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Combustion Optimization for Decreased Emissions and Improved Efficiency J. Estrada, Progress Energy St. Petersburg, FL D. Earley, Combustion Technologies Apex, NC B. Kirkenir, Progress Energy Raleigh, NC
Acknowledgements Bob Sisson Crystal River Plant Engineer Crystal River Power Plant Crystal River, FL
Ideal Furnace Combustion Proper and even burner stoichiometry leads to consistent flames in furnace Fuel:Air ratio distribution Emissions reduction and improved efficiency  Low hanging fruit Potential alternative to post combustion emission equipment
Crystal River Unit 4 B&W Opposed Fire Pulverized Coal 770 MW 6 MPS-89 Puvlerizers 9 Coal Outlets per Mill 54 B&W DRB-4Z Low NOx Burners ,[object Object]
3 x Front, 3 X Rear
SCR, Cold Side ESP& Wet FGD,[object Object]
Coal Balancing Problem:  Uneven Coal distribution Solution:  Online coal measurement + adjustment Coal Out Adjustable Coal Valves Pulverizer Discharge Coal In
Coal Flow Measurement Air Monitor Corporation Santa Rosa, CA
Coal Flow Balancing
Coal Flow Balancing
Burner Air:Fuel Ratios
Secondary Air Balance Windbox Air Dampers Windbox Air Dampers ,[object Object]
Solution:  Measure SA flow at each burner and adjust SA dampersSecondary Air Secondary Air
Secondary Air Measurement Wind Tunnel Testing at Air Monitor HQ
Why Automate SA Dampers? Dynamic windbox flow profiles Fluctuating windbox pressure Ash build-up Burner 3 Burner 2 Burner 1
Post-Combustion CO and O2 measurement accuracy is critical Grid configuration preferred
O2 Probe Relocation Old location not representative of furnace O2 profile ,[object Object]
Significant distribution improvement realized due to new location,[object Object]
CRN O2 Distribution Comparisons CR4 O2 Profiles CR5 O2 Profiles Note:  Unit scales are different
CO Probe Augmentation CO is better diagnostic tool than O2 alone Air leakage impact on O2 probe
CCM Tuning
Remote Combustion Dashboard
New O2 Curve LOI benefit
NOx Benefit
Project Results Boiler Efficiency Increase = 0.5% Annual fuel savings Combustion NOx Reduction 7% at full load, 15-25% at part load Annual Ammonia Reagent Usage Reduction SCR Catalyst Life Extension Fan Auxiliary Power Savings

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CCM Mega Presentation

  • 1. Combustion Optimization for Decreased Emissions and Improved Efficiency J. Estrada, Progress Energy St. Petersburg, FL D. Earley, Combustion Technologies Apex, NC B. Kirkenir, Progress Energy Raleigh, NC
  • 2. Acknowledgements Bob Sisson Crystal River Plant Engineer Crystal River Power Plant Crystal River, FL
  • 3. Ideal Furnace Combustion Proper and even burner stoichiometry leads to consistent flames in furnace Fuel:Air ratio distribution Emissions reduction and improved efficiency Low hanging fruit Potential alternative to post combustion emission equipment
  • 4.
  • 5. 3 x Front, 3 X Rear
  • 6.
  • 7. Coal Balancing Problem: Uneven Coal distribution Solution: Online coal measurement + adjustment Coal Out Adjustable Coal Valves Pulverizer Discharge Coal In
  • 8. Coal Flow Measurement Air Monitor Corporation Santa Rosa, CA
  • 12.
  • 13. Solution: Measure SA flow at each burner and adjust SA dampersSecondary Air Secondary Air
  • 14. Secondary Air Measurement Wind Tunnel Testing at Air Monitor HQ
  • 15. Why Automate SA Dampers? Dynamic windbox flow profiles Fluctuating windbox pressure Ash build-up Burner 3 Burner 2 Burner 1
  • 16. Post-Combustion CO and O2 measurement accuracy is critical Grid configuration preferred
  • 17.
  • 18.
  • 19. CRN O2 Distribution Comparisons CR4 O2 Profiles CR5 O2 Profiles Note: Unit scales are different
  • 20. CO Probe Augmentation CO is better diagnostic tool than O2 alone Air leakage impact on O2 probe
  • 23. New O2 Curve LOI benefit
  • 25. Project Results Boiler Efficiency Increase = 0.5% Annual fuel savings Combustion NOx Reduction 7% at full load, 15-25% at part load Annual Ammonia Reagent Usage Reduction SCR Catalyst Life Extension Fan Auxiliary Power Savings
  • 26.
  • 27. Additional “Soft” Benefits Reduced emissions Reduced pulverizer wear Reduced wear on Coal Yard equipment. Reduced boiler tube & non-pressure part erosion due to lower flue gas velocities. Improved ESP performance due to lower flue gas velocities. Reduced potential for slagging and fouling events Improved Pressure part life due to improved temperature profile Reduced ash disposal costs Reduced boiler tube failures due to reducing atmospheres
  • 28. Contact Joe Estrada – jose.estrada@pgnmail.com David Earley – dearley@combustiontc.com Bill Kirkenir – bill.kirkenir@pgnmail.com

Editor's Notes

  1. Thank plant here.
  2. 135 test points9 4th orderequationsPressure andtemperature compensated