WO2002027154A1 - Verfahren zum betreiben einer gas- und dampfturbinenanlage sowie entsprechende anlage - Google Patents
Verfahren zum betreiben einer gas- und dampfturbinenanlage sowie entsprechende anlage Download PDFInfo
- Publication number
- WO2002027154A1 WO2002027154A1 PCT/EP2001/010749 EP0110749W WO0227154A1 WO 2002027154 A1 WO2002027154 A1 WO 2002027154A1 EP 0110749 W EP0110749 W EP 0110749W WO 0227154 A1 WO0227154 A1 WO 0227154A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- cfl
- gas
- pressure
- steam
- steam turbine
- Prior art date
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/30—Injector mixers
- B01F25/31—Injector mixers in conduits or tubes through which the main component flows
- B01F25/313—Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced in the centre of the conduit
- B01F25/3132—Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced in the centre of the conduit by using two or more injector devices
-
- 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
- F01K23/00—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids
- F01K23/02—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled
- F01K23/06—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled combustion heat from one cycle heating the fluid in another cycle
- F01K23/10—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled combustion heat from one cycle heating the fluid in another cycle with exhaust fluid of one cycle heating the fluid in another cycle
- F01K23/106—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled combustion heat from one cycle heating the fluid in another cycle with exhaust fluid of one cycle heating the fluid in another cycle with water evaporated or preheated at different pressures in exhaust boiler
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/40—Mixing liquids with liquids; Emulsifying
- B01F23/45—Mixing liquids with liquids; Emulsifying using flow mixing
- B01F23/451—Mixing liquids with liquids; Emulsifying using flow mixing by injecting one liquid into another
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/40—Mixing liquids with liquids; Emulsifying
- B01F23/49—Mixing systems, i.e. flow charts or diagrams
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/71—Feed mechanisms
- B01F35/717—Feed mechanisms characterised by the means for feeding the components to the mixer
- B01F35/71805—Feed mechanisms characterised by the means for feeding the components to the mixer using valves, gates, orifices or openings
Definitions
- heated feed water can be drawn from the medium-pressure system, from the high-pressure system or from both systems.
- the removal essentially depends on the heat required for heating up the condensate and on the plant efficiency that should at least be maintained when the gas turbine is operated as a backup oil operation only.
- the heated feed water or hot water is expediently in a two-pressure system, i.e. H.' in a two-pressure system from a high-pressure drum and in a three-pressure system or in a three-pressure system from the high-pressure drum and / or from a medium-pressure drum as feed water partial flow.
- the partial flow can also be withdrawn at the outlet of the high-pressure economizer or the medium-pressure economizer.
- the pressure of the low-pressure system can also be raised in order to shift the heat contained in the flue gas from the low-pressure system to the condensate preheater downstream of the flue gas side. It is essential that the heated feed water in the form of a feed water partial stream removed from the water-steam cycle at a suitable point without prior heating, i.e. is added to the cold condensate without heat exchange in an additional heat exchanger.
- Inlet temperature is required. Standardization is also possible as a result of the operating range being expanded in a particularly effective manner in terms of circuitry. Furthermore, the investment costs are particularly low.
- FIG. 1 schematically shows a gas and steam turbine system designed for a change of operation from gas to oil with a hot water mixing device
- FIG. 2 shows the mixing device according to FIG. 1 on a larger scale with a number of spray heads
- FIG. 3 shows a detail III from FIG. 2 on a larger scale with a spray head having a valve.
- the gas and steam turbine system 1 comprises a gas turbine system 1 a and a steam turbine system 1 b.
- the gas turbine system 1 a comprises a gas turbine 2 with a coupled air compressor 4 and a combustion chamber 6 connected upstream of the gas turbine 2 and which is connected to a fresh air line 8 of the air compressor 4.
- a fuel line 10 opens into the combustion chamber 6 and can be used to supply gas or oil as the fuel B to the combustion chamber 6. This is burned with the supply of compressed air L to the working fluid or fuel gas for the gas turbine 2.
- the gas turbine 2 and the air compressor 4 and a generator 12 sit on a common turbine shaft 14.
