JPH09151750A - Hydrogen oxygen combustion turbine plant - Google Patents
Hydrogen oxygen combustion turbine plantInfo
- Publication number
- JPH09151750A JPH09151750A JP30894095A JP30894095A JPH09151750A JP H09151750 A JPH09151750 A JP H09151750A JP 30894095 A JP30894095 A JP 30894095A JP 30894095 A JP30894095 A JP 30894095A JP H09151750 A JPH09151750 A JP H09151750A
- Authority
- JP
- Japan
- Prior art keywords
- turbine
- gas
- steam
- hydrogen
- compressor
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
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
- F01K25/00—Plants or engines characterised by use of special working fluids, not otherwise provided for; Plants operating in closed cycles and not otherwise provided for
- F01K25/005—Plants or engines characterised by use of special working fluids, not otherwise provided for; Plants operating in closed cycles and not otherwise provided for the working fluid being steam, created by combustion of hydrogen with oxygen
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は水素酸素燃焼タービ
ンプラントの改良、特にガスタービンの冷却蒸気の抽気
手段に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an improvement of a hydrogen-oxygen combustion turbine plant, and more particularly to a means for extracting cooling steam of a gas turbine.
【0002】[0002]
【従来の技術】図3は従来の水素酸素燃焼タービンプラ
ントの一例を示す系統図である。2. Description of the Related Art FIG. 3 is a system diagram showing an example of a conventional hydrogen-oxygen combustion turbine plant.
【0003】水素と酸素および圧縮機(1)で圧縮され
た蒸気が燃焼器(2)に供給されて混合され、燃焼して
高温の燃焼蒸気となりガスタービン(3)を駆動する。
その排気蒸気はガスタービン(3)の下流側の熱交換器
(4),(5)によって熱回収された後、再び圧縮機
(1)入口に戻される。また上記排気蒸気の一部は熱交
換器(4),(5)の間の連通管から抽気されて第2の
タービン(6)を駆動する。この第2のタービン(6)
の排気は復水器(10)で復水となり、管路の熱交換器
(7)で加熱され、更に熱交換器(5),(4)で加熱
されて低温低圧の蒸気となり、第3のタービン(8)を
駆動した後、燃焼器(2)の入口側に戻る。なお(1
1)は給水加圧ポンプである。Hydrogen, oxygen, and the steam compressed by the compressor (1) are supplied to the combustor (2) and mixed with each other to combust and become high-temperature combustion steam, which drives the gas turbine (3).
The exhaust steam is subjected to heat recovery by the heat exchangers (4) and (5) on the downstream side of the gas turbine (3) and then returned to the inlet of the compressor (1) again. Further, a part of the exhaust steam is extracted from the communication pipe between the heat exchangers (4) and (5) to drive the second turbine (6). This second turbine (6)
Of the exhaust gas becomes condensed water in the condenser (10), is heated in the heat exchanger (7) of the pipeline, and is further heated in the heat exchangers (5) and (4) to become low-temperature low-pressure steam, and the third After driving the turbine (8), the combustor (2) is returned to the inlet side. Note that (1
1) is a feed water pressure pump.
【0004】またガスタービン(3)のタービン翼、デ
ィスクの冷却蒸気およびシ−ル蒸気は、圧縮機(1)か
ら冷却蒸気管(9)によって抽出され、ガスタービン
(3)に供給される。The cooling steam and seal steam of the turbine blades and disks of the gas turbine (3) are extracted from the compressor (1) by the cooling steam pipe (9) and supplied to the gas turbine (3).
【0005】[0005]
【発明が解決しようとする課題】前述した従来の水素酸
素燃焼タービンプラントのサイクルは、あくまで概念的
なものであり、圧縮機の圧力比が高いと、構造上、単一
の圧縮機では成立しない。これはガスタービンも同様で
ある。The cycle of the conventional hydrogen-oxygen combustion turbine plant described above is conceptual only, and if the pressure ratio of the compressor is high, it cannot be realized by a single compressor due to its structure. . This also applies to gas turbines.
【0006】またタービン翼やディスクの冷却蒸気およ
びシ−ル蒸気として、従来のガスタービンのように圧縮
機の圧縮蒸気を利用することは、エネルギーの高い圧縮
された蒸気を冷却・シ−ルのみに使用することになり、
大きなロスとなる。Further, the use of the compressed steam of the compressor as cooling steam and seal steam for the turbine blades and disks, as in the conventional gas turbine, only cools and seals high-energy compressed steam. Will be used for
It will be a big loss.
