being fired, performing VE observations of the DIFF or DLS/FF stack as specified in § 63.8620(e) using Method 22 of 40 CFR part 60, appendix A–7; and observing no VE from the DIFF or DLS/FF stack. E:\FR\FM\01NOR1.SGM 01NOR1 Federal Register / Vol. 84, No. 212 / Friday, November 1, 2019 / Rules and Regulations 58621 TABLE 7 TO SUBPART KKKKK OF PART 63—CONTINUOUS COMPLIANCE WITH EMISSION LIMITATIONS AND WORK PRACTICE STANDARDS—Continued As stated in § 63.8620, you must demonstrate continuous compliance with each emission limitation and work practice standard that applies to you according to the following table: For each . . . For the following . . . You must demonstrate continuous compliance by . . . Or by . . . ii. If your last calculated total facility maximum potential HCl-equivalent was not at or below the health-based standard in Table 1 to this subpart, collecting the kiln process rate data according to § 63.8600(a); reducing the kiln process rate data to 3-hour block averages according to § 63.8600(a); maintaining the average kiln process rate for each 3-hour block period at or below the kiln process rate determined according to § 63.8595(g)(1); and iii. Collecting the operating temperature data according to § 63.8600(a); and maintaining the operating temperature at or below the highest operating temperature established during the dioxin/furan performance test in which compliance was demonstrated. 6. Glaze spray operation equipped with a FF. Each emission limit in Table 1 to this subpart and each operating limit in Item 6 of Table 2 to this subpart for glaze spray operations equipped with a FF. 7. Glaze spray operation equipped with a WS. a. Each emission limit in Table 1 to this subpart and each operating limit in Item 7 of Table 2 to this subpart for kilns equipped with WS. 8. Glaze spray operation equipped with a water curtain. a. Each emission limit in Table 1 to this subpart and each operating limit in Item 8 of Table 2 to this subpart for kilns equipped with a water curtain. VerDate Sep<11>2014 16:01 Oct 31, 2019 Jkt 250001 If you use a bag leak detection system, initiating corrective action within 1 hour of a bag leak detection system alarm and completing corrective actions in accordance with your OM&M plan; operating and maintaining the fabric filter such that the alarm is not engaged for more than 5 percent of the total operating time in a 6-month block reporting period; in calculating this operating time fraction, if inspection of the fabric filter demonstrates that no corrective action is required, no alarm time is counted; if corrective action is required, each alarm is counted as a minimum of 1 hour; if you take longer than 1 hour to initiate corrective action, the alarm time is counted as the actual amount of time taken by you to initiate corrective action. i. Collecting the scrubber pressure drop data according to § 63.8600(a); reducing the scrubber pressure drop data to 3-hour block averages according to § 63.8600(a); maintaining the average scrubber pressure drop for each 3-hour block period at or above the average pressure drop established during the PM performance test in which compliance was demonstrated; and ii. Collecting the scrubber liquid flow rate data according to § 63.8600(a); reducing the scrubber liquid flow rate data to 3-hour block averages according to § 63.8600(a); maintaining the average scrubber liquid flow rate for each 3-hour block period at or above the average scrubber liquid flow rate established during the PM performance test in which compliance was demonstrated. i. Conducting daily inspections to verify the presence of water flow to the wet control system; and PO 00000 Frm 00023 Fmt 4700 Sfmt 4700 (1) Collecting the operating temperature data according to § 63.8600(a); reducing the operating temperature data to a 12-hour block average; and maintaining the average operating temperature for each 12-hour block period at or below the highest operating temperature established during the dioxin/ furan performance test in which compliance was demonstrated. Performing VE observations of the FF stack at the frequency specified in § 63.8620(e) using Method 22 of 40 CFR part 60, appendix A–7; and maintaining no VE from the FF stack. E:\FR\FM\01NOR1.SGM 01NOR1 58622 Federal Register / Vol. 84, No. 212 / Friday, November 1, 2019 / Rules and Regulations TABLE 7 TO SUBPART KKKKK OF PART 63—CONTINUOUS COMPLIANCE WITH EMISSION LIMITATIONS AND WORK PRACTICE STANDARDS—Continued As stated in § 63.8620, you must demonstrate continuous compliance with each emission limitation and work practice standard that applies to you according to the following table: For each . . . For the following . . . 9. Glaze spray operation equipped with baffles. 10. Spray dryer ............ Each emission limit in Table 1 to this subpart and each operating limit in Item 9 of Table 2 to this subpart for kilns equipped with baffles. Each emission limit in Table 1 to this subpart and each operating limit in Item 10 of Table 2 to this subpart for spray dryers. 11. Floor tile press dryer. Each emission limit in Table 1 to this subpart and each operating limit in Item 11 of Table 2 to this subpart for floor tile press dryers. 12. Sanitaryware shuttle kiln. a. Minimize HAP emissions. VerDate Sep<11>2014 16:01 Oct 31, 2019 Jkt 250001 You must demonstrate continuous compliance by . . . Or by . . . ii. Conducting annual inspections of the interior of the control equipment (if applicable) to determine the structural integrity and condition of the control equipment; and iii. Recording as deviations any observations of particulates or other impurities getting into the glaze that has been sprayed onto a piece of ware and completing corrective actions in accordance with your OM&M plan. Conducting an annual visual inspection of the baffles to confirm the baffles are in place. Collecting the operating temperature data according to § 63.8600(a); reducing the operating temperature data to 4-hour block averages according to § 63.8600(a); maintaining the average operating temperature for each 4-hour block period at or above the average operating temperature established during the dioxin/furan performance test in which compliance was demonstrated. Collecting the operating temperature data according to § 63.8600(a); reducing the operating temperature data to 4-hour block averages according to § 63.8600(a); maintaining the average operating temperature for each 4-hour block period at or below the average operating temperature established during the dioxin/furan performance test in which compliance was demonstrated. i. Maintaining records documenting your use of natural gas, or an equivalent fuel, as the kiln fuel at all times except during periods of natural gas curtailment or supply interruption; and ii. If you intend to use an alternative fuel, submitting a notification of alternative fuel use within 48 hours of the declaration of a period of natural gas curtailment or supply interruption, as defined in § 63.8665; and. iii. Submitting a report of alternative fuel use within 10 working days after terminating the use of the alternative fuel, as specified in § 63.8635(g); and iv. Using a designed firing time and temperature cycle for each sanitaryware shuttle kiln; and v. For each firing load, documenting the total tonnage of greenware placed in the kiln to ensure that it is not greater than the maximum load identified in Item 1.a.iii of Table 3 to this subpart; and vi. Following maintenance procedures for each kiln that, at a minimum, specify the frequency of inspection and maintenance of temperature monitoring devices, controls that regulate air-to-fuel ratios, and controls that regulate firing cycles; and PO 00000 Frm 00024 Fmt 4700 Sfmt 4700 E:\FR\FM\01NOR1.SGM 01NOR1 Federal Register / Vol. 84, No. 212 / Friday, November 1, 2019 / Rules and Regulations 58623 TABLE 7 TO SUBPART KKKKK OF PART 63—CONTINUOUS COMPLIANCE WITH EMISSION LIMITATIONS AND WORK PRACTICE STANDARDS—Continued As stated in § 63.8620, you must demonstrate continuous compliance with each emission limitation and work practice standard that applies to you according to the following table: For each . . . For the following . . . You must demonstrate continuous compliance by . . . Or by . . . vii. Developing and maintaining records for each sanitaryware shuttle kiln, as specified in § 63.8640. telephone number: (703) 305–7090; email address: RDFRNotices@epa.gov. SUPPLEMENTARY INFORMATION: [FR Doc. 2019–22812 Filed 10–31–19; 8:45 am] BILLING CODE 6560–50–P I. General Information ENVIRONMENTAL PROTECTION AGENCY 40 CFR Part 180 [EPA–HQ–OPP–2018–0047; FRL–10000–79] Isotianil; Pesticide Tolerances Environmental Protection Agency (EPA). ACTION: Final rule. AGENCY: This regulation establishes a tolerance for residues of isotianil in or on banana. Bayer CropScience requested this tolerance under the Federal Food, Drug, and Cosmetic Act (FFDCA). DATES: This regulation is effective November 1, 2019. Objections and requests for hearings must be received on or before December 31, 2019, and must be filed in accordance with the instructions provided in 40 CFR part 178 (see also Unit I.C. of the SUPPLEMENTARY INFORMATION). ADDRESSES: The docket for this action, identified by docket identification (ID) number EPA–HQ–OPP–2018–0047, is available at https://www.regulations.gov or at the Office of Pesticide Programs Regulatory Public Docket (OPP Docket) in the Environmental Protection Agency Docket Center (EPA/DC), West William Jefferson Clinton Bldg., Rm. 3334, 1301 Constitution Ave. NW, Washington, DC 20460–0001. The Public Reading Room is open from 8:30 a.m. to 4:30 p.m., Monday through Friday, excluding legal holidays. The telephone number for the Public Reading Room is (202) 566–1744, and the telephone number for the OPP Docket is (703) 305–5805. Please review the visitor instructions and additional information about the docket available at https://www.epa.gov/dockets. FOR FURTHER INFORMATION CONTACT: Michael L. Goodis, P.E., Registration Division (7505P), Office of Pesticide Programs, Environmental Protection Agency, 1200 Pennsylvania Ave. NW, Washington, DC 20460–0001; main SUMMARY: VerDate Sep<11>2014 16:01 Oct 31, 2019 Jkt 250001 A. Does this action apply to me? You may be potentially affected by this action if you are an agricultural producer, food manufacturer, or pesticide manufacturer. The following list of North American Industrial Classification System (NAICS) codes is not intended to be exhaustive, but rather provides a guide to help readers determine whether this document applies to them. Potentially affected entities may include: • Crop production (NAICS code 111). • Animal production (NAICS code 112). • Food manufacturing (NAICS code 311). • Pesticide manufacturing (NAICS code 32532). B. How can I get electronic access to other related information? You may access a frequently updated electronic version of EPA’s tolerance regulations at 40 CFR part 180 through the Government Publishing Office’s eCFR site at https://www.ecfr.gov/cgi-bin/ text-idx?&c=ecfr&tpl=/ecfrbrowse/ Title40/40tab_02.tpl. To access the OCSPP test guidelines referenced in this document electronically, please go to https://www.epa.gov/ocspp and select ‘‘Test Methods and Guidelines.’’ C. How can I file an objection or hearing request? Under FFDCA section 408(g), 21 U.S.C. 346a, any person may file an objection to any aspect of this regulation and may also request a hearing on those objections. You must file your objection or request a hearing on this regulation in accordance with the instructions provided in 40 CFR part 178. To ensure proper receipt by EPA, you must identify docket ID number EPA–HQ– OPP–2018–0047 in the subject line on the first page of your submission. All objections and requests for a hearing must be in writing, and must be received by the Hearing Clerk on or PO 00000 Frm 00025 Fmt 4700 Sfmt 4700 before December 31, 2019. Addresses for mail and hand delivery of objections and hearing requests are provided in 40 CFR 178.25(b). In addition to filing an objection or hearing request with the Hearing Clerk as described in 40 CFR part 178, please submit a copy of the filing (excluding any Confidential Business Information (CBI)) for inclusion in the public docket. Information not marked confidential pursuant to 40 CFR part 2 may be disclosed publicly by EPA without prior notice. Submit the non-CBI copy of your objection or hearing request, identified by docket ID number EPA–HQ–OPP– 2018–0047, by one of the following methods: • Federal eRulemaking Portal: https:// www.regulations.gov. Follow the online instructions for submitting comments. Do not submit electronically any information you consider to be CBI or other information whose disclosure is restricted by statute. • Mail: OPP Docket, Environmental Protection Agency Docket Center (EPA/ DC), (28221T), 1200 Pennsylvania Ave. NW, Washington, DC 20460–0001. • Hand Delivery: To make special arrangements for hand delivery or delivery of boxed information, please follow the instructions at https:// www.epa.gov/dockets/contacts.html. Additional instructions on commenting or visiting the docket, along with more information about dockets generally, is available at https://www.epa.gov/ dockets. II. Summary of Petitioned-For Tolerance In the Federal Register of April 11, 2018 (83 FR 15528) (FRL–9975–57), EPA issued a document pursuant to FFDCA section 408(d)(3), 21 U.S.C. 346a(d)(3), announcing the filing of a pesticide petition (PP 7E8656) by Bayer CropScience, 2 T.W. Alexander Drive, Research Triangle Park, NC 27709. The petition requested that 40 CFR part 180 be amended by establishing a tolerance for residues of the fungicide isotianil in or on banana at 0.01 parts per million (ppm). That document referenced a summary of the petition prepared by E:\FR\FM\01NOR1.SGM 01NOR1

Agencies

ENVIRONMENTAL PROTECTION AGENCY

[Federal Register Volume 84, Number 212 (Friday, November 1, 2019)]
[Rules and Regulations]
[Pages 58601-58623]
From the Federal Register Online via the Government Publishing Office [www.gpo.gov]
[FR Doc No: 2019-22812]


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ENVIRONMENTAL PROTECTION AGENCY

40 CFR Part 63

[EPA-HQ-OAR-2013-0290; FRL-10001-21-OAR]
RIN 2060-AT25


National Emission Standards for Hazardous Air Pollutants for Clay 
Ceramics Manufacturing

AGENCY: Environmental Protection Agency (EPA).

ACTION: Final rule.

-----------------------------------------------------------------------

SUMMARY: This action finalizes certain amendments to the National 
Emission Standards for Hazardous Air Pollutants (NESHAP): Clay Ceramics 
Manufacturing source category. The final amendments are being issued in 
response to a petition for reconsideration filed by an affected 
industry (Kohler Company) on the final rule promulgated on October 26, 
2015, as well as our review of the 2015 rule with respect to certain 
other issues raised by Kohler. This action revises the temperature 
monitoring methodology used to demonstrate continuous compliance with 
the dioxin/furan (D/F) emissions limit of the final rule. In addition, 
we are addressing concerns raised by Kohler regarding visible emissions 
(VE) monitoring of tunnel kiln stacks for continuous compliance with 
particulate matter (PM) and mercury (Hg) emission limitations. This 
action also amends the requirements for weekly visual inspections of 
system ductwork and control device equipment for water curtain spray 
booths. Lastly, this action amends the NESHAP to include provisions for 
emissions averaging, makes technical corrections, and adds certain 
definitions.

DATES: This final rule is effective on November 1, 2019.

ADDRESSES: The U.S. Environmental Protection agency (EPA) has 
established a docket for this rulemaking under Docket ID No. EPA-HQ-
OAR-2013-0290. All documents in the docket are listed on the https://www.regulations.gov/ website. Although listed, some information is not 
publicly available, e.g., confidential business information (CBI) or 
other information whose disclosure is restricted by statute. Certain 
other material, such as copyrighted material, is not placed on the 
internet and will be publicly available only in hard copy form. 
Publicly available docket materials are available either electronically 
through https://www.regulations.gov/, or in hard copy form at the EPA 
Docket Center, Room 3334, WJC West Building, 1301 Constitution Avenue 
NW, Washington, DC. The Public Reading Room is open from 8:30 a.m. to 
4:30 p.m., Monday through Friday, excluding legal holidays. The 
telephone number for the Public Reading Room is (202) 566-1744, and the 
telephone number for the EPA Docket Center is (202) 566-1742.

FOR FURTHER INFORMATION CONTACT: For questions about this final action, 
contact Mr. Brian Storey, Sector Policies and Programs Division (D243-
04), Office of Air Quality Planning and Standards, U.S. Environmental 
Protection Agency, Research Triangle Park, North Carolina 27711; 
telephone number: (919) 541-1103; fax number: (919) 541-4991; and email 
address: [email protected].

