An owner or operator of an ethylene dichloride, vinyl
chloride, or polyvinyl chloride plant shall comply with the requirements of
this section.
(1) RELIEF VALVE
DISCHARGE. Except for an emergency relief discharge, there may be no discharge
to the atmosphere from any relief valve on any equipment in vinyl chloride
service. An emergency relief discharge means a discharge which could not have
been avoided by taking measures to prevent the discharge. Within 10 days of any
relief valve discharge, the owner or operator of the source from which the
relief valve discharge occurs shall submit to the department a report in
writing containing information on the source, nature and cause of the
discharge, the date and time of the discharge, the approximate total vinyl
chloride loss during the discharge, the method used for determining the vinyl
chloride loss, the action that was taken to prevent the discharge, and measures
adopted to prevent future discharges.
(2) FUGITIVE EMISSION SOURCES.
(a) Vinyl chloride emissions from loading and
unloading lines in vinyl chloride service which are opened to the atmosphere
after each loading and unloading operation shall be minimized as follows:
1. After each loading and unloading operation
and before opening a loading or unloading line to the atmosphere, the quantity
of vinyl chloride in all parts of each loading or unloading line that are to be
opened to the atmosphere shall be reduced so that the parts combined contain no
greater than 0.0038 cubic meter (0.13 cubic feet) of vinyl chloride, at
standard temperature and pressure.
2. Any vinyl chloride removed from a loading
or unloading line in accordance with subd. 1. shall be ducted through a control
system from which the concentration of vinyl chloride in the exhaust gases may
not exceed 10 parts per million, or equivalent as provided in s.
NR 449.08.
(b) During loading or unloading operations,
the vinyl chloride emissions from each slip gauge in vinyl chloride service
shall be minimized by ducting any vinyl chloride discharged from the slip gauge
through a control system from which the concentration of vinyl chloride in the
exhaust gases may not exceed 10 parts per million, or equivalent as provided in
s.
NR 449.08.
(c)
1.
Rotating pumps. Vinyl chloride emissions from seals on all rotating pumps in
vinyl chloride service shall be minimized by installing sealless pumps, pumps
with double mechanical seals, or equivalent as provided in s.
NR 449.08. If double mechanical seals are used, vinyl
chloride emissions from the seals shall be minimized by maintaining the
pressure between the 2 seals so that any leak that occurs is into the pump, by
ducting any vinyl chloride between the 2 seals through a control system from
which the concentration of vinyl chloride in the exhaust gases may not exceed
10 parts per million, or equivalent as provided in s.
NR 449.08.
2.
Reciprocating pumps. Vinyl chloride emissions from seals on all reciprocating
pumps in vinyl chloride service shall be minimized by installing double
outboard seals, or equivalent as provided in s.
NR 449.08. If double outboard seals are used, vinyl
chloride emissions from the seals shall be minimized by maintaining the
pressure between the 2 seals so that any leak that occurs is into the pump, by
ducting any vinyl chloride between the 2 seals through a control system from
which the concentration of vinyl chloride in the exhaust gases may not exceed
10 parts per million, or equivalent as provided in s.
NR 449.08.
3.
Rotating compressors. Vinyl chloride emissions from seals on all rotating
compressors in vinyl chloride service shall be minimized by installing
compressors with double mechanical seals, or equivalent as provided in s.
NR 449.08. If double mechanical seals are used, vinyl
chloride emissions from the seals shall be minimized by maintaining the
pressure between the 2 seals so that any leak that occurs is into the
compressor, by ducting any vinyl chloride between the 2 seals through a control
system from which the concentration of vinyl chloride in the exhaust gases may
not exceed 10 parts per million, or equivalent as provided in s.
NR 449.08.
4.
Reciprocating compressors. Vinyl chloride emissions from seals on all
reciprocating compressors in vinyl chloride service shall be minimized by
installing double outboard seals, or equivalent as provided in s.
