SOUTH COAST AIR QUALITY MANAGEMENT DISTRICT
RULE 1103 - PHARMACEUTICALS AND COSMETICS MANUFACTURING OPERATIONS
(Adopted April 6, 1980) (Amended December 7, 1990) (Amended March 12, 1999)
The purpose of this rule is to reduce VOC emissions from; and the provisions of this rule shall apply to:
(2) The production and separation of medicinal chemicals such as antibiotics and vitamins from microorganisms.
(3) The manufacture of botanical and biological products by the extraction of organic chemicals from vegetable materials or animal tissues.
(4) The formulation of pharmaceuticals into various dosage forms such as tablets, capsules, injectable solutions or ointments, that can be taken by the patient immediately and in an accurate amount; and the formulation of cosmetics into configurations intended for consumer use.
For the purpose of this rule, the following definitions shall apply:
Capture Efficiency = [Wc/We] x 100
|Where:||Wc||=||weight of VOC entering control device|
|We||=||weight of VOC emitted from the process|
(2) CONTROL DEVICE EFFICIENCY, in percent, is the ratio of the weight of the VOC removed by the control device from the effluent stream entering the control device to the weight of VOC in the effluent stream entering the control device, both measured simultaneously, and shall be calculated by the following equation:
Control Device Efficiency = [(Wc-Wa)/Wc] x 100
|Where:||Wc||=||Weight of VOC entering control device|
|Wa||=||Weight of VOC discharged from the control device|
(3) COSMETICS MANUFACTURING PLANT is any plant producing or blending chemicals for use in cosmetic products and/or manufacturing cosmetic products by chemical processes.
(4) EXEMPT COMPOUNDS See Rule 102 - Definition of Terms are any of the following compounds that have been determined to be non-precursors of ozone:
(5) IN-PROCESS TANKS are containers used for mixing, blending, heating, reacting, holding, crystallizing, evaporating, or cleaning operations in the manufacture of pharmaceuticals or cosmetics.
(6) KEY SYSTEM OPERATING PARAMETER is an emission control system operating parameter, such as temperature, flow rate or pressure, that ensures operation of the abatement equipment within manufacturer specifications and compliance with the standards in Paragraphs (d)(1), (d)(2), and (d)(3).
(7) LIQUID LEAK is the dripping of liquid volatile organic compounds at the rate of more than three drops per minute.
(8) PHARMACEUTICAL MANUFACTURING PLANT is any plant producing or blending chemicals for use in pharmaceutical products and/or manufacturing pharmaceutical products by chemical processes with the Standard Industrial Classification of 2833, 2834, 2835, and 2836.
(9) PRODUCTION EQUIPMENT is any equipment using or emitting VOC that is used in the manufacture of cosmetics or pharmaceuticals and is not exempt from permits pursuant to Rule 219 and does not include reactors, distillation columns, crystallizers and centrifuges which are subject to Subdivision (c) of this rule.
(10) TOTAL VOC VAPOR PRESSURE is the sum of the vapor pressures of each of the compounds defined as VOCs.
VOC Composite Total Pressure is calculated as follows:
|Wc||=||Weight of VOC entering control device|
|Wi||=||Weight of the "i"th VOC compound, in grams (g)|
|Ww||=||Weight of water, in grams (g)|
|We||=||Weight of exempt compound, in grams (g)|
|MWi||=||Molecular weight of the "i"th VOC compound, in||
|MWw||=||Molecular weight of water, in||
|MWe||=||Molecular weight of exempt compound, in||
|TPc||=||VOC composite partial pressure at 20oC, in mm Hg|
|VPi||=||Vapor pressure of the "i"th VOC compound at 20oC, in mm Hg|
(11) VOLATILE ORGANIC COMPOUND (VOC) is any chemical compound containing the element carbon, excluding methane, carbon monoxide, carbon dioxide, carbonic acid, metallic carbides and carbonates, ammonium carbonate, and exempt compounds.
(c) Equipment Requirements
|0.5 psi to 1.0 psi||25oC|
|1.0 psi to 1.5 psi||10|
|1.5 psi to 2.9 psi||0|
|2.9 psi to 5.8 psi||- 15|
|over 5.8 psi||- 25|
(B) An equivalent control devices may be used with the approval of the Executive Officer. Equivalent control is achieved when VOC emissions are reduced by at if it can achieve the equivalent percent of VOC condensed as determined by the method outlined in Subsection 4.1.1 (Condenser Performance) of Section 4.0 "Performance of Control Systems" in the EPA Document No. EPA-450/2-78-029 "Control of Volatile Organic Emissions from Manufacture of Synthesized Pharmaceutical Products" December 1978. A condensed version of this method is shown below.
The percent of VOC condensed shall be calculated with the following equation:
|Where||PC||=||percent of VOC condensed|
|MFS1||=||mole fraction VOC into condenser|
|MFS2||=||mole fraction VOC out of condenser|
Mole fraction of VOC in the condenser inlet and outlet shall can be determined by chemical analysis or by dew point method as described in EPA document "Control of Volatile Organic Emissions from Manufacture of Synthesized Pharmaceutical Products," Report No. EPA-450/2-78-029, Section 4.0 "Performance of Control Systems," pages 4-2 through 4-6.
(2) An operator shall not use centrifuges, rotary vacuum filters, or any other filters, or devices having an exposed liquid surface where the liquid contains VOC having a total VOC vapor pressure of 0.5 psi or more at 20oC, unless such devices incorporate a hood or enclosure with a delivery system or ductwork to collect VOC emissions, exhausting to a control device which meets the applicable requirements in either Paragraphs (d)(1) or (d)(2) of this rule.
(3)An operator shall not use in-process tanks for material containing VOC unless an apparatus or cover which prevents VOC evaporation is provided for the tank. The cover shall be closed or in place on the tank at all times except while loading or unloading the tank.
(d) Operating Requirements
An operator shall conform to the following operational requirements:
(2) If the basic permit unit for air dryer or production equipment including air dryers emits less than 330 pounds per day of volatile organic compounds, the emissions of such organic materials into the atmosphere shall be reduced to less than 33 pounds per day.
(3) An operator shall not transfer VOC having a total VOC vapor pressure greater than 4.1 psi at 20 oC, from any truck or rail car into any storage tank of a 2,000 gallon capacity or greater, unless VOC emissions during transfer are reduced by 90 percent by weight.
(4) An operator shall install pressure/vacuum vents set at +0.03 psig on all storage tanks that store VOC with a total VOC vap