SUPPLEMENTARY INFORMATION: 

    Preamble acronyms and abbreviations. We use multiple acronyms and 
terms in this preamble. While this list may not be exhaustive, to

[[Page 58602]]

ease the reading of this preamble and for reference purposes, the EPA 
defines the following terms and acronyms here:

BSCP brick and structural clay products
CAA Clean Air Act
CBI Confidential Business Information
CFR Code of Federal Regulations
D/F dioxins/furans
EJ environmental justice
EPA U.S. Environmental Protection Agency
HAP hazardous air pollutant(s)
Hg mercury
HON Hazardous Organic NESHAP
lb pounds
NAICS North American Industry Classification System
NESHAP national emission standards for hazardous air pollutants
No. number
NTTAA National Technology Transfer and Advancement Act
OMB Office of Management and Budget
PM particulate matter
POC products of combustion
PRA Paperwork Reduction Act
RFA Regulatory Flexibility Act
UMRA Unfunded Mandates Reform Act
U.S. United States
U.S.C. United States Code
v. versus
VE visible emissions

    Background information. On August 20, 2018, the EPA proposed 
revisions to the Clay Ceramics Manufacturing NESHAP. In this action, we 
are finalizing revisions to the rule. The EPA briefly summarizes the 
more significant comments we received regarding the proposed rule that 
have resulted in changes to the final rule, and we provide our 
responses in this preamble. A more comprehensive summary of the public 
comments on the proposal and the EPA's responses to those comments is 
available in the National Emission Standards for Hazardous Air 
Pollutants for Clay Ceramics Manufacturing; Amendments--Background 
Information for Final Rule: Summary of Public Comments and Responses. A 
``track changes'' version of the regulatory language that incorporates 
the changes in this action is available in the docket.
    Organization of this document. The information in this preamble is 
organized as follows:

Table of Contents

I. General Information
    A. Does this action apply to me?
    B. Where can I get a copy of this document and other related 
information?
    C. Judicial Review and Administrative Reconsideration
II. Background
    A. What is the statutory authority for this action?
    B. What actions preceded these final amendments?
III. Summary of the Final Amendments
IV. Rationale for Changes to the Proposed Amendments
    A. Visible Emissions Monitoring of Tunnel Kiln Exhaust
    B. Weekly Visual Inspections of Water Curtain Spray Booths
    C. Emissions Averaging
V. Summary of Cost, Environmental, and Economic Impacts
VI. Statutory and Executive Order Reviews
    A. Executive Order 12866: Regulatory Planning and Review and 
Executive Order 13563: Improving Regulation and Regulatory Review
    B. Executive Order 13771: Reducing Regulations and Controlling 
Regulatory Costs
    C. Paperwork Reduction Act (PRA)
    D. Regulatory Flexibility Act (RFA)
    E. Unfunded Mandates Reform Act (UMRA)
    F. Executive Order 13132: Federalism
    G. Executive Order 13175: Consultation and Coordination With 
Indian Tribal Governments
    H. Executive Order 13045: Protection of Children From 
Environmental Health Risks and Safety Risks
    I. Executive Order 13211: Actions Concerning Regulations That 
Significantly Affect Energy Supply, Distribution, or Use
    J. National Technology Transfer and Advancement Act (NTTAA)
    K. Executive Order 12898: Federal Actions To Address 
Environmental Justice in Minority Populations and Low-Income 
Populations
    L. Congressional Review Act (CRA)

I. General Information

A. Does this action apply to me?

    Table 1 of this preamble lists the NESHAP and associated regulated 
industrial source categories that are the subject of this final action. 
Table 1 is not intended to be exhaustive but rather provides a guide 
for readers regarding the entities that this final action is likely to 
affect. The final amendments will be directly applicable to the 
affected sources. Federal, state, local and tribal government entities 
would not be affected by this final action. As defined in the Initial 
List of Categories of Sources Under Section 112(c)(1) of the Clean Air 
Act Amendments of 1990 (see 57 FR 31576, July 16, 1992) and 
Documentation for Developing the Initial Source Category List (see EPA-
450/3-91-030), the Clay Products Manufacturing source category as 
originally listed included any facility engaged in manufacturing of 
clay products such as brick, vitrified clay pipe, structural clay tile, 
and clay refractories. The Clay Products Manufacturing source category 
has since been replaced by the Brick and Structural Clay Products 
(BSCP) Manufacturing source category and the Clay Ceramics 
Manufacturing source category (see 67 FR 47894, July 22, 2002).

 Table 1--NESHAP and Industrial Source Categories Affected by This Final
                                 Action
------------------------------------------------------------------------
                                                 Examples of potentially
            Category             NAICS code \1\     regulated entities
------------------------------------------------------------------------
Industry.......................          327120  Ceramic wall and floor
                                                  tile manufacturing
                                                  facilities (Clay
                                                  Ceramics Manufacturing
                                                  NESHAP).
                                         327110  Vitreous plumbing
                                                  fixtures
                                                  (sanitaryware)
                                                  manufacturing
                                                  facilities (Clay
                                                  Ceramics Manufacturing
                                                  NESHAP).
Federal government.............  ..............  Not affected.
State/local/tribal government..  ..............  Not affected.
------------------------------------------------------------------------
\1\ North American Industry Classification System.

B. Where can I get a copy of this document and other related 
information?

    In addition to being available in the docket, an electronic copy of 
this final action is available on the internet. Following signature by 
the EPA Administrator, the EPA will post a copy of this final action at 
https://www.epa.gov/stationary-sources-air-pollution/brick-and-structural-clay-products-national-emission-standards. Following 
publication in the Federal Register, the EPA will post the Federal 
Register version of the final amendments and key technical documents at 
this same website.
    A redline version of the regulatory language that incorporates the 
changes in this final action is available in the docket for this action 
(Docket ID No. EPA-HQ-OAR-2013-0290).

[[Page 58603]]

C. Judicial Review and Administrative Reconsideration

    Under Clean Air Act (CAA) section 307(b)(1), judicial review of 
this final action is available only by filing a petition for review in 
the United States Court of Appeals for the District of Columbia Circuit 
by December 31, 2019. Under CAA section 307(b)(2), the requirements 
established by this final rule may not be challenged separately in any 
civil or criminal proceedings brought by the EPA to enforce the 
requirements.
    Section 307(d)(7)(B) of the CAA further provides that only an 
objection to a rule or procedure which was raised with reasonable 
specificity during the period for public comment (including any public 
hearing) may be raised during judicial review. This section also 
provides a mechanism for the EPA to reconsider the rule if the person 
raising an objection can demonstrate to the Administrator that it was 
impracticable to raise such objection within the period for public 
comment or if the grounds for such objection arose after the period for 
public comment (but within the time specified for judicial review) and 
if such objection is of central relevance to the outcome of the rule. 
Any person seeking to make such a demonstration should submit a 
Petition for Reconsideration to the Office of the Administrator, U.S. 
EPA, Room 3000, WJC South Building, 1200 Pennsylvania Ave. NW, 
Washington, DC 20460, with a copy to both the person listed in the 
preceding FOR FURTHER INFORMATION CONTACT section, and the Associate 
General Counsel for the Air and Radiation Law Office, Office of General 
Counsel (Mail Code 2344A), U.S. EPA, 1200 Pennsylvania Ave. NW, 
Washington, DC 20460.

II. Background

A. What is the statutory authority for this action?

    The statutory authority for this action is provided by sections 112 
and 307(d)(7)(B) of the CAA as amended (42 U.S.C. 7412 and 
7607(d)(7)(B)).

B. What actions preceded these final amendments?

    The initial NESHAP for Clay Ceramics Manufacturing was published in 
the Federal Register on May 16, 2003 (68 FR 26690), and codified at 40 
CFR part 63, subpart KKKKK, pursuant to section 112 of the CAA. These 
standards were challenged and subsequently vacated by the United States 
Court of Appeals for the District of Columbia Circuit in 2007. See 
Sierra Club v. EPA, 479 F.3d 875, 876 (D.C. Cir. 2007). Following the 
2007 vacatur of the 2003 rule, the EPA collected additional data and 
information to support new standards for the clay ceramics industry. 
This information is contained in the docket at https://www.regulations.gov/ (see Docket ID No. EPA-HQ-OAR-2013-0290). On 
December 18, 2014, the EPA proposed the new NESHAP for Clay Ceramics 
Manufacturing (79 FR 75622). The EPA received additional data and 
comments during the public comment period. These data and comments were 
considered and analyzed and, where appropriate, revisions to the NESHAP 
were made. The NESHAP for Clay Ceramics Manufacturing was finalized on 
October 26, 2015 (80 FR 65470).
    On December 23, 2015, Kohler Company (Kohler) petitioned the EPA 
for reconsideration of the final rule for Clay Ceramics Manufacturing 
(Docket ID No. EPA-HQ-OAR-2013-0290-0316). On August 20, 2018, we 
proposed revisions to the Clay Ceramics Manufacturing NESHAP based on 
the information provided by Kohler in their petition and information 
collected by the EPA (83 FR 42066). Public comments were received on 
the proposal requesting some changes to the proposed revisions. This 
action finalizes the revisions to the NESHAP and, where deemed 
appropriate, incorporates the requested changes. The intent of these 
amendments is to provide flexibility to the clay ceramics manufacturing 
industry, while maintaining the emissions and operational standards of 
the NESHAP.

III. Summary of the Final Amendments

    The EPA is issuing the following amendments to 40 CFR part 63, 
subpart KKKKK, in response to Kohler's petition for reconsideration on 
the October 26, 2015, final rule (80 FR 65470):
     Revise the temperature monitoring methodology used to 
demonstrate continuous compliance with the D/F emissions limits from 
sanitaryware first-fire tunnel kilns;
     Provide an alternative to the monitoring provisions for VE 
from tunnel kiln exhaust stacks;
     Amend the requirements for weekly visual inspections of 
system ductwork and control device equipment for water curtain spray 
booths;
     Define cooling stacks in the rule and differentiate 
cooling stacks from kiln exhaust stacks for compliance purposes; and
     Include provisions to allow emissions averaging for 
emissions from existing tunnel kilns and glaze spray booths and make 
associated revisions to the definition of affected source and 
recordkeeping and reporting requirements.

We are finalizing all the amendments listed above as proposed except 
for the provisions to allow emissions averaging. A description of the 
changes made to the emissions averaging provisions since proposal along 
with the rationale for those changes is provided in section IV of this 
preamble.
    This final rule achieves meaningful burden reduction by providing 
regulated facilities with the ability to use existing monitoring 
equipment and removing the requirements for periodic inspections that 
we have determined are not necessary to demonstrate compliance. We also 
more clearly identify which stacks are cooling stacks; thus, avoiding 
the possibility that a source might be required to perform an emission 
test on a stack that emits only cooling air. Finally, this action 
provides additional compliance flexibility for sources to meet certain 
emissions limits by averaging; thereby, simplifying compliance. All of 
these actions should reduce the overall burden to the regulated 
sources.
    This action is limited to the specific issues raised in the 
petition for reconsideration, plus some minor technical corrections. 
There are no changes to emission limits as a result of these final 
amendments. Technical corrections are being issued as proposed to 
correct inaccuracies that were promulgated in the final rule, replace 
text that might be considered confusing, and correct outdated 
information. These changes are described in Table 2 of this preamble.

     Table 2--Technical Corrections to 40 CFR Part 63, Subpart KKKKK
------------------------------------------------------------------------
         Table to subpart KKKKK             Description of correction
------------------------------------------------------------------------
40 CFR 63.8635(g)(1)...................  Update the addresses for EPA
                                          websites.
Table 2, item 3........................  To avoid confusion, revise the
                                          description of the operating
                                          limit for carbon flow rate.

[[Page 58604]]

 
Table 2, items 10 and 11...............  Revise the block period for
                                          average operating temperature
                                          for spray dryers and floor
                                          tile press dryers from 3-hour
                                          to 4-hour to align with the
                                          test run length for EPA Method
                                          23.
Table 4, item 8........................  In the measurement of carbon
                                          flow rate data, include data
                                          from the Hg and D/F
                                          performance test data for
                                          tunnel or roller kilns
                                          equipped with an activated
                                          carbon injection system.
Table 4, items 11 and 12...............  Revise the block average for
                                          operating temperature for
                                          spray dryers and floor tile
                                          press dryers from 3-hour to 4-
                                          hour to align with the test
                                          run length for EPA Method 23.
Table 6, items 2.a.ii, 2.b.ii, 2.c.ii,   To avoid confusion, remove
 3.a.ii, 3.b.ii, 3.c.ii, 4.a.ii,          mention of the specific block
 4.b.ii, 4.c.ii, 5.a.ii, 5.b.ii,          period and simply refer to
 6.a.ii, 7.a.ii, 8.a.ii, 9.a.ii,          ``the period of the initial
 10.a.ii, 11.a.ii, 12.a.ii, 12.b.ii,      performance test.''
 12.c.ii, 13.a.ii, 13.b.ii, 13.c.ii,
 14.a.ii, 14.b.ii, 14.c.ii, 15.a.ii,
 15.b.ii, 16.a.ii, 17.a.ii, 18.a.ii,
 19.a.ii, 20.a.ii, and 21.a.ii.
Table 7, items 10 and 11...............  Revise the block average for
                                          operating temperature for
                                          spray dryers and floor tile
                                          press dryers from 3-hour to 4-
                                          hour to align with the test
                                          run length for EPA Method 23.
------------------------------------------------------------------------

IV. Rationale for Changes to the Proposed Amendments

A. Visible Emissions Monitoring of Tunnel Kiln Exhaust

    In its petition for reconsideration, Kohler stated that the EPA 
failed to adequately respond to Kohler's public comments regarding VE 
monitoring in the Agency's response to comments document and in the 
preamble for the final rule. In their comments on the December 18, 
2014, proposal, Kohler had argued that VE monitoring is not a useful 
parameter to assess kiln operation nor to assess hazardous air 
pollutant (HAP) emissions. Kohler requested that the EPA open a new 
public comment period to reconsider and respond to Kohler's concerns. 
In response to the petition, we proposed amendments to 40 CFR 63.8620 
in the Clay Ceramics Manufacturing NESHAP, adding a new paragraph 
(e)(2) which provided an alternative to VE testing that allowed sources 
to demonstrate compliance by maintaining the kiln temperature profile 
within acceptable parameters and, for any incidence where the kiln 
exceeds its temperature profile, monitor VE at each kiln stack as 
specified.
    In public comments on the proposed amendments, a commenter 
questioned Kohler's assertion about VE monitoring and recommended that 
the EPA define what a ``temperature profile'' is and clarify what it 
means to ``maintain'' it v. ``exceed'' it. In response to this comment, 
we are finalizing amendments to 40 CFR 63.8620(e)(2), the operating 
limits table (Table 2), and the continuous compliance table (Table 7) 
to clarify that the owner or operator will be required to maintain 
their kiln operating temperature within the range of acceptable 
temperatures (i.e., a temperature profile) established for each kiln 
and product. For any incident where the kiln is operating outside of 
its acceptable temperature range (i.e., exceeding its temperature 
profile) for the product being fired, the owner or operator will be 
required to record the incident as a deviation, and perform corrective 
action in accordance with the facility's operation, maintenance, and 
monitoring (OM&M) plan.

B. Weekly Visual Inspections of Water Curtain Spray Booths

    In its petition for reconsideration, Kohler requested that the EPA 
reconsider the frequency of visual inspection requirements for system 
ductwork and control device equipment for water curtain spray booths. 
In response to the petition, we proposed amendments to the operating 
limits table (Table 2) and the continuous compliance table (Table 7) to 
remove the requirement to conduct weekly visual inspections of the 
system ductwork and control equipment for leaks for all glaze spray 
operations equipped with water curtains.
    In public comments on the proposal, one commenter stated that if 
the EPA is relying on operator observations of visible particulate on 
the product to determine when there is a leak in the spray booth 
ductwork, the rule should require operators to log such incidents and 
report them as deviations when they occur. We recognize the commenter's 
concerns and agree that if there is an indication of particulate in the 
glaze of the product, then it is likely there is a failure in the 
ductwork requiring corrective action, and, therefore, this would be 
considered a deviation. We are finalizing amendments to Table 7 to 
require owners or operators to record as deviations any observations of 
particulates or other impurities getting into the glaze that has been 
sprayed onto a piece of ware and perform corrective action in 
accordance with the facility's OM&M plan.

