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JPH05332167A - Fuel reforming type gas turbine power generator - Google Patents

Fuel reforming type gas turbine power generator

Info

Publication number
JPH05332167A
JPH05332167A JP13814692A JP13814692A JPH05332167A JP H05332167 A JPH05332167 A JP H05332167A JP 13814692 A JP13814692 A JP 13814692A JP 13814692 A JP13814692 A JP 13814692A JP H05332167 A JPH05332167 A JP H05332167A
Authority
JP
Japan
Prior art keywords
gas
reformer
gas turbine
high temperature
line
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.)
Pending
Application number
JP13814692A
Other languages
Japanese (ja)
Inventor
Mutsuo Kato
睦男 加藤
Keiji Makino
啓二 牧野
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
IHI Corp
Original Assignee
Ishikawajima Harima Heavy Industries Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Ishikawajima Harima Heavy Industries Co Ltd filed Critical Ishikawajima Harima Heavy Industries Co Ltd
Priority to JP13814692A priority Critical patent/JPH05332167A/en
Publication of JPH05332167A publication Critical patent/JPH05332167A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01KSTEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K21/00Steam engine plants not otherwise provided for
    • F01K21/04Steam 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
    • F01K21/047Steam 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

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Hydrogen, Water And Hydrids (AREA)
  • Fuel Cell (AREA)

Abstract

PURPOSE:To carry out reformation reaction of prime combustion sufficiently as so to improve efficiency of a system by providing a high temperature reformer on a reformation fuel line, and also returning back a high temperature gas which is extracted from the intermediate step of the gas turbine into the intermediate step of the gas turbine through the high temperature reformer again. CONSTITUTION:In a reformer 2, steam is led into a prime fuel line 1 to reform prime fuel. Reformed fuel is supplied into a combustor 8 passing a reformation fuel line 7. A gas turbine 12, a power generator 15 is rotatably driven by using a means of combustion gas generated in the combustor 8. The reformer 2 is constituted as a low temperature reformer. In this case, a high temperature reformer 18 is provided on the way of the reformation fuel line 7. On the other hand, by a gas extracting line 19, high temperature gas is extracted from the intermediate step 21 of the gas turbine 12 to supply into the high temperature reformer 18. And by a gas returning-back line 20, gas passing the high temperature reformer 18 from the gas extracting line 19 is returned back to the intermediate step 22 of the gas turbine 12.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、燃料改質形ガスタービ
ン発電装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a fuel reforming type gas turbine power generator.

【0002】[0002]

【従来の技術】従来のこの種の発電装置は、たとえば、
図2に示すような構成からなっている。図2において、
1は原燃料(NG、LPG、ナフサ)ライン、2は低温
改質器、3は排熱回収ボイラ、4は給水ライン、5はポ
ンプ、6は蒸気ライン、7は改質燃料ライン、8は燃焼
器、9は空気圧縮機、10は給気ライン、11は圧縮空
気ライン、12はガスタービン、13はタービン入口ラ
イン、14はタービン排気ライン、15は発電機、16
は排ガスライン、17はスタックである。
2. Description of the Related Art A conventional power generator of this type is, for example,
The structure is as shown in FIG. In FIG.
1 is a raw fuel (NG, LPG, naphtha) line, 2 is a low temperature reformer, 3 is an exhaust heat recovery boiler, 4 is a water supply line, 5 is a pump, 6 is a steam line, 7 is a reformed fuel line, 8 is a Combustor, 9 air compressor, 10 air supply line, 11 compressed air line, 12 gas turbine, 13 turbine inlet line, 14 turbine exhaust line, 15 generator, 16
Is an exhaust gas line, and 17 is a stack.

