IGCC design and operation for maximum plant output and minimum heat rate

• US 7,874,139 B2
• Filed: 10/13/2006
• Issued: 01/25/2011
• Est. Priority Date: 10/13/2006
• Status: Expired due to Fees

• Current Assignee: Siemens Energy Incorporated (Siemens AG)
• Original Assignee: Siemens Energy Incorporated (Siemens AG)
• Inventors: Briesch, Michael Scot, Sullivan, Terrence Blaise
• Primary Examiner(s): Rodríguez; William H
• Assistant Examiner(s): NGUYEN, ANDREW H
• Application Number:
  US11/581,166
• Publication Number:
  US 20080087022A1
• Time in Patent Office: 1,565 Days
• Field of Search: 60/394.64, 60/392.81, 60/395.11, 607/36, 607/81, 607/79, 607/76, 607/73, 60/394.63, 60/391.2
• US Class Current: 60/39.464
• CPC Class Codes: F01K 23/068 in combination with an oxygen producing plant, e.g. an air separation plant
• CPC Class Codes: F02C 3/28 using a separate gas producer for gasifying the fuel before combustion
• CPC Class Codes: F02C 9/40 specially adapted to the use of a special fuel or a plurality of fuels
• CPC Class Codes: Y02E 20/16 Combined cycle power plant [CCPP], or combined cycle gas turbine [CCGT]
• CPC Class Codes: Y02E 20/18 Integrated gasification combined cycle [IGCC], e.g. combined with carbon capture and storage [CCS]

Abstract

A system and method for operating an integrated gasification combined cycle (IGCC) gas turbine system that utilizes the fuel stream as a means of controlling the operation of the IGCC to achieve a target output and efficiency. The methods and systems enable the IGCC to be operated at reduced output, but without a corresponding drop in efficiency as compared to prior art gas turbine systems. Conversely, the IGCC may be operated at higher outputs. The methods and systems achieve the target output and efficiency by adjusting the chemical potential energy, sensible energy, or both of a fuel stream entering the combustion turbine. The chemical potential energy and sensible energy may be manually or automatically controlled.

Claims

1. A method for operating an integrated gasification combined cycle gas turbine having a design operation point for a chemical potential energy of a fuel stream, comprising:

operating an integrated gasification combined cycle gas turbine at a design operation point output and efficiency;

determining a target output and target efficiency, whereby at least one of the target output and the target efficiency is different than the design operation point output and efficiency of the integrated gasification combined cycle gas turbine; and

adjusting a chemical potential energy of a fuel stream during operation of the integrated gasification combined cycle gas turbine by changing a heating value of the fuel stream to achieve the target output or target efficiency;

wherein changing the heating value of the fuel stream comprises at least one of;

a) increasing the heating value of the fuel stream and decreasing a flow rate of the fuel stream to effect at least one of a decrease in output or an increase in efficiency of the integrated gasification combined cycle gas turbine; and

b) decreasing the heating value of the fuel stream and increasing a flow rate of the fuel stream to effect at least one of an increase in output or a decrease in efficiency of the integrated gasification combined cycle gas turbine.

2. The method of claim 1, further comprising:

measuring a fuel energy characteristic of the fuel stream; and

adjusting the chemical potential energy of the fuel stream in response to the measured fuel energy characteristic to achieve the target output or target efficiency.

3. The method of claim 1, wherein the heating value of the fuel stream is adjusted by mixing the fuel stream with a mixing stream having a heating value different from the heating value of the fuel stream.

4. The method of claim 3, wherein the mixing stream comprises a fluid selected from the group consisting of nitrogen, water, steam, natural gas, synthesis gas, and combinations thereof.

14. The method of claim 1, wherein the target output and target efficiency correspond to a part load operation of the integrated gasification combined cycle gas turbine having a power output less than the power output at the design operation point.

5. A method for operating an integrated gasification combined cycle gas turbine having a design operation point for a sensible energy of a fuel stream, comprising:

operating an integrated gasification combined cycle gas turbine at a design operation point output and efficiency;

determining a target output and target efficiency, whereby at least one of the target output and the target efficiency is different than the design operation point output and efficiency of the integrated gasification combined cycle gas turbine; and

adjusting a sensible energy of a fuel stream during operation of the integrated gasification combined cycle gas turbine by changing a temperature of the fuel stream to achieve the target output or target efficiency;

wherein changing the temperature of the fuel stream comprises at least one of;

a) increasing the fuel stream temperature and decreasing the flow rate of the fuel stream to effect at least one of a decrease in output or an increase in efficiency of the integrated gasification combined cycle gas turbine; and

b) decreasing the fuel stream temperature and increasing the flow rate of the fuel system to effect at least one of an increase in output or a decrease in efficiency of the integrated gasification combined cycle gas turbine.

6. The method of claim 5, wherein said integrated gasification combined cycle gas turbine has a design operation point for a chemical potential energy comprising a heating value of the fuel stream, further comprising adjusting the chemical potential energy of the fuel stream to achieve the target output or efficiency.

7. The method of claim 5, further comprising:

measuring a fuel energy characteristic of the fuel system; and

adjusting the sensible energy of the fuel stream in response to the measured fuel energy characteristic to achieve the target output or efficiency.

8. The method of claim 5, wherein the fuel stream temperature is adjusted by mixing the fuel stream with a mixing stream comprising a gas selected from the group consisting of nitrogen, water, steam, natural gas, synthesis gas, and combinations thereof.

9. The method of claim 5, wherein the fuel stream temperature is adjusted using a closed system heat exchanger and an exchanger stream having a temperature different from the fuel stream.

10. The method of claim 9, wherein the exchanger stream comprises a fluid selected from the group consisting of synthesis gas, steam, nitrogen gas, flue gas, water, air, and combinations thereof.

15. The method of claim 5, wherein the target output and target efficiency correspond to a part load operation of the integrated gasification combined cycle gas turbine having a power output less than the power output at the design operation point.

11. An integrated gasification combined cycle gas turbine system comprising:

a combustor;

a turbine;

a fuel stream having a design operation point for a chemical potential energy comprising a heating value of the fuel stream and a sensible energy comprising a temperature of the fuel stream, the fuel being combusted in the combustor and expanded in the turbine to generate power output;

a mechanism for adjusting the heating value or the temperature of the fuel stream to a target value different than the design operation point prior to entering the combustor, the target value providing a target output and target efficiency wherein at least one of the target output and target efficiency is different than an output and efficiency for said design operation point; and

the mechanism for adjusting the chemical potential energy or the sensible energy of the fuel stream comprising a control system including a sensor and processor for sensing a fuel energy characteristic of the fuel stream entering the combustor and changing at least one of the heating value and the temperature of the fuel stream in response to the sensed fuel energy characteristic to change the chemical potential energy of the fuel stream from the design operation point to the target value during operation of the integrated gasification combined cycle gas turbine system;

wherein the target output and target efficiency correspond to a part load operation of the integrated gasification combined cycle gas turbine system having a power output less than the power output at the design operation point.

12. The system of claim 11, wherein the mechanism for adjusting the temperature is a closed system heat exchanger or a mixing valve used to combine the fuel stream with a mixing stream having a temperature different from the fuel stream.

13. The system of claim 11, wherein the mechanism for adjusting the heating value comprises a mixing valve used to combine the fuel stream with a mixing stream having a different heating value than the fuel stream.