Open Table
Type of Stream Control Device Basis Values of Coefficients
a b c d
Nonhalogenated Flare 1.935 3.660 × 10−1 −7.687 × 10−3 −7.333 × 10−4
    Thermal Incinerator 0 Percent Heat Recovery 1.492 6.267 × 10−2 3.177 × 10−2 −1.159 × 10−3
    Thermal Incinerator 70 Percent Heat Recovery 2.519 1.183 × 10−2 1.300 × 10−2 4.790 × 10−2
Halogenated Thermal Incinerator and Scrubber 3.995 5.200 × 10−2 −1.769 × 10−3 9.700 × 10−4

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