【0003】すなわち、原燃料に水蒸気を導入して該燃
料を改質(H2 、COを有する燃料に変換)する低温改
質器2と、その蒸気を発生する排熱回収ボイラ3と、こ
のボイラ3から低温改質器2へ蒸気を供給する蒸気ライ
ン6と、低温改質器2で改質された燃料を燃焼器8に供
給する改質燃料ライン7と、燃焼器8で発生した燃焼ガ
スを駆動源として導入して発電機15を回転駆動するガ
スタービン12などを有している。
That is, a low temperature reformer 2 for reforming the fuel (converting it into a fuel having H 2 and CO) by introducing steam into the raw fuel, an exhaust heat recovery boiler 3 for generating the steam, A steam line 6 for supplying steam from the boiler 3 to the low temperature reformer 2, a reformed fuel line 7 for supplying the fuel reformed by the low temperature reformer 2 to the combustor 8, and combustion generated in the combustor 8. It has a gas turbine 12 and the like that introduces gas as a drive source to drive the generator 15 to rotate.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、図2に
示した従来の発電装置においては、改質器としては低温
改質器2だけであるため、つまり、ガスタービン12か
ら出て排気ライン14から低温改質器2に供給されるタ
ービン排ガスの温度が約600°Cというように低く、
原燃料の改質が十分に行われないままで、燃焼器8で燃
焼するので、改質反応を利用したシステムの効率向上が
少ないという問題点があった。
However, in the conventional power generator shown in FIG. 2, since only the low temperature reformer 2 is used as the reformer, that is, the reformer is discharged from the gas turbine 12 and the exhaust line 14. The temperature of the turbine exhaust gas supplied to the low temperature reformer 2 is as low as about 600 ° C,
Since the raw fuel is burned in the combustor 8 without being sufficiently reformed, there is a problem in that the efficiency of the system utilizing the reforming reaction is not improved much.

【0005】本発明は、上記のような問題点を解決しよ
うとするものである。すなわち、本発明は、改質器での
原燃料の改質反応が十分に行われて、システムの効率向
上を図ることができる燃料改質形ガスタービン発電装置
を提供することを目的とするものである。
The present invention is intended to solve the above problems. That is, it is an object of the present invention to provide a fuel reforming type gas turbine power generator in which the reforming reaction of the raw fuel in the reformer is sufficiently performed and the efficiency of the system can be improved. Is.

【0006】[0006]

【課題を解決するための手段】上記目的を達成するため
に、本発明は、原燃料に水蒸気を導入して該燃料を改質
する改質器と、該改質器で改質された燃料を燃焼器へ供
給する改質燃料ラインと、該燃焼器で発生した燃焼ガス
を駆動源として導入して発電機を回転駆動するガスター
ビンとを有し、かつ、前記改質器が低温改質器である発
電装置において、前記改質燃料ラインの途中に設置され
た高温改質器を備え、しかも、該ガスタービンの中間段
と前記高温改質器の一側とを接続して該ガスタービンの
中間段から高温ガスを抽気して前記高温改質器に供給す
るガス抽気ラインと、前記高温改質器の他側と該ガスタ
ービンの中間段とを接続して該ガス抽気ラインから前記
高温改質器を通ったガスを該ガスタービンの中間段へ戻
すガス戻しラインとを備えているものとした。
To achieve the above object, the present invention provides a reformer for introducing steam into a raw fuel to reform the fuel, and a fuel reformed by the reformer. And a gas turbine for introducing a combustion gas generated in the combustor as a drive source to drive the generator to rotate, and the reformer has a low-temperature reformer. In a power generator that is a gas turbine, the gas turbine is provided with a high temperature reformer installed in the middle of the reforming fuel line, and the intermediate stage of the gas turbine is connected to one side of the high temperature reformer. Of the high temperature reformer and the other side of the high temperature reformer and the intermediate stage of the gas turbine by connecting the gas extraction line for extracting high temperature gas from the intermediate stage of Gas return line for returning the gas passing through the reformer to the intermediate stage of the gas turbine It was assumed to have a.

【0007】[0007]

【作用】本発明によれば、改質器が低温改質器である燃
料改質形ガスタービン発電装置において、該低温改質器
で改質された燃料を燃焼器へ供給する改質燃料ラインの
途中に設置された高温改質器を備え、しかも、該ガスタ
ービンの中間段と前記高温改質器の一側とを接続して該
ガスタービンの中間段から高温ガスを抽気して前記高温
改質器に供給するガス抽気ラインと、前記高温改質器の
他側と該ガスタービンの中間段とを接続して該ガス抽気
ラインから前記高温改質器を通ったガスを該ガスタービ
ンの中間段へ戻すガス戻しラインとを備えているから、
前記低温改質器で十分に改質されなかった改質燃料が前
記高温改質器で十分に改質され、したがって、改質効果
による効率向上が図れる。
According to the present invention, in a fuel reforming type gas turbine power generator in which the reformer is a low temperature reformer, a reformed fuel line for supplying the fuel reformed by the low temperature reformer to a combustor. A high-temperature reformer installed in the middle of the gas turbine, and further, by connecting the intermediate stage of the gas turbine and one side of the high-temperature reformer to extract the high-temperature gas from the intermediate stage of the gas turbine, The gas extraction line supplied to the reformer, the other side of the high temperature reformer and the intermediate stage of the gas turbine are connected to each other, and the gas passing through the high temperature reformer from the gas extraction line is connected to the gas turbine of the gas turbine. Since it has a gas return line that returns to the intermediate stage,
The reformed fuel that has not been sufficiently reformed in the low-temperature reformer is sufficiently reformed in the high-temperature reformer, so that the efficiency can be improved by the reforming effect.