【0007】[0007]
【課題を解決するための手段】本発明者は、前記従来の
課題を解決するために、次の1)〜5)に示される水素
酸素燃焼タービンプラントを提案するものである。In order to solve the above-mentioned conventional problems, the present inventor proposes the hydrogen-oxygen combustion turbine plant shown in the following 1) to 5).
【0008】1) 圧縮機,水素酸素燃焼器およびガス
タービンから成るガスタービン装置と、上記ガスタービ
ンの排気から熱回収する第1の熱交換器と、上記第1の
熱交換器を出たガスタービン排気の一部から更に熱回収
する第2の熱交換器と、上記第2の熱交換器を出たガス
タービン排気を上記圧縮機の入口に戻す管路と、上記第
1の熱交換器を出たガスタービン排気の残部により駆動
される第2のタービンと、上記第2のタービンの復水を
上記第2および第1の熱交換器で順次加熱して得られた
蒸気により駆動され、排気は上記水素酸素燃焼器に戻さ
れる第3のタービンとを備えた水素酸素燃焼タービンプ
ラントにおいて、上記圧縮機および上記ガスタービンが
それぞれ複数に分割され、上記分割された圧縮機の間に
上記第2のタービンの復水を水源とする水噴射装置が設
けられるとともに、上記分割されたガスタービンの回転
軸が互いに異なることを特徴とする水素酸素燃焼タービ
ンプラント。1) A gas turbine device comprising a compressor, a hydrogen-oxygen combustor and a gas turbine, a first heat exchanger for recovering heat from the exhaust gas of the gas turbine, and a gas leaving the first heat exchanger. A second heat exchanger that further recovers heat from a portion of the turbine exhaust, a pipe line that returns the gas turbine exhaust that has exited the second heat exchanger to the inlet of the compressor, and the first heat exchanger. Driven by the second turbine driven by the remaining part of the gas turbine exhaust that has exited and the steam obtained by sequentially heating the condensate of the second turbine by the second and first heat exchangers, The exhaust gas is returned to the hydrogen-oxygen combustor. In a hydrogen-oxygen combustion turbine plant including a third turbine, the compressor and the gas turbine are each divided into a plurality of parts, and the third compressor is provided between the divided compressors. Two turbines A hydrogen-oxygen combustion turbine plant, characterized in that a water injection device using the condensate as a water source is provided, and the rotation axes of the divided gas turbines are different from each other.
【0009】2) 上記要件に加えて、上記圧縮機およ
び/または上記第2のタービンから抽気した蒸気を上記
ガスタービンの冷却蒸気としたことを特徴とする水素酸
素燃焼タービンプラント。2) In addition to the above requirements, a hydrogen-oxygen combustion turbine plant characterized in that steam extracted from the compressor and / or the second turbine is used as cooling steam for the gas turbine.
【0010】3) 上記1)の要件に加えて、上記第3
のタービンの排気から抽気した蒸気を上記ガスタービン
の冷却蒸気としたことを特徴とする水素酸素燃焼タービ
ンプラント。3) In addition to the requirement 1) above, the third
A hydrogen-oxygen combustion turbine plant, characterized in that the steam extracted from the exhaust of the turbine is used as the cooling steam for the gas turbine.
【0011】4) 上記1)要件に加えて、上記第3の
タービンの排気から抽気した蒸気を上記ガスタービンお
よび/または上記燃焼器の回収型冷却蒸気としたことを
特徴とする水素酸素燃焼タービンプラント。4) In addition to the requirement 1) above, a hydrogen-oxygen combustion turbine characterized in that the steam extracted from the exhaust gas of the third turbine is used as recovery cooling steam for the gas turbine and / or the combustor. plant.
【0012】上記解決手段1)においては、圧力比が大
きい場合、圧縮機は分割型、ガスタービンは多軸(分割
され且つ回転軸が異なる)とすることによって回転数を
最適に選択できるので、効率の向上は勿論のこと、圧縮
機のサージングやタービンの軸振動の回避、羽根車周速
と蒸気流れ速度に起因する性能低下(衝撃波の発生)の
抑制といった課題を解決し易くなる。In the solution means 1), when the pressure ratio is large, the number of rotations can be optimally selected by making the compressor a split type and the gas turbine multi-axis (divided and the rotation axis is different). In addition to improving efficiency, it is easy to solve problems such as surging of the compressor, avoiding shaft vibration of the turbine, and suppressing performance degradation (generation of shock waves) due to impeller peripheral speed and steam flow speed.
