Wisconsin Administrative Code
Department of Natural Resources
NR 400-499 - Environmental Protection - Air Pollution Control
Chapter NR 440 - Standards of performance for new stationary sources
Subchapter II - Standards of Performance
Section NR 440.35 - Primary lead smelters
Universal Citation: WI Admin Code ยง NR 440.35
Current through August 26, 2024
(1) APPLICABILITY AND DESIGNATION OF AFFECTED FACILITY.
(a) The provisions of this section
are applicable to the following affected facilities in primary lead smelters:
sintering machine, sintering machine discharge end, blast furnace, dross
reverberatory furnace, electric smelting furnace and converter.
(b) Any facility under par. (a) that
commences construction or modification after October 16, 1974, is subject to
the requirements of this section.
(2) DEFINITIONS. As used in this section, terms not defined in this subsection have the meanings given in s. NR 440.02.
(a) "Blast
furnace" means any reduction furnace to which sinter is charged and which forms
separate layers of molten slag and lead bullion.
(b) "Converter" means any vessel which lead
concentrate or bullion is charged and refined.
(c) "Dross reverberatory furnace" means any
furnace used for the removal or refining of impurities from lead
bullion.
(d) "Electric smelting
furnace" means any furnace in which the heat necessary for smelting of the lead
sulfide ore concentrate charge is generated by passing an electric current
through a portion of the molten mass in the furnace.
(e) "Primary lead smelter" means any
installation or any intermediate process engaged in the production of lead from
lead sulfide ore concentrates through the use of pyrometallurgical
techniques.
(f) "Sinter bed" means
the lead sulfide ore concentrate charge within a sintering machine.
(g) "Sintering machine" means any furnace in
which a lead sulfide ore concentrate charge is heated in the presence of air to
eliminate sulfur contained in the charge and to agglomerate the charge into a
hard porous mass called "sinter."
(h) "Sintering machine discharge end" means
any apparatus which receives sinter as it is discharged from the conveying
grate of a sintering machine.
(i)
"Sulfuric acid plant" means any facility producing sulfuric acid by the contact
process.
(3) STANDARD FOR PARTICULATE MATTER.
(a) On and after the
date on which the performance test required to be conducted by s.
NR 440.08 is
completed, no owner or operator subject to the provisions of this section may
cause to be discharged into the atmosphere from any blast furnace, dross
reverberatory furnace or sintering machine discharge end any gases which
contain particulate matter in excess of 50 mg/dscm (0.022 gr/dscf).
(4) STANDARD FOR SULFUR DIOXIDE.
(a) On and after the date on which the
performance test required to be conducted by s.
NR 440.08 is
completed, no owner or operator subject to the provisions of this section may
cause to be discharged into the atmosphere from any sintering machine, electric
smelting furnace, or converter gases which contain sulfur dioxide in excess of
0.065% by volume.
(5) STANDARD FOR VISIBLE EMISSIONS.
(a) On and
after the date on which the performance test required to be conducted by s.
NR 440.08 is
completed, no owner or operator subject to the provisions of this section may
cause to be discharged into the atmosphere from any blast furnace, dross
reverberatory furnace, or sintering machine discharge end any visible emissions
which exhibit greater than 20% opacity.
(b) On and after the date on which the
performance test required to be conducted by s.
NR 440.08 is
completed, no owner or operator subject to the provisions of this section may
cause to be discharged into the atmosphere from any affected facility that uses
a sulfuric acid plant to comply with the standard set forth in sub. (4), any
visible emissions which exhibit greater than 20% opacity.
(6) MONITORING OF OPERATIONS.
(a) The owner or operator of any primary lead
smelter subject to the provisions of this section shall install and operate:
1. A continuous monitoring system to monitor
and record the opacity of gases discharged into the atmosphere from any blast
furnace, dross reverberatory furnace, or sintering machine discharge end. The
span of this system shall be set at 80 to 100% opacity.
2. A continuous monitoring system to monitor
and record sulfur dioxide emissions discharged into the atmosphere from any
sintering machine, electric furnace or converter subject to sub. (4). The span
of this system shall be set at a sulfur dioxide concentration of 0.20% by
volume.
a. The continuous monitoring system
performance evaluation required under s.
NR 440.13(3) shall be completed prior to
the initial performance test required under s.
NR 440.08.
b.
For the purpose of the continuous monitoring system performance evaluation
required under s.
NR 440.13(3), the reference method
referred to under the Relative Accuracy Test Procedure in Performance
Specification 2 of 40 CFR part 60, Appendix B, incorporated by reference in s.
NR 440.17, shall be Method 6 of 40 CFR part 60, Appendix
A, incorporated by reference in s.
NR 440.17. For the performance evaluation, each
concentration measurement shall be of one hour duration. The pollutant gas used
to prepare the calibration gas mixtures required under Performance
Specification 2 of Appendix B and for calibration checks under s.
NR 440.13(4) shall be sulfur
dioxide.
(b)
Two-hour average sulfur dioxide concentrations shall be calculated and recorded
daily for the 12 consecutive 2-hour periods of each operating day. Each 2-hour
average shall be determined as the arithmetic mean of the appropriate 2
contiguous one-hour average sulfur dioxide concentrations provided by the
continuous monitoring system installed under par. (a).
(c) For the purpose of reports required under
s.
NR 440.07(3), periods of excess
emissions that shall be reported are defined as follows:
1. Opacity. Any 6-minute period during which
the average opacity, as measured by the continuous monitoring system installed
under par. (a), exceeds the standard under sub. (5) (a).
2. Sulfur dioxide. Any 2-hour period, as
described in par. (b), during which the average emissions of sulfur dioxide, as
measured by the continuous monitoring system installed under par. (a), exceeds
the standard under sub. (4).
(7) TEST METHODS AND PROCEDURES.
(a) In conducting the performance tests
required in s.
NR 440.08, the
owner or operator shall use as reference methods and procedures the methods in
Appendix A of 40 CFR part 60, incorporated by reference in s.
NR 440.17, or other methods and procedures as specified
in s.
NR 440.08(2).
(b) The owner or operator shall determine
compliance with the particulate matter, sulfur dioxide (SO2) and visible
emission standards in subs. (3) to (5) as follows:
1. Method 5 shall be used to determine the
particulate matter concentration. The sampling time and sample volume for each
run shall be at least 60 minutes and 0.85 dscm (30 dscf).
2. The continuous monitoring system of sub.
(6) (a) 2. shall be used to determine the SO2 concentrations on a dry basis.
The sampling time for each run shall be 2 hours, and the average SO2
concentration for the 2-hour period shall be computed as in sub. (6) (b). The
monitoring system drift during the run may not exceed 2% of the span
value.
3. Method 9 and the
procedures in s.
NR 440.11 shall be used to determine opacity.
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