(1) MACT REQUIREMENTS. Each owner or operator
of an affected source subject to the provisions of this subchapter shall comply
with these requirements on and after the compliance dates specified in s.
NR 463.06(1). All affected sources are
regulated by applying maximum achievable control technology.
(2) APPLICABILITY OF EMISSION LIMITS.
(a) The emission limitations in this section
apply during tank operation as well as during periods of startup and shutdown
as these are routine occurrences for affected sources subject to this
subchapter. The emission limitations do not apply during periods of
malfunction. However, the work practice standards that address operation and
maintenance and that are required by s.
NR 463.05 shall be followed during
malfunctions.
(b) If an owner or
operator is controlling a group of tanks with a common add-on air pollution
control device, the emission limitations of subs. (3), (4) and (5) apply
whenever any one affected source is operated. The emission limitation that
applies to the group of affected sources is as follows:
1. The emission limitation identified in
subs. (3), (4) and (5) if the affected sources are performing the same type of
operation, such as hard chromium electroplating, are subject to the same
emission limitation, and are not controlled by an add-on air pollution control
device also controlling sources not affected by this subchapter.
2. The emission limitation calculated
according to s.
NR 463.09(5) (c) if affected sources are
performing the same type of operation, are subject to the same emission
limitation, and are controlled with an add-on air pollution control device that
is also controlling sources not affected by this subchapter.
3. The emission limitation calculated
according to s.
NR 463.09(5) (d) if affected sources are
performing different types of operations, or affected sources are performing
the same operations but subject to different emission limitations, and are
controlled with an add-on air pollution control device that may also be
controlling emissions from sources not affected by this subchapter.
(3) STANDARDS FOR HARD
CHROMIUM ELECTROPLATING.
(a) Open surface
tanks. During tank operation, each owner or operator of an existing, new or
reconstructed affected source shall control chromium emissions discharged to
the atmosphere from that affected source by doing any of the following:
1. Not allowing the concentration of total
chromium in the exhaust gas stream discharged to the atmosphere to exceed 0.015
milligrams of total chromium per dry standard cubic meter (mg/dscm) of
ventilation air (6.6 x 10-6 grains per dry standard cubic foot (gr/dscf)) for
all open surface hard chromium electroplating tanks that are affected sources
other than those that are existing affected sources located at small hard
chromium electroplating facilities.
2. Not allowing the concentration of total
chromium in the exhaust gas stream discharged to the atmosphere to exceed 0.03
mg/dscm (1.3 x 10-5 gr/dscf) if the open surface hard chromium electroplating
tank is an existing affected source and is located at a small, hard chromium
electroplating facility.
3. If a
chemical fume suppressant containing a wetting agent is used, not allowing the
surface tension of the electroplating or anodizing bath contained within the
affected tank to exceed 45 dynes per centimeter (dynes/cm) (3.1 x 10-3
pound-force per foot (lbf /ft)) as measured by a stalagmometer or 35 dynes/cm
(2.4 x 10-3 lbf /ft) as measured by a tensiometer at any time during tank
operation.
(b) Enclosed
tanks. During tank operation, each owner or operator of an existing, new or
reconstructed affected source shall control chromium emissions discharged to
the atmosphere from that affected source by doing any of the following:
1. Not allowing the concentration of total
chromium in the exhaust gas stream discharged to the atmosphere to exceed 0.015
mg/dscm (6.6 x 10-6 gr/dscf) for all enclosed hard chromium electroplating
tanks that are affected sources other than those that are existing affected
sources at small, hard chromium electroplating facilities.
2. Not allowing the concentration of total
chromium in the exhaust gas stream discharged to the atmosphere to exceed 0.03
mg/dscm (1.3 x 10-5 gr/dscf) if the enclosed hard chromium electroplating tank
is an existing affected source and is located at a small, hard chromium
electroplating facility.
3. If a
chemical fume suppressant containing a wetting agent is used, not allowing the
surface tension of the electroplating or anodizing bath contained within the
affect tank to exceed 45 dynes/cm (3.1 x 10-3 lbf /ft) as measured by a
stalagmometer or 35 dynes/cm (2.4 x 10-3 lbf /ft) as measured by a tensiometer
at any time during tank operation.
4. Not allowing the mass rate of total
chromium in the exhaust gas stream discharged to the atmosphere to exceed the
maximum allowable mass emission rate determined by using the calculation
procedure in s.