C. Emissions Averaging

    In its petition for reconsideration, Kohler requested that the EPA 
allow the use of emissions averaging as a compliance option in the Clay 
Ceramics Manufacturing NESHAP for existing tunnel kilns and glaze spray 
booths. In response to the petition, we proposed amendments to 40 CFR 
63.8595 in the Clay Ceramics Manufacturing NESHAP that included 
alternative emissions averaging limits for the following:
     PM and Hg, in units of pounds per ton (lb/ton) of fired 
product for existing floor tile roller kilns;
     PM and Hg in units of lb/ton of fired product for existing 
wall tile roller kilns;
     PM and Hg, in units of lb/ton of greenware fired for 
existing first-fired sanitaryware tunnel kilns;
     PM and Hg, in units of lb/ton of first-fired glaze sprayed 
(dry weight basis) for existing tile glaze lines with glaze spraying; 
and
     PM, in units of lb/ton of first-fire glaze sprayed (dry 
weight basis), for existing sanitaryware manual, spray machine, or 
robot glaze applications.
    The proposed conditions required for emissions averaging included 
the following: (1) Emissions averaging would only be permitted between 
individual sources at a single existing affected source; (2) emissions 
averaging would only be permitted between individual sources subject to 
the Clay Ceramics Manufacturing NESHAP; (3) emissions averaging would 
not be permitted between two or more different affected sources; (4) 
emissions averaging would not be permitted between two or more sources 
in different subcategories;

[[Page 58605]]

(5) new sources could not use emissions averaging; and (6) averaged 
emissions could not exceed 90 percent of the applicable emission limit, 
which translates to a discount factor of 1.1 applied to actual 
emissions.
    The emissions averaging provisions that we proposed were based, in 
part, on the emissions averaging provisions in the Hazardous Organic 
NESHAP (HON). The legal basis and rationale for the HON emissions 
averaging provisions were provided in the preamble to the final HON (59 
FR 19425, April 22, 1994).
    In public comments on the proposal, two commenters requested that 
the EPA remove the requirement that averaged emissions cannot exceed 90 
percent of the applicable emission limit, and a third commenter stated 
that no justification was provided for the selection of 90 percent 
(instead of an alternate value, such as 80 or 99 percent). While 
averaging should only be permitted if it can be demonstrated that the 
total quantity of any HAP will not be greater than it could be if each 
individually affected unit complied separately with the applicable 
standard, one commenter stated this requirement can be demonstrated 
without the ``90 percent of the limit'' safety factor. The commenter 
noted that the EPA has allowed emissions averaging across similar 
emission units in other NESHAP, such as the Reinforced Plastics 
Composites NESHAP (40 CFR part 63, subpart WWWW), and stated that 
similar logic for averaging should be applied to this subpart to 
eliminate the unnecessary factor.
    In response to these comments, we have re-evaluated whether a 
discount factor is appropriate for the emissions averaging provisions 
in this subpart and have concluded that a discount factor is not 
necessary here. The issues faced in the HON, where a discount factor of 
1.1 was applied to the emissions averaging calculation, included 
significant differences in toxicity of the various HAP and a situation 
where facilities were applying emissions controls. This is not the case 
here. All facilities are meeting the relevant standards in this subpart 
without added controls and are using pollution prevention where needed. 
Accordingly, a straight average, without any discount factor, is 
appropriate in this situation. This straight-average approach is 
consistent with other rules, such as the Reinforced Plastic Composites 
NESHAP. Therefore, the EPA has decided not to include a discount factor 
in 40 CFR 63.8595(h), Equation 9, and 40 CFR 63.8620, Equation 10 to 
calculate the average weighted emissions.
    In addition, a commenter noted that the proposed emissions 
averaging provisions prohibited emissions averaging of new sources but 
did not prohibit emissions averaging of reconstructed sources. The 
commenter stated that reconstructed sources should not be allowed to 
use the emissions averaging provisions. We agree with the commenter, 
and in the final amendments the EPA has revised 40 CFR 63.8595(h)(1) to 
indicate that neither new nor reconstructed sources can be included in 
the emissions averaging.
    Finally, we note that Equations 9 through 11 were all proposed to 
be added to 40 CFR 63.8595(h). However, one commenter noted an apparent 
discrepancy between Equation 9 and Equation 10, and it appears that the 
commenter misunderstood that Equation 9 is intended to determine 
initial compliance based on an initial performance test, while Equation 
10 is intended to determine ongoing compliance based on the latest 
performance test. Equation 11 is also used for ongoing compliance and 
is intended to determine the 12-month rolling average of the monthly 
weighted average emission rates. Therefore, in the final amendments, 
Equations 10 and 11 have been moved to 40 CFR 63.8620, the section that 
describes how to demonstrate continuous compliance.

V. Summary of Cost, Environmental, and Economic Impacts

    This action will have no cost, environmental, energy, or economic 
impacts beyond those impacts presented in the October 26, 2015, final 
rule for Clay Ceramics Manufacturing and may result in a cost savings 
due to the changes in monitoring and testing requirements discussed in 
section III of this preamble. The technical corrections are cost 
neutral.

VI. Statutory and Executive Order Reviews

    Additional information about these statutes and Executive Orders 
can be found at https://www.epa.gov/laws-regulations/laws-and-executive-orders.

A. Executive Order 12866: Regulatory Planning and Review and Executive 
Order 13563: Improving Regulation and Regulatory Review

    This action is not a significant regulatory action and was, 
therefore, not submitted to the OMB for review.

B. Executive Order 13771: Reducing Regulations and Controlling 
Regulatory Costs

    This action is considered an Executive Order 13771 deregulatory 
action. This final rule provides meaningful burden reduction by 
providing additional regulatory flexibilities.

C. Paperwork Reduction Act (PRA)

    This action does not impose any new information collection burden 
under the PRA. OMB has previously approved the information collection 
activities contained in the existing regulation (40 CFR part 63, 
subpart KKKKK) and has assigned OMB control number 2060-0513. This 
action does not change the information collection requirements.

D. Regulatory Flexibility Act (RFA)

    I certify that this action will not have a significant economic 
impact on a substantial number of small entities under the RFA. In 
making this determination, the impact of concern is any significant 
adverse economic impact on small entities. An agency may certify that a 
rule will not have a significant economic impact on a substantial 
number of small entities if the rule relieves regulatory burden, has no 
net burden, or otherwise has a positive economic effect on the small 
entities subject to the rule. This final rule will not impose any 
additional requirements on small entities, only alternatives to 
existing requirements. We have, therefore, concluded that this action 
will have no net regulatory burden for all directly regulated small 
entities.

E. Unfunded Mandates Reform Act (UMRA)

    This action does not contain an unfunded mandate as described in 
UMRA, 2 U.S.C. 1531-1538, and does not significantly or uniquely affect 
small governments. The action imposes no enforceable duty on any state, 
local, or tribal governments or the private sector.

F. Executive Order 13132: Federalism

    This action does not have federalism implications. It will not have 
substantial direct effects on the states, on the relationship between 
the national government and the states, or on the distribution of power 
and responsibilities among the various levels of government.

G. Executive Order 13175: Consultation and Coordination With Indian 
Tribal Governments

    This action does not have tribal implications as specified in 
Executive

[[Page 58606]]

Order 13175. It will neither impose substantial direct compliance costs 
on federally recognized tribal governments, nor preempt tribal law. The 
final amendments impose no requirements on tribal governments. Thus, 
Executive Order 13175 does not apply to this action.

H. Executive Order 13045: Protection of Children From Environmental 
Health Risks and Safety Risks

    The EPA interprets Executive Order 13045 as applying only to those 
regulatory actions that concern environmental health or safety risks 
that the EPA has reason to believe may disproportionately affect 
children, per the definition of ``covered regulatory action'' in 
section 2-202 of the Executive Order. This action is not subject to 
Executive Order 13045 because it does not concern an environmental 
health risk or safety risk.

I. Executive Order 13211: Actions Concerning Regulations That 
Significantly Affect Energy Supply, Distribution, or Use

    This action is not subject to Executive Order 13211, because it is 
not a significant regulatory action under Executive Order 12866.

J. National Technology Transfer and Advancement Act (NTTAA)

    This rulemaking does not involve technical standards.

K. Executive Order 12898: Federal Actions To Address Environmental 
Justice in Minority Populations and Low-Income Populations

    The EPA believes that this action does not have disproportionately 
high and adverse human health or environmental effects on minority 
populations, low-income populations, and/or indigenous peoples, as 
specified in Executive Order 12898 (59 FR 7629, February 16, 1994). The 
documentation for this decision is contained in the docket. (See EJ 
Screening Report for Clay Ceramics, Docket ID Item No. EPA-HQ-OAR-2013-
0290-0241.)

L. Congressional Review Act (CRA)

    This action is subject to the CRA, and the EPA will submit a rule 
report to each House of the Congress and to the Comptroller General of 
the United States. This action is not a ``major rule'' as defined by 5 
U.S.C. 804(2).

List of Subjects in 40 CFR Part 63

    Environmental protection, Administrative practices and procedures, 
Air pollution control, Hazardous substances, Intergovernmental 
relations, Reporting and recordkeeping requirements.

    Dated: October 10, 2019.
Andrew R. Wheeler,
Administrator.

    For the reasons set out in the preamble, 40 CFR part 63 is amended 
as follows:

PART 63--NATIONAL EMISSION STANDARDS FOR HAZARDOUS AIR POLLUTANTS 
FOR SOURCE CATEGORIES

0
1. The authority citation for part 63 continues to read as follows:

    Authority:  42 U.S.C. 7401 et seq.

Subpart KKKKK--National Emission Standards for Hazardous Air 
Pollutants for Clay Ceramics Manufacturing

0
2. Section 63.8595 is amended by:
0
a. Revising paragraph (c);
0
b. Redesignating paragraph (h) as paragraph (i);
0
c. Adding a new paragraph (h); and
0
d. Revising newly redesignated paragraphs (i) introductory text and 
(i)(1) introductory text.
    The revisions and addition read as follows:


Sec.  63.8595  How do I conduct performance tests and establish 
operating limits?

* * * * *
    (c) Each performance test must be conducted according to the 
requirements in Sec.  63.7 and under the specific conditions in Table 4 
to this subpart. Stacks to be tested at sanitaryware manufacturing 
facilities shall be limited to products of combustion (POC) stacks and 
not include cooling stacks.
* * * * *
    (h)(1) As an alternative to meeting the requirements of Sec.  
63.8555 for PM or mercury, if you have more than one existing source in 
any subcategories located at your facility, you may demonstrate 
compliance by emissions averaging, if your averaged emissions are no 
higher than the applicable emission limit, according to the procedures 
in this section. You may not include new or reconstructed sources in an 
emissions average.
    (2) For a group of two or more existing sources in the same 
subcategory that each vent to a separate stack, you may average PM or 
mercury emissions among existing units to demonstrate compliance with 
the limits in Table 1 to this subpart as specified in paragraph 
(h)(2)(i) through (iv) of this section, if you satisfy the requirements 
in paragraphs (h)(3) and (4) of this section.
    (i) You may average across existing sources in the same kiln type 
and size category (e.g., roller or tunnel kilns, large or small kilns) 
and the same subcategory (e.g., sanitaryware manual or spray machine or 
robot glaze application) where applicable;
    (ii) You may not include a unit in the emissions average if the 
unit shares a common stack with units in other subcategories;
    (iii) You may not include spray dryers or press dryers in the 
emissions average; and
    (iv) You may not average between different types of pollutants.
    (3) The averaged emissions rate from the existing sources 
participating in the emissions averaging option must not exceed the 
limits in Table 1 to this subpart at all times the affected units are 
subject to numeric emission limits following the compliance date 
specified in Sec.  63.8545.
    (4)(i) You must demonstrate initial compliance using the maximum 
process rate and the results of the initial performance tests.
    (ii) You must use Equation 9 of this section to demonstrate that 
the PM or mercury emissions from all existing units participating in 
the emissions averaging option for that pollutant do not exceed the 
emission limits in Table 1 to this subpart.
[GRAPHIC] [TIFF OMITTED] TR01NO19.003

Where:

ERi = Average weighted emissions for PM or mercury, in 
units of kilograms (pounds) per megagram (ton) of fired product for 
existing floor tile roller kilns and wall tile roller kilns, 
greenware fired for existing first-fired sanitaryware tunnel kilns, 
and first-fire glaze sprayed (dry weight basis) for existing tile 
glaze lines with glaze spraying and average weighted emissions for 
PM, in units of kilograms (pounds) per megagram (ton)

[[Page 58607]]

of first-fire glaze sprayed (dry weight basis) for existing 
sanitaryware manual, spray machine, or robot glaze applications.
Ei = Emission rate (as determined during the initial 
compliance demonstration) of PM or mercury from unit i, in units of 
kilograms (pounds) per megagram (ton). Determine the emission rate 
for PM or mercury by performance testing according to Table 4 to 
this subpart using the applicable equation in paragraph (f) of this 
section.
Pmax i = Maximum process rate for unit i, in units of 
megagrams per hour (tons per hour).
n = Number of units participating in the emissions averaging option.

    (5) You must develop and submit upon request to the applicable 
Administrator for review and approval, an implementation plan for 
emissions averaging according to the following procedures and 
requirements in paragraphs (h)(5)(i) through (iv) of this section.
    (i) If requested, you must submit the implementation plan no later 
than 180 days before the date that the facility intends to demonstrate 
compliance using the emissions averaging option.
    (ii) You must include the information contained in paragraphs 
(h)(5)(ii)(A) through (D) of this section in your implementation plan 
for all emission sources included in an emissions average:
    (A) The identification of all existing sources in the averaging 
group, including for each either the applicable HAP emissions level or 
the control technology installed and the date on which you are 
requesting emissions averaging to commence;
    (B) The specific control technology or pollution prevention measure 
to be used for each source in the averaging group and the date of its 
installation or application. If the pollution prevention measure 
reduces or eliminates emissions from multiple sources, the owner or 
operator must identify each source;
    (C) The test plan for the measurement of emissions in accordance 
with the requirements in this section; and
    (D) The operating parameters to be monitored for each control 
system or device consistent with Sec.  63.8555 and Table 2 to this 
subpart, and a description of how the operating limits will be 
determined.
    (iii) If submitted upon request, the Administrator shall review and 
approve or disapprove the plan according to the following criteria:
    (A) Whether the content of the plan includes all of the information 
specified in paragraph (h)(5)(ii) of this section; and
    (B) Whether the plan presents sufficient information to determine 
that compliance will be achieved and maintained.
    (iv) The applicable Administrator shall not approve an emissions 
averaging implementation plan containing any of the following 
provisions:
    (A) Any averaging between emissions of differing pollutants or 
between differing sources; or
    (B) The inclusion of any emission source other than an existing 
unit in the same subcategories.
    (i) For each affected source that is subject to the emission limits 
specified in Table 1 to this subpart and is equipped with an APCD that 
is not addressed in Table 2 to this subpart or that is using process 
changes as a means of meeting the emission limits in Table 1 to this 
subpart, you must meet the requirements in Sec.  63.8(f) and paragraphs 
(i)(1) and (2) of this section.
    (1) Submit a request for approval of alternative monitoring 
procedures to the Administrator no later than the notification of 
intent to conduct a performance test. The request must contain the 
information specified in paragraphs (i)(1)(i) through (iv) of this 
section.
* * * * *

0
3. Section 63.8620 is amended by:
0
a. Redesignating paragraphs (e) introductory text and (e)(1) through 
(3) as paragraphs (e)(1) introductory text and (e)(1)(i) through (iii), 
respectively;
0
b. Revising newly redesignated paragraph (e)(1) introductory text; and
0
c. Adding new paragraph (e)(2) and paragraphs (f) and (g).
    The revision and additions read as follows:


Sec.  63.8620  How do I demonstrate continuous compliance with the 
emission limitations and work practice standards?

* * * * *
    (e)(1) Visible emissions testing. You must demonstrate continuous 
compliance with the operating limits in Table 2 to this subpart for 
visible emissions (VE) from tunnel or roller kilns that are 
uncontrolled or equipped with DIFF, DLS/FF, or other dry control device 
by monitoring VE at each kiln stack according to the requirements in 
paragraphs (e)(1)(i) through (iii) of this section.
* * * * *
    (2) Alternative to VE testing. You must demonstrate continuous 
compliance with the operating limits in Table 2 to this subpart for 
kiln temperature profile for tunnel or roller kilns that are 
uncontrolled or equipped with DIFF, DLS/FF, or other dry control device 
by maintaining the kiln operating temperature within the range of 
acceptable temperatures (i.e., temperature profile) established for 
each kiln and product. For any incidence where the kiln is operating 
outside of its acceptable temperature range (i.e., exceeds its 
temperature profile) for the product being fired, you must record the 
incident as a deviation, and perform the necessary corrective action in 
accordance with your OM&M plan to return the kiln to the acceptable 
operating temperature for the product being fired. To confirm the kiln 
has returned to the acceptable temperature range, you will monitor VE 
at the kiln stack according to the requirements in paragraphs (e)(2)(i) 
through (iii) of this section.
    (i) Perform VE observations at the stack of each kiln operating 
outside of its temperature profile according to the procedures of 
Method 22 of 40 CFR part 60, appendix A-7. The duration of each Method 
22 test must be at least 15 minutes.
    (ii) If VE are observed during any test conducted using Method 22 
of 40 CFR part 60, appendix A-7, you must continue to perform 
corrective action until VE are no longer observed.
    (iii) If VE are observed during any test conducted using Method 22 
of 40 CFR part 60, appendix A-7, you must report these deviations by 
following the requirements in Sec.  63.8635.
    (f) Following the compliance date, you must demonstrate compliance 
with the emissions averaging provision under this subpart on a 
continuous basis by meeting the requirements of paragraphs (f)(1) 
through (3) of this section.
    (1)(i) After the initial compliance demonstration described in 
Sec.  63.8595(h)(4), you must demonstrate compliance on a monthly basis 
determined at the end of every month (12 times per year) according to 
paragraph (f)(1)(ii) of this section. The first monthly period begins 
on the compliance date specified in Sec.  63.8545.
    (ii) For each calendar month, you must use Equation 10 of this 
section to calculate the average weighted emission rate for that month.

[[Page 58608]]

[GRAPHIC] [TIFF OMITTED] TR01NO19.004

Where:

ERi = Average weighted emissions for PM or mercury, in 
units of kilograms (pounds) per megagram (ton) of fired product for 
existing floor tile roller kilns and wall tile roller kilns, 
greenware fired for existing first-fired sanitaryware tunnel kilns, 
and first-fire glaze sprayed (dry weight basis) for existing tile 
glaze lines with glaze spraying and average weighted emissions for 
PM, in units of kilograms (pounds) per megagram (ton) of first-fire 
glaze sprayed (dry weight basis) for existing sanitaryware manual, 
spray machine, or robot glaze applications, for that calendar month.
Ei = Emission rate (as determined during the most recent 
compliance demonstration) of PM or mercury from unit i, in units of 
kilograms (pounds) per megagram (ton). Determine the emission rate 
for PM or mercury by performance testing according to Table 4 to 
this subpart using the applicable equation in Sec.  63.8595(f).
Pmonth i = The process rate for that calendar month for 
unit i, in units of megagrams (tons).
n = Number of units participating in the emissions averaging option.

