Ariz. Admin. Code § R18-2-705 - Standards of Performance for Existing Portland Cement Plants
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. No person shall cause,
allow or permit the discharge of particulate matter from any identifiable
process source within any existing cement plant subject to the provisions of
this Section which exceeds the amounts calculated by one of the following
equations:
1. For process sources having a
process weight rate of 60,000 pounds per hour (30 tons per hour) or less, the
maximum allowable emissions shall be determined by the following equation:
E = 4.10P0.67
where:
E = the maximum allowable particulate emissions rate in pounds-mass per hour.
P = the process weight rate in tons-mass per hour.
2. For process sources
having a process weight rate greater than 60,000 pounds per hour (30 tons per
hour), the maximum allowable emissions shall be determined by the following
equation:
E = 55.0P0.11 -40
where "E" and "P" are defined as indicated in subsection (B)(1).
C. No process source within
any portland cement plant shall exceed 20% opacity.
D. No person shall cause, allow or permit
discharge into the atmosphere of an amount in excess of 6 pounds of sulfur
oxides, calculated as sulfur dioxide, per ton cement kiln feed from cement
plants subject to the provisions of this Section.
E. The owner or operator of any portland
cement plant subject to the provisions of this Section shall record the daily
production rates and the kiln feed rates.
F. The test methods and procedures required
by this Section are as follows:
1. The
reference methods in 40 CFR 60, Appendix A, except as provided for in
R18-2-312 shall be used to
determine compliance with the standards prescribed in subsection (B) as
follows:
a. Method 5 for the concentration of
particulate matter and the associated moisture content;
b. Method 1 for sample and velocity
traverses;
c. Method 2 for velocity
and volumetric flow rate;
d. Method
3 for gas analysis.
2.
For Method 5, the minimum sampling time and minimum sample volume for each run
except when process variables or other factors justifying otherwise to the
satisfaction of the Director, shall be as follows:
a. 60 minutes and 0.85 dscm (30.0 dscf) for
the kiln,
b. 60 minutes and 1.15
dscm (40.6 dscf) for the clinker cooler.
3. Total kiln feed rate, except fuels,
expressed in metric tons per hour on a dry basis, shall be both:
a. Determined during each testing period by
suitable methods; and
b. Confirmed
by a material balance over the production system.
4. For each run, particulate matter
emissions, expressed in g/metric ton of kiln feed, shall be determined by
dividing the emission rate in g/hr by the kiln feed rate. The emission rate
shall be determined by the equation, g/hr = Qs x c, where Qs = volumetric flow
rate of the total effluent in dscm/hr as determined in accordance with
subsection (F)(1)(c), and c = particulate concentration in g/dscm as determined
in accordance with subsection (F)(1)(a).
Notes
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