Combined cycle electric power plant and a heat recovery steam generator with improved fluid level control therefor

• US 3,955,358 A
• Filed: 08/08/1974
• Issued: 05/11/1976
• Est. Priority Date: 08/08/1974
• Status: Expired due to Term

• Current Assignee: Westinghouse Electric Corporation (Paramount Global (f/k/a ViacomCBS Inc.))
• Original Assignee: Westinghouse Electric Corporation (Paramount Global (f/k/a ViacomCBS Inc.))
• Inventors: Martz, Lyle F., Plotnick, Richard J.
• Primary Examiner(s): Ostrager, Allen M.
• Application Number:
  US05/495,738
• Time in Patent Office: 642 Days
• Field of Search: 122/451 S, 122/451 R, 60/660-667, 60/646, 60/39.18 B
• US Class Current: 60/39.182
• CPC Class Codes: F01K 13/02 Controlling, e.g. stopping or starting
• 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]
• CPC Class Codes: Y02P 80/15 On-site combined power, heat or cool generation or distribution, e.g. combined heat and power [CHP] supply

Abstract

A combined cycle electric power plant includes gas and steam turbines and a steam generator for recovering the heat in the exhaust gases exited from the gas turbine and for using the recovered heat to produce and supply steam to the steam turbine. A condenser receives the spent steam from the steam turbine for converting it into condensate. The steam generator includes a deaerator for receiving the condensate flow from the condenser and for storing it in a storage portion, a feedwater pump for directing the stored condensate through a first heat exchange tube whereby heat is transferred from the gas turbine exhaust gases to the fluid, a main drum for receiving and storing the heated fluid and a second heat exchange tube for heating the fluid by the gas turbine exhaust gases into superheated steam to be supplied to the steam turbine. A water make-up system is associated with the condenser and includes a water make-up storage tank, a return valve for extracting condensate from that supplied to the deaerator for storage in the water make-up storage tank, and a make-up valve for returning water from the water make-up storage tank into the condenser. Fluid level control is provided for maintaining the fluid level within a hotwell storage portion of the condenser, and within the storage portion of the deaerator, by controlling the position of the condensate valve. In particular, the fluid level control is responsive primarily to a measurement of the superheated steam as supplied to said steam turbine and in particular to a difference signal between the flow of superheated steam to said steam turbine and the condensate flow to said deaerator for the control of the position of the condensate valve, and secondarily, to measurements of the fluid level within the deaerator storage portion and the hotwell storage portion to trim the effect of the aforementioned difference signal upon the position of the condensate valve.

Claims

1. A combined cycle electric power plant comprising:

a. at least one gas turbine including an exit through which heated exhaust gases pass;

b. means for generating steam coupled to said gas turbine exit for transferring heat from the exhaust gases to a fluid passing through said steam generating means;

c. a steam turbine coupled to said steam generating means and driven by the steam supplied thereby;

d. means for generating electric power by the driving power of said turbines;

e. condenser means for receiving and converting the spent steam from said steam turbine into condensate, said condenser means including a hotwell storage portion for receiving and storing the condensate;

f. said steam generating means including a deaerator for receiving condensate from said condenser and storing the received condensate in a storage portion thereof, a feedwater pump for directing the stored fluid from said deaerator storage portion to a first heat exchange tube, a main drum associated with said first heat exchange tube for receiving the heated fluid therefrom, and a second heat exchange tube associated with said main drum for receiving fluid therefrom and for heating the fluid by the exhaust gases from said gas turbine into superheated steam to be directed to said steam turbine;

g. condensate valve means for controlling the flow of condensate from said condenser hotwell storage portion to said deaerator; and

h. means for controlling the operation of said turbines and said steam generating means comprising fluid level control means responsive to the flow of superheated steam to said steam turbine for regulating the flow of condensate into said deaerator storage portion in accordance therewith.

2. The combined cycle electric power plant as claimed in claim 1, wherein said water level control means is responsive to the difference between the flow of superheated steam to said steam turbine and the flow condensate to said deaerator for controlling the flow of the condensate to said deaerator storage portion.

3. The combined cycle electric power plant as claimed in claim 1, wherein said water level control means comprises means for measuring and providing a signal indicative of the condensate flow to said deaerator storage portion, means for measuring and providing an output signal indicative of the flow of superheated steam of said steam turbine, and substraction means responsive to the aforementioned outputs to provide a signal indicative of the difference between the condensate and superheated flows for controlling the position of said condensate valve means.