    (2) Until 12 monthly weighted average emission rates have been 
accumulated, calculate and report only the average weighted emission 
rate determined under paragraph (f)(1)(ii) of this section for each 
calendar month. After 12 monthly weighted average emission rates have 
been accumulated, for each subsequent calendar month, use Equation 11 
of this section to calculate the 12-month rolling average of the 
monthly weighted average emission rates for the current calendar month 
and the previous 11 calendar months.
[GRAPHIC] [TIFF OMITTED] TR01NO19.005

Where:

Eavg = 12-month rolling average emission rate for PM or 
mercury, in units of kilograms (pounds) per megagram (ton) of fired 
product for existing floor tile roller kilns and wall tile roller 
kilns, greenware fired for existing first-fired sanitaryware tunnel 
kilns, and first-fire glaze sprayed (dry weight basis) for existing 
tile glaze lines with glaze spraying and average weighted emissions 
for PM, in units of kilograms (pounds) per megagram (ton) of first-
fire glaze sprayed (dry weight basis) for existing sanitaryware 
manual, spray machine, or robot glaze applications.
ERi = Monthly weighted average, for calendar month ``i,'' 
in units of kilograms (pounds) per megagram (ton), as calculated by 
paragraph (f)(1)(ii) of this section.

    (3) For each existing unit participating in the emissions averaging 
option, you must comply with the continuous compliance requirements in 
Table 7 to this subpart.
    (g) Any instance where you fail to comply with the continuous 
monitoring requirements in paragraphs (f)(1) through (3) of this 
section is a deviation.

0
4. Section 63.8630 is amended by revising paragraph (c) introductory 
text and adding paragraph (c)(4) to read as follows:


Sec.  63.8630  What notifications must I submit and when?

* * * * *
    (c) If you are required to conduct a performance test or other 
initial compliance demonstration as specified in Tables 4 and 6 to this 
subpart, your Notification of Compliance Status as specified in Table 9 
to this subpart must include the information in paragraphs (c)(1) 
through (4) of this section.
* * * * *
    (4) Identification of whether you plan to demonstrate compliance by 
emissions averaging. If you plan to demonstrate compliance by emissions 
averaging, report the emissions level that was being achieved or the 
control technology employed on December 28, 2015.
* * * * *

0
5. Section 63.8635 is amended by:
0
a. Revising paragraphs (c) introductory text and (c)(4)(iii)(C);
0
b. Adding paragraph (c)(9); and
0
c. Revising paragraph (g)(1).
    The revisions and addition read as follows:


Sec.  63.8635  What reports must I submit and when?

* * * * *
    (c) The compliance report must contain the information in 
paragraphs (c)(1) through (9) of this section.
* * * * *
    (4) * * *
    (iii) * * *
    (C) Based on the information recorded under paragraphs 
(c)(4)(iii)(A) and (B) of this section, compute the annual percent of 
affected source operating uptime during which the control device was 
offline for routine maintenance using Equation 12 of this section.
[GRAPHIC] [TIFF OMITTED] TR01NO19.006

Where:

RM = Annual percentage of affected source uptime during which 
control device was offline for routine control device maintenance.
DTp = Control device downtime claimed under the routine 
control device maintenance alternative standard for the previous 
semiannual compliance period.
DTc = Control device downtime claimed under the routine 
control device maintenance alternative standard for the current 
semiannual compliance period.
SUp = Affected source uptime for the previous semiannual 
compliance period.
SUc = Affected source uptime for the current semiannual 
compliance period.

* * * * *
    (9) If you plan to demonstrate compliance by emissions averaging, 
certify the emissions level achieved or the control technology employed 
is no less stringent than the level or control technology contained in 
the notification of compliance status in Sec.  63.8630(c)(4), including 
all necessary documentation

[[Page 58609]]

to support this certification, such as inputs to Equations 9 through 11 
of this subpart.
* * * * *
    (g) * * *
    (1) For data collected using test methods supported by the EPA's 
Electronic Reporting Tool (ERT) as listed on the EPA's ERT website 
(https://www.epa.gov/electronicreporting-air-emissions/electronicreporting-tool-ert) at the time of the test, you must submit 
the results of the performance test to the EPA via the Compliance and 
Emissions Data Reporting Interface (CEDRI). (CEDRI can be accessed 
through the EPA's Central Data Exchange (CDX) (https://cdx.epa.gov/).) 
Performance test data must be submitted in a file format generated 
through the use of the EPA's ERT or an alternate electronic file format 
consistent with the extensible markup language (XML) schema listed on 
the EPA's ERT website. If you claim that some of the performance test 
information being submitted is confidential business information (CBI), 
you must submit a complete file generated through the use of the EPA's 
ERT or an alternate electronic file consistent with the XML schema 
listed on the EPA's ERT website, including information claimed to be 
CBI, on a compact disc, flash drive, or other commonly used electronic 
storage media to the EPA. The electronic media must be clearly marked 
as CBI and mailed to U.S. EPA/OAPQS/CORE CBI Office, Attention: Group 
Leader, Measurement Policy Group, MD C404-02, 4930 Old Page Rd., 
Durham, NC 27703. The same ERT or alternate file with the CBI omitted 
must be submitted to the EPA via the EPA's CDX as described earlier in 
this paragraph (g)(1).
* * * * *

0
6. Section 63.8640 is amended by revising paragraph (c) introductory 
text and adding paragraph (c)(11) to read as follows:


Sec.  63.8640  What records must I keep?

* * * * *
    (c) You must also maintain the records listed in paragraphs (c)(1) 
through (11) of this section.
* * * * *
    (11) If you elect to average emissions consistent with Sec.  
63.8595(h), you must additionally keep a copy of the emissions 
averaging implementation plan required in Sec.  63.8595(h)(5), all 
calculations required under Sec.  63.8595(h), including monthly records 
of process rate, as applicable, and monitoring records consistent with 
Sec.  63.8620(f).

0
7. Section 63.8665 is amended by adding definitions for ``Cooling 
stack,'' ``Emissions averaging sources,'' and ``Products of combustion 
(POC) stack'' in alphabetical order to read as follows:


Sec.  63.8665  What definitions apply to this subpart?

* * * * *
    Cooling stack means a stack (release point) installed on the 
cooling zone of a tunnel kiln to release air used to cool down the 
fired product from its maximum temperature to room temperature. A 
cooling stack does not release any air from the firing zone of the 
tunnel kiln.
* * * * *
    Emissions averaging sources means, for purposes of the emissions 
averaging provisions of Sec.  63.8595(h), the collection of all 
existing ceramic tile roller kilns, sanitaryware tunnel kilns, ceramic 
tile glaze lines using glaze spraying, and sanitaryware glaze spray 
booths, within a kiln type and size category and within a subcategory.
* * * * *
    Products of combustion (POC) stack means a stack (release point) 
installed on the front end of the firing zone of a tunnel kiln to 
release air used to heat the greenware from room temperature to its 
maximum temperature.
* * * * *

0
8. Table 1 to subpart KKKKK is revised to read as follows:

          Table 1 to Subpart KKKKK of Part 63--Emission Limits
  As stated in Sec.   63.8555, you must meet each emission limit in the
                  following table that applies to you:
------------------------------------------------------------------------
                                    You must meet the following emission
          For each . . .                        limits . . .
------------------------------------------------------------------------
1. Collection of all tunnel or      HF and HCl emissions must not exceed
 roller kilns at facility.           62 kilograms per hour (kg/hr) (140
                                     pounds per hour (lb/hr)) HCl
                                     equivalent, under the health-based
                                     standard, as determined using
                                     Equations 4 and 5 of this subpart.
2. Existing floor tile roller kiln  a. PM emissions must not exceed
                                     0.063 kilogram per megagram (kg/Mg)
                                     (0.13 pound per ton (lb/ton)) of
                                     fired product.
                                    b. Hg emissions must not exceed 6.3
                                     E-05 kg/Mg (1.3 E-04 lb/ton) of
                                     fired product.
                                    c. Dioxin/furan emissions must not
                                     exceed 2.8 nanograms per kilogram
                                     (ng/kg) of fired product.
3. Existing wall tile roller kiln.  a. PM emissions must not exceed 0.19
                                     kg/Mg (0.37 lb/ton) of fired
                                     product.
                                    b. Hg emissions must not exceed 1.1
                                     E-04 kg/Mg (2.1 E-04 lb/ton) of
                                     fired product.
                                    c. Dioxin/furan emissions must not
                                     exceed 0.22 ng/kg of fired product.
4. Existing first-fire              a. PM emissions must not exceed 0.17
 sanitaryware tunnel kiln.           kg/Mg (0.34 lb/ton) of greenware
                                     fired.
                                    b. Hg emissions must not exceed 1.3
                                     E-04 kg/Mg (2.6 E-04 lb/ton) of
                                     greenware fired.
                                    c. Dioxin/furan emissions must not
                                     exceed 3.3 ng/kg of greenware
                                     fired.
5. Existing tile glaze line with    a. PM emissions must not exceed 0.93
 glaze spraying.                     kg/Mg (1.9 lb/ton) of first-fire
                                     glaze sprayed (dry weight basis).
                                    b. Hg emissions must not exceed 8.0
                                     E-05 kg/Mg (1.6 E-04 lb/ton) of
                                     first-fire glaze sprayed (dry
                                     weight basis).
6. Existing sanitaryware manual     PM emissions must not exceed 18 kg/
 glaze application.                  Mg (35 lb/ton) of first-fire glaze
                                     sprayed (dry weight basis).
7. Existing sanitaryware spray      PM emissions must not exceed 6.2 kg/
 machine glaze application.          Mg (13 lb/ton) of first-fire glaze
                                     sprayed (dry weight basis).
8. Existing sanitaryware robot      PM emissions must not exceed 4.5 kg/
 glaze application.                  Mg (8.9 lb/ton) of first-fire glaze
                                     sprayed (dry weight basis).
9. Existing floor tile spray dryer  Dioxin/furan emissions must not
                                     exceed 19 ng/kg of throughput
                                     processed.
10. Existing wall tile spray dryer  Dioxin/furan emissions must not
                                     exceed 0.058 ng/kg of throughput
                                     processed.
11. Existing floor tile press       Dioxin/furan emissions must not
 dryer.                              exceed 0.024 ng/kg of throughput
                                     processed.
12. New or reconstructed floor      a. PM emissions must not exceed
 tile roller kiln.                   0.019 kg/Mg (0.037 lb/ton) of fired
                                     product.
                                    b. Hg emissions must not exceed 2.0
                                     E-05 kg/Mg (3.9 E-05 lb/ton) of
                                     fired product.
                                    c. Dioxin/furan emissions must not
                                     exceed 1.3 ng/kg of fired product.

[[Page 58610]]

 
13. New or reconstructed wall tile  a. PM emissions must not exceed 0.19
 roller kiln.                        kg/Mg (0.37 lb/ton) of fired
                                     product.
                                    b. Hg emissions must not exceed 1.1
                                     E-04 kg/Mg (2.1 E-04 lb/ton) of
                                     fired product.
                                    c. Dioxin/furan emissions must not
                                     exceed 0.22 ng/kg of fired product.
14. New or reconstructed first-     a. PM emissions must not exceed
 fire sanitaryware tunnel kiln.      0.048 kg/Mg (0.095 lb/ton) of
                                     greenware fired.
                                    b. Hg emissions must not exceed 6.1
                                     E-05 kg/Mg (1.3 E-04 lb/ton) of
                                     greenware fired.
                                    c. Dioxin/furan emissions must not
                                     exceed 0.99 ng/kg of greenware
                                     fired.
15. New or reconstructed tile       a. PM emissions must not exceed 0.31
 glaze line with glaze spraying.     kg/Mg (0.61 lb/ton) of first-fire
                                     glaze sprayed (dry weight basis).
                                    b. Hg emissions must not exceed 8.0
                                     E-05 kg/Mg (1.6 E-04 lb/ton) of
                                     first-fire glaze sprayed (dry
                                     weight basis).
16. New or reconstructed            PM emissions must not exceed 2.0 kg/
 sanitaryware manual glaze           Mg (3.9 lb/ton) of first-fire glaze
 application.                        sprayed (dry weight basis).
17. New or reconstructed            PM emissions must not exceed 1.6 kg/
 sanitaryware spray machine glaze    Mg (3.2 lb/ton) of first-fire glaze
 application.                        sprayed (dry weight basis).
18. New or reconstructed            PM emissions must not exceed 1.2 kg/
 sanitaryware robot glaze            Mg (2.3 lb/ton) of first-fire glaze
 application.                        sprayed (dry weight basis).
19. New or reconstructed floor      Dioxin/furan emissions must not
 tile spray dryer.                   exceed 0.071 ng/kg of throughput
                                     processed.
20. New or reconstructed wall tile  Dioxin/furan emissions must not
 spray dryer.                        exceed 0.058 ng/kg of throughput
                                     processed.
21. New or reconstructed floor      Dioxin/furan emissions must not
 tile press dryer.                   exceed 0.024 ng/kg of throughput
                                     processed.
22. Collection of emissions         PM emissions must not exceed the
 averaging sources.                  applicable emission limit, under
                                     the emissions averaging option, as
                                     determined using Equations 9
                                     through 11 of this subpart.
23. Collection of emissions         Hg emissions must not exceed the
 averaging sources.                  applicable emission limit, under
                                     the emissions averaging option, as
                                     determined using Equations 9
                                     through 11 of this subpart.
------------------------------------------------------------------------


0
9. Table 2 to subpart KKKKK is revised to read as follows:

          Table 2 to Subpart KKKKK of Part 63--Operating Limits
 As stated in Sec.   63.8555, you must meet each operating limit in the
                  following table that applies to you:
------------------------------------------------------------------------
       For each . . .            You must . . .       Or you must . . .
------------------------------------------------------------------------
1. Tunnel or roller kiln      a. If you use a bag   i. Maintain no VE
 equipped with a DIFF or DLS/  leak detection        from the DIFF or
 FF.                           system, initiate      DLS/FF stack; or
                               corrective action    ii. Maintain your
                               within 1 hour of a    kiln operating
                               bag leak detection    temperature within
                               system alarm and      the range of
                               complete corrective   acceptable
                               actions in            temperatures (i.e.,
                               accordance with       temperature profile
                               your OM&M plan;       established for
                               operate and           each kiln and
                               maintain the fabric   product.
                               filter such that
                               the alarm is not
                               engaged for more
                               than 5 percent of
                               the total operating
                               time in a 6-month
                               block reporting
                               period; and
                              b. Maintain free-
                               flowing lime in the
                               feed hopper or silo
                               and to the APCD at
                               all times for
                               continuous
                               injection systems;
                               maintain the feeder
                               setting (on a per
                               ton of throughput
                               basis) at or above
                               the level
                               established during
                               the performance
                               test for continuous
                               injection systems
                               in which compliance
                               was demonstrated.
2. Tunnel or roller kiln      a. Maintain the
 equipped with a WS.           average scrubber
                               liquid pH for each
                               3-hour block period
                               at or above the
                               average scrubber
                               liquid pH
                               established during
                               the HF/HCl
                               performance test in
                               which compliance
                               was demonstrated;
                               and
                              b. Maintain the
                               average scrubber
                               liquid flow rate
                               for each 3-hour
                               block period at or
                               above the highest
                               average scrubber
                               liquid flow rate
                               established during
                               the HF/HCl and PM
                               performance tests
                               in which compliance
                               was demonstrated.
3. Tunnel or roller kiln      Maintain the 3-hour
 equipped with an ACI system.  block average
                               carbon flow rate at
                               or above the
                               highest average
                               carbon flow rate
                               established during
                               the Hg and dioxin/
                               furan performance
                               tests in which
                               compliance was
                               demonstrated.

