Method and apparatus for operating a combined cycle power plant having a defective deaerator

• US 4,896,500 A
• Filed: 05/15/1989
• Issued: 01/30/1990
• Est. Priority Date: 05/15/1989
• Status: Expired due to Term

• Current Assignee: Siemens Power Generation, Inc.
• Original Assignee: Westinghouse Electric Corporation (Paramount Global (f/k/a ViacomCBS Inc.))
• Inventors: Richardson, Bennie L., Pavel, James, Myers, Gerald A.
• Primary Examiner(s): Ostrager, Allen M.
• Application Number:
  US07/352,599
• Time in Patent Office: 260 Days
• Field of Search: 60/646, 60/657, 60/39.182
• US Class Current: 60/39.182
• CPC Class Codes: B01D 19/0068 General arrangements, e.g. flowsheets B01D19/0063 takes precedence
• CPC Class Codes: F01K 23/101 Regulating means specially adapted therefor F01K23/105, F01K23/108 take precedence
• CPC Class Codes: F01K 23/108 Regulating means specially adapted therefor
• CPC Class Codes: Y02E 20/16 Combined cycle power plant [CCPP], or combined cycle gas turbine [CCGT]

Abstract

A deaerating subsystem in a combined cycle power plant includes a deaerator and a storage tank coupled to the deaerator, the deaerating subsystem being adapted for isolation of the deaerator when it is defective even while the overall combined cycle power plant is operating. Blind flanges are provided in a downcomer and in vapor risers between the deaerator and the storage tank for such isolation. Also provided is a condensate bypass for preventing the reception of the condensate by the deaerator, and for enabling the storage tank to receive the condensate directly. Thermal energy is input into the storage tank such that controlled amounts of heated condensate from the steam generator, and controlled amounts of dry steam can be input to the storage tank while the deaerator is isolated for repairs.

Claims

1. A combined cycle power plant, comprising:

a deaerator having primary and secondary functions, said primary function to degasify feedwater for use in the combined cycle power plant;

means for normally coupling said deaerator to the combined cycle power plant as a normally functioning part thereof;

means for isolating said deaerator from the combined cycle power plant during operations thereof; and

alternate means for performing said primary and secondary functions when said deaerator is isolated from the combined cycle power plant, during operations thereof, by said isolating means.

2. The combined cycle power plant according to claim 1, further comprising a low pressure storage tank coupled to receive said degasified feedwater from said deaerator.

3. The combined cycle power plant according to claim 2, wherein said secondary functions comprise:

a first function of heating said feedwater to a temperature sufficient to avoid corrosion of selected points within the combined cycle power plant;

a second function of providing a source of said feedwater that is of sufficient capacity and head pressure for steady state and transient operations of the combined cycle power plant; and

a third function of providing a location for input of low level thermal energy to the combined cycle power plant in order to enhance its overall efficiency. power plant in order to enhance its overall efficiency.

4. The combined cycle power plant according to claim 3, wherein said alternate means is connected to said low pressure storage tank.

5. In a deaerating subsystem of a combined cycle power plant which includes a deaerator that is coupled to receive condensate from a source for degasification of the condensate by the deaerator, and a storage tank, the improvement comprising:

condensate bypass means for preventing reception of the condensate by the deaerator, and for enabling the storage tank to receive the condensate;

means for inputting thermal energy into the storage tank, wherein said thermal energy input means is adapted to input controlled amounts of heated condensate and controlled amounts of dry steam;

a spray nozzle coupled to said condensate bypass means within the storage tank, said spray nozzle adapted to atomize the condensate;

downcomer means for coupling the deaerator to the storage tank to receive the degasified condensate therefrom, said downcomer means including flange means with a blind flange adapted to be inserted within said downcomer means to selectively prevent reception of the degasified condensate by the storage tank; and

vapor riser means coupling the storage tank to the deaerator to receive dry steam from the storage tank, said vapor riser means including flange means with a blind flange adapted to be inserted within said vapor riser means to selectively prevent reception of the dry steam by the deaerator;

whereby the deaerator, through insertion of said blind flanges in said downcomer means and said vapor riser means, is adapted to be isolated from the combined cycle power plant during operations thereof.

