WO1996006268A2 - Method and apparatus for regulating and augmenting the power output of a gas turbine - Google Patents
Method and apparatus for regulating and augmenting the power output of a gas turbine Download PDFInfo
- Publication number
- WO1996006268A2 WO1996006268A2 PCT/US1995/010330 US9510330W WO9606268A2 WO 1996006268 A2 WO1996006268 A2 WO 1996006268A2 US 9510330 W US9510330 W US 9510330W WO 9606268 A2 WO9606268 A2 WO 9606268A2
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- steam
- gas
- mixture
- turbine
- flow rate
- Prior art date
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
- F01K21/00—Steam engine plants not otherwise provided for
- F01K21/04—Steam engine plants not otherwise provided for using mixtures of steam and gas; Plants generating or heating steam by bringing water or steam into direct contact with hot gas
- F01K21/047—Steam engine plants not otherwise provided for using mixtures of steam and gas; Plants generating or heating steam by bringing water or steam into direct contact with hot gas having at least one combustion gas turbine
Definitions
- a gas turbine is comprised of a compressor section that produces compressed air that is subsequently heated by burning fuel in a combustion section.
- the hot gas from the combustion section is directed to a turbine section where the hot gas is used to drive a rotor shaft, thereby producing shaft power.
- the shaft power is used to drive the compressor.
- the excess power not consumed by the compressor drives a generator that produces electrical power.
- the amount of power imparted to the shaft is a function of the mass flow and temperature of the hot gas flowing through the turbine.
- the step of directing a variable flow rate of steam into the hot gas comprises generating the variable flow rate of steam by transforming feed water into the steam at a variable pressure.
- the flow rate of the steam being adjusted so as to obtain the desired steam flow rate by adjusting the pressure at which the steam is generated, thereby varying the saturation temperature of the feed water.
- the step of transforming the feed water into the steam at a variable pressure comprises directing the feed water and the expanded gas through a heat recovery steam generator.
- Figure 1 is a schematic diagram of a gas turbine power plant having the capability of regulating and augmenting power output by varying the rate of injection of steam into the combustor according to the current invention.
- Figure 2 is a graph of (i) a curve showing the relationship of saturation temperature, Tsat, versus pressure for water and (ii) a curve showing the effect that varying the pressure Pev maintained in the evaporator of Figure 1 (and, therefore, the saturation temperature of the water therein) has on the ratio, Gst/Gex, of the flow rate of saturated steam produced by the evaporator to the flow rate of exhaust gas directed to the evaporator for a typical gas turbine having an exhaust temperature of 575°C (1070 » F) .
- Figure 1 a schematic diagram of a gas turbine power plant.
- the major components of the power plant include a gas turbine 1 and a heat recovery steam generator 12.
- the gas turbine 1 includes a compressor 2, a turbine 4 having a rotor shaft 8 connected to the compressor and to an electrical generator 10, and a combustor 6.
- the HRSG 12 includes a superheater 16, an evaporator 18, a steam drum 20, an economizer 22, and a pressure control valve 24.
- the expanded gas/steam mixture 34 is then directed to the HRSG 12.
- the expanded gas/steam mixture 34 is directed by ductwork so that it flows successively over the superheater 16, the evaporator 18 and the economizer 22.
- the gas/steam mixture 36 is then discharged to atmosphere.
- the superheater 16, the evaporator 18 and the economizer 22 may have heat transfer surfaces comprised of finned tubes.
- the expanded gas/steam mixture 34 flows over these finned tubes and the feedwat ⁇ r/steam flows within the tubes.
- the expanded gas/steam mixture 34 transfers a considerable portion of its heat to the feedwater/steam.
- the temperature of the gas/steam mixture 36 discharged from the HRSG 12 is considerably lower than that of the expanded gas/steam mixture 34 entering the HRSG and may be as low as 150 ⁇ C (300°F) , or lower.
- the rate at which the feedwater 40 is converted to steam 42 — that is, the steam generation rate — is a function of the heat transfer surface area and the operating pressure of the evaporator, as well as the temperature and flow rate of the expanded gas/steam mixture 34, as discussed below.
- a conventional feedwater control system which may include a feedwater control valve, water level sensors, etc., may be utilized to maintain the level of feedwater 40 in the drum 20 within an appropriate range in order to prevent the flooding of the drum or the drying out of the evaporator 18 as the steam generation rate varies.
- the steam 42 is directed to a superheater 16 in which its temperature is raised into the superheat region.
- a certain amount of superheating is desirable to reduce the additional fuel 30 that must be burned in the combustor 6 in order to heat the hot gas/steam mixture 32 directed to the turbine to the desired temperature, the amount of superheat is not critical to achieve the benefits of the current invention.
- the expanded gas/steam mixture 34 gives up a portion of its heat in the superheater 16 before it reaches the evaporator 18, the greater the amount of superheating, the lower the steam generation rate.
- the temperature of the steam 44 is less than the optimum temperature of the fluid to be expanded in the turbine 4 that will result in optimum performance (i.e., the base load turbine inlet design temperature) .
