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A new approach to improving heater efficiency ,[object Object],www.heatflux.com
Typical Fired Heater Fluid------    Convection section    Radiant section www.heatflux.com
Conventional Approach to Efficiency Improvement www.heatflux.com Additional Heat Transfer Surface in Convection Section
Split flow Fired Heater www.heatflux.com
Typical Reformer Heater ,[object Object],[object Object],[object Object],www.heatflux.com
Split Flow Reformer Heater ,[object Object],[object Object],[object Object],[object Object],www.heatflux.com
Case Studies ,[object Object],[object Object],www.heatflux.com
Citgo, Corpus Christi No. 4 Platformer Heater ,[object Object],[object Object],[object Object],[object Object],[object Object],www.heatflux.com
Current  Heater Operation www.heatflux.com Parameter Units Operating  Value Total Heater Duty MMBtu/hr 158.10 Radiant Heat Duty MMBtu/hr 120.19 Convection Heat Duty MMBtu/hr 37.91 Firing Rate MMBtu/hr 229.20 Efficiency % 68.98
Flow Scheme - Before Revamp #4 Platformer Heater www.heatflux.com
Existing  #4 Platformer Heater www.heatflux.com
Proposed Conventional Design High Pressure Drop www.heatflux.com
Conventional Design with  Series Flow  www.heatflux.com
Comparison of Pressure Drop at 22,000 BPD  www.heatflux.com Pressure Drop, psi Original Design  Series flow Design Cell 1 3.1 4.5 Cell 2 3.3 4.6 Cell 3 1.2 2.5 Cell 4 1.1 2.3 Total 8.7 13.9
Disadvantages ,[object Object],[object Object],[object Object],[object Object],www.heatflux.com
FIS Split Flow* Scheme *  Split flow - US Patent  www.heatflux.com
FIS Split flow  *  design - Proposed * Patented. www.heatflux.com
Comparison (Cell 1) Parameters at 22,000 BPD www.heatflux.com Parameter Original Design  Split flow Design Pressure Drop, psi 3.1 2.1 Firebox temperature, F 1,615 1,551 Radiant flux, Btu/hr ft2 19,823 15,047 Radiant tube metal temp, F 1,151 1,120 Firing rate, MMBtu/hr 116.35 82.65
#4 Platformer Heater Data Comparison www.heatflux.com Item Units  Before Revamp After Revamp Capacity BPD 18,500 24,000 Heat Duty MM Btu/hr 158.0 194.5 Heat Release MM Btu/hr 234 225 Efficiency % 67.50 86.60 Stack Temp. °F 1,092 478 Fuel MSCFH 244 242.8 Fuel Savings $/annum 5.8 Million* *Based on $6.0 / MM Btu
#4 Platformer Heater  Before and After Revamp www.heatflux.com
Case Study-2
Platformer Heaters - Existing ,[object Object],[object Object],[object Object],[object Object],[object Object],www.heatflux.com
Platformer Heaters (H-20/21/22) www.heatflux.com Parameter Units Original Design Total Heater Duty MMBtu/hr 155.98 Radiant Heat Duty MMBtu/hr 74.09 Convection Heat Duty MMBtu/hr 81.89 Radiant Fuel Efficiency % 54.2
Plan View of heater www.heatflux.com
Convection Section ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],www.heatflux.com
H-18- Hydrotreater Charge Heater ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],www.heatflux.com
H-19 Hydrotreater Stripper Reboiler ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],www.heatflux.com
H-23 Depropanizer Reboiler ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],www.heatflux.com
Field Survey ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],www.heatflux.com
Operating Data Simulation Results ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],www.heatflux.com
Conventional Scheme ,[object Object],[object Object],www.heatflux.com Description Units Design Stack temperature °F 404 BFW flow rate Lb/hr 94,000 SSH flow rate Lb/hr 92,120 SSH temperature °F 623 Steam pressure psig 472
Split Flow Scheme ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],www.heatflux.com
Valero Proposed Revamp – Split Flow Scheme www.heatflux.com
Split Flow for H-20/H-21 ,[object Object],[object Object],www.heatflux.com
H-18/H-19/ H-23 Revamping Options ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],www.heatflux.com
H-18/H-19/H-23 Revamping Options  ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],www.heatflux.com
Valero Proposed Revamp – Split Flow Scheme www.heatflux.com
H-18/H-19/H-23 Split Flow  ,[object Object],[object Object],[object Object],[object Object],www.heatflux.com
Split flow Convection Section ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],www.heatflux.com
Proposed Split Flow Revamp ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],www.heatflux.com
Split flow – Control Scheme ,[object Object],[object Object],[object Object],www.heatflux.com
Advantages of FIS  Split flow scheme ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],www.heatflux.com
Thank you very much  ,[object Object],www.heatflux.com

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A new approach to improving heater efficiency

  • 1.