6. The improvement according to claim 5, wherein said thermal energy input means further comprises means for inputting flash vapor.

7. The improvement according to claim 5, further comprising means for venting the storage tank.

8. A deaerating subsystem for use in a combined cycle power plant of the type having a gas turbine, a steam turbine, and a steam generator producing motive steam from feedwater that is pumped therethrough by a boiler feed pump, wherein the combined cycle power plant is adapted to be operated at an overall efficiency, said deaerating subsystem comprising;

a deaerator adapted for receiving a supply of condensate, and for performing a primary function of degasifying said condensate as well as a plurality of secondary functions including heating the feedwater a sufficient amount to prevent corrosion of selected portions of the steam generator, providing a source of the feedwater of a sufficient capacity and head pressure to satisfy requirements of the boiler feed pump during steady state and transient operations of the plant, and providing a location for inputting selected amounts of thermal energy to enhance the overall efficiency;

a storage tank coupled to the deaerator by downcomer means, said downcomer means including flange means with a blind flange which is adapted to be inserted within the downcomer means for selectively preventing reception of said degasified condensate by the storage tank;

condensate bypass means for preventing the reception of the condensate by the deaerator, and for enabling the storage tank to receive the condensate;

means for inputting thermal energy into the storage tank, wherein said thermal energy input means is adapted to input controlled amounts of heated condensate from the steam generator, and controlled amounts of dry steam; and

vapor riser means coupling the storage tank to the deaerator for reception thereby of the dry steam from the storage tank, said vapor riser means including flange means with a blind flange which is adapted to be inserted within the vapor riser means for selectively preventing such reception of the dry steam by the deaerator;

whereby the deaerator is adapted to be isolated from an operating combined cycle power plant.

9. The deaerating subsystem according to claim 8, wherein said condensate bypass means comprises:

first valve means for controlling a level of the condensate in said storage tank, said first valve means coupled to said supply of condensate;

pipe means coupled to said first valve means downstream thereof, said pipe means including a first branch connected to said deaerator and a second branch connected to said storage tank;

second valve means for controlling said supply of condensate through said first branch;

third valve means for controlling said supply of condensate through said second branch; and

means, coupled to an end of said second branch within said storage tank, for substantially atomizing said supply of condensate to said storage tank.

10. The deaerating subsystem according to claim 9, wherein said first valve means comprises:

a flow control valve capable of being throttled between a fully open position and a fully closed position, said flow control valve adapted to be operated by remote means;

a check valve downstream of said flow control valve, said check valve adapted to prevent said supply of condensate from flowing in a direction through said first valve means other than towards said deaerator.

11. The deaerating subsystem according to claim 9, wherein said second valve means comprises a stop valve.

12. The deaerating subsystem according to claim 9, wherein said third valve means comprises a stop valve.

13. The deaerating subsystem according to claim 9, wherein said atomizing means comprises a spray nozzle.

14. The deaerating subsystem according to claim 8, wherein said thermal energy input means comprises:

means, coupled in a loop with said storage tank, for heating said condensate and for returning same to said storage tank;

means, coupled in a loop with said storage tank, for producing steam from the feedwater and for returning said steam so produced to said storage tank; and

means for inputting flash vapor to said storage tank.

15. The deaerating subsystem according to claim 14, wherein said condensate heating means comprises:

first means, within the steam generator, for receiving said condensate from said storage tank and for heating same to a first degree;

second means, within the steam generator, for receiving said heated condensate from said storage tank and for heating same to a second degree;

pipe means from said second heating means to said storage tank;

a flow control valve capable of being throttled between a fully open position and a fully closed position, said flow control valve adapted to be operated by remote means;

a stop valve downstream of said flow control valve, said stop valve adapted to prevent said supply of condensate heated to said second degree from flowing into said storage tank.

