Heat recovery method and device suitable for combined cycles

• US 5,570,578 A
• Filed: 12/01/1993
• Issued: 11/05/1996
• Est. Priority Date: 12/02/1992
• Status: Expired due to Fees

• Current Assignee: Stein Industrie
• Original Assignee: Stein Industrie
• Inventors: Morin, Jean-Xavier, Hrisafovic, Francine, Hubert, Georges, Saujet, Jean-Fran.cedilla.ois, Amadieu, Pascale
• Primary Examiner(s): HEYMAN, LEONARD
• Application Number:
  US08/159,541
• Time in Patent Office: 1,070 Days
• Field of Search: 60/647, 60/655, 60/676, 60/677, 60/679, 122/1 R, 122/1 C, 122/DIG. 5
• US Class Current: 60/647
• CPC Class Codes: F01K 23/106 with water evaporated or preheated at different pressures in exhaust boiler
• CPC Class Codes: F01K 7/32 the engines using steam of critical or overcritical pressure
• CPC Class Codes: Y02E 20/16 Combined cycle power plant [CCPP], or combined cycle gas turbine [CCGT]

Abstract

A heat recovery method is disclosed suitable for combined gas turbine/steam turbine cycles including at the exhaust of a gas turbine a waste heat boiler in which water is first treated in a degassing unit connected to a first evaporator and comprising a certain number of heat exchangers. The boiler uses an ultrasupercritical steam cycle with four pressure levels with subcritical fluid intermediate evaporator stages.

Claims

1. Apparatus for implementing a heat recovery method suitable for combined gas turbine/steam turbine plant, said apparatus using an ultrasupercritical steam cycle operating at a first, second, third and fourth pressure levels and using a combination of interleaved heat exchangers and subcritical fluid intermediate evaporator stages, said apparatus comprising:

a degassing unit for feeding circuits at said four pressure levels;

a first evaporator connected to said degassing unit;

a first group of at least four economizer type exchangers, connected to said degassing unit, for receiving fluids at said first, second, third and fourth pressure levels;

a first reservoir connected to one of said exchangers of said first group for receiving one of said fluids;

a second evaporator connected to said first reservoir and operating at said first pressure level;

a second group of at least three economizer type heat exchangers connected to at least three economizer type heat exchangers of said first group for receiving fluids at said second, third and fourth pressure levels;

a second reservoir connected to one of said exchangers of said second group;

a third evaporator connected to said second reservoir and operating at said second pressure level;

at least one first superheater, connected to said first reservoir, for outputting steam at said first pressure level;

a third group of at least two economizer type exchangers connected to at least two economizer type heat exchangers of said second group, for receiving said fluids at said third and fourth pressure levels;

a third reservoir connected to one of said exchangers of said third group;

a fourth evaporator connected to said third reservoir and operating at said third pressure level;

at least one second superheater connected to said second reservoir, for outputting steam at said second pressure level;

a fourth group of at least two economizer and superheater type exchangers connected to at least two exchangers of said third group for receiving said fluids at said third and fourth pressure levels, said exchanger for said fluid at said third pressure level being connected to an outlet for steam at said third pressure level;

a fifth group of at least one exchanger connected to at least one exchanger of said fourth group and operating at said fourth pressure level;

a sixth group of at least three exchangers, a first one of said exchangers of said sixth group receiving and reheating fluids at said third pressure level from said exchanger of said fourth group for said fluid at said third pressure level, a second one of said exchangers of said sixth group receiving and heating fluids at said second pressure level from said second superheated and a third one of said exchangers of said sixth group superheating steam at said fourth pressure level from said exchanger of said fifth group, said third exchanger being connected to a outlet for outputting steam at said fourth pressure level.

3. Method according to claim 1 wherein the heat exchangers and said evaporator stages are interleaved.

2. A heat recovery method suitable for combined gas turbine/steam turbine cycles, comprising the steps of:

receiving in a waste heat boiler gas exhaust from a gas turbine;

passing water through an evaporator of said waste heat boiler;

treating said water in a degassing unit of said waste heat boiler;

passing said treated water through an evaporator of said waste heat boiler;

passing outputs of said degassing unit through a plurality of heat exchangers and subcritical fluid intermediate evaporator stages utilizing an ultrasupercritical steam cycle, wherein said cycle operates at a first, second, third and fourth pressure levels, said first, second, third and fourth pressure levels being 6, 28, 96 and 320 bars, respectively; and

producing steam outputs at each of said four pressure levels.

4. A heat recovery system for combined gas turbine/steam turbine cycles, said system comprising:

a waste heat boiler disposed at the exhaust of a gas turbine, said waste heat boiler having a degassing unit for treating water, a first evaporator connected to said degassing unit and a plurality of heat exchangers and subcritical fluid intermediate evaporator stages for receiving an output of said degassing unit;

said waste heat boiler operating with an ultrasupercritical steam cycle at a first, second, third and fourth pressure levels; and

a steam turbine having a high pressure stage, a first intermediate pressure stage, a second intermediate pressure stage and a low pressure stage;

said high pressure stage being connected to receive steam at said fourth pressure level from said waste heat boiler and heated fluid from said degassing unit through a circulating fluidized bed boiler, said heated fluid being heated by exchangers of said circulating fluidized bed boiler.

5. The system according to claim 4, wherein said waste heat boiler further comprises a reheater, said reheater operating in conjunction with said circulating fluidized bed boiler for providing said heated fluid to said high pressure stage.

6. A heat recovery system for combined gas turbine/steam cycles, said system comprising:

a waste heat boiler disposed at the exhaust of a gas turbine, said waste heat boiler having a degassing unit for treating water, a first evaporator connected to said degassing unit and a plurality of heat exchangers and subcritical fluid intermediate evaporating stages for receiving an output of said degassing unit;

said waste heat boiler operating with an ultrasupercritical steam cycle at a first, second, third and fourth pressure level; and

a steam turbine having a high pressure stage, a first intermediate pressure stage, a second intermediate pressure stage and a low pressure stage;

said first intermediate pressure stage receiving steam from exhaust of said high pressure stage, said steam being reheated by exchangers of a circulating fluidized bed boiler and by a reheater receiving steam at said third pressure level from said waste heat boiler.

7. A heat recovery system for a combined gas turbine/steam turbine cycles, said system comprising:

a waste heat boiler disposed at the exhaust of a gas turbine, said waste heat boiler having a degassing unit for treating water, a first evaporator connected to said degassing unit and a plurality of heat exchangers and subcritical fluid intermediate evaporating stages for receiving an output of said degassing unit;

said waste heat boiler operating with an ultrasupercritical steam cycle at a first, second, third and fourth pressure level; and

a steam turbine having a high pressure stage, a first intermediate pressure stage, a second intermediate pressure stage and a low pressure stage;

said second intermediate pressure stage receiving steam from exhaust of said first intermediate pressure stage, said steam being reheated by exchangers of a circulating fluidized bed boiler and by a reheater receiving steam at said second pressure level from said waste heat boiler.