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Control of Volatile Organic Compounds Emissions from Manufacturing

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3.1.3.1 Catalytic Incinerator VOC Destruction Efficiency, The<br />

destruction efficiency <strong>of</strong> catalytic incinerators is a function <strong>of</strong> many<br />

variables, including type <strong>of</strong> catalyst, its surface area, volume, and<br />

pore size distribution, gas composition, uniformity <strong>of</strong> flow through the<br />

catalyst bed, oxygen concentration, and temperature in the unit .26,27<br />

The efficiency <strong>of</strong> a catalytic incinerator will deteriorate over<br />

time, necessitating periodic repl acement <strong>of</strong> the catalyst. The repl ace-<br />

ment time varies widely, depending on the service <strong>of</strong> the unit, <strong>from</strong> less<br />

than 1 year up to 10 years,12 with an average life between 3 and 5 years,28<br />

A 1980 study by Engelhard Industries for the EPA involved testing<br />

<strong>of</strong> both pi1 ot and full -scale catalytic incineration systems. The full -scale<br />

unit installed on a formaldehyde plant achieved control efficiencies<br />

ranging <strong>from</strong> 97.9 to 98.5 percent. These efficiencies represent overall<br />

control levels for carbon monoxide, methanol, dimethyl ether, and formaldehyde.<br />

Measurements indicated the ability <strong>of</strong> the system to control at this<br />

level consistently over a 1-year period. No trend in the data points<br />

gave indication <strong>of</strong> a maximum catalyst life.29<br />

3.1.3.2 Applicability <strong>of</strong> Catalytic Incinerator's. - A catalytic<br />

incinerator is best applied to a continuous stream that is (1) low in<br />

VOlC (higher VOC concentrations lead to higher catalyst temperatures,<br />

which can seriously damage the catalyst activity and possibly create<br />

fire hazards) and (2) free <strong>from</strong> solid particles and catalyst "poisons."<br />

A catalytic incinerator in many situations may be fitvored over a thermal<br />

-incinerator because it can destroy the VOC at a lower temperature and,<br />

therefore, use less fuel. However, since most <strong>of</strong> the streams involved<br />

in the polymers and resins industry are high enough in heating value to<br />

sel f-combust without using auxi 1 iary fuel , vi rtual ly no advantage is<br />

achieved by using a catalytic unit and thei r applicabi 1 ity in thi s<br />

industry is very limited.<br />

3.1.4 Industrial Boilers<br />

Fireboxes <strong>of</strong> boilers and fired heaters can be used, under proper<br />

conditions, to incinerate waste streams that contai n VOC1s. Combusti bl e<br />

contaminants, includi ng smoke, organic vapors, and gases can be converted<br />

essentially to carbon dioxide and water in boiler f'ireboxes. As the<br />

primary purpose <strong>of</strong> the boiler is to generate steam, a1 1 aspects <strong>of</strong><br />

operation must be thoroughly evaluated before this method <strong>of</strong> air pollution<br />

1<br />

I<br />

I

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