16. The deaerating subsystem according to claim 14, wherein said steam producing means comprises:

third heating means, within the steam generator, for receiving said condensate heated to a second degree and converting same to saturated steam;

means, coupled to said third heating means, for converting same to substantially dry steam;

a flow control valve capable of being throttled between a fully open position and a fully closed position, said flow control valve adapted to be operated by remote means;

a stop valve downstream of said flow control valve, said stop valve adapted to prevent said supply of condensate heated to said second degree from flowing into said storage tank.

17. A method of constructing a combined cycle power plant, comprising the steps of:

providing a deaerator having a primary and secondary functions, said primary function to degasify feedwater for use in the combined cycle power plant;

providing means for normally coupling said deaerator to the combined cycle power plant as a normally functioning part thereof;

providing means for isolating said deaerator from the combined cycle power plant during operations thereof; and

providing alternate means for performing said primary and secondary functions when said deaerator is isolated from the combined cycle power plant, during operations thereof, by said isolating means.

18. The method according to claim 17, further comprising the step of providing a low pressure storage tank coupled to receive said degasified feedwater from said deaerator.

19. The method according to claim 18, wherein said secondary functions comprise the steps of:

performing a first function of heating said feedwater to a temperature sufficient to avoid corrosion of selected points within the combined cycle power plant;

performing a second function of providing a source of said feedwater that is of sufficient capacity and head pressure for steady state and transient operations of the combined cycle power plant; and

performing a third function of providing a location for input of low level thermal energy to the combined cycle power plant in order to enhance its overall efficiency.

20. The method according to claim 19, wherein said step of providing alternate means includes the step of connecting said alternate means to said low pressure storage tank.

21. A method of operating a combined cycle power plant that includes a condenser, a heat recovery steam generator including a deaerator adapted to receive and degasify condensate from the condenser and a storage tank coupled to receive the degasified condensate from the deaerator and adapted to store feedwater in the form of the degasified condensate, said method comprising the steps of:

providing condensate bypass means for preventing the reception of the condensate by the deaerator, and for enabling the storage tank to receive the condensate;

providing means for inputting thermal energy into the storage tank, wherein said thermal energy input means is adapted to input controlled amounts of heated condensate from the heat recovery steam generator, and controlled amounts of dry steam;

providing a spray nozzle coupled to said condensate bypass means within the storage tank, said spray nozzle adapted to atomize the condensate;

providing vent means for the storage tank;

providing downcomer means coupling the deaerator to the storage tank for reception thereby of the degasified condensate from the deaerator, said downcomer means including flange means with a blind flange which is adapted to be inserted within the downcomer means for selectively preventing such reception of the degasified condensate by the storage tank;

providing vapor riser means coupling the storage tank to the deaerator for reception thereby of the dry steam from the storage tank, said vapor riser means including flange means with a blind flange which is adapted to be inserted within the vapor riser means for selectively preventing such reception of the dry steam by the deaerator;

detecting a failure of the deaerator;

reducing the operating temperature and pressure of said failed deaerator;

isolating said thermal energy inputs to the storage tank;

venting said failed deaerator;

redirecting flow of the condensate through said condensate bypass means, thereby preventing flow of the condensate to said failed deaerator and permitting same to flow to the storage tank;

inserting said blind flanges in said downcomer means and said vapor riser means to isolate said failed deaerator from the storage tank; and

reopening said thermal energy input means to the storage tank;

whereby the deaerator is adapted to be isolated from the combined cycle power plant during operations thereof.

22. The method according to claim 21, wherein said step providing said thermal energy input means further comprises the step of providing means for inputting flash vapor.

23. The method according to claim 21, further comprising the steps of:

providing chemical treatment means for the feedwater in the combined cycle plant; and

scavenging gases from the feedwater in the combined cycle plant by injecting selected chemicals through said chemical treatment means.