- the steam turbine system 1b comprises a steam turbine 20 with a coupled generator 22 and, in a water-steam circuit 24, a condenser 26 connected downstream of the steam turbine 20 and a waste heat steam generator 30.
- the steam turbine 20 has a first pressure stage or a high pressure part 20a and a second pressure stage or a medium pressure part 20b and a third pressure stage or a low-pressure part 20c, which drive the generator 22 via a common turbine shaft 32.
- An exhaust pipe 34 is connected to an inlet 30a of the heat recovery steam generator 30 in order to supply working fluid or flue gas AM relaxed in the gas turbine 2 to the heat recovery steam generator 30.
- the flue gas AM from the gas turbine 2 which cools down along the heat recovery steam generator 30 as a result of indirect heat exchange with condensate K and feed water S conducted in the water-steam circuit 24, leaves the heat recovery steam generator 30 via its outlet 30b in the direction of a chimney (not shown).
- the heat recovery steam generator 30 comprises, as heating surfaces, a condensate preheater 36 which is fed with condensate K from the condenser 26 via a condensate line 38 into which a condensate pump 40 is connected.
- the condensate preheater 36 is guided on the outlet side to the suction side of a feed water pump 42.
- a mixing device 44 with a tubular hot water mixer 46 is connected into the condensate line 38.
- the feed water pump 42 is designed as a high-pressure feed pump with medium pressure extraction. It brings the condensate K to a pressure level of approximately 120 bar to 150 bar, which is suitable for a high pressure stage 50 of the water-steam circuit 24 assigned to the high pressure part 20a of the steam turbine 20. About the The medium pressure is removed from the condensate K by means of the feed water pump 42 to a pressure level of approximately 40 bar to 60 bar suitable for a medium pressure stage 70 assigned to the medium pressure part 20b of the steam turbine 20.
- the condensate K which is fed via the feed water pump 42 and is referred to as feed water S on the pressure side of the feed water pump 42, is partly fed at high pressure to a first high-pressure economizer 51 or feed-water preheater and via this to a second high-pressure economizer 52. This is connected on the output side to a high-pressure drum 54 via a valve 57.
- the feed water S is also partially fed to a feed water preheater or medium pressure economizer 73 at a medium pressure via a non-return flap 71 and a valve 72 connected downstream of this. On the output side, this is connected to a medium-pressure drum 75 via a valve 74.
- the condensate preheater 36 is connected on the output side to a low-pressure drum 92 via a valve 91.
- the medium pressure drum 75 is connected to a medium pressure evaporator 76 arranged in the heat recovery steam generator 30 in order to form a water-steam circulation 77.
- an intermediate superheater 78 is connected to the medium-pressure drum 75, which is led on the outlet side (hot CLOSE) to an inlet 79 of the medium-pressure section 20b and in the inlet-side (cold CLOSE) one with an outlet 80 of the high-pressure section 20a of the steam turbine 20 connected steam line 81 is guided.
- the feed water pump 42 is connected via two valves 55, 56 as well as via the first high-pressure economizer 51 and the downstream downstream of the feed water side and inside the waste heat steam generator 30 on the flue gas side o O IV) rv> P 1 c ⁇ o C ⁇ o C ⁇ o c ⁇ o rt ⁇ NSP o £ rt P- P ⁇
- a valve 102 with an upstream check valve is used via a partial flow or hot water line 101
- adjustable partial flow tS of heated feed water S ' is fed to the mixing device 44, 46 and in the interior thereof
- the partial flow tS of heated feed water S ' is preferably taken from the high-pressure drum 54 on the water side via a valve 106.
- the heated feed water S ⁇ can be taken as an adjustable partial flow tS via a valve 107 from the first high-pressure economizer 51 or via a valve 108 from the second high-pressure economizer 52.
- an adjustable partial flow tS can also be taken from the medium-pressure economizer 73 on the output side via a valve 109 or the medium-pressure drum 75 on the water side via a valve 110 heated feed water S ⁇ .
- the admixture of the partial flow tS to the condensate K by injecting the heated feed water S conducted via the hot water line 101 into the cold condensate K leads to a targeted evaporation and subsequent condensation of the water-steam mixture formed in the mixing device 44, 46.
