Best Available Control Technology (BACT ) Guideline 1.3.1|
Last Update: 8/27/2005
Fluidized-Bed Combustor => 272 MMBtu/hr, Cogeneration Operation, Fired with Delayed Petroleum Coke (DPC)
|Pollutant||Achieved in Practice or in the SIP||Technologically Feasible||Alternate Basic Equipment|
|CO||natural gas and fuel oil as auxiliary fuel|
|NOx||28 ppmvd (as NO2 corrected to 3% O2), ammonia injection (less than 30 ppmvd ammonia slip) and natural gas and fuel oil as auxiliary fuel)|
|PM10||0.005 gr/dscf corrected to 12% CO2, baghouse, natural gas and low sulfur fuel oil as auxiliary fuel|
|SOx||20.2 ppmvd (as SO2 corrected to 3% O2) (DPC with 2% sulfur by weight) or lowest sulfur content fuel available when 2% sulfur by weight fuel is not available, Sorbent injection and natural gas and low-sulfur fuel oil (15 ppmvd sulfur or less), as auxiliary fuel||lowest sulfur content DPC fuel available, with Sorbent Injection and scrubber; natural gas and low-sulfur fuel oil (15 ppmvd sulfur or less), as auxiliary fuel|
|VOC||0.008 lb/MMBtu, natural gas and fuel oil as auxiliary fuel|
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.