  • 2. Typical Fired Heater Fluid------  Convection section  Radiant section www.heatflux.com
  • 3. Conventional Approach to Efficiency Improvement www.heatflux.com Additional Heat Transfer Surface in Convection Section
  • 4. Split flow Fired Heater www.heatflux.com
  • 5.
  • 6.
  • 7.
  • 8.
  • 9. Current Heater Operation www.heatflux.com Parameter Units Operating Value Total Heater Duty MMBtu/hr 158.10 Radiant Heat Duty MMBtu/hr 120.19 Convection Heat Duty MMBtu/hr 37.91 Firing Rate MMBtu/hr 229.20 Efficiency % 68.98
  • 10. Flow Scheme - Before Revamp #4 Platformer Heater www.heatflux.com
  • 11. Existing #4 Platformer Heater www.heatflux.com
  • 12. Proposed Conventional Design High Pressure Drop www.heatflux.com
  • 13. Conventional Design with Series Flow www.heatflux.com
  • 14. Comparison of Pressure Drop at 22,000 BPD www.heatflux.com Pressure Drop, psi Original Design Series flow Design Cell 1 3.1 4.5 Cell 2 3.3 4.6 Cell 3 1.2 2.5 Cell 4 1.1 2.3 Total 8.7 13.9
  • 15.
  • 16. FIS Split Flow* Scheme * Split flow - US Patent www.heatflux.com
  • 17. FIS Split flow * design - Proposed * Patented. www.heatflux.com
  • 18. Comparison (Cell 1) Parameters at 22,000 BPD www.heatflux.com Parameter Original Design Split flow Design Pressure Drop, psi 3.1 2.1 Firebox temperature, F 1,615 1,551 Radiant flux, Btu/hr ft2 19,823 15,047 Radiant tube metal temp, F 1,151 1,120 Firing rate, MMBtu/hr 116.35 82.65
  • 19. #4 Platformer Heater Data Comparison www.heatflux.com Item Units Before Revamp After Revamp Capacity BPD 18,500 24,000 Heat Duty MM Btu/hr 158.0 194.5 Heat Release MM Btu/hr 234 225 Efficiency % 67.50 86.60 Stack Temp. °F 1,092 478 Fuel MSCFH 244 242.8 Fuel Savings $/annum 5.8 Million* *Based on $6.0 / MM Btu
  • 20. #4 Platformer Heater Before and After Revamp www.heatflux.com
  • 22.
  • 23. Platformer Heaters (H-20/21/22) www.heatflux.com Parameter Units Original Design Total Heater Duty MMBtu/hr 155.98 Radiant Heat Duty MMBtu/hr 74.09 Convection Heat Duty MMBtu/hr 81.89 Radiant Fuel Efficiency % 54.2
  • 24. Plan View of heater www.heatflux.com
  • 25.
  • 26.
  • 27.
  • 28.
  • 29.
  • 30.
  • 31.
  • 32.
  • 33. Valero Proposed Revamp – Split Flow Scheme www.heatflux.com
  • 34.
  • 35.
  • 36.
  • 37. Valero Proposed Revamp – Split Flow Scheme www.heatflux.com
  • 38.
  • 39.
  • 40.
  • 41.
  • 42.
  • 43.