- the greater the steam generation rate the less the amount of superheat that can be achieved. Therefore, additional fuel must be burned in the combustor 6 to maintain the temperature of the hot gas/steam mixture 32 at the optimum constant value as the steam injection rate increases and the steam temperature decreases. As a result of this increased fuel flow, the thermal efficiency of the gas turbine 1 begins decreasing beyond a certain steam flow rate, as shown in Figure 3.
- an increase in power output of approximately 35% can be accomplished by merely opening the pressure control valve 24 sufficiently far to drop the pressure in the evaporator 18 from 1800 kPa to 1600 kPa, thereby increasing the steam generation rate ratio Gst/Gex from 0.085 to 0.175, as shown in Figure 2, and, therefore, increasing the power output from 150% to 205% of the dry combustion power, as shown in Figure 3.
- the method of operation according to the current invention allows augmentation of the gas turbine power output to meet demands in excess of those that would otherwise be possible from dry operation of the turbine without exceeding safe operating temperatures levels for the turbine 4.
- the turbine 4 is comprised of an outer cylinder 66 that encloses an inner cylinder 64. Within the inner cylinder 64, the hot steam/gas 32 flows over alternating rows of stationary vanes and rotating blades. The rows of stationary vanes are affixed to the inner cylinder 64. The rows of rotating blades are affixed to discs that form the turbine portion of the rotor 8.
- Figure 6 shows two adjacent first stage vanes 50 of the turbine 4. The shortest distance from the trailing edge portion 52 of one vane 50 to the suction surface 54 of the adjacent vane is indicated by T and constitutes the exit opening, or throat, of the stage.
- the flow area of the stage is equal to the throat T times the height of the vanes 50. This flow area determines the inlet flow capacity of the turbine 4. Since the cooling air 3 bleed from the compressor 2 is eventually returned to the working fluid downstream of the first stage vanes 50, downstream stages of the turbine have flow areas that are sized to handle the increase in flow associated with the return of cooling air to the working fluid.
- a portion of the compressed air flowing through the compressor is bled off for cooling purposes — typically, approximately 5-12% of the compressor inlet air flow.
- the cross-sectional area of the compressor discharge annulus 56 is sized to accommodate the flow rate of the compressed air 28 discharging from the compressor, which, for the reasons discussed above, is less than the flow rate of the compressor inlet air 26.
- the rate of flow of the fuel 30 is typically equal to about 2 to 3% of the flow rate of the compressor inlet air.
- the flow capacity of the turbine 4 is increased to permit the use of higher flow rates of steam 44 than has heretofore been possible in order to maximize the ability of the operator to augment the power output of the turbine by the use of steam injection.
- the flow area of the first stage turbine vanes 50 has been increased so that the ratio of the throat area of the first stage turbine vanes 50 to the cross- sectional area of the compressor exit annulus 56 is at least approximately 1.05. The pressure at the inlet to the turbine 4 it a function of the flow rate of the gas/steam mixture flowing through the turbine and, therefore, is also a function of the flow rate of steam 44.
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Engine Equipment That Uses Special Cycles (AREA)
Abstract
Description
Claims
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP8508160A JPH10504630A (en) | 1994-08-24 | 1995-08-15 | Method and apparatus for adjusting and increasing output of gas turbine |
EP95931524A EP0777820B1 (en) | 1994-08-24 | 1995-08-15 | Method and apparatus for regulating and augmenting the power output of a gas turbine |
DE69510803T DE69510803T2 (en) | 1994-08-24 | 1995-08-15 | METHOD AND DEVICE FOR REGULATING AND INCREASING THE OUTPUT PERFORMANCE OF A GAS TURBINE |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US08/295,114 | 1994-08-24 | ||
US08/295,114 US5566542A (en) | 1994-08-24 | 1994-08-24 | Method for regulating and augmenting the power output of a gas turbine |
Publications (2)
Publication Number | Publication Date |
---|---|
WO1996006268A2 true WO1996006268A2 (en) | 1996-02-29 |
WO1996006268A3 WO1996006268A3 (en) | 1996-05-30 |
Family
ID=23136271
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/US1995/010330 WO1996006268A2 (en) | 1994-08-24 | 1995-08-15 | Method and apparatus for regulating and augmenting the power output of a gas turbine |
Country Status (6)
Country | Link |
---|---|
US (1) | US5566542A (en) |
EP (1) | EP0777820B1 (en) |
JP (1) | JPH10504630A (en) |
CA (1) | CA2198224A1 (en) |
DE (1) | DE69510803T2 (en) |
WO (1) | WO1996006268A2 (en) |