NR 449.08. If double outboard seals are used, vinyl
chloride emissions from the seals shall be minimized by maintaining the
pressure between the 2 seals so that any leak that occurs is into the
compressor, by ducting any vinyl chloride between the 2 seals through a control
system from which the concentration of vinyl chloride in the exhaust gases may
not exceed 10 parts per million, or equivalent as provided in s.
NR 449.08.
5.
Agitators. Vinyl chloride emissions from seals on all agitators in vinyl
chloride service shall be minimized by installing agitators with double
mechanical seals, or equivalent as provided in s.
NR 449.08. If double mechanical seals are used, vinyl
chloride emissions from the seals shall be minimized by maintaining the
pressure between the 2 seals so that any leak that occurs is into the agitated
vessels, by ducting any vinyl chloride between the 2 seals through a control
system from which the concentration of vinyl chloride in the exhaust gases may
not exceed 10 parts per million, or equivalent as provided in s.
NR 449.08.
(d) Vinyl chloride emissions due to leakage
from each relief valve on equipment in vinyl chloride service shall be
minimized by installing a rupture disk between the equipment and the relief
valve, by connecting the relief valve discharge to a process line or recovery
system, or equivalent as provided in s.
NR 449.08.
(e) Except as provided in s.
NR 449.06(1) (c), all gases which are
manually vented from equipment in vinyl chloride service shall be ducted
through a control system from which the concentration of vinyl chloride in the
exhaust gases may not exceed 10 parts per million, or equivalent as provided in
s.
NR 449.08.
(f) Vinyl chloride emissions from opening of
equipment (including loading or unloading lines that are not opened to the
atmosphere after each loading or unloading operation) shall be minimized as
follows:
1. Before opening any equipment for
any reason, the quantity of vinyl chloride shall be reduced so that the
equipment contains no more than 2.0 % by volume vinyl chloride or 0.0950 cubic
meter (25 gallons) of vinyl chloride, whichever is larger, at standard
temperature and pressure.
2. Any
vinyl chloride removed from the equipment in accordance with subd. 1. shall be
ducted through a control system from which the concentration of vinyl chloride
in the exhaust gases may not exceed 10 parts per million, or equivalent as
provided in s.
NR 449.08.
(g) Unused portions of samples containing at
least 10% by weight vinyl chloride shall be returned to the process, and
sampling techniques shall be such that sample containers in vinyl chloride
service are purged into a closed process system.
(h) Vinyl chloride emissions due to leaks
from equipment in vinyl chloride service shall be minimized by instituting and
implementing a formal leak detection and elimination program. The owner or
operator of a source on which construction or modification commenced after
February 1, 1984 shall submit a description of the program to the department
for approval. The program shall be submitted within 45 days after startup
unless a waiver is granted by the department. If a waiver of compliance is
granted, the program is to be submitted on a date scheduled by the department.
Approval of a program shall be granted by the department provided it finds:
1. It includes a reliable and accurate vinyl
chloride monitoring system for detection of major leaks and identification of
the general area of the plant where a leak is located. A vinyl chloride
monitoring system means a device which obtains air samples from one or more
points on a continuous sequential basis and analyzes the samples with gas
chromatography or, if the owner or operator assumes that all hydrocarbons
measured are vinyl chloride, with infrared spectrophotometry flame ion
detection, or an equivalent or alternative method.
2. It includes a reliable and accurate
portable hydrocarbon detector to be used routinely to find small leaks and to
pinpoint the major leaks indicated by the vinyl chloride monitoring system. A
portable hydrocarbon detector means a device which measures hydrocarbons with a
sensitivity of at least 10 parts per million and is of such design and size
that it can be used to measure emissions from localized points.
