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 portland cement plants:
Kiln, clinker cooler, raw mill system, finish mill system, raw mill dryer, raw
material storage, clinker storage, finished product storage, conveyor transfer
points, bagging and bulk loading and unloading systems.
(b) Any facility under par. (a) that
commences construction or modification after August 17, 1971, 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)
"Portland cement plant" means any facility manufacturing portland cement by
either the wet or dry process.
(b)
"Bypass" means any system that prevents all or a portion of the kiln or clinker
cooler exhaust gases from entering the main control device and ducts the gases
through a separate control device. This does not include emergency systems
designed to duct exhaust gases directly to the atmosphere in the event of a
malfunction of any control device controlling kiln or clinker cooler
emissions.
(c) "Bypass stack" means
the stack that vents exhaust gases to the atmosphere from the bypass control
device.
(d) "Monovent" means an
exhaust configuration of a building or emission control device, for example a
positive-pressure fabric filter, that extends the length of the structure and
has a width very small in relation to its length, that is, length to width
ratio is typically greater than 5:1. The exhaust may be an open vent with or
without a roof, louvered vents or a combination of such features.
(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 kiln any gases which:
1. Contain particulate matter in excess of
0.15 kg per metric ton of feed (dry basis) to the kiln (0.30 lb per
ton).
2. 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 clinker cooler any gases
which:
1. Contain particulate matter in
excess of 0.050 kg per metric ton of feed (dry basis) to the kiln (0.10 lb. per
ton).
2. Exhibit 10% opacity, or
greater.
(c) 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 other
than the kiln and clinker cooler any gases which exhibit 10% opacity, or
greater.
(4) MONITORING
OF OPERATIONS.
(a) The owner or operator of
any portland cement plant subject to the provisions of this section shall
record the daily production rates and kiln feed rates.
(b) Except as provided for in par. (c), each
owner or operator of a kiln or clinker cooler that is subject to the provisions
of this section shall install, calibrate, maintain and operate in accordance
with s.
NR 440.13
a continuous opacity monitoring system to measure the opacity of the emissions
discharged into the atmosphere from any kiln or clinker cooler. Except as
provided for in par. (c), a continuous opacity monitoring system shall be
installed on each stack of any multiple stack device controlling emissions from
any kiln or clinker cooler. If there is a separate bypass installed, each owner
or operator of a kiln or clinker cooler shall also install, calibrate, maintain
and operate a continuous opacity monitoring system on each bypass stack in
addition to the main control device stack. Each owner or operator of an
affected kiln or clinker cooler for which the performance test required under
s.
NR 440.08 has
been completed prior to December 14, 1988, shall install the continuous opacity
monitoring system within 180 days after December 14, 1988.
(c) Each owner or operator of a kiln or
clinker cooler subject to the provisions of this section using a
positive-pressure fabric filter with multiple stacks, or an electrostatic
precipitator with multiple stacks may, in lieu of installing the continuous
opacity monitoring system required by par. (b), monitor visible emissions at
least once per day by using a certified visible emissions observer. If the
control device exhausts gases through a monovent, visible emissions
observations in lieu of a continuous opacity monitoring system are required.
These observations shall be taken in accordance with Method 9 of 40 CFR part 60
Appendix A, incorporated by reference in s.
NR 440.17. Visible emissions shall be observed during
conditions representative of normal operation. Observations shall be recorded
for at least 3 6-minute periods each day. In the event that visible emissions
are observed for a number of emission sites from the control device with
multiple stacks, Method 9 observations shall be recorded for the emission site
with the highest opacity. All records of visible emissions shall be maintained
for a period of 2 years.
(d) For
the purpose of reports under sub. (6), periods of excess emissions that shall
be reported are defined as all 6-minute periods during which the average
opacity exceeds that allowed by sub. (3) (a) 2. or (b) 2.
(e) The provisions of pars. (a), (b) and (c)
apply to kilns and clinker coolers for which construction, modification or
reconstruction commenced after August 17, 1971.
(5) 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 test
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 this subsection, except as provided in s.
NR 440.08(2).
(b) The owner or operator shall determine
compliance with the particulate matter standard in sub. (3) as follows:
1. The emission rate (E) of particulate
matter shall be computed for each run using the following equation:
See PDF
for diagram
where:
E is the emission rate of particulate matter, kg/metric
ton (lb/ton) of kiln feed
cs is the concentration of particulate matter, g/dscm
(gr/dscf)
Qsd is the volumetric flow rate of effluent gas, dscm/hr
(dscf/hr)
P is the total kiln feed (dry basis) rate, metric ton/hr
(ton/hr)
K is the conversion factor, 1000 g/kg (7000 gr/lb)
2. Method 5 shall be used to
determine the particulate matter concentration (cs) and the volumetric flow
rate (Q sd) of the effluent gas. The sampling time and sample volume for each
run shall be at least 60 minutes and 0.85 dscm (30.0 dscf) for the kiln and at
least 60 minutes and 1.15 dscm (40.6 dscf) for the clinker cooler.
3. Suitable methods shall be used to
determine the kiln feed rate (P), except fuels, for each run. Material balance
over the production system shall be used to confirm the feed rate.
4. Method 9 and the procedures in s.
NR 440.11 shall be used to determine opacity.
(6) RECORDKEEPING AND
REPORTING REQUIREMENTS.
(a) Each owner or
operator required to install a continuous opacity monitoring system under sub.
(4) (b) shall submit reports of excess emissions as defined in sub. (4) (d).
The content of these reports shall comply with the requirements in s.
NR 440.07(3). Notwithstanding the
provisions of s.
NR 440.07(3), reports shall be submitted
semiannually.
(b) Each owner or
operator monitoring visible emissions under sub. (4) (c) shall submit
semiannual reports of observed excess emissions as defined in sub. (4)
(d).
(c) Each owner or operator
subject to the provisions of sub. (4) (c) shall submit semiannual reports of
the malfunction information required to be recorded by s.
NR 440.07(2). These reports shall
include the frequency, duration and cause of any incident resulting in
deenergization of any device controlling kiln emissions or in the venting of
emissions directly to the atmosphere.