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Control of Volatile Organic Compounds Emissions from Manufacturing

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D.2.2 Environmental Protection Agency (EPA) Air Oxidation Unit Test<br />

-Data<br />

The EPA test study represents the most in-depth work available<br />

for full-scale incinerators on air oxidation vents at three chemical<br />

plants. Data includes inlet/outlet tests on three large incinerators.<br />

The tests measured inlet and outlet VOC concentrations by compound for<br />

different incinerator temperatures. The referenced test reports<br />

include complete test results, process rates, and test method descriptions.<br />

The three plants tested are Denka's maleic anhydride unit in Houston,<br />

Texas, Rohm and Haas's acrylic acid unit in Deer Park, Texas, and<br />

Union Carbide's acrylic acid unit in Taft, Louisiana. The data <strong>from</strong><br />

Union Carbide include test results for two different incinerator<br />

temperatures. The data <strong>from</strong> Rohm and Haas include results for three<br />

temperatures. In all tests, bags were used for collecting integrated<br />

samples and a GC/FID was used for organic analysis.<br />

D.2.2.1 Denka Test ~ata.4 The Denka maleic anhydride facility<br />

has a nameplate capacity <strong>of</strong> 23 Gg/yr (50 mill ion 1 bs/yy). Maleic<br />

anhydride is produced by vapor-phase catalytic oxidation <strong>of</strong> benzene.<br />

The liquid effluent <strong>from</strong> the absorber, after undergoing recovery<br />

operations, is about 40 weight percent aqueous solution <strong>of</strong> maleic<br />

acid. The absorber vent is directed to the incinerator. The thermal<br />

incinerator has a primary heat recovery system to generate process<br />

steam and uses natural gas as supplemental fuel. The plant was operating<br />

at about 70 percent <strong>of</strong> capacity when the sampling was conducted. The<br />

plant personnel did not think that the lowered production rate would<br />

seriously affect the validity or representativeness <strong>of</strong> the results.<br />

1. <strong>Control</strong> Device. The size <strong>of</strong> the incinerator combustion<br />

chamber is 204 m2 (2,195 ft2). There are three thermocouples used to<br />

sense the flame temperature, and these are averaged to give the temperature<br />

recorded in the control room.<br />

is provided in Figure D-3.<br />

A rough sketch <strong>of</strong> the combustion chamber<br />

2. Sampling and Analytical Techniques. Gas samples <strong>of</strong> total<br />

hydrocarbons (THC), benzene, methane, and ethane were obtai ned according<br />

to the September 27, 1977, EPA draft benzene method. Seventy-liter<br />

a1 uminized MylarR bags were used to collect samples over periods <strong>of</strong>

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