- the temperature TS of the partial flow tS when it is removed as heated feed water S from the high-pressure drum 54 is, for example, 320 ° C.
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Engine Equipment That Uses Special Cycles (AREA)
- Investigating, Analyzing Materials By Fluorescence Or Luminescence (AREA)
Abstract
Description
Claims
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE50106221T DE50106221D1 (de) | 2000-09-29 | 2001-09-17 | Verfahren zum betreiben einer gas- und dampfturbinenanlage sowie entsprechende anlage |
US10/381,847 US6874322B2 (en) | 2000-09-29 | 2001-09-17 | Method for operating a gas and steam turbine system and a corresponding system |
EP01978376A EP1320665B1 (de) | 2000-09-29 | 2001-09-17 | Verfahren zum betreiben einer gas- und dampfturbinenanlage sowie entsprechende anlage |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP00121502.9 | 2000-09-20 | ||
EP00121502A EP1193373A1 (de) | 2000-09-29 | 2000-09-29 | Verfahren zum Betreiben einer Gas- und Dampfturbinenanlage sowie entsprechende Anlage |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2002027154A1 true WO2002027154A1 (de) | 2002-04-04 |
Family
ID=8169992
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/EP2001/010749 WO2002027154A1 (de) | 2000-09-29 | 2001-09-17 | Verfahren zum betreiben einer gas- und dampfturbinenanlage sowie entsprechende anlage |
Country Status (6)
Country | Link |
---|---|
US (1) | US6874322B2 (de) |
EP (2) | EP1193373A1 (de) |
DE (1) | DE50106221D1 (de) |
ES (1) | ES2240527T3 (de) |
TW (1) | TW541392B (de) |
WO (1) | WO2002027154A1 (de) |
Families Citing this family (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8321498B2 (en) * | 2005-03-01 | 2012-11-27 | Oracle International Corporation | Policy interface description framework |
US7934383B2 (en) * | 2007-01-04 | 2011-05-03 | Siemens Energy, Inc. | Power generation system incorporating multiple Rankine cycles |
US8596073B2 (en) * | 2008-07-18 | 2013-12-03 | General Electric Company | Heat pipe for removing thermal energy from exhaust gas |
US8186152B2 (en) * | 2008-07-23 | 2012-05-29 | General Electric Company | Apparatus and method for cooling turbomachine exhaust gas |
US8359824B2 (en) * | 2008-07-29 | 2013-01-29 | General Electric Company | Heat recovery steam generator for a combined cycle power plant |
US8157512B2 (en) * | 2008-07-29 | 2012-04-17 | General Electric Company | Heat pipe intercooler for a turbomachine |
US8425223B2 (en) * | 2008-07-29 | 2013-04-23 | General Electric Company | Apparatus, system and method for heating fuel gas using gas turbine exhaust |
US20100064655A1 (en) * | 2008-09-16 | 2010-03-18 | General Electric Company | System and method for managing turbine exhaust gas temperature |
US8230686B2 (en) * | 2008-10-09 | 2012-07-31 | Banas John M | Start-up system mixing sphere |
US8240149B2 (en) * | 2009-05-06 | 2012-08-14 | General Electric Company | Organic rankine cycle system and method |
US9696027B2 (en) * | 2009-12-21 | 2017-07-04 | General Electric Technology Gmbh | Economizer water recirculation system for boiler exit gas temperature control in supercritical pressure boilers |
US9003763B2 (en) * | 2012-10-04 | 2015-04-14 | Lightsail Energy, Inc. | Compressed air energy system integrated with gas turbine |
US10180086B2 (en) * | 2013-09-26 | 2019-01-15 | Nooter/Eriksen, Inc. | Heat exchanging system and method for a heat recovery steam generator |