Editor's Notes

  1. Premcor Refinining Energy Managers Conference February 9, 2005 Furnace Improvements, Low cost solutions for fired heaters
  2. Reliance Refinery, Jaam Nagar India February 24, 2007 What is this Novel Approach? Typically in a fired heater, the feed is preheated in the convection section and further heated in the radiant section.
  3. Premcor Refinining Energy Managers Conference February 9, 2005 Furnace Improvements, Low cost solutions for fired heaters
  4. Reliance Refinery, Jaam Nagar India February 24, 2007
  5. Premcor Refinining Energy Managers Conference February 9, 2005 Furnace Improvements, Low cost solutions for fired heaters
  6. Premcor Refinining Energy Managers Conference February 9, 2005 Furnace Improvements, Low cost solutions for fired heaters
  7. Flint Hills - Corpus Christi, TX 12/01/11
  8. Premcor Refinining Energy Managers Conference February 9, 2005 Furnace Improvements, Low cost solutions for fired heaters
  9. Premcor Refinining Energy Managers Conference February 9, 2005 Furnace Improvements, Low cost solutions for fired heaters
  10. Premcor Refinining Energy Managers Conference February 9, 2005 Furnace Improvements, Low cost solutions for fired heaters
  11. Premcor Refinining Energy Managers Conference February 9, 2005 Furnace Improvements, Low cost solutions for fired heaters
  12. Premcor Refinining Energy Managers Conference February 9, 2005 Furnace Improvements, Low cost solutions for fired heaters
  13. Premcor Refinining Energy Managers Conference February 9, 2005 Furnace Improvements, Low cost solutions for fired heaters
  14. Premcor Refinining Energy Managers Conference February 9, 2005 Furnace Improvements, Low cost solutions for fired heaters
  15. Premcor Refinining Energy Managers Conference February 9, 2005 Furnace Improvements, Low cost solutions for fired heaters
  16. Premcor Refinining Energy Managers Conference February 9, 2005 Furnace Improvements, Low cost solutions for fired heaters
  17. Premcor Refinining Energy Managers Conference February 9, 2005 Furnace Improvements, Low cost solutions for fired heaters
  18. Premcor Refinining Energy Managers Conference February 9, 2005 Furnace Improvements, Low cost solutions for fired heaters
  19. Premcor Refinining Energy Managers Conference February 9, 2005 Furnace Improvements, Low cost solutions for fired heaters
  20. Premcor Refinining Energy Managers Conference February 9, 2005 Furnace Improvements, Low cost solutions for fired heaters
  21. Valero, Texas City Refinery,TX 12/01/11
  22. Valero, Texas City Refinery,TX 12/01/11
  23. Valero, Texas City Refinery,TX 12/01/11
  24. Valero, Texas City Refinery,TX 12/01/11
  25. Valero, Texas City Refinery,TX 12/01/11
  26. Valero, Texas City Refinery,TX 12/01/11
  27. Valero, Texas City Refinery,TX 12/01/11
  28. Valero, Texas City Refinery,TX 12/01/11
  29. Valero, Texas City Refinery,TX 12/01/11
  30. Valero, Texas City Refinery,TX 12/01/11
  31. Valero, Texas City Refinery,TX 12/01/11
  32. Valero, Texas City Refinery,TX 12/01/11
  33. Valero, Texas City Refinery,TX 12/01/11
  34. Valero, Texas City Refinery,TX 12/01/11
  35. Valero, Texas City Refinery,TX 12/01/11
  36. Valero, Texas City Refinery,TX 12/01/11
  37. Valero, Texas City Refinery,TX 12/01/11
  38. Valero, Texas City Refinery,TX 12/01/11
  39. Valero, Texas City Refinery,TX 12/01/11
  40. Valero, Texas City Refinery,TX 12/01/11
  41. Premcor Refinining Energy Managers Conference February 9, 2005 Furnace Improvements, Low cost solutions for fired heaters
  42. Premcor Refinining Energy Managers Conference February 9, 2005 Furnace Improvements, Low cost solutions for fired heaters
  43. Premcor Refinining Energy Managers Conference February 9, 2005 Furnace Improvements, Low cost solutions for fired heaters