NR 463.09(6) (b) for all enclosed hard
electroplating tanks that are affected sources other than those that are
existing affected sources located at small, hard chromium electroplating
facilities.
5. Not allowing the
mass rate of total chromium in the exhaust gas stream discharged to the
atmosphere to exceed the maximum allowable mass emission rate determined by
using the calculation procedure in s.
NR 463.09(6) (d) if the enclosed hard
chromium electroplating tank is an existing affected source and is located at a
small, hard chromium electroplating facility.
(c) Facility size.
1. An owner or operator may demonstrate the
size of a hard chromium electroplating facility by meeting the criteria of s.
NR 463.02(20) or (26). Alternatively, an
owner or operator of a facility with a maximum cumulative potential rectifier
capacity of 60 million A-hr/yr or more may be considered small if the actual
cumulative rectifier capacity is less than 60 million A-hr/yr as demonstrated
using one of the following procedures:
a. If
records show that the facility's previous annual actual rectifier capacity was
less than 60 million A-hr/yr, by using nonresettable ampere-hour meters and
keeping monthly records of actual ampere-hour usage for each 12-month rolling
period following the compliance date in accordance with s.
NR 463.103(2)
(L). The actual cumulative rectifier capacity
for the previous 12-month rolling period shall be tabulated monthly by adding
the capacity for the current month to the capacities for the previous 11
months.
b. By accepting a
federally-enforceable limit on the maximum cumulative potential rectifier
capacity of a hard chromium electroplating facility and by maintaining monthly
records in accordance with s.
NR 463.103(2)
(L) to demonstrate that the limit has not
been exceeded. The actual cumulative rectifier capacity for the previous
12-month rolling period shall be tabulated monthly by adding the capacity for
the current month to the capacities for the previous 11 months.
2. Once the monthly records
required to be kept by s.
NR 463.103(2)
(L) and by this paragraph show that the
actual cumulative rectifier capacity over the previous 12-month rolling period
corresponds to the large designation, the owner or operator is subject to the
emission limitation identified in par. (a) 1. or 3. or (b) 1., 3. or 4., in
accordance with the compliance schedule of s.
NR 463.06(1)
(e).
(4) STANDARDS FOR DECORATIVE CHROMIUM
ELECTROPLATING TANKS USING A CHROMIC ACID BATH AND CHROMIUM ANODIZING TANKS.
During tank operation, each owner or operator of an existing, new or
reconstructed decorative chromium electroplating tank using a chromic acid bath
or chromium anodizing tank shall control chromium emissions discharged to the
atmosphere from that affected source by one of the following:
(a) By not allowing the concentration of
total chromium in the exhaust gas stream discharged to the atmosphere to exceed
0.01 mg/dscm (4.4Ã10-6 gr/dscf).
(b) If a chemical fume suppressant containing
a wetting agent is used, by not allowing the surface tension of the
electroplating or anodizing bath contained within the affected tank to exceed
45 dynes per centimeter (dynes/cm) (3.1 x 10-3 pound-force per foot (lbf /ft))
as measured by a stalagmometer or 35 dynes/cm (2.4 x 10-3 lbf /ft) as measured
by a tensiometer at any time during operation of the tank.
(5) STANDARDS FOR DECORATIVE CHROMIUM
ELECTROPLATING TANKS USING A TRIVALENT CHROMIUM BATH.
(a) Each owner or operator of an existing,
new or reconstructed decorative chromium electroplating tank that uses a
trivalent chromium bath that incorporates a wetting agent as a bath ingredient
is subject to the recordkeeping and reporting requirements of ss.
NR 463.103(2)
(n) and 463.106(9), but is
not subject to the work practice requirements of s.
NR 463.05, or the continuous compliance monitoring
requirements in s.
NR 463.07. The wetting agent shall be an ingredient in
the trivalent chromium bath components purchased from vendors.
(b) Each owner or operator of an existing,
new or reconstructed decorative chromium electroplating tank that uses a
trivalent chromium bath that does not incorporate a wetting agent as a bath
ingredient is subject to the standards of sub. (4).
(c) Each owner or operator of existing, new
or reconstructed decorative chromium electroplating tank that had been using a
trivalent chromium bath that incorporates a wetting agent and ceases using this
type of bath shall fulfill the reporting requirements of s.
NR 463.106(9)
(c) and comply with the applicable emission
limitation within the timeframe specified in s.
NR 463.06(1)
(f).