【0013】解決手段1)ではまた、分割された圧縮機
の間に水噴射装置が設けられているので、圧縮により昇
温した蒸気を効果的に冷却し、次段の圧縮機への流入温
度を低下させて、構造設計を容易にすることができる。
そしてその水源としては第2のタービンの復水を用いる
ので、ロスを最小にとどめることができ、別途水源を準
備する手間やコストを省略できる。In the solution means 1), since the water injection device is provided between the divided compressors, the steam heated by the compression is effectively cooled and the inflow temperature to the next-stage compressor is increased. Can be reduced to facilitate structural design.
Since the condensate of the second turbine is used as the water source, loss can be minimized, and the labor and cost of separately preparing a water source can be omitted.
【0014】ガスタービンの冷却蒸気として、上記解決
手段2)では第2のタービンの抽気蒸気、上記解決手段
3)では第3のタービンの排気をそれぞれ利用するの
で、温度、圧力的に木目細かな冷却蒸気の供給を行なう
ことができる。そして第2,第3のタービンからの蒸気
は、既にそれらのタービンで仕事を終えた蒸気であるか
ら、効率上のメリットは大きい。As the cooling steam for the gas turbine, the extraction steam of the second turbine is used in the solving means 2) and the exhaust gas of the third turbine is used in the solving means 3). Therefore, the temperature and the pressure are fine. Cooling steam can be supplied. Since the steam from the second and third turbines is steam that has already finished work in those turbines, the efficiency advantage is great.
【0015】また、冷却蒸気を主流に排出すると大きな
ロスになるが、上記解決手段4)においては、第3のタ
ービンの排気から抽気した蒸気でガスタービンおよびま
たは燃焼器を冷却した後これを回収し、主流に排出しな
いので、効率が向上する。Further, if the cooling steam is discharged to the main stream, a large loss occurs, but in the solution means 4), the gas turbine and / or the combustor is cooled by the steam extracted from the exhaust of the third turbine, and then recovered. However, the efficiency is improved because it is not discharged into the mainstream.
【0016】[0016]
【発明の実施の形態】図1は本発明の実施の第1形態を
示す系統図である。この図において、前記図3により説
明した従来のものと同様の部分については、冗長になる
のを避けるため、同一の符号を付け詳しい説明を省く。1 is a system diagram showing a first embodiment of the present invention. In this figure, the same parts as those of the conventional one described with reference to FIG. 3 are designated by the same reference numerals to avoid redundancy, and detailed description thereof is omitted.
【0017】本実施形態においては、圧縮機が複数の圧
縮機(1A),(1B)に分割されていて、圧縮機(1
A)と圧縮機(1B)との間には、水噴射装置(14)
が設置されている。この水噴射装置(14)の水源とし
ては、第2のタービン(6)の復水器(10)の排水が
流用されていて、ロスを最小にとどめている。またガス
タービンは、多軸ガスタービン(3A),(3B),
(3C)として構成されている。In this embodiment, the compressor is divided into a plurality of compressors (1A) and (1B).
A water injection device (14) is provided between A) and the compressor (1B).
Is installed. As the water source of the water injection device (14), the waste water of the condenser (10) of the second turbine (6) is diverted to minimize the loss. The gas turbine is a multi-shaft gas turbine (3A), (3B),
(3C).
【0018】ガスタービン(3A),(3B),(3
C)の翼、ディスクなどの冷却蒸気は、圧縮機(1
A),(1B)から冷却蒸気管(9A),(9B)によ
って供給されるのに加えて、第2のタービン(6)の抽
気が冷却蒸気管(12A),(12B)によって供給さ
れる。更に第3のタービン(8)の排気からも冷却蒸気
管(13A),(13B)により抽出して供給される。Gas turbines (3A), (3B), (3
The cooling steam for the blades, disks, etc.
A) and (1B) are supplied by cooling steam pipes (9A) and (9B), and bleed air of the second turbine (6) is supplied by cooling steam pipes (12A) and (12B). . Further, the exhaust gas from the third turbine (8) is also extracted and supplied by the cooling steam pipes (13A) and (13B).
【0019】図2は本発明の実施の第2形態として、冷
却蒸気を回収する場合を示す系統図である。この図にお
いても、前記と同様の部分については、同一の符号を付
け詳しい説明を省く。FIG. 2 is a system diagram showing a case where the cooling steam is recovered as the second embodiment of the present invention. Also in this figure, the same parts as those described above are designated by the same reference numerals, and detailed description thereof will be omitted.
