Regulations last checked for updates: May 17, 2024

Title 40 - Protection of Environment last revised: May 15, 2024
Appendix - Table 7 to Subpart U of Part 63—Operating Parameters for Which Monitoring Levels Are Required To Be Established for Continuous and Batch Front-End Process Vents and Aggregate Batch Vent Streams
Control/recovery device Parameters to be monitored Established operating parameter(s)
Thermal incineratorFirebox temperatureMinimum temperature.
Catalytic incineratorTemperature upstream and downstream of the catalyst bedMinimum upstream temperature; and minimum temperature difference across the catalyst bed.
Boiler or process heaterFirebox temperatureMinimum temperature.
Scrubber for halogenated ventspH of scrubber effluent; and scrubber liquid and gas flow rates
[§ 63.489(b)(4)(ii)]
Minimum pH; and minimum liquid/gas ratio.
AbsorberExit temperature of the absorbing liquid; and exit specific gravity of the absorbing liquidMaximum temperature; and maximum specific gravity.
CondenserExit temperatureMaximum temperature.
Carbon adsorberTotal regeneration steam flow or nitrogen flow, or pressure (gauge or absolute) a during carbon bed regeneration cycle; and temperature of the carbon bed after regeneration (and within 15 minutes of completing any cooling cycle(s))Maximum flow or pressure; and maximum temperature.
Other devices (or as an alternate to the above) bHAP concentration level or reading at outlet of deviceMaximum HAP concentration or reading.

a 25 to 50 mm (absolute) is a common pressure level obtained by pressure swing absorbers.

b Concentration is measured instead of an operating parameter.

[65 FR 38093, June 19, 2000]
authority: 42 U.S.C. 7401
source: 57 FR 61992, Dec. 29, 1992, unless otherwise noted.