Steam attemperation circuit for a combined cycle steam cooled gas turbine

• US RE36,524 E
• Filed: 12/21/1998
• Issued: 01/25/2000
• Est. Priority Date: 11/04/1993
• Status: Expired due to Fees

• Current Assignee: General Electric Company
• Original Assignee: General Electric Company
• Inventors: Tomlinson, Leroy O.
• Primary Examiner(s): Casaregola, Louis J.
• Application Number:
  US09/217,085
• Time in Patent Office: 400 Days
• Field of Search: 60/39.02, 60/39.182, 122/7 R, 122/7 B
• US Class Current: 60/783
• CPC Class Codes: F01K 23/106 with water evaporated or preheated at different pressures in exhaust boiler
• CPC Class Codes: F02C 6/18 using the waste heat of gas-turbine plants outside the plants themselves, e.g. gas-turbine power heat plants using waste heat as source of energy for refrigeration plants F25B27/02; using the waste heat of a gasturbine for steam generation or in a steam cycle see F01K23/10
• CPC Class Codes: F02C 7/16 characterised by cooling medium
• CPC Class Codes: F02C 7/18 the medium being gaseous, e.g. air F02C7/125 takes precedence
• CPC Class Codes: F05D 2260/2322 steam
• CPC Class Codes: Y02E 20/16 Combined cycle power plant [CCPP], or combined cycle gas turbine [CCGT]

Abstract

In a combined cycle system including a gas turbine, a steam turbine and a heat recovery steam generator (HRSG), wherein gas turbine exhaust gas is used in the heat recovery steam generator for heating steam for the steam turbine, the gas turbine exhaust gas flowing from an entry end to an exit end of the HRSG, and wherein the HRSG includes at least one high pressure evaporator arranged to supply steam to a superheater including multiple passes including a first pass at one end thereof adjacent the evaporator, and a final pass adjacent an opposite end thereof and adjacent the entry end of the heat recovery steam generator, and one or more intermediate passes between the first and final passes, the improvement comprising an attemperating conduit not exposed to the gas turbine exhaust gas, connecting the one end and the opposite end of the superheater, bypassing the intermediate passes to thereby introduce cooler superheated steam from the one end into the superheater at the opposite end.

Claims

1. In a combined cycle system including a gas turbine, a steam turbine and a heat recovery steam generator, wherein gas turbine exhaust gas is used in the heat recovery steam generator for heating steam for the steam turbine, said gas turbine exhaust gas flowing from an entry end to an exit end of the heat recovery steam generator, and wherein said heat recovery steam generator includes at least one high pressure evaporator arranged to supply steam to a superheater including multiple passes including a first pass at one end thereof adjacent the evaporator, and a final pass adjacent an opposite end thereof and adjacent the entry end of the heat recovery steam generator, and one or more intermediate passes between the first and final passes, the improvement comprising an attemperating conduit not exposed to the gas turbine exhaust gas, connecting said one end of said superheater and said finish pass of said superheater, bypassing the intermediate passes to thereby introduce cooler superheated steam from said one end into said superheater at said opposite end to thereby allow a greater reduction in gas turbine exhaust temperature by reason of enhanced absorption of heat into the superheated steam in said opposite end of said superheater.

2. The system of claim 1 and including a flow control valve in said attemperating conduit.

3. The system of claim 1 and including means for supplying gas turbine cooling duty steam from a high pressure section of the steam turbine and conducting the gas turbine cooling duty steam to the gas turbine for cooling hot gas turbine parts, and means for returning the gas turbine cooling duty steam to an intermediate pressure section of the steam turbine.

4. The improvement of claim 3 wherein steam from a reheater in the heat recovery steam generator is mixed with said gas turbine cooling duty steam before the gas turbine cooling duty steam is returned to the intermediate pressure section of the steam turbine.

5. A reheat steam cycle configuration for a steam turbine and gas turbine combined cycle system comprising:

a steam turbine connected to a load;

a condenser for receiving exhaust steam from the steam turbine and for condensing said exhaust steam to water;

at least one heat recovery steam generator for receiving water from said condenser and for converting said water to steam for return to said steam turbine;

at least one gas turbine for supplying heat to said heat recovery steam generator in the form of exhaust gases;

wherein said at least one heat recovery steam generator includes a reheater of receiving cold reheat steam from the steam turbine and superheater for receiving high pressure steam from a high pressure evaporator within said heat recovery steam generator, said superheater having first and final passes at opposite ends with one or more intermediate passes therebetween, and wherein said cold reheat steam and said high pressure steam flow in a direction opposite to that of said exhaust gases from said gas turbine, said final pass of said superheater being located within said heat recovery steam generator where gas turbine exhaust gas temperatures are highest, and wherein an attemperating conduit extends outside said heat recovery steam generator and connects said opposite ends of said superheater so as to introduce cooler superheated steam from said first pass into said final pass of said superheater.

6. The system of claim 5 and including a flow control valve in said attemperating conduit.

7. The system of claim 5 and including means for supplying gas turbine cooling duty steam from a high pressure section of the steam turbine and conducting the gas turbine cooling duty steam to the gas turbine for cooling hot gas turbine parts, and means for returning the gas turbine cooling duty steam to an intermediate pressure section of the steam turbine.

8. A method of controlling temperature of superheated steam in a heat recovery steam generator which includes at least one evaporator and a superheater having first and second opposite ends thereof and one or more intermediate passes therebetween, the method comprising the steps of:

a) extracting superheater steam from the first end of the superheater in the heat recovery steam generator adjacent said at least one evaporator;

b) conducting the extracted steam outside the heat recovery steam generator; and

c) reintroducing the extracted steam into the heat recovery steam generator at the second end of said superheater.

9. The method of claim 8 and including the step of determining an amount of superheated steam to be reintroduced in step (b) by a control valve.

10. The method of claim 8 wherein the superheated steam is hotter at said second end than at said first end. .Iadd.

11. A method of controlling temperature of superheated steam in a heat recovery steam generator which includes at least one evaporator and a superheater having first and second opposite ends thereof and one or more intermediate passes therebetween, the method comprising the steps of:

a) extracting superheater steam from the first end of the superheater in the heat recovery steam generator;

b) conducting the extracted steam outside the heat recovery steam generator; and

c) reintroducing the extracted steam into the heat recovery steam generator at the second end of said superheater..Iaddend..Iadd.12. The method of claim 11 and including the step of determining an amount of superheated steam to be introduced in step (b) by a control valve..Iaddend.