Best Available Control Technology (BACT ) Guideline 3.4.10|
Last Update: 11/21/2006
Oxy-Fuel Combustor Powering a Steam Turbine, Power Output < 3 MW, without Heat Recovery, Uniform and Variable Load, Research Facility
|Pollutant||Achieved in Practice or in the SIP||Technologically Feasible||Alternate Basic Equipment|
|NOx||Emissions less than or equal to 5.3 ppmvd @ 15% O2, equivalent to 0.3 lb/MW-hr||0.53 ppmv @ 15% O2, equivalent to 0.03 lb/MW-hr (90% control using selective catalytic reduction, or equivalent)||n/a|
|PM10||PUC-regulated natural gas, LPG, or non-PUC-regulated gas with < 1.0 grains S/100 dscf, or equivalent||n/a|
|SOx||PUC-regulated natural gas, LPG, or non-PUC-regulated gas with < 1.0 grams S/100 dscf, or equivalent|
|VOC||Emissions less than or equal to 5.0 ppmv @ 15% O2, equivalent to 0.1 lb/MW-hr||2.5 ppmv @ 15% O2, equivalent to 0.05 lb/MW-hr (50% control using an oxidation catalyst, or equivalent)||n/a|
BACT is the most stringent control technique for the emissions unit and class of source. Control techniques that are not achieved in practice or contained in s a state implementation plan must be cost effective as well as feasible. Economic analysis to demonstrate cost effectiveness is requried for all determinations that are not achieved in practice or contained in an EPA approved State Implementation Plan.
This is a Summary Page for this Class of Source. For background information, see Permit Specific BACT Determinations on Details Page.