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Control of Mercury Emissions by Injecting Powdered Activated Carbon (PAC). Presentation to Utility MACT Working Group May 13, 2002 EPA, RTP, NC. Michael D. Durham, Ph.D., MBA ADA Environmental Solutions 8100 SouthPark Way B-2 Littleton, CO 80120 303 734-1727. Outline.
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Control of Mercury Emissionsby Injecting Powdered Activated Carbon (PAC) Presentation to Utility MACT Working Group May 13, 2002 EPA, RTP, NC Michael D. Durham, Ph.D., MBA ADA Environmental Solutions 8100 SouthPark Way B-2 Littleton, CO 80120 303 734-1727
Outline • ADA-ES DOE/NETL Hg Control Program • Background on PAC Injection Technology • Results from PAC with an ESP • Results from PAC with a FF • Conclusions and Future Plans
ADA-ES Hg Control Program • Full-scale field testing of sorbent-based mercury control on non-scrubbed coal-fired boilers • Primary funding from DOE National Energy Technology Laboratory (NETL) • Cofunding provided by: • Southern Company • Wisconsin Electric • PG&E NEG • EPRI • Ontario Power Generation • TVA • First Energy • Kennecott Energy • Arch Coal
Project Overview • Perform first full-scale evaluations of mercury control on coal-fired boilers (up to 150 MW equivalent). • Evaluate effectiveness of sorbent-based Hg control (activated carbon). • Test several different power plant configurations. • Document all costs associated with Hg control.
DOE/NETL Test Sites Test Site Coal Particulate Test Control Dates Alabama Power Bituminous HS ESP Spring Gaston COHPAC FF 2001 Wisconsin Electric PRB Cold Side ESP Fall Pleasant Prairie 2001 PG&E NEG Bituminous Cold Side ESP Summer Brayton Point 2002 PG&E NEG Bituminous Cold Side ESP Fall Salem Harbor 2002
Sorbent Injection Air Hg CEM ESP or FF H2O Spray Cooling Ash and Sorbent Coal-Fired Boiler with Sorbent Injection and Spray Cooling
Semi-Continuous Mercury Analyzer Heater Dry Air CVAA Flue Gas Chilled Impingers Gold Trap Mass Flow Controller Micro controller with Display Waste
Capture of Vapor Phase Hg by Solid Sorbents • Mass Transfer Limits (getting the Hg to the sorbent) • Removal increases with particle concentration • Produces percentage removal independent of concentration • Particle control device (FF vs ESP) is a critical parameter • Sorbent Capacity to hold Hg depends upon: • Sorbent characteristics • Temperature • Mercury concentration • Concentrations of SO3 and other contaminants
Equilibrium Adsorption Capacities at 250°FUpstream and Downstream of SO3 Injection
WEPCO Pleasant Prairie • Testing completed fall of 2001 • PRB coal • ESP only • Spray cooling • SO3 conditioning system
ESP 2-4 Carbon Injection Spray Cooling ESP Configuration, PPPP
Speciated Mercury Measured by Ontario Hydro Method (10 lbs/MMacf) (microgram/dncm) PARTICULATE ELEMENTAL OXIDIZED TOTAL Baseline ESP Inlet 1.97 12.22 2.51 16.71 ESP Outlet 0.01 9.80 6.01 15.82 Removal Efficiency 99.5% 19.8% -139.3 5.3% PAC Injection ESP Inlet 0.98 14.73 1.73 17.44 ESP Outlet 0.00 4.27 0.44 4.71 Removal Efficiency 100.0% 71.0% 74.5% 73.0%
Alabama Power E.C. Gaston • Alabama Power Company E.C. Gaston Electric Generating Plant Unit 3, Wilsonville, AL • 270 MW Firing a Variety of Low-Sulfur, Washed Eastern Bituminous Coals • Particulate Collection System • Hot-side ESP, SCA = 274 ft2/1000 acfm • COHPAC baghouse supplied by Hamon Research-Cottrell • Wet Ash Disposal to Pond
Sorbent Injection COHPAC Electrostatic Coal Precipitator Fly Ash (98%) Fly Ash (2%) + PAC Site Test Configuration with EPRI TOXECON at Alabama Power Plant Gaston
PAC Rate Limit Due to Pressure Drop Mercury Removal vs. Injection Rate
Average Mercury Removal Long-Term Tests Gaston, Ontario Hydro (microgram/dncm) PARTICULATE OXIDIZED ELEMENTAL TOTAL Baseline COHPAC Inlet 0.09 9.54 5.97 15.60 COHPAC Outlet 0.01 11.19 3.34 14.54 Removal Efficiency 89.1% -17.3% 44.1% 6.8% PAC Injection COHPAC Inlet 0.23 6.37 4.59 11.19 COHPAC Outlet 0.12 0.91 0.03 1.05 Removal Efficiency 45.6% 85.7%99.3%90.6%
Conclusions (PAC General) • PAC injection can effectively capture elemental and oxidized mercury from both bituminous and subbituminous coals • Additional field tests and long-term demonstrations are necessary to continue to mature the technology • Fabric filters provide better contact between the sorbent and mercury than ESPs resulting in higher removal levels at lower sorbent costs • New COHPAC FF’s will have to be designed to handle higher loadings of PAC to insure high (>90%) mercury removal • Conventional FF’s should not require any modifications for PAC
Conclusions (Response to Concentration Variations) • Response times to changes in inlet concentrations: • Feedback data from outlet CEMs—tens of minutes • Impact of changes in injection rate: tens of minutes to hours • Long averaging times will be required to recover from upsets • Injection at somewhat higher rates will make the technology more capable to handle inlet fluctuations • PAC injection lends itself to the use of feed rate parameters as a definition of Maximum Achievable Control Technology
Future Plans • Short-term testing at additional sites • PG&E Brayton Point (Bituminous coal, large ESP) 6/ 2002 • PG&E Salem Harbor (Bituminous coal, SNCR, large ESP) 9/2002 • * TBD (PRB coal, small ESP) 3/2003 • * Southern Company (Bituminous coal, small ESP) 8/ 2003 • Long-term testing • *Alabama Power (Bituminous coal, COHPAC FF) 2002-2003 • *CCPI Program (PRB Coal, COHPAC FF) 2004-2006 • *CCPI Program (Bituminous Coal, COHPAC FF) 2004-2006 • * Proposed
For More Information • www.adaes.com • www.adaes.com/mercury.htm • Link to other mercury related web sites • Publications/reports • www.adaes.com/MercuryPublic.htm • Public information on DOE/NETL Mercury Control Program • www.netl.doe.gov/products/environment/index.html DOE/NETL Website