【0020】本実施形態では、第3のタービン(8)の
排気を燃焼器(2)に回収するラインからガスタービン
(3)と燃焼器(2)の冷却蒸気を抽出して利用してお
り、各冷却蒸気は、例えばガスタービン(3)の翼や燃
焼器(2)の尾筒等と冷却した後、再びラインに戻され
回収される。In this embodiment, the cooling steam of the gas turbine (3) and the combustor (2) is extracted from the line for recovering the exhaust gas of the third turbine (8) to the combustor (2) and used. The respective cooling steams are cooled, for example, with the blades of the gas turbine (3) and the transition piece of the combustor (2), and then returned to the line again and collected.
【0021】[0021]
【発明の効果】本発明によれば、水素酸素燃焼タービン
プラントの熱損失が減少して効率が向上するばかりでな
く、木目細かな構造設計ができるので、圧縮機のサージ
ングやタービンの軸振動、衝撃波の発生等を防止し易く
なる。According to the present invention, not only the heat loss of the hydrogen-oxygen combustion turbine plant is reduced and the efficiency is improved, but also the fine structure design can be carried out, so that the surging of the compressor and the shaft vibration of the turbine, It becomes easy to prevent the generation of shock waves.
【図1】図1は本発明の実施の第1形態を示す系統図で
ある。FIG. 1 is a system diagram showing a first embodiment of the present invention.
【図2】図2は本発明の実施の第2形態を示す系統図で
ある。FIG. 2 is a system diagram showing a second embodiment of the present invention.
【図3】図3は従来の水素酸素燃焼タービンプラントの
一例を示す系統図である。FIG. 3 is a system diagram showing an example of a conventional hydrogen-oxygen combustion turbine plant.
(1),(1A),(1B) 圧縮機 (2) 燃焼器 (3),(3A),(3B),(3C) ガスタービン (4),(5) 熱交換器 (6) 第2のタービン (7) 熱交換器 (8) 第3のタービン (9),(9A),(9B) 冷却蒸気管 (10) 復水器 (11) 給水加圧ポンプ (12A),(12B) 冷却蒸気管 (13A),(12B) 冷却蒸気管 (14) 水噴射装置 (1), (1A), (1B) Compressor (2) Combustor (3), (3A), (3B), (3C) Gas turbine (4), (5) Heat exchanger (6) Second Turbine (7) Heat exchanger (8) Third turbine (9), (9A), (9B) Cooling steam pipe (10) Condenser (11) Water supply pressure pump (12A), (12B) Cooling Steam pipe (13A), (12B) Cooling steam pipe (14) Water injection device
フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 F01K 25/00 F01K 25/00 F F02C 3/22 F02C 3/22 3/30 3/30 C 6/18 6/18 A 7/143 7/143 7/16 7/16 Z Continuation of the front page (51) Int.Cl. 6 Identification number Office reference number FI Technical display location F01K 25/00 F01K 25/00 F F02C 3/22 F02C 3/22 3/30 3/30 C 6/18 6 / 18 A 7/143 7/143 7/16 7/16 Z
Claims (4)
ビンから成るガスタービン装置と、上記ガスタービンの
排気から熱回収する第1の熱交換器と、上記第1の熱交
換器を出たガスタービン排気の一部から更に熱回収する
第2の熱交換器と、上記第2の熱交換器を出たガスター
ビン排気を上記圧縮機の入口に戻す管路と、上記第1の
熱交換器を出たガスタービン排気の残部により駆動され
る第2のタービンと、上記第2のタービンの復水を上記
第2および第1の熱交換器で順次加熱して得られた蒸気
により駆動され、排気は上記水素酸素燃焼器に戻される
第3のタービンとを備えた水素酸素燃焼タービンプラン
トにおいて、上記圧縮機および上記ガスタービンがそれ
ぞれ複数に分割され、上記分割された圧縮機の間に上記
第2のタービンの復水を水源とする水噴射装置が設けら
れるとともに、上記分割されたガスタービンの回転軸が
互いに異なることを特徴とする水素酸素燃焼タービンプ
ラント。1. A gas turbine device comprising a compressor, a hydrogen-oxygen combustor and a gas turbine, a first heat exchanger for recovering heat from exhaust gas of the gas turbine, and a gas leaving the first heat exchanger. A second heat exchanger that further recovers heat from a portion of the turbine exhaust, a pipe line that returns the gas turbine exhaust that has exited the second heat exchanger to the inlet of the compressor, and the first heat exchanger. Driven by the second turbine driven by the remaining part of the gas turbine exhaust that has exited and the steam obtained by sequentially heating the condensate of the second turbine by the second and first heat exchangers, The exhaust gas is returned to the hydrogen-oxygen combustor. In a hydrogen-oxygen combustion turbine plant including a third turbine, the compressor and the gas turbine are each divided into a plurality of parts, and the third compressor is provided between the divided compressors. 2 turbine recovery A hydrogen-oxygen combustion turbine plant, wherein a water injection device using water as a water source is provided, and the rotating shafts of the divided gas turbines are different from each other.
