A. This section applies to industrial and commercial installations which are less than seventy-three megawatts capacity (two hundred fifty million British thermal units per hour); but in the aggregate on any premises are rated at greater than five hundred thousand British thermal units per hour (0.146 megawatts); and in which fuel is burned for the primary purpose of producing steam, hot water, hot air or other liquids, gases or solids and in the course of doing so the products of combustion do not come into direct contact with process materials. When any products or by-products of a manufacturing process are burned for the same purpose or in conjunction with any fuel, the same maximum emission limitations shall apply.
B. For purposes of this section, the heat input shall be the aggregate heat content of all fuels whose products of combustion pass through a stack or other outlet. The heat content of solid fuel shall be determined in accordance with Section 17.11.160. Compliance tests shall be conducted during operation at the nominal rated capacity of each unit. The total heat input of all fuel-burning units on a plant or premises shall be used for determining the maximum allowable amount of particulate matter that may be emitted.
C. No person shall cause, allow or permit the emission of particulate matter, caused by combustion of fuel, from any fuel-burning operation in excess of the amounts calculated by one of the following equations:
1. For equipment having a heat input rate of four thousand two hundred million BTU per hour or less, the maximum allowable emissions shall be determined by the following equation:
E = 1.02Q 0.769
where:
E = The maximum allowable particulate emissions rate in pounds-mass per hour.
Q = The heat input in million BTU per hour.
2. For equipment having a heat input rate greater than four thousand two hundred million BTU per hour, the maximum allowable emissions shall be determined by the following equation:
E = 17.0Q 0.432
where "E" and "Q" have the same meanings as in subdivision 1 of this subsection.
D. The actual values shall be calculated from the applicable equations and rounded off to two decimal places.
E. Fossil-fuel fired industrial and commercial equipment installations shall not emit more than 1.0 pounds of sulfur dioxide per million BTU heat input when low sulfur oil is fired.
F. Fossil-fuel fired industrial and commercial equipment installations shall not emit more than 2.2 pounds of sulfur dioxide per million BTU heat input when high sulfur oil is fired.
G. Any permit issued for the operation of an existing source, or any renewal or modification of such a permit, shall include a condition prohibiting the use of high sulfur oil by the permittee. This condition may be omitted from the permit if the applicant demonstrates to the satisfaction of the control officer both that sufficient quantities of low sulfur oil are not available for use by the source and that it has adequate facilities and contingency plans to insure that the sulfur dioxide ambient air quality standards set forth in Section 17.08.020 will not be violated.
1. The terms of the permit may authorize the use of high sulfur oil under such conditions as are justified.
2. In cases where the permittee is authorized to use high sulfur oil it shall submit to the control officer monthly reports detailing its efforts to obtain low sulfur oil.
3. When the conditions justifying the use of high sulfur oil no longer exist, the permit shall be modified accordingly.
4. Nothing in this section shall be construed as allowing the use of a supplementary control system or other form of dispersion technology.
H. When coal is fired, fossil-fuel fired industrial and commercial equipment installations shall not emit more than 1.0 pound of sulfur dioxide per million BTU heat input.
I. The owner or operator subject to the provisions of this section shall install, calibrate, maintain and operate a continuous monitoring system for measurement of the opacity of emissions discharged into the atmosphere from the control device.
J. The test methods and procedures required 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 as prescribed in this section.
a. Method 1 for selection of sampling site and sample traverses.
b. Method 3 for gas analysis to be used when applying Reference Methods 5 and 6.
c. Methods 4 and 5 for concentration of particulate matter and the associated moisture content.
d. Method 6 for concentration of SO 2 .
2. For Method 5, Method 1 shall be used to select the sampling site and the number of traverse sampling points. The sampling time for each run shall be at least sixty minutes and the minimum sampling volume shall be 0.85 dscm (30 dscf), except that smaller sampling times or volumes, when necessitated by process variables or other factors, may be approved by the control officer. The probe and filter holder heating systems in the sampling train shall be set to provide a gas temperature no greater than one hundred sixty degrees Celsius (three hundred twenty degrees Fahrenheit).
3. For Method 6, the sampling site shall be the same as that selected for Method 5. The sampling point in the duct shall be at the centroid of the cross section or at a point no closer to the walls than one meter (3.28 ft). For Method 6, the sample shall be extracted at a rate proportional to the gas velocity at the sampling point.
4. For Method 6, the minimum sampling time shall be twenty minutes and the minimum sampling volume 0.02 dscm (0.71 dscf) for each sample. The arithmetic mean of two samples shall constitute one run. Samples shall be taken at approximately thirty-minute intervals.
5. Gross calorific value shall be determined in accordance with the applicable ASTM methods: D-2015-91 (Test for Gross Calorific Value of Solid Fuel by the Adiabatic Bomb Calorimeter) for solid fuels, D-240-87 (Test Method for Heat of Combustion of Liquid Hydrocarbon Fuels by Bomb Calorimeter) for liquid fuels, and D-1826-88 (Test Method for Calorific Value of Gases in Natural Gas Range by Continuous Recording Calorimeter) for gaseous fuels. The rate of fuels burned during each testing period shall be determined by suitable methods and shall be confirmed by a material balance over the fossil-fuel fired system.
(Ord. 2017-20 § 3 (part), 2017: Ord. 2005-43 § 3 (part), 2005; Ord. 2004-97 § 4 (part), 2004; Ord. 1994-83 § 54, 1994: Ord. 1993-128 § 4 (part), 1993)