[[Page 58611]]

 
4. Tunnel or roller kiln      Maintain the average  i. Maintain your
 intending to comply with      operating             kiln operating
 dioxin/furan emission limit   temperature for       temperature within
 without an ACI system.        each 12-hour block    the range of
                               period at or below    acceptable
                               the highest           temperatures (i.e.,
                               operating             temperature profile
                               temperature           established for
                               established during    each kiln and
                               the dioxin/furan      product.
                               performance test in
                               which compliance
                               was demonstrated.
5. Tunnel or roller kiln      a. Maintain no VE
 with no add-on control.       from the stack; and
                              b. Maintain the kiln
                               process rate at or
                               below the kiln
                               process rate
                               determined
                               according to Sec.
                               63.8595(g)(1) if
                               your total facility
                               maximum potential
                               HCl-equivalent
                               emissions are
                               greater than the
                               HCl-equivalent
                               limit in Table 1 to
                               this subpart; and
                              c. Maintain the       i. Maintain no VE
                               average operating     from the FF stack.
                               temperature for
                               each 12-hour block
                               period at or below
                               the highest
                               operating
                               temperature
                               established during
                               the dioxin/furan
                               performance test in
                               which compliance
                               was demonstrated.
6. Glaze spray operation      a. If you use a bag
 equipped with a FF.           leak detection
                               system, initiate
                               corrective action
                               within 1 hour of a
                               bag leak detection
                               system alarm and
                               complete corrective
                               actions in
                               accordance with
                               your OM&M plan;
                               operate and
                               maintain the fabric
                               filter such that
                               the alarm is not
                               engaged for more
                               than 5 percent of
                               the total operating
                               time in a 6-month
                               block reporting
                               period.
7. Glaze spray operation      a. Maintain the
 equipped with a WS.           average scrubber
                               pressure drop for
                               each 3-hour block
                               period at or above
                               the average
                               pressure drop
                               established during
                               the PM performance
                               test in which
                               compliance was
                               demonstrated; and
                              b. Maintain the
                               average scrubber
                               liquid flow rate
                               for each 3-hour
                               block period at or
                               above the average
                               scrubber liquid
                               flow rate
                               established during
                               the PM performance
                               test in which
                               compliance was
                               demonstrated.
8. Glaze spray operation      a. Conduct daily
 equipped with a water         inspections to
 curtain.                      verify the presence
                               of water flow to
                               the wet control
                               system; and
                              b. Conduct annual
                               inspections of the
                               interior of the
                               control equipment
                               (if applicable) to
                               determine the
                               structural
                               integrity and
                               condition of the
                               control equipment.
9. Glaze spray operation      Conduct an annual
 equipped with baffles.        visual inspection
                               of the baffles to
                               confirm the baffles
                               are in place.
10. Spray dryer.............  Maintain the average
                               operating
                               temperature for
                               each 4-hour block
                               period at or above
                               the average
                               temperature
                               established during
                               the dioxin/furan
                               performance test in
                               which compliance
                               was demonstrated.
11. Floor tile press dryer..  Maintain the average
                               operating
                               temperature for
                               each 4-hour block
                               period at or below
                               the average
                               temperature
                               established during
                               the dioxin/furan
                               performance test in
                               which compliance
                               was demonstrated.
------------------------------------------------------------------------


0
10. Table 4 to subpart KKKKK is revised to read as follows:

                     Table 4 to Subpart KKKKK of Part 63--Requirements for Performance Tests
 As stated in Sec.   63.8595, you must conduct each performance test in the following table that applies to you:
----------------------------------------------------------------------------------------------------------------
                                                                                      According to the following
           For each . . .                You must . . .            Using . . .            requirements . . .
----------------------------------------------------------------------------------------------------------------
1. Tunnel or roller kiln...........  a. Select locations of  Method 1 or 1A of 40    Sampling sites must be
                                      sampling ports and      CFR part 60, appendix   located at the outlet of
                                      the number of           A-1.                    the APCD and prior to any
                                      traverse points.                                releases to the atmosphere
                                                                                      for all affected sources.
                                     b. Determine            Method 2 of 40 CFR      You may use Method 2A, 2C,
                                      velocities and          part 60, appendix A-1.  2D, or 2F of 40 CFR part
                                      volumetric flow rate.                           60, appendix A-1, or
                                                                                      Method 2G of 40 CFR part
                                                                                      60, appendix A-2, as
                                                                                      appropriate, as an
                                                                                      alternative to using
                                                                                      Method 2 of 40 CFR part
                                                                                      60, appendix A-1.

[[Page 58612]]

 
                                     c. Conduct gas          Method 3 of 40 CFR      You may use Method 3A or 3B
                                      molecular weight        part 60, appendix A-2.  of 40 CFR part 60,
                                      analysis.                                       appendix A-2, as
                                                                                      appropriate, as an
                                                                                      alternative to using
                                                                                      Method 3 of 40 CFR part
                                                                                      60, appendix A-2. ANSI/
                                                                                      ASME PTC 19.10-1981
                                                                                      (incorporated by
                                                                                      reference, see Sec.
                                                                                      63.14) may be used as an
                                                                                      alternative to the manual
                                                                                      procedures (but not the
                                                                                      instrumental procedures)
                                                                                      in Methods 3A and 3B.
                                     d. Measure moisture     Method 4 of 40 CFR
                                      content of the stack    part 60, appendix A-3.
                                      gas.
                                     e. Measure HF and HCl   i. Method 26A of 40     You may use Method 26 of 40
                                      emissions.              CFR part 60, appendix   CFR part 60, appendix A-8,
                                                              A-8; or                 as an alternative to using
                                                                                      Method 26A of 40 CFR part
                                                                                      60, appendix A-8, when no
                                                                                      acid PM (e.g., HF or HCl
                                                                                      dissolved in water
                                                                                      droplets emitted by
                                                                                      sources controlled by a
                                                                                      WS) is present. ASTM D6735-
                                                                                      01 (Reapproved 2009)
                                                                                      (incorporated by
                                                                                      reference, see Sec.
                                                                                      63.14) may be used as an
                                                                                      alternative to Methods 26
                                                                                      and 26A.
                                                             ii. Method 320 of       When using Method 320 of
                                                              appendix A of this      appendix A of this part,
                                                              part.                   you must follow the
                                                                                      analyte spiking procedures
                                                                                      of section 13 of Method
                                                                                      320 of appendix A of this
                                                                                      part, unless you can
                                                                                      demonstrate that the
                                                                                      complete spiking procedure
                                                                                      has been conducted at a
                                                                                      similar source. ASTM D6348-
                                                                                      03 (Reapproved 2010)
                                                                                      (incorporated by
                                                                                      reference, see Sec.
                                                                                      63.14) may be used as an
                                                                                      alternative to Method 320
                                                                                      if the test plan
                                                                                      preparation and
                                                                                      implementation in Annexes
                                                                                      A1-A8 are mandatory and
                                                                                      the %R in Annex A5 is
                                                                                      determined for each target
                                                                                      analyte.
                                     f. Measure PM           i. Method 5 of 40 CFR
                                      emissions.              part 60, appendix A-
                                                              3; or
                                                             ii. Method 29 of 40
                                                              CFR part 60, appendix
                                                              A-8.
                                     g. Measure Hg           Method 29 of 40 CFR     ASTM D6784-02 (Reapproved
                                      emissions.              part 60, appendix A-8.  2008) (incorporated by
                                                                                      reference, see Sec.
                                                                                      63.14) may be used as an
                                                                                      alternative to Method 29
                                                                                      (portion for Hg only).
                                     h. Measure dioxin/      Method 23 of 40 CFR
                                      furan emissions.        part 60, appendix A-7.
2. Glaze spray operation...........  a. Select locations of  Method 1 or 1A of 40    Sampling sites must be
                                      sampling ports and      CFR part 60, appendix   located at the outlet of
                                      the number of           A-1.                    the APCD and prior to any
                                      traverse points.                                releases to the atmosphere
                                                                                      for all affected sources.
                                     b. Determine            Method 2 of 40 CFR      You may use Method 2A, 2C,
                                      velocities and          part 60, appendix A-1.  2D, or 2F of 40 CFR part
                                      volumetric flow rate.                           60, appendix A-1, or
                                                                                      Method 2G of 40 CFR part
                                                                                      60, appendix A-2, as
                                                                                      appropriate, as an
                                                                                      alternative to using
                                                                                      Method 2 of 40 CFR part
                                                                                      60, appendix A-1.
                                     c. Conduct gas          Method 3 of 40 CFR      You may use Method 3A or 3B
                                      molecular weight        part 60, appendix A-2.  of 40 CFR part 60,
                                      analysis.                                       appendix A-2, as
                                                                                      appropriate, as an
                                                                                      alternative to using
                                                                                      Method 3 of 40 CFR part
                                                                                      60, appendix A-2. ANSI/
                                                                                      ASME PTC 19.10-1981
                                                                                      (incorporated by
                                                                                      reference, see Sec.
                                                                                      63.14) may be used as an
                                                                                      alternative to the manual
                                                                                      procedures (but not the
                                                                                      instrumental procedures)
                                                                                      in Methods 3A and 3B.
                                     d. Measure moisture     Method 4 of 40 CFR
                                      content of the stack    part 60, appendix A-3.
                                      gas.
                                     e. Measure PM           Method 5 of 40 CFR
                                      emissions.              part 60, appendix A-3.
                                     f. Measure Hg           Method 29 of 40 CFR     ASTM D6784-02 (Reapproved
                                      emissions (tile glaze   part 60, appendix A-8.  2008) (incorporated by
                                      spray operations                                reference, see Sec.
                                      only).                                          63.14) may be used as an
                                                                                      alternative to Method 29
                                                                                      (portion for Hg only).
3. Spray dryer or floor tile press   a. Select locations of  Method 1 or 1A of 40    Sampling sites must be
 dryer.                               sampling ports and      CFR part 60, appendix   located at the outlet of
                                      the number of           A-1.                    the APCD and prior to any
                                      traverse points.                                releases to the atmosphere
                                                                                      for all affected sources.
                                     b. Determine            Method 2 of 40 CFR      You may use Method 2A, 2C,
                                      velocities and          part 60, appendix A-1.  2D, or 2F of 40 CFR part
                                      volumetric flow rate.                           60, appendix A-1, or
                                                                                      Method 2G of 40 CFR part
                                                                                      60, appendix A-2, as
                                                                                      appropriate, as an
                                                                                      alternative to using
                                                                                      Method 2 of 40 CFR part
                                                                                      60, appendix A-1.

[[Page 58613]]

 
                                     c. Conduct gas          Method 3 of 40 CFR      You may use Method 3A or 3B
                                      molecular weight        part 60, appendix A-2.  of 40 CFR part 60,
                                      analysis.                                       appendix A-2, as
                                                                                      appropriate, as an
                                                                                      alternative to using
                                                                                      Method 3 of 40 CFR part
                                                                                      60, appendix A-2. ANSI/
                                                                                      ASME PTC 19.10-1981
                                                                                      (incorporated by
                                                                                      reference, see Sec.
                                                                                      63.14) may be used as an
                                                                                      alternative to the manual
                                                                                      procedures (but not the
                                                                                      instrumental procedures)
                                                                                      in Methods 3A and 3B.
                                     d. Measure moisture     Method 4 of 40 CFR
                                      content of the stack    part 60, appendix A-3.
                                      gas.
                                     e. Measure dioxin/      Method 23 of 40 CFR
                                      furan emissions.        part 60, appendix A-7.
4. Tunnel or roller kiln with no     a. Establish the        HCl-equivalent limit    Using the procedures in
 add-on control.                      operating limit(s)      in Table 1 to this      Sec.   63.8595(g)(1), you
                                      for kiln process rate   subpart and emissions   must determine the maximum
                                      if the total facility   and production data     process rate(s) for your
                                      maximum potential HCl-  from the HF/HCl/Cl2     kiln(s) that would ensure
                                      equivalent emissions    performance test.       total facility maximum
                                      are greater than the                            potential HCl-equivalent
                                      HCl-equivalent limit                            emissions remain at or
                                      in Table 1 to this                              below the HCl-equivalent
                                      subpart.                                        limit in Table 1 to this
                                                                                      subpart. The maximum
                                                                                      process rate(s) would
                                                                                      become your site-specific
                                                                                      process rate operating
                                                                                      limit(s).
                                     b. Establish the        i. Data from the kiln   (1) You must continuously
                                      operating limit for     operating temperature   measure the kiln operating
                                      kiln operating          measurement device      temperature during three 4-
                                      temperature.            during the dioxin/      hour test runs and, from a
                                                              furan performance       12-hour block of time
                                                              test.                   consisting of 1-hour
                                                                                      increments, calculate the
                                                                                      following two values:
                                                                                     (a) The standard deviation
                                                                                      of the 12 1-hour
                                                                                      temperature measurements
                                                                                      (refer to Note 1).
                                                                                     (b) 1 percent of the 12-
                                                                                      hour block average.
                                                                                     (2) You must decide which
                                                                                      of the two values would
                                                                                      provide the greatest
                                                                                      variability (i.e., the
                                                                                      highest value), and then
                                                                                      add this value to the 12-
                                                                                      hour block average
                                                                                      measured during the
                                                                                      compliance testing. The
                                                                                      result is the maximum
                                                                                      temperature at which your
                                                                                      kiln may operate during
                                                                                      normal operations.
5. Tunnel or roller kiln that is     Determine the           Production data         You must measure and record
 complying with PM and/or Hg          production rate         collected during the    the production rate, on a
 production-based emission limits.    during each PM/Hg       PM/Hg performance       ton of throughput
                                      test run in order to    tests (e.g., the        processed basis, of the
                                      determine compliance    number of ceramic       affected kiln for each of
                                      with PM and/or Hg       pieces and weight per   the three test runs.
                                      production-based        piece in the kiln
                                      emission limits.        during a test run
                                                              divided by the amount
                                                              of time to fire a
                                                              piece).
6. Tunnel or roller kiln equipped    Establish the           Data from the lime      For continuous lime
 with a DIFF or DLS/FF.               operating limit for     feeder during the HF/   injection systems, you
                                      the lime feeder         HCl performance test.   must ensure that lime in
                                      setting.                                        the feed hopper or silo
                                                                                      and to the APCD is free-
                                                                                      flowing at all times
                                                                                      during the performance
                                                                                      test and record the feeder
                                                                                      setting, on a per ton of
                                                                                      throughput basis, for the
                                                                                      three test runs. If the
                                                                                      feed rate setting varies
                                                                                      during the three test
                                                                                      runs, determine and record
                                                                                      the average feed rate from
                                                                                      the three test runs. The
                                                                                      average of the three test
                                                                                      runs establishes your
                                                                                      minimum site-specific feed
                                                                                      rate operating limit.
7. Tunnel or roller kiln equipped    a. Establish the        Data from the pH        You must continuously
 with a WS.                           operating limit for     measurement device      measure the scrubber
                                      the average scrubber    during the HF/HCl       liquid pH, determine and
                                      liquid pH.              performance test.       record the block average
                                                                                      pH values for the three
                                                                                      test runs, and determine
                                                                                      and record the 3-hour
                                                                                      block average of the
                                                                                      recorded pH measurements
                                                                                      for the three test runs.
                                                                                      The average of the three
                                                                                      test runs establishes your
                                                                                      minimum site-specific
                                                                                      liquid pH operating limit.
                                     b. Establish the        Data from the flow      You must continuously
                                      operating limit for     rate measurement        measure the scrubber
                                      the average scrubber    device during the HF/   liquid flow rate,
                                      liquid flow rate.       HCl and PM              determine and record the
                                                              performance tests.      block average flow rate
                                                                                      values for the three test
                                                                                      runs, and determine and
                                                                                      record the 3-hour block
                                                                                      average of the recorded
                                                                                      flow rate measurements for
                                                                                      the three test runs. The
                                                                                      average of the three test
                                                                                      runs establishes your
                                                                                      minimum site-specific
                                                                                      liquid flow rate operating
                                                                                      level. If different
                                                                                      average wet scrubber
                                                                                      liquid flow rate values
                                                                                      are measured during the HF/
                                                                                      HCl and PM tests, the
                                                                                      highest of the average
                                                                                      values become your site-
                                                                                      specific operating limit.

[[Page 58614]]

 
8. Tunnel or roller kiln equipped    Establish the           Data from the carbon    You must measure the carbon
 with an ACI system.                  operating limit for     flow rate measurement   flow rate during each test
                                      the average carbon      conducted during the    run, determine and record
                                      flow rate.              Hg and dioxin/furan     the block average carbon
                                                              performance tests.      flow rate values for the
                                                                                      three test runs, and
                                                                                      determine and record the 3-
                                                                                      hour block average of the
                                                                                      recorded carbon flow rate
                                                                                      measurements for the three
                                                                                      test runs. The average of
                                                                                      the three test runs
                                                                                      establishes your minimum
                                                                                      site-specific activated
                                                                                      carbon flow rate operating
                                                                                      limit.
9. Tunnel or roller kiln intending   a. Establish the        i. Data from the kiln   (1) You must continuously
 to comply with dioxin/furan          operating limit for     operating temperature   measure the kiln operating
 emission limit without an ACI        kiln operating          measurement device      temperature during three 4-
 system.                              temperature.            during the dioxin/      hour test runs and, from a
                                                              furan performance       12-hour block of time
                                                              test.                   consisting of 1-hour
                                                                                      increments, calculate the
                                                                                      following two values:
                                                                                     (a) The standard deviation
                                                                                      of the 12 1-hour
                                                                                      temperature measurements
                                                                                      (refer to Note 1).
                                                                                     (b) 1 percent of the 12-
                                                                                      hour block average
                                                                                     (2) You must decide which
                                                                                      of the two values would
                                                                                      provide the greatest
                                                                                      variability (i.e., the
                                                                                      highest value), and then
                                                                                      add this value to the 12-
                                                                                      hour block average
                                                                                      measured during the
                                                                                      compliance testing. The
                                                                                      result is the maximum
                                                                                      temperature at which your
                                                                                      kiln may operate during
                                                                                      normal operations.
10. Glaze spray operation equipped   a. Establish the        Data from the pressure  You must continuously
 with a WS.                           operating limit for     drop measurement        measure the scrubber
                                      the average scrubber    device during the PM    pressure drop, determine
                                      pressure drop.          performance test.       and record the block
                                                                                      average pressure drop
                                                                                      values for the three test
                                                                                      runs, and determine and
                                                                                      record the 3-hour block
                                                                                      average of the recorded
                                                                                      pressure drop measurements
                                                                                      for the three test runs.
                                                                                      The average of the three
                                                                                      test runs establishes your
                                                                                      minimum site-specific
                                                                                      pressure drop operating
                                                                                      limit.
                                     b. Establish the        Data from the flow      You must continuously
                                      operating limit for     rate measurement        measure the scrubber
                                      the average scrubber    device during the PM    liquid flow rate,
                                      liquid flow rate.       performance test.       determine and record the
                                                                                      block average flow rate
                                                                                      values for the three test
                                                                                      runs, and determine and
                                                                                      record the 3-hour block
                                                                                      average of the recorded
                                                                                      flow rate measurements for
                                                                                      the three test runs. The
                                                                                      average of the three test
                                                                                      runs establishes your
                                                                                      minimum site-specific
                                                                                      liquid flow rate operating
                                                                                      limit.
11. Spray dryer....................  Establish the           Data from the           You must continuously
                                      operating limit for     temperature             measure the operating
                                      operating temperature.  measurement device      temperature, determine and
                                                              during the dioxin/      record the block average
                                                              furan performance       temperature values for the
                                                              test.                   three test runs, and
                                                                                      determine and record the 4-
                                                                                      hour block average of the
                                                                                      recorded temperature
                                                                                      measurements for the three
                                                                                      test runs. The average of
                                                                                      the three test runs
                                                                                      establishes your minimum
                                                                                      site-specific operating
                                                                                      limit.
12. Floor tile press dryer.........  Establish the           Data from the           You must continuously
                                      operating limit for     temperature             measure the operating
                                      operating temperature.  measurement device      temperature, determine and
                                                              during the dioxin/      record the block average
                                                              furan performance       temperature values for the
                                                              test.                   three test runs, and
                                                                                      determine and record the 4-
                                                                                      hour block average of the
                                                                                      recorded temperature
                                                                                      measurements for the three
                                                                                      test runs. The average of
                                                                                      the three test runs
                                                                                      establishes your maximum
                                                                                      site-specific operating
                                                                                      limit.
----------------------------------------------------------------------------------------------------------------