Families Citing this family (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP3196549B2 (en) * | 1995-01-09 | 2001-08-06 | 株式会社日立製作所 | Power generation system with fuel reformer |
DE19535228C2 (en) * | 1995-09-22 | 2003-05-08 | Alstom | Process for operating a power plant |
DE19723543C2 (en) * | 1997-06-05 | 2003-04-17 | Deutsch Zentr Luft & Raumfahrt | Power generation plant |
US5778675A (en) * | 1997-06-20 | 1998-07-14 | Electric Power Research Institute, Inc. | Method of power generation and load management with hybrid mode of operation of a combustion turbine derivative power plant |
DE19918346A1 (en) * | 1999-04-22 | 2000-10-26 | Asea Brown Boveri | Method and appliance for rapidly increasing output and maintaining additional output for limited period of gas turbine plant |
US6405521B1 (en) | 2001-05-23 | 2002-06-18 | General Electric Company | Gas turbine power augmentation injection system and related method |
US6357218B1 (en) | 2001-06-20 | 2002-03-19 | General Electric Company | Steam generation system and method for gas turbine power augmentation |
US6460490B1 (en) | 2001-12-20 | 2002-10-08 | The United States Of America As Represented By The Secretary Of The Navy | Flow control system for a forced recirculation boiler |
JP2006517636A (en) * | 2003-02-11 | 2006-07-27 | アルストム テクノロジー リミテッド | Operation method of gas turbine group |
JP4270176B2 (en) * | 2005-07-14 | 2009-05-27 | トヨタ自動車株式会社 | Flying machine control device |
US9355571B2 (en) * | 2008-01-23 | 2016-05-31 | Sikorsky Aircraft Corporation | Modules and methods for biasing power to a multi-engine power plant suitable for one engine inoperative flight procedure training |
US8833079B2 (en) * | 2008-09-18 | 2014-09-16 | Douglas W. P. Smith | Method and apparatus for generating electricity |
US10465907B2 (en) * | 2015-09-09 | 2019-11-05 | General Electric Company | System and method having annular flow path architecture |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR1134503A (en) * | 1955-07-29 | 1957-04-12 | Babcock & Wilcox France | Improvements to steam generators and method of operating such generators |
US4128994A (en) * | 1974-12-19 | 1978-12-12 | International Power Technology, Inc. | Regenerative parallel compound dual-fluid heat engine |
DE3419560A1 (en) * | 1984-05-25 | 1985-11-28 | Brown, Boveri & Cie Ag, 6800 Mannheim | Method for the operation of a gas turbine plant and plant for the method |
US5329758A (en) * | 1993-05-21 | 1994-07-19 | The United States Of America As Represented By The Secretary Of The Navy | Steam-augmented gas turbine |
Family Cites Families (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3693347A (en) * | 1971-05-12 | 1972-09-26 | Gen Electric | Steam injection in gas turbines having fixed geometry components |
US3747336A (en) * | 1972-03-29 | 1973-07-24 | Gen Electric | Steam injection system for a gas turbine |
CA1170842A (en) * | 1978-10-26 | 1984-07-17 | Ivan G. Rice | Steam cooled turbines |
US4680927A (en) * | 1979-07-23 | 1987-07-21 | International Power Technology, Inc. | Control system for Cheng dual-fluid cycle engine system |
DE3419960A1 (en) * | 1984-05-29 | 1985-12-05 | Eberhardt Pflugfabrik GmbH, 8871 Waldstetten | Stone and overload protection for ploughs and the like |
US4893467A (en) * | 1988-07-13 | 1990-01-16 | Gas Research Institute | Control system for use with steam injected gas turbine |
US5170622A (en) * | 1991-04-02 | 1992-12-15 | Cheng Dah Y | Advanced regenerative parallel compound dual fluid heat engine Advanced Cheng Cycle (ACC) |
-
1994
- 1994-08-24 US US08/295,114 patent/US5566542A/en not_active Expired - Lifetime
-
1995
- 1995-08-15 JP JP8508160A patent/JPH10504630A/en active Pending
- 1995-08-15 CA CA002198224A patent/CA2198224A1/en not_active Abandoned
- 1995-08-15 WO PCT/US1995/010330 patent/WO1996006268A2/en active IP Right Grant
- 1995-08-15 DE DE69510803T patent/DE69510803T2/en not_active Expired - Lifetime
- 1995-08-15 EP EP95931524A patent/EP0777820B1/en not_active Expired - Lifetime
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR1134503A (en) * | 1955-07-29 | 1957-04-12 | Babcock & Wilcox France | Improvements to steam generators and method of operating such generators |
US4128994A (en) * | 1974-12-19 | 1978-12-12 | International Power Technology, Inc. | Regenerative parallel compound dual-fluid heat engine |
DE3419560A1 (en) * | 1984-05-25 | 1985-11-28 | Brown, Boveri & Cie Ag, 6800 Mannheim | Method for the operation of a gas turbine plant and plant for the method |
US5329758A (en) * | 1993-05-21 | 1994-07-19 | The United States Of America As Represented By The Secretary Of The Navy | Steam-augmented gas turbine |
Also Published As
Publication number | Publication date |
---|---|
US5566542A (en) | 1996-10-22 |
EP0777820B1 (en) | 1999-07-14 |
JPH10504630A (en) | 1998-05-06 |
EP0777820A2 (en) | 1997-06-11 |
CA2198224A1 (en) | 1996-02-29 |
WO1996006268A3 (en) | 1996-05-30 |
DE69510803D1 (en) | 1999-08-19 |
DE69510803T2 (en) | 1999-12-09 |
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