4. The combined cycle electric power plant as claimed in claim 3, wherein said fluid level control means comprises means for measuring the fluid level within said hotwell storage portion to provide a hotwell fluid level signal, subtraction means for providing a difference signal indicative of the difference between the hotwell fluid level signal and a normal value thereof, and trim means for trimming the effect of the condensate superheated steam difference signal upon the control of said condensate valve means.

5. The combined cycle electric power plant as claimed in claim 4, said fluid level control means includes means for measuring the fluid level within said deaerator storage portion to provide a deaerator fluid level signal, and said trim means responsive to the deaerator fluid level signal for trimming the effect of the condensate superheated steam difference signal upon the control of said condensate valve means.

6. The combined cycle electric power plant as claimed in claim 1, wherein there is included a second gas turbine;

second steam generating means comprising a second deaerator for receiving the flow of condensate from said condenser and storing it in a storage portion thereof, a second feedwater pump for directing water from said second deaerator storage portion into a third heat exchange tube whereby the fluid passing therethrough is heated by the exhaust gases from said second gas turbine, a second main drum for receiving and storing the heated fluid from said third heat exchange tube, and a fourth heat exchange tube for receiving and heating the fluid derived from said second main drum by the exhaust gases from said second turbine and supplying superheated steam to said steam turbine;

second condensate valve means for controlling the flow of condensate to said second deaerator;

said fluid level control means comprising means for measuring the flows of condensate to said first-mentioned and second steam generating means and providing signals indicative thereof and for measuring the flows of superheated steam from said first-mentioned and second steam generators to said steam turbine and for providing signals thereof, summing means responsive to the first and second condensate flow signals to provide a total condensate flow signal and responsive to the steam flow signals to provide a total steam flow signal, and subtraction circuit means responsive to the total condensate flow and superheated steam flow signals to provide a difference signal for the control of said first-mentioned and second condensate valve means.

7. The combined cycle electric power plant as claimed in claim 6, wherein said fluid level control means comprises means for measuring the fluid level within said hotwell storage portion to provide a signal indicative thereof, subtraction means responsive to the hotwell fluid level signal and a signal indicative of a normal value within said hotwell storage portion to provide a difference signal indicative thereof, and trim means for trimming the condensate superheated steam difference signal in accordance with the hotwell difference signal, whereby said first and second condensate valves tend to restore the fluid level within said hotwell storage portion.

8. The combined cycle electric power plant as claimed in claim 7, wherein said fluid level control means comprises subtraction means responsive to the flow signals corresponding to the flows of superheated steam to said steam turbine, for providing a difference signal therebetween.

9. The combined cycle electric power plant as claimed in claim 8, wherein said fluid level control means comprises subtraction means responsive to the flow signals of condensate to said first and second steam generating means for providing a difference signal therebetween, and trim means responsive to the superheated steam and condensate flow difference signals for providing a summed output thereof and for applying the summed output to said trim means for modifying the effect of the superheated steam-condensate difference signal on the control of said first-mentioned and second condensate valve means.

10. The combined cycle electric power plant as claimed in claim 9, wherein said fluid level control means comprises means for measuring the fluid level within said first-mentioned and second deaerator storage portions for providing signals indicative thereof, and subtraction means responsive to the deaerator storage portion fluid level signals to provide a difference signal therebetween to be applied to said trim means for effecting a trim of the influence of the condensate superheated steam difference signal upon the control of said first-mentioned and second condensate valve means.

11. The combined cycle electric power plant as claimed in claim 9, wherein said fluid level control means comprises first and second summing means whose outputs are applied to control, respectively, the positions of said first-mentioned and second condensate valve means, said first and second summing means each having a first input for receiving the condensate superheated steam difference signal and a second input, said trim means applying its output to said second input of said first and second summing circuits in a manner to have an opposite effect upon the control of said first mentioned and second condensate valve means.

12. The combined cycle electric power plant as claimed in claim 11, wherein said fluid level control means is operative in a first mode for applying, respectively, the output of said first and second summing circuits for the control of said first and second condensate valve means, and in a second mode for applying the first and second deaerator fluid level signals for the control of said first and second condensate valve means, respectively.

13. The combined cycle electric power plant as claimed in claim 12, wherein there is included third switch means operative in a first mode for applying the output of said trim means to each of said first and second summing means, and in a second mode for disconnecting the output of said trim means therefrom.

14. The combined cycle electric power plant as claimed in claim 6, wherein there is included a makeup water system comprising a makeup water storage tank, a return valve actuatable to extract condensate from the flow to said first-mentioned and second deaerators and for supplying it to said makeup water storage tank, and a makeup valve for permitting a flow of the condensate within said makeup water storage tank to said condenser means, and said fluid level control means responsive to a fluid level within at least one of said deaerator storage portions in excess of that of a predetermined maximum limit, for opening said return valve to extract water from the condensate and responsive to a fluid level within said one deaerator storage portion below a minimum level for opening said makeup valve to return condensate to said condenser.

