{"data":{"id":"us/40-cfr-table-1-to-subpart-g-of-part-63","jurisdiction":"us","citation":"40 CFR Table 1 to Subpart G of Part 63","heading":"Table 1 to Subpart G of Part 63—Process Vents—Coefficients for Total Resource Effectiveness for Existing Source Nonhalogenated and Halogenated Vent Streams","body":"Type of Stream Control Device Basis Values of Coefficients\na b c d\nNonhalogenated Flare 1.935 3.660 × 10−1 −7.687 × 10−3 −7.333 × 10−4\nThermal Incinerator 0 Percent Heat Recovery 1.492 6.267 × 10−2 3.177 × 10−2 −1.159 × 10−3\nThermal Incinerator 70 Percent Heat Recovery 2.519 1.183 × 10−2 1.300 × 10−2 4.790 × 10−2\nHalogenated Thermal Incinerator and Scrubber 3.995 5.200 × 10−2 −1.769 × 10−3 9.700 × 10−4","path":["Title 40—Protection of Environment","CHAPTER I—ENVIRONMENTAL PROTECTION AGENCY","SUBCHAPTER C—AIR PROGRAMS","PART 63—NATIONAL EMISSION STANDARDS FOR HAZARDOUS AIR POLLUTANTS FOR SOURCE CATEGORIES","Subpart G—National Emission Standards for Hazardous Air Pollutants From the Synthetic Organic Chemical Manufacturing Industry for Process Vents, Storage Vessels, Transfer Operations, and Wastewater"],"source_url":"https://www.ecfr.gov/api/versioner/v1/full/2026-08-25/title-40.xml","current_through":"2026-08-25","vintage":"","retrieved_at":"2026-08-27T02:26:04Z","sha256":"97d1472cc33f1fea9a959c0c27540729324c366d5afb6795d5cd630c595b959c","source_id":"us-cfr","stale":true,"prev":"us/40-cfr-63.153","next":"us/40-cfr-table-1a-to-subpart-g-of-part-63"},"notice":"GroundRules: Original legal text. Not legal advice."}