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Presented by: Eastern Research Group, Inc.

Status Report to the Stationary Sources Joint Forum: Task 2: Control Technology Analysis. May 10, 2005. Presented by: Eastern Research Group, Inc. Overview. Objective: Provide costs and impacts for options used to control emissions of NO x , SO 2 , PM, VOC, and Ammonia

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Presented by: Eastern Research Group, Inc.

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  1. Status Report to the Stationary Sources Joint Forum: Task 2: Control Technology Analysis May 10, 2005 Presented by: Eastern Research Group, Inc.

  2. Overview Objective: Provide costs and impacts for options used to control emissions of NOx, SO2, PM, VOC, and Ammonia NOx from EGUs • EGUs firing coal – Draft report has been issued. • EGUs firing oil and gas – Database of sources has been assembled. Working on identifying control options and costs and emission reductions of options. Other • NOx from non-EGU’s • SO2 • PM, VOC, and ammonia

  3. Plan for NOx From Coal-fired EGUs • Assemble database of all EGUs in WRAP • Profile state of the art NOx combustion controls • Identify control options • Calculate costs and impacts of options

  4. Database of All EGUs in WRAP • Data obtained from EPA databases • CAMD • EIA 767 • EIA 423 • Data from telephone contacts w/utilities • Coal and combustor properties • Database is available on website

  5. Bins for Coal-fired EGU’s in WRAP • EGU’s were grouped into bins based on similarities in combustor type, coal fired, and nitrogen content of coal. • Bins were further specified by the generation of existing combustion control. • E.g., 1st generation LNB, 2nd generation LNB, State of the Art LNB • Insufficient information was available on more specific combustor parameters (e.g., residence time, combustor volume, and heat release rate).

  6. Bins for Coal-fired EGU’s in WRAP (cont.)

  7. Summary of Combustor Configurations LNB = Low NOx burner, this includes an older low technology found on some tangentially-fired boilers and a technology used on tangential units. LNBO = Low NOx burner with over-fire air LNC1 = Low NOx burner with closed-coupled OFA LNC2 = Low NOx burner with separated OFA LNC3 = Low NOx burner with close-coupled and separated OFA OFA = Over-fired air SCR = Selective Catalytic Reduction

  8. Control Scenarios • Identified 5-7 control options for bins (except for fluidized bed, cell, and cyclone burners). • Options 1-3 are existing combustion controls that are widely used. • Most are variations of LNB and/or OFA • Options 4-7 are next generation burners or state of art combustion controls. • E.g., ULNB, ULNB+OFA, ROFA

  9. Control Options Applied to Bin 1A

  10. Costs and Impacts of Scenarios • Costs for LNB and OFA from CAMD analysis were updated to 2004 $. • Vendor information on LNB and OFA in 2004 $ were compared to updated CAMD costs. If significantly different, vendor data used to reflect decrease in costs. • O & M costs were based on CAMD data • Vendor information used for new state of the art combustion controls. • Costs and emission reductions based on few data points

  11. Costs and Impacts Methodology • Incorporated the generation of the control category to determine the baseline level of control • Baseline NOx emissions were based on CEM information from CAMD • Emission reductions were calculated using the percent reduction the control option can achieve, but bounded by the emission limit that can be achieved

  12. Results • Costs and emission reductions for control options were compared to costs and emission reductions of applying SCR to only BART sources to meet the BART level of control (0.2 lb NOx/MMBtu). • BART sources comprise 64 of 110 EGU’s. Additional 21 EGU’s are likely BART sources. • To match the emissions reduction achieved by applying SCR, EGU’s would need to apply more advanced state of the art controls.

  13. Results (cont.)

  14. Results (cont.)

  15. Results (cont.)

  16. Example Scenarios

  17. Example Scenarios (cont.)

  18. Example Scenario by State

  19. Plan for Other Pollutants/Sources • For EGU’s, identify unique units by ORIS codes. • Identify highest emitting sources and SCC’s using latest inventory work. • Use previous study (plus additional controls) to identify potential controls that may be used per source category.

  20. SO2 Emissions by SIC

  21. SO2 Emissions by State

  22. SO2 Emissions by Process Group

  23. Group 1 Processes

  24. Group 2 Processes

  25. Group 3 Processes

  26. Group 4 Processes

  27. Group 6 Processes

  28. Group 11 Process

  29. SO2 Emissions by Group with BART-eligibility

  30. Proposed BART Level of SO2 Control for EGUs • In establishing BART emission limits, States as a general matter, must apply EPA’s specified “Default Control Level” for each individual EGU greater than 250 MW. • The “Default Control Level” for SO2 is either: • SO2 emissions from the EGU must be 95% controlled, OR • The EGU’s control(s) must achieve in the range of 0.1 to 0.15 lbs SO2/MMBtu. • States may establish a different level of control if the State can demonstrate that an alternative determination is justified based on a consideration of evidence before it. • EPA says that it will be extremely difficult to justify a BART determination less than the “default control level” for a plant greater than 750 MW, less difficult for a plant 750 MW or smaller.

  31. Rough Estimate of SO2 Reductions due to BART for EGUs

  32. North Dakota SO2 Emissions

  33. Colorado SO2 Emissions

  34. Nevada SO2 Emissions

  35. Washington SO2 Emissions

  36. Montana SO2 Emissions

  37. California SO2 Emissions

  38. Idaho SO2 Emissions

  39. South Dakota SO2 Emissions

  40. Alaska SO2 Emissions

  41. Next Steps • Address comments on draft report. • Obtain input on control scenarios for NOx from non-coal EGU’s, NOx from non-EGUs, SO2 for non-Annex States, and PM, VOC, and ammonia from all sources.

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