    Note 1: The standard deviation of the 12 1-hour temperature 
measurements is calculated as follows:
[GRAPHIC] [TIFF OMITTED] TR01NO19.007

Where:

[sigma] = standard deviation
xi = each 1-hour temperature measurement
[mu] = mean of all 12 1-hour measurements
N = 12 measurements


0
11. Table 6 to subpart KKKKK is revised to read as follows:

[[Page 58615]]



  Table 6 to Subpart KKKKK of Part 63--Initial Compliance With Emission
                 Limitations and Work Practice Standards
  As stated in Sec.   63.8605, you must demonstrate initial compliance
with each emission limitation and work practice standard that applies to
                  you according to the following table:
------------------------------------------------------------------------
                                                   You have demonstrated
        For each . . .          For the following  initial compliance if
                                      . . .                . . .
------------------------------------------------------------------------
1. Collection of all tunnel or  a. HF, HCl, and    i. You measure HF and
 roller kilns at the facility.   Cl2 emissions      HCl emissions for
                                 must not exceed    each kiln using
                                 62 kg/hr (140 lb/  Method 26 or 26A of
                                 hr) HCl            40 CFR part 60,
                                 equivalent.        appendix A-8 or its
                                                    alternative, ASTM
                                                    D6735-01 (Reapproved
                                                    2009) (incorporated
                                                    by reference, see
                                                    Sec.   63.14); or
                                                    Method 320 of
                                                    appendix A of this
                                                    part or its
                                                    alternative, ASTM
                                                    D6348-03 (Reapproved
                                                    2010) (incorporated
                                                    by reference, see
                                                    Sec.   63.14); and
                                                   ii. You calculate the
                                                    HCl-equivalent
                                                    emissions for HF for
                                                    each kiln using
                                                    Equation 4 to this
                                                    subpart; and
                                                   iii. You sum the HCl-
                                                    equivalent values
                                                    for all kilns at the
                                                    facility using
                                                    Equation 5 to this
                                                    subpart; and
                                                   iv. The facility
                                                    total HCl-equivalent
                                                    does not exceed 62
                                                    kg/hr (140 lb/hr).
2. Existing floor tile roller   a. PM emissions    i. The PM emissions
 kiln.                           must not exceed    measured using
                                 0.063 kg/Mg        Method 5 of 40 CFR
                                 (0.13 lb/ton) of   part 60, appendix A-
                                 fired product.     3 or Method 29 of 40
                                                    CFR part 60,
                                                    appendix A-8, over
                                                    the period of the
                                                    initial performance
                                                    test, according to
                                                    the calculations in
                                                    Sec.
                                                    63.8595(f)(1), do
                                                    not exceed 0.063 kg/
                                                    Mg (0.13 lb/ton) of
                                                    fired product; and
                                                   ii. You establish and
                                                    have a record of the
                                                    applicable operating
                                                    limits listed in
                                                    Table 2 to this
                                                    subpart over the
                                                    period of the
                                                    initial performance
                                                    test during which PM
                                                    emissions did not
                                                    exceed 0.063 kg/Mg
                                                    (0.13 lb/ton) of
                                                    fired product.
                                b. Hg emissions    i. The Hg emissions
                                 must not exceed    measured using
                                 6.3 E-05 kg/Mg     Method 29 of 40 CFR
                                 (1.3 E-04 lb/      part 60, appendix A-
                                 ton) of fired      8 or its
                                 product.           alternative, ASTM
                                                    D6784-02 (Reapproved
                                                    2008) (incorporated
                                                    by reference, see
                                                    Sec.   63.14), over
                                                    the period of the
                                                    initial performance
                                                    test, do not exceed
                                                    6.3 E-05 kg/Mg (1.3
                                                    E-04 lb/ton) of
                                                    fired product; and
                                                   ii. You establish and
                                                    have a record of the
                                                    operating limits
                                                    listed in Table 2 to
                                                    this subpart over
                                                    the period of the
                                                    initial performance
                                                    test during which Hg
                                                    emissions did not
                                                    exceed 6.3 E-05 kg/
                                                    Mg (1.3 E-04 lb/ton)
                                                    of fired product.
                                c. Dioxin/furan    i. The dioxin/furan
                                 emissions must     emissions measured
                                 not exceed 2.8     using Method 23 of
                                 ng/kg of fired     40 CFR part 60,
                                 product.           appendix A-7, over
                                                    the period of the
                                                    initial performance
                                                    test, do not exceed
                                                    2.8 ng/kg of fired
                                                    product; and
                                                   ii. You establish and
                                                    have a record of the
                                                    operating limits
                                                    listed in Table 2 to
                                                    this subpart over
                                                    the period of the
                                                    initial performance
                                                    test during which
                                                    dioxin/furan
                                                    emissions did not
                                                    exceed 2.8 ng/kg of
                                                    fired product.
3. Existing wall tile roller    a. PM emissions    i. The PM emissions
 kiln.                           must not exceed    measured using
                                 0.19 kg/Mg (0.37   Method 5 of 40 CFR
                                 lb/ton) of fired   part 60, appendix A-
                                 product.           3 or Method 29 of 40
                                                    CFR part 60,
                                                    appendix A-8, over
                                                    the period of the
                                                    initial performance
                                                    test, according to
                                                    the calculations in
                                                    Sec.
                                                    63.8595(f)(1), do
                                                    not exceed 0.19 kg/
                                                    Mg (0.37 lb/ton) of
                                                    fired product; and
                                                   ii. You establish and
                                                    have a record of the
                                                    operating limits
                                                    listed in Table 2 to
                                                    this subpart over
                                                    the period of the
                                                    initial performance
                                                    test during which PM
                                                    emissions did not
                                                    exceed 0.19 kg/Mg
                                                    (0.37 lb/ton) of
                                                    fired product.
                                b. Hg emissions    i. The Hg emissions
                                 must not exceed    measured using
                                 1.1 E-04 kg/Mg     Method 29 of 40 CFR
                                 (2.1 E-04 lb/      part 60, appendix A-
                                 ton) of fired      8 or its
                                 product.           alternative, ASTM
                                                    D6784-02 (Reapproved
                                                    2008) (incorporated
                                                    by reference, see
                                                    Sec.   63.14), over
                                                    the period of the
                                                    initial performance
                                                    test, do not exceed
                                                    1.1 E-04 kg/Mg (2.1
                                                    E-04 lb/ton) of
                                                    fired product; and
                                                   ii. You establish and
                                                    have a record of the
                                                    operating limits
                                                    listed in Table 2 to
                                                    this subpart over
                                                    the period of the
                                                    initial performance
                                                    test during which Hg
                                                    emissions did not
                                                    exceed 1.1 E-04 kg/
                                                    Mg (2.1 E-04 lb/ton)
                                                    of fired product.
                                c. Dioxin/furan    i. The dioxin/furan
                                 emissions must     emissions measured
                                 not exceed 0.22    using Method 23 of
                                 ng/kg of fired     40 CFR part 60,
                                 product.           appendix A-7, over
                                                    the period of the
                                                    initial performance
                                                    test, do not exceed
                                                    0.22 ng/kg of fired
                                                    product; and
                                                   ii. You establish and
                                                    have a record of the
                                                    operating limits
                                                    listed in Table 2 to
                                                    this subpart over
                                                    the period of the
                                                    initial performance
                                                    test during which
                                                    dioxin/furan
                                                    emissions did not
                                                    exceed 0.22 ng/kg of
                                                    fired product.
4. Existing first-fire          a. PM emissions    i. The PM emissions
 sanitaryware tunnel kiln.       must not exceed    measured using
                                 0.17 kg/Mg (0.34   Method 5 of 40 CFR
                                 lb/ton) of         part 60, appendix A-
                                 greenware fired.   3 or Method 29 of 40
                                                    CFR part 60,
                                                    appendix A-8, over
                                                    the period of the
                                                    initial performance
                                                    test, according to
                                                    the calculations in
                                                    Sec.
                                                    63.8595(f)(1), do
                                                    not exceed 0.17 kg/
                                                    Mg (0.34 lb/ton) of
                                                    greenware fired; and

[[Page 58616]]

 
                                                   ii. You establish and
                                                    have a record of the
                                                    operating limits
                                                    listed in Table 2 to
                                                    this subpart over
                                                    the period of the
                                                    initial performance
                                                    test during which PM
                                                    emissions did not
                                                    exceed 0.17 kg/Mg
                                                    (0.34 lb/ton) of
                                                    greenware fired.
                                b. Hg emissions    i. The Hg emissions
                                 must not exceed    measured using
                                 1.3 E-04 kg/Mg     Method 29 of 40 CFR
                                 (2.6 E-04 lb/      part 60, appendix A-
                                 ton) of            8 or its
                                 greenware fired.   alternative, ASTM
                                                    D6784-02 (Reapproved
                                                    2008) (incorporated
                                                    by reference, see
                                                    Sec.   63.14), over
                                                    the period of the
                                                    initial performance
                                                    test, do not exceed
                                                    1.3 E-04 kg/Mg (2.6
                                                    E-04 lb/ton) of
                                                    greenware fired; and
                                                   ii. You establish and
                                                    have a record of the
                                                    operating limits
                                                    listed in Table 2 to
                                                    this subpart over
                                                    the period of the
                                                    initial performance
                                                    test during which Hg
                                                    emissions did not
                                                    exceed 1.3 E-04 kg/
                                                    Mg (2.6 E-04 lb/ton)
                                                    of greenware fired.
                                c. Dioxin/furan    i. The dioxin/furan
                                 emissions must     emissions measured
                                 not exceed 3.3     using Method 23 of
                                 ng/kg of           40 CFR part 60,
                                 greenware fired.   appendix A-7, over
                                                    the period of the
                                                    initial performance
                                                    test, do not exceed
                                                    3.3 ng/kg of
                                                    greenware fired; and
                                                   ii. You establish and
                                                    have a record of the
                                                    operating limits
                                                    listed in Table 2 to
                                                    this subpart over
                                                    the period of the
                                                    initial performance
                                                    test during which
                                                    dioxin/furan
                                                    emissions did not
                                                    exceed 3.3 ng/kg of
                                                    greenware fired.
5. Existing tile glaze line     a. PM emissions    i. The PM emissions
 with glaze spraying.            must not exceed    measured using
                                 0.93 kg/Mg (1.9    Method 5 of 40 CFR
                                 lb/ton) of first-  part 60, appendix A-
                                 fire glaze         3, over the period
                                 sprayed (dry       of the initial
                                 weight basis).     performance test,
                                                    according to the
                                                    calculations in Sec.
                                                      63.8595(f)(2), do
                                                    not exceed 0.93 kg/
                                                    Mg (1.9 lb/ton) of
                                                    first-fire glaze
                                                    sprayed (dry weight
                                                    basis); and
                                                   ii. You establish and
                                                    have a record of the
                                                    operating limits
                                                    listed in Table 2 to
                                                    this subpart over
                                                    the period of the
                                                    initial performance
                                                    test during which PM
                                                    emissions did not
                                                    exceed 0.93 kg/Mg
                                                    (1.9 lb/ton) of
                                                    first-fire glaze
                                                    sprayed (dry weight
                                                    basis).
                                b. Hg emissions    i. The Hg emissions
                                 must not exceed    measured using
                                 8.0 E-05 kg/Mg     Method 29 of 40 CFR
                                 (1.6 E-04 lb/      part 60, appendix A-
                                 ton) of first-     8 or its
                                 fire glaze         alternative, ASTM
                                 sprayed (dry       D6784-02 (Reapproved
                                 weight basis).     2008) (incorporated
                                                    by reference, see
                                                    Sec.   63.14), over
                                                    the period of the
                                                    initial performance
                                                    test, do not exceed
                                                    8.0 E-05 kg/Mg (1.6
                                                    E-04 lb/ton) of
                                                    first-fire glaze
                                                    sprayed (dry weight
                                                    basis); and
                                                   ii. You establish and
                                                    have a record of the
                                                    operating limits
                                                    listed in Table 2 to
                                                    this subpart over
                                                    the period of the
                                                    initial performance
                                                    test during which Hg
                                                    emissions did not
                                                    exceed 8.0 E-05 kg/
                                                    Mg (1.6 E-04 lb/ton)
                                                    of first-fire glaze
                                                    sprayed (dry weight
                                                    basis).
6. Existing sanitaryware        a. PM emissions    i. The PM emissions
 manual glaze application.       must not exceed    measured using
                                 18 kg/Mg (35 lb/   Method 5 of 40 CFR
                                 ton) of first-     part 60, appendix A-
                                 fire glaze         3, over the period
                                 sprayed (dry       of the initial
                                 weight basis).     performance test,
                                                    according to the
                                                    calculations in Sec.
                                                      63.8595(f)(2), do
                                                    not exceed 18 kg/Mg
                                                    (35 lb/ton) of first-
                                                    fire glaze sprayed
                                                    (dry weight basis);
                                                    and
                                                   ii. You establish and
                                                    have a record of the
                                                    operating limits
                                                    listed in Table 2 to
                                                    this subpart over
                                                    the period of the
                                                    initial performance
                                                    test during which PM
                                                    emissions did not
                                                    exceed 18 kg/Mg (35
                                                    lb/ton) of first-
                                                    fire glaze sprayed
                                                    (dry weight basis).
7. Existing sanitaryware spray  a. PM emissions    i. The PM emissions
 machine glaze application.      must not exceed    measured using
                                 6.2 kg/Mg (13 lb/  Method 5 of 40 CFR
                                 ton) of first-     part 60, appendix A-
                                 fire glaze         3, over the period
                                 sprayed (dry       of the initial
                                 weight basis).     performance test,
                                                    according to the
                                                    calculations in Sec.
                                                      63.8595(f)(2), do
                                                    not exceed 6.2 kg/Mg
                                                    (13 lb/ton) of first-
                                                    fire glaze sprayed
                                                    (dry weight basis);
                                                    and
                                                   ii. You establish and
                                                    have a record of the
                                                    operating limits
                                                    listed in Table 2 to
                                                    this subpart over
                                                    the period of the
                                                    initial performance
                                                    test during which PM
                                                    emissions did not
                                                    exceed 6.2 kg/Mg (13
                                                    lb/ton) of first-
                                                    fire glaze sprayed
                                                    (dry weight basis).
8. Existing sanitaryware robot  a. PM emissions    i. The PM emissions
 glaze application.              must not exceed    measured using
                                 4.5 kg/Mg (8.9     Method 5 of 40 CFR
                                 lb/ton) of first-  part 60, appendix A-
                                 fire glaze         3, over the period
                                 sprayed (dry       of the initial
                                 weight basis).     performance test,
                                                    according to the
                                                    calculations in Sec.
                                                      63.8595(f)(2), do
                                                    not exceed 4.5 kg/Mg
                                                    (8.9 lb/ton) of
                                                    first-fire glaze
                                                    sprayed (dry weight
                                                    basis); and
                                                   ii. You establish and
                                                    have a record of the
                                                    operating limits
                                                    listed in Table 2 to
                                                    this subpart over
                                                    the period of the
                                                    initial performance
                                                    test during which PM
                                                    emissions did not
                                                    exceed 4.5 kg/Mg
                                                    (8.9 lb/ton) of
                                                    first-fire glaze
                                                    sprayed (dry weight
                                                    basis).
9. Existing floor tile spray    a. Dioxin/furan    i. The dioxin/furan
 dryer.                          emissions must     emissions measured
                                 not exceed 19 ng/  using Method 23 of
                                 kg of throughput   40 CFR part 60,
                                 processed.         appendix A-7, over
                                                    the period of the
                                                    initial performance
                                                    test, do not exceed
                                                    19 ng/kg of
                                                    throughput
                                                    processed; and
                                                   ii. You establish and
                                                    have a record of the
                                                    operating limits
                                                    listed in Table 2 to
                                                    this subpart over
                                                    the period of the
                                                    initial performance
                                                    test during which
                                                    dioxin/furan
                                                    emissions did not
                                                    exceed 19 ng/kg of
                                                    throughput
                                                    processed.