15. The combined cycle electric power lant as claimed in claim 14, wherein said fluid level control means comprises first means responsive to the higher of the deaerator fluid level signals for applying same to control said return valve, and second means responsive to the deaerator level signals for applying the lesser of the two input signals to control said makeup valve.

16. The combined cycle electric power plant as claimed in claim 2 wherein said fluid level control means comprises means for measuring the fluid level within said deaerator storage portion for providing an output indicative thereof, and trim means responsive to the deaerator fluid level signal and to a normal level value of the fluid level within said deaerator storage portion for providing a difference output therebetween for trimming the effect of the steamcondensate difference signal upon the control of said condensate valve means.

17. The combined cycle electric power plant as claimed in claim 16, wherein said fluid level control means comprises means for measuring the fluid level within said hotwell storage portion and for providing a signal corresponding thereto, and summing means responsive to the hotwell fluid level signal and to a normal level value of the fluid within said hotwell storage portion to provide a difference output signal therebetween, said trim means responsive to the hotwell difference signal to trim the effect of the steam condensate difference signal upon the control of said condensate valve.

18. The combined cycle electric power plant as claimed in claim 17, wherein there is further included a makeup water system comprised of a makeup water storage tank, a return valve for extracting condensate from the flow to said steam generating means for storage within said makeup water storage tank, and a makeup valve for returning water from said makeup water storage tank to said condenser, said fluid level control means comprising means for measuring the fluid level within said hotwell storage portion for providing a signal indicative thereof, summing means responsive to the hotwell fluid level signal and to a normal level value thereof for providing a difference signal, and a makeup water level controller responsive to the hotwell fluid level signal above a predetermined maximum limit for opening said return valve and responsive to the hotwell fluid level signal below a minimum limit for opening said makeup valve.

19. The combined cycle electric power plant as claimed in claim 2 wherein there is further included a second gas turbine;

a second condensate valve means;

second steam generating means comprised of a second deaerator having a second deaerator storage portion, a second feedwater pump for directing fluid from said second deaerator storage portion to a third heat transfer tube whereby the fluid therein is heated by the exhaust gases from a second gas turbine, a second main drum for receiving and storing the heated fluid from said third heat exchange tube, and a fourth heat exchange tube for heating the fluid by the exhaust gases from said second gas turbine into superheated steam to be supplied to said steam turbine, and said fluid level control means comprising means for measuring the condensate flow to and the superheated steam flow from said second steam generating means for providing signals indicative thereof, and subtraction means responsive to the second condensate flow and superheated steam flow signals for providing a second difference output for controlling said second condensate valve means to regulate the flow of condensate to said second steam generating means.

20. The combined cycle electric power plant as claimed in claim 19, wherein said fluid level control means comprises means for measuring the fluid level within said second deaerator storage portion for providing an output indicative thereof and trim means responsive to the second fluid level deaerator signal and a value of the normal fluid level therein for providing a difference signal and for using same to trim the influence of the second superheated steam condensate flow difference signal upon the control of said second condensate valve means.

21. The combined cycle electric power plant as claimed in claim 19, wherein said fluid level control means comprises means for measuring the fluid level within said hotwell storage portion and providing an output indicative thereof, and summing means responsive to the fluid level signal and to a normal level value thereof for providing a difference signal, said trim means responsive to the output of said aforementioned summing means for trimming the influence of the second superheated steam condensate flow difference signal upon the control of said second condensate valve means.

22. The combined cycle electric power plant as claimed in claim 19, wherein either one of said first-mentioned and said second steam generating means is capable of being operated in a STANDBY mode, wherein said fluid level control means comprises summing means responsive to the deaerator fluid level signal corresponding to said one steam generating means and to a second fluid level signal indicative of the normal level in a STANDBY mode, said summing circuit providing an output indicative of the difference therebetween, and transfer function means operative in a first normal mode for applying the superheated steam condensate flow difference signal for the control of said condensate valve means coupled to said one steam generating means, and in a second mode responsive to the output of said summing circuit for controlling thereby the position of said condensate valve means coupled to said one steam generating means.

