Table 1 to Subpart G of Part 63—Process Vents—Coefficients for Total Resource Effectiveness for Existing Source Nonhalogenated and Halogenated Vent Streams

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