[[Page 58617]]

 
10. Existing wall tile spray    a. Dioxin/furan    i. The dioxin/furan
 dryer.                          emissions must     emissions measured
                                 not exceed 0.058   using Method 23 of
                                 ng/kg of           40 CFR part 60,
                                 throughput         appendix A-7, over
                                 processed.         the period of the
                                                    initial performance
                                                    test, do not exceed
                                                    0.058 ng/kg of
                                                    throughput
                                                    processed; and
                                                   ii. You establish and
                                                    have a record of the
                                                    operating limits
                                                    listed in Table 2 to
                                                    this subpart over
                                                    the period of the
                                                    initial performance
                                                    test during which
                                                    dioxin/furan
                                                    emissions did not
                                                    exceed 0.058 ng/kg
                                                    of throughput
                                                    processed.
11. Existing floor tile press   a. Dioxin/furan    i. The dioxin/furan
 dryer.                          emissions must     emissions measured
                                 not exceed 0.024   using Method 23 of
                                 ng/kg of           40 CFR part 60,
                                 throughput         appendix A-7, over
                                 processed.         the period of the
                                                    initial performance
                                                    test, do not exceed
                                                    0.024 ng/kg of
                                                    throughput
                                                    processed; and
                                                   ii. You establish and
                                                    have a record of the
                                                    operating limits
                                                    listed in Table 2 to
                                                    this subpart over
                                                    the period of the
                                                    initial performance
                                                    test during which
                                                    dioxin/furan
                                                    emissions did not
                                                    exceed 0.024 ng/kg
                                                    of throughput
                                                    processed.
12. New or reconstructed floor  a. PM emissions    i. The PM emissions
 tile roller kiln.               must not exceed    measured using
                                 0.019 kg/Mg        Method 5 of 40 CFR
                                 (0.037 lb/ton)     part 60, appendix A-
                                 of fired product.  3 or Method 29 of 40
                                                    CFR part 60,
                                                    appendix A-8, over
                                                    the period of the
                                                    initial performance
                                                    test, according to
                                                    the calculations in
                                                    Sec.
                                                    63.8595(f)(1), do
                                                    not exceed 0.019 kg/
                                                    Mg (0.037 lb/ton) of
                                                    fired product; and
                                                   ii. You establish and
                                                    have a record of the
                                                    operating limits
                                                    listed in Table 2 to
                                                    this subpart over
                                                    the period of the
                                                    initial performance
                                                    test during which PM
                                                    emissions did not
                                                    exceed 0.019 kg/Mg
                                                    (0.037 lb/ton) of
                                                    fired product.
                                b. Hg emissions    i. The Hg emissions
                                 must not exceed    measured using
                                 2.0 E-05 kg/Mg     Method 29 of 40 CFR
                                 (3.9 E-05 lb/      part 60, appendix A-
                                 ton) of fired      8 or its
                                 product.           alternative, ASTM
                                                    D6784-02 (Reapproved
                                                    2008) (incorporated
                                                    by reference, see
                                                    Sec.   63.14), over
                                                    the period of the
                                                    initial performance
                                                    test, do not exceed
                                                    2.0 E-05 kg/Mg (3.9
                                                    E-05 lb/ton) of
                                                    fired product; and
                                                   ii. You establish and
                                                    have a record of the
                                                    operating limits
                                                    listed in Table 2 to
                                                    this subpart over
                                                    the period of the
                                                    initial performance
                                                    test during which Hg
                                                    emissions did not
                                                    exceed 2.0 E-05 kg/
                                                    Mg (3.9 E-05 lb/ton)
                                                    of fired product.
                                c. Dioxin/furan    i. The dioxin/furan
                                 emissions must     emissions measured
                                 not exceed 1.3     using Method 23 of
                                 ng/kg of fired     40 CFR part 60,
                                 product.           appendix A-7, over
                                                    the period of the
                                                    initial performance
                                                    test, do not exceed
                                                    1.3 ng/kg of fired
                                                    product; and
                                                   ii. You establish and
                                                    have a record of the
                                                    operating limits
                                                    listed in Table 2 to
                                                    this subpart over
                                                    the period of the
                                                    initial performance
                                                    test during which
                                                    dioxin/furan
                                                    emissions did not
                                                    exceed 1.3 ng/kg of
                                                    fired product.
13. New or reconstructed wall   a. PM emissions    i. The PM emissions
 tile roller kiln.               must not exceed    measured using
                                 0.19 kg/Mg (0.37   Method 5 of 40 CFR
                                 lb/ton) of fired   part 60, appendix A-
                                 product.           3 or Method 29 of 40
                                                    CFR part 60,
                                                    appendix A-8, over
                                                    the period of the
                                                    initial performance
                                                    test, according to
                                                    the calculations in
                                                    Sec.
                                                    63.8595(f)(1), do
                                                    not exceed 0.19 kg/
                                                    Mg (0.37 lb/ton) of
                                                    fired product; and
                                                   ii. You establish and
                                                    have a record of the
                                                    operating limits
                                                    listed in Table 2 to
                                                    this subpart over
                                                    the period of the
                                                    initial performance
                                                    test during which PM
                                                    emissions did not
                                                    exceed 0.19 kg/Mg
                                                    (0.37 lb/ton) of
                                                    fired product.
                                b. Hg emissions    i. The Hg emissions
                                 must not exceed    measured using
                                 1.1 E-04 kg/Mg     Method 29 of 40 CFR
                                 (2.1 E-04 lb/      part 60, appendix A-
                                 ton) of fired      8 or its
                                 product.           alternative, ASTM
                                                    D6784-02 (Reapproved
                                                    2008) (incorporated
                                                    by reference, see
                                                    Sec.   63.14), over
                                                    the period of the
                                                    initial performance
                                                    test, do not exceed
                                                    1.1 E-04 kg/Mg (2.1
                                                    E-04 lb/ton) of
                                                    fired product; and
                                                   ii. You establish and
                                                    have a record of the
                                                    operating limits
                                                    listed in Table 2 to
                                                    this subpart over
                                                    the period of the
                                                    initial performance
                                                    test during which Hg
                                                    emissions did not
                                                    exceed 1.1 E-04 kg/
                                                    Mg (2.1 E-04 lb/ton)
                                                    of fired product.
                                c. Dioxin/furan    i. The dioxin/furan
                                 emissions must     emissions measured
                                 not exceed 0.22    using Method 23 of
                                 ng/kg of fired     40 CFR part 60,
                                 product.           appendix A-7, over
                                                    the period of the
                                                    initial performance
                                                    test, do not exceed
                                                    0.22 ng/kg of fired
                                                    product; and
                                                   ii. You establish and
                                                    have a record of the
                                                    operating limits
                                                    listed in Table 2 to
                                                    this subpart over
                                                    the period of the
                                                    initial performance
                                                    test during which
                                                    dioxin/furan
                                                    emissions did not
                                                    exceed 0.22 ng/kg of
                                                    fired product.

[[Page 58618]]

 
14. New or reconstructed first- a. PM emissions    i. The PM emissions
 fire sanitaryware tunnel kiln.  must not exceed    measured using
                                 0.048 kg/Mg        Method 5 of 40 CFR
                                 (0.095 lb/ton)     part 60, appendix A-
                                 of greenware       3 or Method 29 of 40
                                 fired.             CFR part 60,
                                                    appendix A-8, over
                                                    the period of the
                                                    initial performance
                                                    test, according to
                                                    the calculations in
                                                    Sec.
                                                    63.8595(f)(1), do
                                                    not exceed 0.048 kg/
                                                    Mg (0.095 lb/ton) of
                                                    greenware fired; and
                                                   ii. You establish and
                                                    have a record of the
                                                    operating limits
                                                    listed in Table 2 to
                                                    this subpart over
                                                    the period of the
                                                    initial performance
                                                    test during which PM
                                                    emissions did not
                                                    exceed 0.048 kg/Mg
                                                    (0.095 lb/ton) of
                                                    greenware fired.
                                b. Hg emissions    i. The Hg emissions
                                 must not exceed    measured using
                                 6.1 E-05 kg/Mg     Method 29 of 40 CFR
                                 (1.3 E-04 lb/      part 60, appendix A-
                                 ton) of            8 or its
                                 greenware fired.   alternative, ASTM
                                                    D6784-02 (Reapproved
                                                    2008) (incorporated
                                                    by reference, see
                                                    Sec.   63.14), over
                                                    the period of the
                                                    initial performance
                                                    test, do not exceed
                                                    6.1 E-05 kg/Mg (1.3
                                                    E-04 lb/ton) of
                                                    greenware fired; and
                                                   ii. You establish and
                                                    have a record of the
                                                    operating limits
                                                    listed in Table 2 to
                                                    this subpart over
                                                    the period of the
                                                    initial performance
                                                    test during which Hg
                                                    emissions did not
                                                    exceed 6.1 E-05 kg/
                                                    Mg (1.3 E-04 lb/ton)
                                                    of greenware fired.
                                c. Dioxin/furan    i. The dioxin/furan
                                 emissions must     emissions measured
                                 not exceed 0.99    using Method 23 of
                                 ng/kg of           40 CFR part 60,
                                 greenware fired.   appendix A-7, over
                                                    the period of the
                                                    initial performance
                                                    test, do not exceed
                                                    0.99 ng/kg of
                                                    greenware fired; and
                                                   ii. You establish and
                                                    have a record of the
                                                    operating limits
                                                    listed in Table 2 to
                                                    this subpart over
                                                    the period of the
                                                    initial performance
                                                    test during which
                                                    dioxin/furan
                                                    emissions did not
                                                    exceed 0.99 ng/kg of
                                                    greenware fired.
15. New or reconstructed tile   a. PM emissions    i. The PM emissions
 glaze line with glaze           must not exceed    measured using
 spraying.                       0.31 kg/Mg (0.61   Method 5 of 40 CFR
                                 lb/ton) of first-  part 60, appendix A-
                                 fire glaze         3, over the period
                                 sprayed (dry       of the initial
                                 weight basis).     performance test,
                                                    according to the
                                                    calculations in Sec.
                                                      63.8595(f)(2), do
                                                    not exceed 0.31 kg/
                                                    Mg (0.61 lb/ton) of
                                                    first-fire glaze
                                                    sprayed (dry weight
                                                    basis); and
                                                   ii. You establish and
                                                    have a record of the
                                                    operating limits
                                                    listed in Table 2 to
                                                    this subpart over
                                                    the period of the
                                                    initial performance
                                                    test during which PM
                                                    emissions did not
                                                    exceed 0.31 kg/Mg
                                                    (0.61 lb/ton) of
                                                    first-fire glaze
                                                    sprayed (dry weight
                                                    basis).
                                b. Hg emissions    i. The Hg emissions
                                 must not exceed    measured using
                                 8.0 E-05 kg/Mg     Method 29 of 40 CFR
                                 (1.6 E-04 lb/      part 60, appendix A-
                                 ton) of first-     8 or its
                                 fire glaze         alternative, ASTM
                                 sprayed (dry       D6784-02 (Reapproved
                                 weight basis).     2008) (incorporated
                                                    by reference, see
                                                    Sec.   63.14), over
                                                    the period of the
                                                    initial performance
                                                    test, do not exceed
                                                    8.0 E-05 kg/Mg (1.6
                                                    E-04 lb/ton) of
                                                    first-fire glaze
                                                    sprayed (dry weight
                                                    basis); and
                                                   ii. You establish and
                                                    have a record of the
                                                    operating limits
                                                    listed in Table 2 to
                                                    this subpart over
                                                    the period of the
                                                    initial performance
                                                    test during which Hg
                                                    emissions did not
                                                    exceed 8.0 E-05 kg/
                                                    Mg (1.6 E-04 lb/ton)
                                                    of first-fire glaze
                                                    sprayed (dry weight
                                                    basis).
16. New or reconstructed        a. PM emissions    i. The PM emissions
 sanitaryware manual glaze       must not exceed    measured using
 application.                    2.0 kg/Mg (3.9     Method 5 of 40 CFR
                                 lb/ton) of first-  part 60, appendix A-
                                 fire glaze         3, over the period
                                 sprayed (dry       of the initial
                                 weight basis).     performance test,
                                                    according to the
                                                    calculations in Sec.
                                                      63.8595(f)(2), do
                                                    not exceed 2.0 kg/Mg
                                                    (3.9 lb/ton) of
                                                    first-fire glaze
                                                    sprayed (dry weight
                                                    basis); and
                                                   ii. You establish and
                                                    have a record of the
                                                    operating limits
                                                    listed in Table 2 to
                                                    this subpart over
                                                    the period of the
                                                    initial performance
                                                    test during which PM
                                                    emissions did not
                                                    exceed 2.0 kg/Mg
                                                    (3.9 lb/ton) of
                                                    first-fire glaze
                                                    sprayed (dry weight
                                                    basis).
17. New or reconstructed        a. PM emissions    i. The PM emissions
 sanitaryware spray machine      must not exceed    measured using
 glaze application.              1.6 kg/Mg (3.2     Method 5 of 40 CFR
                                 lb/ton) of first-  part 60, appendix A-
                                 fire glaze         3, over the period
                                 sprayed (dry       of the initial
                                 weight basis).     performance test,
                                                    according to the
                                                    calculations in Sec.
                                                      63.8595(f)(2), do
                                                    not exceed 1.6 kg/Mg
                                                    (3.2 lb/ton) of
                                                    first-fire glaze
                                                    sprayed (dry weight
                                                    basis); and
                                                   ii. You establish and
                                                    have a record of the
                                                    operating limits
                                                    listed in Table 2 to
                                                    this subpart over
                                                    the period of the
                                                    initial performance
                                                    test during which PM
                                                    emissions did not
                                                    exceed 1.6 kg/Mg
                                                    (3.2 lb/ton) of
                                                    first-fire glaze
                                                    sprayed (dry weight
                                                    basis).
18. New or reconstructed        a. PM emissions    i. The PM emissions
 sanitaryware robot glaze        must not exceed    measured using
 application.                    1.2 kg/Mg (2.3     Method 5 of 40 CFR
                                 lb/ton) of first-  part 60, appendix A-
                                 fire glaze         3, over the period
                                 sprayed (dry       of the initial
                                 weight basis).     performance test,
                                                    according to the
                                                    calculations in Sec.
                                                      63.8595(f)(2), do
                                                    not exceed 1.2 kg/Mg
                                                    (2.3 lb/ton) of
                                                    first-fire glaze
                                                    sprayed (dry weight
                                                    basis); and
                                                   ii. You establish and
                                                    have a record of the
                                                    operating limits
                                                    listed in Table 2 to
                                                    this subpart over
                                                    the period of the
                                                    initial performance
                                                    test during which PM
                                                    emissions did not
                                                    exceed 1.2 kg/Mg
                                                    (2.3 lb/ton) of
                                                    first-fire glaze
                                                    sprayed (dry weight
                                                    basis).