ービンから抽気した蒸気を上記ガスタービンの冷却蒸気
としたことを特徴とする請求項1記載の水素酸素燃焼タ
ービンプラント。2. The hydrogen-oxygen combustion turbine plant according to claim 1, wherein the steam extracted from the compressor and / or the second turbine is used as the cooling steam for the gas turbine.
蒸気を上記ガスタービンの冷却蒸気としたことを特徴と
する請求項1記載の水素酸素燃焼タービンプラント。3. The hydrogen-oxygen combustion turbine plant according to claim 1, wherein the steam extracted from the exhaust gas of the third turbine is used as the cooling steam of the gas turbine.
蒸気を上記タービンおよび/または上記燃焼器の回収型
冷却蒸気としたことを特徴とする請求項1の水素酸素燃
焼タービンプラント。4. The hydrogen-oxygen combustion turbine plant according to claim 1, wherein the steam extracted from the exhaust gas of the third turbine is used as recovery-type cooling steam for the turbine and / or the combustor.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP7308940A JP2883030B2 (en) | 1995-11-28 | 1995-11-28 | Hydrogen-oxygen combustion turbine plant |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP7308940A JP2883030B2 (en) | 1995-11-28 | 1995-11-28 | Hydrogen-oxygen combustion turbine plant |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH09151750A true JPH09151750A (en) | 1997-06-10 |
JP2883030B2 JP2883030B2 (en) | 1999-04-19 |
Family
ID=17987101
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP7308940A Expired - Lifetime JP2883030B2 (en) | 1995-11-28 | 1995-11-28 | Hydrogen-oxygen combustion turbine plant |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2883030B2 (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1999030018A3 (en) * | 1997-12-09 | 1999-08-12 | Rerum Cognitio | Multistep steam power operating method for generating electric power in a cycle and device for the implementation thereof |
DE19808119A1 (en) * | 1996-09-30 | 1999-09-02 | Mitsubishi Heavy Ind Ltd | Low temperature hydrogen combustion turbine |
EP0900921A3 (en) * | 1997-09-05 | 2000-01-26 | Mitsubishi Heavy Industries, Ltd. | Hydrogen burning turbine plant |
JP2016502619A (en) * | 2012-11-02 | 2016-01-28 | エクソンモービル アップストリーム リサーチ カンパニー | System and method for oxidant compression in a stoichiometric exhaust gas recirculation gas turbine system |
CN105986902A (en) * | 2015-03-02 | 2016-10-05 | 袁志平 | Water combustion type turbine engine |
-
1995
- 1995-11-28 JP JP7308940A patent/JP2883030B2/en not_active Expired - Lifetime
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE19808119A1 (en) * | 1996-09-30 | 1999-09-02 | Mitsubishi Heavy Ind Ltd | Low temperature hydrogen combustion turbine |
DE19808119C2 (en) * | 1996-09-30 | 2002-06-27 | Mitsubishi Heavy Ind Ltd | Hydrogen combustion turbine plant |
EP0900921A3 (en) * | 1997-09-05 | 2000-01-26 | Mitsubishi Heavy Industries, Ltd. | Hydrogen burning turbine plant |
US6282883B1 (en) | 1997-09-05 | 2001-09-04 | Mitsubishi Heavy Industries, Ltd. | Hydrogen burning turbine plant |
WO1999030018A3 (en) * | 1997-12-09 | 1999-08-12 | Rerum Cognitio | Multistep steam power operating method for generating electric power in a cycle and device for the implementation thereof |
AU760916B2 (en) * | 1997-12-09 | 2003-05-22 | Rerum Cognitio | Multistep steam power operating method for generating electric power in a cycle and device for the implementation thereof |
JP2016502619A (en) * | 2012-11-02 | 2016-01-28 | エクソンモービル アップストリーム リサーチ カンパニー | System and method for oxidant compression in a stoichiometric exhaust gas recirculation gas turbine system |
JP2019031979A (en) * | 2012-11-02 | 2019-02-28 | エクソンモービル アップストリーム リサーチ カンパニー | System and method for oxidant compression in stoichiometric exhaust gas recirculation gas turbine system |
US10683801B2 (en) | 2012-11-02 | 2020-06-16 | General Electric Company | System and method for oxidant compression in a stoichiometric exhaust gas recirculation gas turbine system |
CN105986902A (en) * | 2015-03-02 | 2016-10-05 | 袁志平 | Water combustion type turbine engine |
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