3. It provides for an acceptable calibration
and maintenance schedule for the vinyl chloride monitoring system and portable
hydrocarbon detector. For the vinyl chloride monitoring system, a daily span
check shall be conducted with a concentration of vinyl chloride equal to the
concentration defined as a leak according to subd. 6. The calibration shall be
done with either one of the following:
a. A
calibration gas mixture prepared from the gases specified in section 5.2.1 and
5.2.2 and in accordance with section 7.1 of Method 106 of 40 CFR part 61, Appendix B, incorporated by reference in s.
NR 484.04(23).
b. A calibration gas cylinder standard
containing the appropriate concentration of vinyl chloride. The gas composition
of the calibration gas cylinder standard shall have been certified by the
manufacturer. The manufacturer must have recommended a maximum shelf life for
each cylinder so that the concentration does not change greater than plus or
minus 5% from the certified value. The date of gas cylinder preparation,
certified vinyl chloride concentration and recommended maximum shelf life must
have been affixed to the cylinder before shipment from the manufacturer to the
buyer. If a gas chromatograph is used as the vinyl chloride monitoring system,
these gas mixtures may be directly used to prepare a chromatograph calibration
curve as described in section 7.3 of Method 106 of 40 CFR part 61, Appendix B,
incorporated by reference in s.
NR 484.04(23). The requirements in
sections 5.2.3.1 and 5.2.3.2 of Method 106 for certification of cylinder
standards and for establishment and verification of calibration standards shall
be followed.
4. The
location and number of points to be monitored and the frequency of monitoring
provided for in the program are acceptable when they are compared with the
number of pieces of equipment in vinyl chloride service and the size and
physical layout of the plant.
5. It
contains an acceptable plan of action to be taken when a leak is
detected.
6. It contains a
definition of leak which is acceptable when compared with the background
concentrations of vinyl chloride in the areas of the plant to be monitored by
the vinyl chloride monitoring system. Measurement of background concentrations
of vinyl chloride in the areas of the plant to be monitored by the vinyl
chloride monitoring system shall be included with the description of the
program. The definition of leak for a given plant may vary among the different
areas within the plant and is also to change over time as background
concentrations in the plant are reduced.
(i) Vinyl chloride emissions to the
atmosphere from inprocess wastewater shall be reduced as specified in this
paragraph.
1. The concentration of vinyl
chloride in each inprocess wastewater stream containing greater than 10 parts
per million vinyl chloride measured immediately as it leaves a piece of
equipment and before being mixed with any other inprocess wastewater stream
shall be reduced to no more than 10 parts per million by weight before being
mixed with any other inprocess wastewater stream which contains less than 10
parts per million vinyl chloride, before being exposed to the atmosphere,
before being discharged to a wastewater treatment process, or before being
discharged untreated as a wastewater. This paragraph does apply to water which
is used to displace vinyl chloride from equipment before it is opened to the
atmosphere in accordance with s.
NR 449.06(1) (b) or par. (f), but does
not apply to water which is used to wash out equipment after the equipment has
already been opened to the atmosphere in accordance with s.
NR 449.06(1) (b) or par. (f).
2. Any vinyl chloride removed from the
inprocess wastewater in accordance with subd. 1. shall be ducted through a
control system from which the concentration of vinyl chloride in the exhaust
gases may not exceed 10 parts per million, or equivalent as provided in s.
NR 449.08
(3) STANDARD OPERATING PROCEDURE. The
requirements in sub. (2) (a), (b) and (e) to (h) shall be incorporated into a
standard operating procedure and made available upon request for inspection by
a department representative. The standard operating procedure shall include
provisions for measuring the vinyl chloride in equipment 4.75 cubic meters
(1,250 gallons) in volume for which an emission limit is prescribed in sub. (2)
(f) 1. prior to opening the equipment and using Method 106 of 40 CFR part 61,
Appendix B, incorporated by reference in s.
NR 484.04(23), a portable hydrocarbon
detector, or an equivalent or alternative method. The method of measurement
shall meet the requirements s.
NR 449.09(6) (e) 1. a. or b.