[[Page 58619]]

 
19. New or reconstructed floor  a. Dioxin/furan    i. The dioxin/furan
 tile spray dryer.               emissions must     emissions measured
                                 not exceed 0.071   using Method 23 of
                                 ng/kg of           40 CFR part 60,
                                 throughput         appendix A-7, over
                                 processed.         the period of the
                                                    initial performance
                                                    test, do not exceed
                                                    0.071 ng/kg of
                                                    throughput
                                                    processed; and
                                                   ii. You establish and
                                                    have a record of the
                                                    operating limits
                                                    listed in Table 2 to
                                                    this subpart over
                                                    the period of the
                                                    initial performance
                                                    test during which
                                                    dioxin/furan
                                                    emissions did not
                                                    exceed 0.071 ng/kg
                                                    of throughput
                                                    processed.
20. New or reconstructed wall   a. Dioxin/furan    i. The dioxin/furan
 tile spray dryer.               emissions must     emissions measured
                                 not exceed 0.058   using Method 23 of
                                 ng/kg of           40 CFR part 60,
                                 throughput         appendix A-7, over
                                 processed.         the period of the
                                                    initial performance
                                                    test, do not exceed
                                                    0.058 ng/kg of
                                                    throughput
                                                    processed; and
                                                   ii. You establish and
                                                    have a record of the
                                                    operating limits
                                                    listed in Table 2 to
                                                    this subpart over
                                                    the period of the
                                                    initial performance
                                                    test during which
                                                    dioxin/furan
                                                    emissions did not
                                                    exceed 0.058 ng/kg
                                                    of throughput
                                                    processed.
21. New or reconstructed floor  a. Dioxin/furan    i. The dioxin/furan
 tile press dryer.               emissions must     emissions measured
                                 not exceed 0.024   using Method 23 of
                                 ng/kg of           40 CFR part 60,
                                 throughput         appendix A-7, over
                                 processed.         the period of the
                                                    initial performance
                                                    test, do not exceed
                                                    0.024 ng/kg of
                                                    throughput
                                                    processed; and
                                                   ii. You establish and
                                                    have a record of the
                                                    operating limits
                                                    listed in Table 2 to
                                                    this subpart over
                                                    the period of the
                                                    initial performance
                                                    test during which
                                                    dioxin/furan
                                                    emissions did not
                                                    exceed 0.024 ng/kg
                                                    of throughput
                                                    processed.
22. Existing, new, or           a. Minimize HAP    i. Use natural gas,
 reconstructed sanitaryware      emissions.         or equivalent, as
 shuttle kiln.                                      the kiln fuel; and
                                                   ii. Develop a
                                                    designed firing time
                                                    and temperature
                                                    cycle for the
                                                    sanitaryware shuttle
                                                    kiln. You must
                                                    either program the
                                                    time and temperature
                                                    cycle into your kiln
                                                    or track each step
                                                    on a log sheet; and
                                                   iii. Label each
                                                    sanitaryware shuttle
                                                    kiln with the
                                                    maximum load (in
                                                    tons) of greenware
                                                    that can be fired in
                                                    the kiln during a
                                                    single firing cycle;
                                                    and
                                                   iv. Develop
                                                    maintenance
                                                    procedures for each
                                                    kiln that, at a
                                                    minimum, specify the
                                                    frequency of
                                                    inspection and
                                                    maintenance of
                                                    temperature
                                                    monitoring devices,
                                                    controls that
                                                    regulate air-to-fuel
                                                    ratios, and controls
                                                    that regulate firing
                                                    cycles.
------------------------------------------------------------------------


0
12. Table 7 to subpart KKKKK is revised to read as follows:

Table 7 to Subpart KKKKK of Part 63--Continuous Compliance With Emission Limitations and Work Practice Standards
 As stated in Sec.   63.8620, you must demonstrate continuous compliance with each emission limitation and work
                     practice standard that applies to you according to the following table:
----------------------------------------------------------------------------------------------------------------
                                                              You must demonstrate
          For each . . .            For the following . .  continuous compliance by .         Or by . . .
                                              .                        . .
----------------------------------------------------------------------------------------------------------------
1. Tunnel or roller kiln equipped   a. Each emission       i. If you use a bag leak    (1) Performing VE
 with a DIFF or DLS/FF.              limit in Table 1 to    detection system, as        observations of the DIFF
                                     this subpart and       prescribed in Sec.          or DLS/FF stack at the
                                     each operating limit   63.8450(e), initiating      frequency specified in
                                     in Item 1 of Table 2   corrective action within    Sec.   63.8620(e) using
                                     to this subpart for    1 hour of a bag leak        Method 22 of 40 CFR part
                                     kilns equipped with    detection system alarm      60, appendix A-7; and
                                     DIFF or DLS/FF.        and completing corrective   maintaining no VE from
                                                            actions in accordance       the DIFF or DLS/FF
                                                            with your OM&M plan;        stack; or
                                                            operating and maintaining  (2) Maintaining your kiln
                                                            the fabric filter such      operating temperature
                                                            that the alarm is not       within the range of
                                                            engaged for more than 5     acceptable temperatures
                                                            percent of the total        (i.e., temperature
                                                            operating time in a 6-      profile for each kiln
                                                            month block reporting       and product; for any
                                                            period; in calculating      incidence where the kiln
                                                            this operating time         is operating outside of
                                                            fraction, if inspection     its acceptable
                                                            of the fabric filter        temperature range (i.e.,
                                                            demonstrates that no        exceeds its temperature
                                                            corrective action is        profile) for the product
                                                            required, no alarm time     being fired, performing
                                                            is counted; if corrective   VE observations of the
                                                            action is required, each    DIFF or DLS/FF stack as
                                                            alarm is counted as a       specified in Sec.
                                                            minimum of 1 hour; if you   63.8620(e) using Method
                                                            take longer than 1 hour     22 of 40 CFR part 60,
                                                            to initiate corrective      appendix A-7; and
                                                            action, the alarm time is   observing no VE from the
                                                            counted as the actual       DIFF or DLS/FF stack.
                                                            amount of time taken by
                                                            you to initiate
                                                            corrective action; and

[[Page 58620]]

 
                                                           ii. Verifying that lime is
                                                            free-flowing via a load
                                                            cell, carrier gas/lime
                                                            flow indicator, carrier
                                                            gas pressure drop
                                                            measurement system, or
                                                            other system; recording
                                                            all monitor or sensor
                                                            output, and if lime is
                                                            found not to be free
                                                            flowing, promptly
                                                            initiating and completing
                                                            corrective actions in
                                                            accordance with your OM&M
                                                            plan; recording the
                                                            feeder setting once each
                                                            shift of operation to
                                                            verify that the feeder
                                                            setting is being
                                                            maintained at or above
                                                            the level established
                                                            during the HF/HCl
                                                            performance test in which
                                                            compliance was
                                                            demonstrated.
2. Tunnel or roller kiln equipped   a. Each emission       i. Collecting the scrubber
 with a WS.                          limit in Table 1 to    liquid pH data according
                                     this subpart and       to Sec.   63.8600(a);
                                     each operating limit   reducing the scrubber
                                     in Item 2 of Table 2   liquid pH data to 3-hour
                                     to this subpart for    block averages according
                                     kilns equipped with    to Sec.   63.8600(a);
                                     WS.                    maintaining the average
                                                            scrubber liquid pH for
                                                            each 3-hour block period
                                                            at or above the average
                                                            scrubber liquid pH
                                                            established during the HF/
                                                            HCl performance test in
                                                            which compliance was
                                                            demonstrated; and
                                                           ii. Collecting the
                                                            scrubber liquid flow rate
                                                            data according to Sec.
                                                            63.8600(a); reducing the
                                                            scrubber liquid flow rate
                                                            data to 3-hour block
                                                            averages according to
                                                            Sec.   63.8600(a);
                                                            maintaining the average
                                                            scrubber liquid flow rate
                                                            for each 3-hour block
                                                            period at or above the
                                                            highest average scrubber
                                                            liquid flow rate
                                                            established during the HF/
                                                            HCl and PM performance
                                                            tests in which compliance
                                                            was demonstrated.
3. Tunnel or roller kiln equipped   Each emission limit    Collecting the carbon flow
 with an ACI system.                 in Table 1 to this     rate data according to
                                     subpart and each       Sec.   63.8600(a);
                                     operating limit in     reducing the carbon flow
                                     Item 3 of Table 2 to   rate data to 3-hour block
                                     this subpart for       averages according to
                                     kilns equipped with    Sec.   63.8600(a);
                                     ACI system.            maintaining the average
                                                            carbon flow rate for each
                                                            3-hour block period at or
                                                            above the highest average
                                                            carbon flow rate
                                                            established during the Hg
                                                            and dioxin/furan
                                                            performance tests in
                                                            which compliance was
                                                            demonstrated.
4. Tunnel or roller kiln intending  Each emission limit    Collecting the operating    Collecting the operating
 to comply with dioxin/furan         in Table 1 to this     temperature data            temperature data
 emission limit without an ACI       subpart and each       according to Sec.           according to Sec.
 system.                             operating limit in     63.8600(a); and             63.8600(a); reducing the
                                     Item 4 of Table 2 to   maintaining the operating   operating temperature
                                     this subpart for       temperature at or below     data to a 12-hour block
                                     kilns intending to     the highest operating       average; and maintaining
                                     comply with dioxin/    temperature established     the average operating
                                     furan emission limit   during the dioxin/furan     temperature for each 12-
                                     without an ACI         performance test in which   hour block period at or
                                     system.                compliance was              below the highest
                                                            demonstrated.               operating temperature
                                                                                        established during the
                                                                                        dioxin/furan performance
                                                                                        test in which compliance
                                                                                        was demonstrated.
5. Tunnel or roller kiln with no    a. Each emission       i. Performing VE            (1) Maintaining your kiln
 add-on control.                     limit in Table 1 to    observations of the stack   operating temperature
                                     this subpart and       at the frequency            within the range of
                                     each operating limit   specified in Sec.           acceptable temperatures
                                     in Item 5 of Table 2   63.8620(e) using Method     (i.e., temperature
                                     to this subpart for    22 of 40 CFR part 60,       profile established for
                                     tunnel or roller       appendix A-7; and           each kiln and product
                                     kilns with no add-on   maintaining no VE from      for any incidence where
                                     control.               the stack; and              the kiln is operating
                                                                                        outside of its
                                                                                        acceptable temperature
                                                                                        range (i.e., exceeds its
                                                                                        temperature profile) for
                                                                                        the product being fired,
                                                                                        performing VE
                                                                                        observations of the DIFF
                                                                                        or DLS/FF stack as
                                                                                        specified in Sec.
                                                                                        63.8620(e) using Method
                                                                                        22 of 40 CFR part 60,
                                                                                        appendix A-7; and
                                                                                        observing no VE from the
                                                                                        DIFF or DLS/FF stack.

[[Page 58621]]

 
                                                           ii. If your last
                                                            calculated total facility
                                                            maximum potential HCl-
                                                            equivalent was not at or
                                                            below the health-based
                                                            standard in Table 1 to
                                                            this subpart, collecting
                                                            the kiln process rate
                                                            data according to Sec.
                                                            63.8600(a); reducing the
                                                            kiln process rate data to
                                                            3-hour block averages
                                                            according to Sec.
                                                            63.8600(a); maintaining
                                                            the average kiln process
                                                            rate for each 3-hour
                                                            block period at or below
                                                            the kiln process rate
                                                            determined according to
                                                            Sec.   63.8595(g)(1); and
                                                           iii. Collecting the         (1) Collecting the
                                                            operating temperature       operating temperature
                                                            data according to Sec.      data according to Sec.
                                                            63.8600(a); and             63.8600(a); reducing the
                                                            maintaining the operating   operating temperature
                                                            temperature at or below     data to a 12-hour block
                                                            the highest operating       average; and maintaining
                                                            temperature established     the average operating
                                                            during the dioxin/furan     temperature for each 12-
                                                            performance test in which   hour block period at or
                                                            compliance was              below the highest
                                                            demonstrated.               operating temperature
                                                                                        established during the
                                                                                        dioxin/furan performance
                                                                                        test in which compliance
                                                                                        was demonstrated.
6. Glaze spray operation equipped   Each emission limit    If you use a bag leak       Performing VE
 with a FF.                          in Table 1 to this     detection system,           observations of the FF
                                     subpart and each       initiating corrective       stack at the frequency
                                     operating limit in     action within 1 hour of a   specified in Sec.
                                     Item 6 of Table 2 to   bag leak detection system   63.8620(e) using Method
                                     this subpart for       alarm and completing        22 of 40 CFR part 60,
                                     glaze spray            corrective actions in       appendix A-7; and
                                     operations equipped    accordance with your OM&M   maintaining no VE from
                                     with a FF.             plan; operating and         the FF stack.
                                                            maintaining the fabric
                                                            filter such that the
                                                            alarm is not engaged for
                                                            more than 5 percent of
                                                            the total operating time
                                                            in a 6-month block
                                                            reporting period; in
                                                            calculating this
                                                            operating time fraction,
                                                            if inspection of the
                                                            fabric filter
                                                            demonstrates that no
                                                            corrective action is
                                                            required, no alarm time
                                                            is counted; if corrective
                                                            action is required, each
                                                            alarm is counted as a
                                                            minimum of 1 hour; if you
                                                            take longer than 1 hour
                                                            to initiate corrective
                                                            action, the alarm time is
                                                            counted as the actual
                                                            amount of time taken by
                                                            you to initiate
                                                            corrective action.
7. Glaze spray operation equipped   a. Each emission       i. Collecting the scrubber
 with a WS.                          limit in Table 1 to    pressure drop data
                                     this subpart and       according to Sec.
                                     each operating limit   63.8600(a); reducing the
                                     in Item 7 of Table 2   scrubber pressure drop
                                     to this subpart for    data to 3-hour block
                                     kilns equipped with    averages according to
                                     WS.                    Sec.   63.8600(a);
                                                            maintaining the average
                                                            scrubber pressure drop
                                                            for each 3-hour block
                                                            period at or above the
                                                            average pressure drop
                                                            established during the PM
                                                            performance test in which
                                                            compliance was
                                                            demonstrated; and
                                                           ii. Collecting the
                                                            scrubber liquid flow rate
                                                            data according to Sec.
                                                            63.8600(a); reducing the
                                                            scrubber liquid flow rate
                                                            data to 3-hour block
                                                            averages according to
                                                            Sec.   63.8600(a);
                                                            maintaining the average
                                                            scrubber liquid flow rate
                                                            for each 3-hour block
                                                            period at or above the
                                                            average scrubber liquid
                                                            flow rate established
                                                            during the PM performance
                                                            test in which compliance
                                                            was demonstrated.
8. Glaze spray operation equipped   a. Each emission       i. Conducting daily
 with a water curtain.               limit in Table 1 to    inspections to verify the
                                     this subpart and       presence of water flow to
                                     each operating limit   the wet control system;
                                     in Item 8 of Table 2   and
                                     to this subpart for
                                     kilns equipped with
                                     a water curtain.

[[Page 58622]]

 
                                                           ii. Conducting annual
                                                            inspections of the
                                                            interior of the control
                                                            equipment (if applicable)
                                                            to determine the
                                                            structural integrity and
                                                            condition of the control
                                                            equipment; and
                                                           iii. Recording as
                                                            deviations any
                                                            observations of
                                                            particulates or other
                                                            impurities getting into
                                                            the glaze that has been
                                                            sprayed onto a piece of
                                                            ware and completing
                                                            corrective actions in
                                                            accordance with your OM&M
                                                            plan.
9. Glaze spray operation equipped   Each emission limit    Conducting an annual
 with baffles.                       in Table 1 to this     visual inspection of the
                                     subpart and each       baffles to confirm the
                                     operating limit in     baffles are in place.
                                     Item 9 of Table 2 to
                                     this subpart for
                                     kilns equipped with
                                     baffles.
10. Spray dryer...................  Each emission limit    Collecting the operating
                                     in Table 1 to this     temperature data
                                     subpart and each       according to Sec.
                                     operating limit in     63.8600(a); reducing the
                                     Item 10 of Table 2     operating temperature
                                     to this subpart for    data to 4-hour block
                                     spray dryers.          averages according to
                                                            Sec.   63.8600(a);
                                                            maintaining the average
                                                            operating temperature for
                                                            each 4-hour block period
                                                            at or above the average
                                                            operating temperature
                                                            established during the
                                                            dioxin/furan performance
                                                            test in which compliance
                                                            was demonstrated.
11. Floor tile press dryer........  Each emission limit    Collecting the operating
                                     in Table 1 to this     temperature data
                                     subpart and each       according to Sec.
                                     operating limit in     63.8600(a); reducing the
                                     Item 11 of Table 2     operating temperature
                                     to this subpart for    data to 4-hour block
                                     floor tile press       averages according to
                                     dryers.                Sec.   63.8600(a);
                                                            maintaining the average
                                                            operating temperature for
                                                            each 4-hour block period
                                                            at or below the average
                                                            operating temperature
                                                            established during the
                                                            dioxin/furan performance
                                                            test in which compliance
                                                            was demonstrated.
12. Sanitaryware shuttle kiln.....  a. Minimize HAP        i. Maintaining records
                                     emissions.             documenting your use of
                                                            natural gas, or an
                                                            equivalent fuel, as the
                                                            kiln fuel at all times
                                                            except during periods of
                                                            natural gas curtailment
                                                            or supply interruption;
                                                            and
                                                           ii. If you intend to use
                                                            an alternative fuel,
                                                            submitting a notification
                                                            of alternative fuel use
                                                            within 48 hours of the
                                                            declaration of a period
                                                            of natural gas
                                                            curtailment or supply
                                                            interruption, as defined
                                                            in Sec.   63.8665; and.
                                                           iii. Submitting a report
                                                            of alternative fuel use
                                                            within 10 working days
                                                            after terminating the use
                                                            of the alternative fuel,
                                                            as specified in Sec.
                                                            63.8635(g); and
                                                           iv. Using a designed
                                                            firing time and
                                                            temperature cycle for
                                                            each sanitaryware shuttle
                                                            kiln; and
                                                           v. For each firing load,
                                                            documenting the total
                                                            tonnage of greenware
                                                            placed in the kiln to
                                                            ensure that it is not
                                                            greater than the maximum
                                                            load identified in Item
                                                            1.a.iii of Table 3 to
                                                            this subpart; and
                                                           vi. Following maintenance
                                                            procedures for each kiln
                                                            that, at a minimum,
                                                            specify the frequency of
                                                            inspection and
                                                            maintenance of
                                                            temperature monitoring
                                                            devices, controls that
                                                            regulate air-to-fuel
                                                            ratios, and controls that
                                                            regulate firing cycles;
                                                            and

[[Page 58623]]

 
                                                           vii. Developing and
                                                            maintaining records for
                                                            each sanitaryware shuttle
                                                            kiln, as specified in
                                                            Sec.   63.8640.
----------------------------------------------------------------------------------------------------------------

[FR Doc. 2019-22812 Filed 10-31-19; 8:45 am]
 BILLING CODE 6560-50-P

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