US10337357B2 (en) * | 2017-01-31 | 2019-07-02 | General Electric Company | Steam turbine preheating system with a steam generator |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3702619A (en) * | 1971-01-28 | 1972-11-14 | Shell Oil Co | In-line mixing apparatus for gases |
EP0281151A2 (de) * | 1987-03-05 | 1988-09-07 | Babcock-Hitachi Kabushiki Kaisha | Abhitzesystem |
US4869595A (en) * | 1983-08-01 | 1989-09-26 | James M. Montgomery, Consulting Engineers, Inc. | Hydraulic diffusion flash mixing |
EP0523467A1 (de) | 1991-07-17 | 1993-01-20 | Siemens Aktiengesellschaft | Verfahren zum Betreiben einer Gas- und Dampfturbinenanlage und Anlage zur Durchführung des Verfahrens |
DE19512466C1 (de) * | 1995-04-03 | 1996-08-22 | Siemens Ag | Verfahren zum Betreiben eines Abhitzedampferzeugers sowie danach arbeitender Abhitzedampferzeuger |
DE19736889C1 (de) | 1997-08-25 | 1999-02-11 | Siemens Ag | Verfahren zum Betreiben einer Gas- und Dampfturbinenanlage und Gas- und Dampfturbinenanlage zur Durchführung des Verfahrens |
Family Cites Families (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3756023A (en) * | 1971-12-01 | 1973-09-04 | Westinghouse Electric Corp | Heat recovery steam generator employing means for preventing economizer steaming |
DE3804605A1 (de) * | 1988-02-12 | 1989-08-24 | Siemens Ag | Verfahren und anlage zur abhitzedampferzeugung |
EP0582898A1 (de) * | 1992-08-10 | 1994-02-16 | Siemens Aktiengesellschaft | Verfahren zum Betreiben einer Gas- und Dampfturbinenanlage sowie danach arbeitende Gud-Anlage |
DE4333439C1 (de) * | 1993-09-30 | 1995-02-02 | Siemens Ag | Vorrichtung zur Kühlmittelkühlung einer gekühlten Gasturbine einer Gas- und Dampfturbinenanlage |
DE59906961D1 (de) * | 1998-05-06 | 2003-10-16 | Siemens Ag | Gas- und dampfturbinenanlage |
-
2000
- 2000-09-29 EP EP00121502A patent/EP1193373A1/de not_active Withdrawn
-
2001
- 2001-08-03 TW TW090118999A patent/TW541392B/zh not_active IP Right Cessation
- 2001-09-17 US US10/381,847 patent/US6874322B2/en not_active Expired - Fee Related
- 2001-09-17 DE DE50106221T patent/DE50106221D1/de not_active Expired - Lifetime
- 2001-09-17 ES ES01978376T patent/ES2240527T3/es not_active Expired - Lifetime
- 2001-09-17 EP EP01978376A patent/EP1320665B1/de not_active Expired - Lifetime
- 2001-09-17 WO PCT/EP2001/010749 patent/WO2002027154A1/de active IP Right Grant
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3702619A (en) * | 1971-01-28 | 1972-11-14 | Shell Oil Co | In-line mixing apparatus for gases |
US4869595A (en) * | 1983-08-01 | 1989-09-26 | James M. Montgomery, Consulting Engineers, Inc. | Hydraulic diffusion flash mixing |
EP0281151A2 (de) * | 1987-03-05 | 1988-09-07 | Babcock-Hitachi Kabushiki Kaisha | Abhitzesystem |
EP0523467A1 (de) | 1991-07-17 | 1993-01-20 | Siemens Aktiengesellschaft | Verfahren zum Betreiben einer Gas- und Dampfturbinenanlage und Anlage zur Durchführung des Verfahrens |
DE19512466C1 (de) * | 1995-04-03 | 1996-08-22 | Siemens Ag | Verfahren zum Betreiben eines Abhitzedampferzeugers sowie danach arbeitender Abhitzedampferzeuger |
DE19736889C1 (de) | 1997-08-25 | 1999-02-11 | Siemens Ag | Verfahren zum Betreiben einer Gas- und Dampfturbinenanlage und Gas- und Dampfturbinenanlage zur Durchführung des Verfahrens |
Also Published As
Publication number | Publication date |
---|---|
EP1320665B1 (de) | 2005-05-11 |
US6874322B2 (en) | 2005-04-05 |
US20040011049A1 (en) | 2004-01-22 |
EP1320665A1 (de) | 2003-06-25 |
ES2240527T3 (es) | 2005-10-16 |
DE50106221D1 (de) | 2005-06-16 |
TW541392B (en) | 2003-07-11 |
EP1193373A1 (de) | 2002-04-03 |
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