23. A fluid level control system for a combined cycle electric power plant comprising at least one gas turbine including an exit through which heated exhaust gases pass, means for generating steam coupled to said gas turbine exit for transferring heat from the exhaust gases to a fluid passing through said steam generating means, a steam turbine coupled to said steam generating means and driven by the steam supplied thereby, means for generating electric power by the driving power of said turbines, condenser means for receiving and converting the spent steam from said steam turbine into condensate, said condenser means including a hotwell storage portion for receiving and storing the condensate, said steam generating means including a deaerator for receiving condensate from said condenser and storing the received condensate in a storage portion thereof, a feedwater pump for directing the stored fluid from said deaerator storage portion to a first heat exchange tube, a main drum associated with said first heat exchange tube for receiving the heated fluid therefrom, and a second heat exchange tube associated with said main drum for receiving fluid therefrom and for heating the fluid in the exhaust gases from said gas turbine into superheated steam to be directed to said steam turbine, and condensate valve means, for controlling the flow of condensate from said condenser hotwell portion to said deaerator,

said fluid level control means responsive to the flow of superheated steam to said steam turbine for controlling the position of said condensate valve means to regulate the flow of condensate into said deaerator storage portion in accordance therewith.

24. The fluid level control system as claimed in claim 23, wherein said system is responsive to the difference between the flow of the superheated steam to said steam turbine and the flow condensate to said deaerator for controlling the flow of the condensate to said deaerator storage storage portion.

25. The fluid level control system as claimed in claim 23, comprising means for measuring and providing a signal indicative of the condensate flow to said deaerator storage portion, means for measuring and providing an output signal indicative of the flow of superheated steam to said steam turbine, and subtraction means responsive to the aforementioned outputs to provide a signal indicative of the difference between the condensate and superheated flows for controlling the position of said condensate valve means.

26. The fluid level control system as claimed in claim 25, wherein said system comprises means for measuring the fluid level within said hotwell storage portion to provide a hotwell fluid level signal, subtraction means for providing a difference signal indicative of the difference between the hotwell fluid level signal and a normal value thereof, and trim means for trimming the effect of the condensate superheated steam difference signal upon the control of said condensate valve means.

27. The fluid level control system as claimed in claim 26, wherein said system comprises means for measuring the fluid level within said deaerator storage portion to provide a deaerator fluid level signal, and said trim means responsive to the deaerator fluid level signal for trimming the effect of the condensate superheated steam difference signal upon the control of said condensate valve means.

28. A fluid level control system for an electric power plant comprising a heat source, means for generating steam coupled to said gas turbine exit for transferring heat from said source to a fluid passing through said steam generating means;

a steam turbine coupled to said steam generating means and driven by the steam supplied thereby, means for generating electric power by the driving power of said turbine, condenser means for receiving and converting the spent steam from said steam turbine into condensate, said condenser means comprising a hotwell portion for receiving and storing the condensate, said steam generating means including a deaerator for receiving condensate from said condenser and storing the receiver condensate in a storage portion thereof, a feedwater pump for directing the stored fluid from said deaerator storage portion to a first heat exchange tube, a main drum associated with said heat exchange tube for receiving the heated fluid therefrom, and a second heat exchange tube associated with said main drum for receiving fluid therefrom and for heating the fluid by the heat supplied from said source into superheated steam to be directed to said steam turbine, and condensate valve means for controlling the flow of condensate from said condenser hotwell storage portion to said deaerator,

said fluid level control system responsive to the flow of superheated steam to said steam turbine for controlling the position of said condensate valve means to regulate the flow of condensate into said deaerator storage portion in accordance therewith.

29. The fluid control system as claimed in claim 28, wherein said fluid level control system in responsive to the difference between the flow of superheated steam to said steam turbine and the flow condensate to said deaerator for controlling the flow of the condensate to said deaerator storage portion.

30. The fluid level control system as claimed in claim 28, wherein said fluid level control system comprises means for measuring and providing a signal indicative of the condensate flow to said deaerator storage portion, means for measuring and providing an output signal indicative of the flow of superheated steam to said steam turbine, and subtraction means responsive to the aforementioned outputs to provide a signal indicative of the difference between the condensate and superheated flows for controlling the position of said condensate valve means.

31. The fluid level control system as claimed in claim 30, wherein said fluid level control system comprises means for measuring the fluid level within said hotwell storage portion to provide a hotwell fluid level signal, subtraction means for providing a difference signal indicative of the difference between the hotwell fluid level signal and a normal value thereof, and trim means for trimming the effect of the condensate superheated steam difference signal upon the control of said condensate valve means.

32. The fluid level control system as claimed in claim 31, wherein said fluid level control system comprises means for measuring the fluid level within said deaerator storage portion to provide a deaerator fluid level signal, and said trim means responsive to the deaerator fluid level signal for trimming the effect of the condensate superheated steam difference signal upon the control of said condensate valve means.