Process for cogasifying and cofiring engineered fuel with coal

• US 8,915,199 B2
• Filed: 04/23/2012
• Issued: 12/23/2014
• Est. Priority Date: 04/22/2011
• Status: Expired due to Fees

• Current Assignee: Repower IP LLC
• Original Assignee: Accordant Energy, LLC
• Inventors: Bohlig, James W., Bai, Dingrong
• Primary Examiner(s): Rinehart, Kenneth
• Assistant Examiner(s): Nguyen, Bao D
• Application Number:
  US13/453,791
• Publication Number:
  US 20120266793A1
• Time in Patent Office: 974 Days
• Field of Search: 110/342, 110/218, 110/229, 110/234, 110/235, 110/341, 110/211, 110/214, 110/216, 110/243, 110/245, 110/246, 110/344, 110/345, 110/346, 110/233, 110/262, 482/09, 481/97.R, 482/10
• US Class Current: 110/342
• CPC Class Codes: F23G 2204/101 solid fuel
• CPC Class Codes: F23G 5/027 pyrolising or gasifying stage pyrolisation of sludge C02F11/00; destructive distillation of carbonaceous materials C10B53/00
• CPC Class Codes: F23G 5/0276 using direct heating
• CPC Class Codes: F23G 5/14 including secondary combustion
• CPC Class Codes: F23G 7/10 of field or garden waste or biomasses

Abstract

Described is an integrated process of cogasifying an engineered fuel, formulated to be suitable for working under reducing environment, with coal and cofiring another engineered fuel, formulated to be suitable for working under oxidizing environment, with coal to produce electric power.

Claims

1. An integrated method for varying an overall cofiring ratio of a combustion system, comprising:

introducing a first engineered fuel and a first fossil fuel into a gasifier at a first cofiring ratio;

cogasifying the first engineered fuel and the first fossil fuel to produce syngas;

introducing a second engineered fuel and a second fossil fuel into a combustor at a second cofiring ratio;

introducing the produced syngas into the combustor;

cofiring the second engineered fuel, the second fossil fuel, and the produced syngas; and

varying the overall cofiring ratio of combustion by varying an input characteristic of at least two of the first engineered fuel, the first fossil fuel, the second engineered fuel, and the second fossil fuel, wherein the first cofiring ratio and the second cofiring ratio are unchanged.

2. The method of claim 1, wherein the varied input characteristic is one of weight, weight per unit time, heat value, and heat value per unit time.

3. The method of claim 1, wherein the overall cofiring ratio is in a range from about 10% to about 50%.

4. The method of claim 1, wherein the second cofiring ratio is in a range from about 5 to about 20%.

5. The method of claim 1, wherein the first cofiring ratio is in a range from about 30% to about 70%.

6. The method of claim 1, wherein the fossil fuel comprises one or more variety of coal.

7. The method of claim 6, wherein the one or more variety of coal are selected from the group consisting of:

anthracite, lignite, bituminous coal, and mixtures thereof.

8. The method of claim 1, wherein the first engineered fuel is optimized for burning in a reducing environment, and where the second engineered fuel is optimized for burning in an oxidizing environment.

9. The method of claim 1, wherein at least one of the first engineered fuel and the second engineered fuel comprises one or more sorbents.

10. The method of claim 9, wherein the one or more sorbents are selected from the group consisting of sodium sesquicarbonate (Trona), sodium bicarbonate, sodium carbonate, zinc ferrite, zinc copper ferrite, zinc titanate, copper ferrite aluminate, copper aluminate, copper manganese oxide, nickel supported on alumina, zinc oxide, iron oxide, copper, copper (I) oxide, copper (II) oxide, limestone, lime, Fe, FeO, Fe₂O₃, Fe₃O₄, iron filings, CaCO₃, Ca(OH)₂, CaCO₃.MgO, CaMg₂(CH₃COO)₆, silica, alumina, china clay, kaolinite, bauxite, emathlite, attapulgite, coal ash, egg shells, Ca-montmorillonite, calcium magnesium acetate, calcium acetate, calcium formate, calcium benzoate, calcium propionate, and magnesium acetate, and mixtures thereof.

11. The method of claim 9, wherein the first engineered fuel comprises one or more sorbents, and wherein said cogasifying is carried out at a temperature above the sintering temperature of the one or more sorbents.

12. The method of claim 1, wherein the cofiring step comprises one of direct cofiring and indirect cofiring.

13. The method of claim 1, wherein the combustor is a boiler, wherein cofiring comprises:

combusting the second engineered fuel and the second fossil fuel in a combustion zone of the boiler; and

combusting the syngas in a reburn zone of the boiler.

14. A combustion system, comprising:

a gasifier for receiving a first engineered fuel and a first fossil fuel at a first cofiring ratio, said gasifier operable for cogasifying the first engineered fuel and the first fossil fuel to produce syngas;

a combustor for receiving a second engineered fuel and a second fossil fuel at a second cofiring ratio, said combustor further receiving the syngas from the gasifier, said combustor operable for cofiring the second engineered fuel, the second fossil fuel, and the produced syngas; and

wherein the combustion system is operable to vary an overall cofiring ratio of the combustion system by varying an input characteristic of at least two of the first engineered fuel, the first fossil fuel, the second engineered fuel, and the second fossil fuel, wherein the first cofiring ratio and the second cofiring ratio are unchanged.

15. The system of claim 14, wherein the varied input characteristic is one of weight, weight per unit time, heat value, and heat value per unit time.

16. The system of claim 14, wherein the overall cofiring ratio is in a range from about 10% to about 50%.

17. The system of claim 14, wherein the second cofiring ratio is in a range from about 5% to about 20%.

18. The system of claim 14, wherein the first cofiring ratio is in a range from about 30% to about 70%.

19. The system of claim 14, wherein the fossil fuel comprises one or more variety of coal.

20. The system of claim 19, wherein the one or more variety of coal is selected from the group consisting of:

anthracite, lignite, bituminous coal and mixtures thereof

21. The system of claim 14, wherein the first engineered fuel is optimized for burning in a reducing environment, and where the second engineered fuel is optimized for burning in an oxidizing environment.

22. The system of claim 14, wherein at least one of the first engineered fuel and the second engineered fuel comprises one or more sorbents.

23. The system of claim 22, wherein the one or more sorbents is selected from the group consisting of sodium sesquicarbonate (Trona), sodium bicarbonate, sodium carbonate, zinc ferrite, zinc copper ferrite, zinc titanate, copper ferrite aluminate, copper aluminate, copper manganese oxide, nickel supported on alumina, zinc oxide, iron oxide, copper, copper (I) oxide, copper (II) oxide, limestone, lime, Fe, FeO, Fe₂O₃, Fe₃O₄, iron filings, CaCO₃, Ca(OH)₂, CaCO₃.MgO, CaMg₂(CH₃COO)₆, silica, alumina, china clay, kaolinite, bauxite, emathlite, attapulgite, coal ash, egg shells, Ca-montmorillonite, calcium magnesium acetate, calcium acetate, calcium formate, calcium benzoate, calcium propionate, and magnesium acetate, and mixtures thereof.

24. The system of claim 14, wherein the first engineered fuel comprises one or more sorbents, and wherein the gasifier carries out the cogasifying at a temperature above the sintering temperature of the one or more sorbents.

25. The system of claim 14, wherein the combustor may be directly or indirectly cofired.

26. The system of claim 14, wherein the combustor is a boiler, wherein the boiler is operable for combusting the second engineered fuel and the second fossil fuel in a combustion zone of the boiler, and wherein the boiler is further operable for combusting the syngas in a reburn zone of the boiler.