Thermal chemical recuperation method and system for use with gas turbine systems

• US 5,896,738 A
• Filed: 04/07/1997
• Issued: 04/27/1999
• Est. Priority Date: 04/07/1997
• Status: Expired due to Fees

• Current Assignee: Siemens Westinghouse Power Corporation
• Original Assignee: Siemens Westinghouse Power Corporation
• Inventors: Bannister, Ronald L., Yang, Wen-Ching, Newby, Richard A.
• Primary Examiner(s): Freay, Charles G.
• Assistant Examiner(s): KIM, TAE JUN
• Application Number:
  US08/835,341
• Time in Patent Office: 750 Days
• Field of Search: 60/39.02, 60/39.05, 60/39.12, 60/39.5, 60/39.511, 60/39.182, 60/39.23
• US Class Current: 60/775
• CPC Class Codes: F01K 21/047 having at least one combustion gas turbine

Abstract

A system and method for efficiently generating power using a gas turbine, a steam generating system (20, 22, 78) and a reformer. The gas turbine receives a reformed fuel stream (74) and an air stream and produces shaft power and exhaust. Some of the thermal energy from the turbine exhaust is received by the reformer (18). The turbine exhaust is then directed to the steam generator system that recovers thermal energy from it and also produces a steam flow from a water stream. The steam flow and a fuel stream are directed to the reformer that reforms the fuel stream and produces the reformed fuel stream used in the gas turbine.

Claims

1. A power generating system comprising:

a) combustor means for receiving a reformed fuel stream and a first portion of a compressed air stream and producing a combustor exhaust stream;

b) gas turbine means for receiving at an input a combination of the combustor exhaust stream and a second portion of the compressed air stream, which has bypassed the combustor, and producing shaft power and a turbine exhaust stream having thermal energy therefrom, the turbine exhaust stream being combined with a third portion of the compressed air stream upstream of a reforming means;

c) steam generating means for receiving said combined turbine exhaust and compressed air stream and a water stream and producing a steam flow and a system exhaust stream therefrom; and

d) said reforming means receiving a fuel stream, said steam flow, and a portion of said combined turbine exhaust and compressed air stream thermal energy, and producing said reformed fuel stream therefrom.

2. The system of claim 1, wherein said fuel stream is natural gas, liquefied natural gas, synthetically-derived hydrocarbon fuel, or a mixture thereof.

3. The system of claim 1, wherein said steam generating means comprises:

a) evaporator means for receiving said combined turbine exhaust and compressed air stream and a heated water stream and producing said steam flow and a cooled combined turbine exhaust and compressed air stream therefrom;

b) economizer means for receiving said cooled combined turbine exhaust and compressed air stream and said water and producing said heated water stream and said system exhaust stream therefrom; and

c) water control means for adjusting a flowrate of said water stream.

4. The system of claim 1, wherein said power generating system is an electricity-steam cogeneration plant.

5. The system of claim 1, wherein said gas turbine means comprises:

a) compressor means for receiving an inlet air stream and producing the compressed air stream therefrom; and

b) directing means for splitting of the third portion of said compressed air stream and for combining said compressed stream third portion with said turbine exhaust stream.

6. The system of claim 1, wherein said reforming means comprises:

a) a reformer with heat exchange means for receiving said combined turbine exhaust and compressed air stream thermal energy; and

b) fuel control means for adjusting a flowrate of said fuel stream.

7. A method for generating power comprising the steps of:

a) compressing an air stream to produce a compressed air stream;

b) burning a reformed fuel stream in a first portion of said compressed air stream to produce a combustor exhaust stream;

c) expanding in combination said combustor exhaust stream and a second portion of said compressed air streamer which has by-passed the combustor, throughout a turbine means for producing shaft power and a turbine exhaust stream having thermal energy, the turbine exhaust stream being combined with a third portion of said compressed air stream upstream of a reformer;

d) reforming a fuel stream with a steam flow and a first portion of said combined turbine exhaust and compressed air stream thermal energy to produce said reformed fuel stream; and

e) generating said steam flow by heating a water stream with a second portion of said combined turbine exhaust and compressed air stream thermal energy.

8. The method of claim 7, wherein said generating said steam flow step further comprises the steps of:

a) directing said combined turbine exhaust and compressed air stream and a heated water stream into evaporator means for producing said steam flow and a cooled combined turbine exhaust and compressed air flow therefrom; and

b) directing a water stream and said cooled combined turbine exhaust and compressed air stream into economizer means for producing said heated water stream and a system exhaust stream therefrom.

9. The method of claim 8, wherein said generating said steam flow step further comprises the step of adjusting a flow rate of said water stream to generate temperature difference of approximately 18°

F. between said cooled combined turbine exhaust and compressed air stream and said heated water stream.

10. The method of claim 7, wherein said reforming step further comprises the step of reforming a fuel stream of natural gas, liquefied natural gas, synthetically-derived hydrocarbon fuel, or a mixture thereof.

11. The method of claim 10, wherein said reforming step further comprises the step of adjusting flow rates of said steam flow and said fuel stream of natural gas such that the steam-to-natural-gas mass ratio thereof is approximately 6.5.

12. The method of claim 11, wherein said reforming step further comprises the steps of:

a) reforming said fuel stream of natural gas comprising methane; and

b) converting approximately 59.6 mole % of said methane to carbon monoxide.

13. The method of claim 7, wherein said reforming step occurs between approximately 400°

F. and 1100°

F.

14. The method of claim 7, wherein said compressing step further comprising the step of compressing said air stream first portion to a pressure ratio of approximately 15.

15. The method of claim 7, wherein said burning step further comprises the step of producing said combustor exhaust stream comprising approximately 6.7 mole % oxygen.