R18

- 2

- 528. Renumbered

Historical Note

Adopted effective May 14, 1979 (Supp. 79

- 1). Amended effective July 9, 1980 (Supp. 80

- 4). Former Section R9

- 3

- 528 renumbered without change as Section R18

- 2

- 528 (Supp. 87

- 3). Amended effective September 26, 1990 (Supp. 90

- 3). Renumbered to R18

- 2

- 728 effective November 15, 1993 (Supp. 93

- 4).

R18

- 2

- 728. Standards of Performance for Existing Ammonium Sulfide Manufacturing Plants A. The provisions of this Section are applicable to the fol lowing affected facilities in ammonium sulfide manufacturing plants: sulfide unloading facilities, reactor

- absorbers, bubble cap scrubbers, and fume incinerators. B. No person shall cause, allow or permit to be emitted into the atmosphere, from any type o f incinerator or other outlet smoke, fumes, gases, particulate matter or other gas

- borne material, the opacity of which exceeds 20%. C. No person shall cause, allow or permit to be emitted into the atmosphere from any emission point from any incinerator, o r to pass a convenient measuring point near such emission point, particulate matter of concentrations in excess of 0.1 grain per cubic foot, based on dry flue gas at standard conditions, corrected to 12% carbon dioxide. D. No person shall allow hydrogen su lfide to be emitted from any location in such manner and amount that the concentration of such emissions into the ambient air at any occupied place beyond the premises on which the source is located exceeds 0.03 parts per million by volume for any averagin g period of 30 minutes or more. E. Where a stack, vent or other outlet is at such a level that fumes, gas mist, odor, smoke, vapor or any combination thereof constituting air pollution are discharged to adjoining property, the Director may require the inst allation of abatement equipment or the alteration of such stack, vent, or other outlet by the owner or operator thereof to a degree that will adequately dilute, reduce or eliminate the discharge of air pollution to adjoining property. F. The owner or opera tor of any ammonium sulfide tailgas incinerator subject to the provisions of this Section shall do both of the following: 1. Install, calibrate, maintain, and operate a flow measuring device which can be used to determine either the mass or volume of tailg as charged to the incinerator. The flow measuring device shall have an accuracy of ± 5% over its operating range. 2. Provide access to the tailgas charged so that a well

- mixed representative grab sample can be obtained. G. The test methods and procedures r equired by this Section are as follows: 1. The reference methods in 40 CFR 60, Appendix A shall be used to determine compliance with the standards prescribed in this Section as follows: a. Method 5 for the concentration of particulate matter and the associ ated moisture content; b. Method 1 for sample and velocity traverse; c. Method 2 for velocity and volumetric flow rate; d. Method 3 for gas analysis and calculation of excess air, using the integrated sample technique;e. Method 11 shall be used to determine the concentration of H 2 S and Method 6 shall be used to determine the concentration of SO 2

. 2. For Method 5, the sampling time for each run shall be at least 60 minutes and the minimum sample volume shall be 0.85 dscm (3 0.0 dscf) except that shorter sampling times and smaller sample volumes, when necessitated by process variables or other factors, may be approved by the Director. 3. Particulate matter emissions, expressed in g/dscm, shall be corrected to 12% CO 2 by using the following formula: C 12 = 12c %CO 2 where: C 12 = the concentration of particulate matter corrected to 12% CO 2 , c = the concentration of particulate matter as measured by Method 5, and %CO 2 = the percentage of CO 2 as measured by Method 3, or, when applic able, the adjusted outlet CO 2 percentage. 4. If Method 11 is used, the gases sampled shall be introduced into the sampling train at approximately atmospheric pressure. Where fuel gas lines are operating at pressures substantially above atmosphere, this may be accomplished with a flow control valve. If the line pressure is high enough to operate the sampling train without a vacuum pump, the pump may be eliminated from the sampling train. The sample shall be drawn from a point near the centroid of the fuel ga s line. The minimum sampling time shall be 10 minutes and the minimum sampling volume 0.01 dscm (0.35 dscf) for each sample. The arithmetic average of two samples of equal sampling time shall constitute one run. Samples shall be taken at approximately one

- hour intervals. For most fuel gases, sample times exceeding 20 minutes may result in depletion of the collecting solution, although fuel gases containing low concentrations of hydrogen sulfide may necessitate sampling for longer periods of time. 5. If Meth od 5 is used, Method 1 shall be used for velocity traverses and Method 2 for determining velocity and volumetric flow rate. The sampling site for determining CO 2 concentration by Method 3 shall be the same as for determining volumetric flow rate by Method 2. The sampling point in the duct for determining SO 2 concentration by Method 3 shall be at the centroid of the cross section if the cross sectional area is less than 5 m 2 (54 ft 2 ) or at a point no closer to the walls than 1 m (3.28 feet) if the cross sect ional area is 5

m 2 or more and the centroid is more than 1 meter from the wall. The sample shall be extracted at a rate proportional to the gas velocity at the sampling point. The minimum sampling time shall be 10 minutes and the minimum sampling volume 0. 01 dscm (0.36 dscf) for each sample. The arithmetic average of two samples of equal sampling time shall constitute one run. Samples shall be taken at approximately one

- hour intervals.
Historical Note Section R18

- 2

- 728 renumbered from R18

- 2

- 528 effective No vember 15, 1993 (Supp. 93

- 4).