【0008】[0008]

【実施例】図1は本発明の一実施例を示している。図1
において、符号1から17までは、図2と同じである。
そして、18は後述する高温改質器、19はタービン中
間段抽気ライン、20はタービン中間段ガス戻しライン
である。
FIG. 1 shows an embodiment of the present invention. Figure 1
2, the reference numerals 1 to 17 are the same as those in FIG.
Further, 18 is a high temperature reformer described later, 19 is a turbine intermediate stage extraction line, and 20 is a turbine intermediate stage gas return line.

【0009】すなわち、前記高温改質器18は、低温改
質器2と燃焼器8を接続している改質燃料ライン7の途
中に設置されている。前記タービン中間段抽気ライン1
9は、ガスタービン12の中間段の一部21と該高温改
質器18の一側とに接続されていて、該ガスタービン1
2の中間段から該高温改質器18に高温ガスを供給する
ようになっている。
That is, the high temperature reformer 18 is installed in the middle of the reforming fuel line 7 connecting the low temperature reformer 2 and the combustor 8. The turbine intermediate stage extraction line 1
9 is connected to a part 21 of the intermediate stage of the gas turbine 12 and one side of the high temperature reformer 18, and the gas turbine 1
A high temperature gas is supplied to the high temperature reformer 18 from an intermediate stage of No. 2.

【0010】前記タービン中間段ガス戻しライン20
は、該高温改質器18の他側と該ガスタービン12の中
間段の前記一部21の直下流部22とに接続されてい
て、該抽気ライン19から高温改質器18を通ったガス
を該タービン12の中間段に戻すようになっている。
The turbine intermediate stage gas return line 20
Is connected to the other side of the high temperature reformer 18 and to the immediate downstream portion 22 of the part 21 of the intermediate stage of the gas turbine 12, and the gas passing through the high temperature reformer 18 from the extraction line 19 Are returned to the intermediate stage of the turbine 12.

【0011】図1に示すように構成された燃料改質形ガ
スタービン発電装置においては、原燃料ライン1からの
原燃料は、蒸気ライン6からの水蒸気によって、低温改
質器2内で、タービン排気ライン14からの約600°
Cのタービン排気を熱源として加熱されて、ある程度改
質されるが、さらに、高温改質器18内で、タービン中
間段抽気ライン19からの約900°Cの抽気ガスを熱
源として加熱されて、十分に改質されるので、改質効果
によるシステムの効率の向上が図れる。
In the fuel reforming type gas turbine power generator constructed as shown in FIG. 1, the raw fuel from the raw fuel line 1 is turbined in the low temperature reformer 2 by the steam from the steam line 6. About 600 ° from the exhaust line 14
The turbine exhaust gas of C is heated as a heat source to be reformed to some extent, and further, in the high temperature reformer 18, the extracted gas at about 900 ° C. from the turbine intermediate stage extraction line 19 is heated as a heat source, Since it is sufficiently reformed, the efficiency of the system can be improved by the reforming effect.

【0012】なお、タービン入口ライン13の燃焼ガス
の温度は、約1600°Cとすることが好ましく、低く
ても、900°Cとすることが望ましい。
The temperature of the combustion gas in the turbine inlet line 13 is preferably about 1600 ° C, and at least 900 ° C is desirable.

【0013】[0013]

【発明の効果】以上説明したように、本発明によれば、
改質器が低温改質器である燃料改質形ガスタービン発電
装置において、該低温改質器で改質された燃料を燃焼器
へ供給する改質燃料ラインの途中に設置された高温改質
器を備え、しかも、該ガスタービンの中間段と前記高温
改質器の一側とを接続して該ガスタービンの中間段から
高温ガスを抽気して前記高温改質器に供給するガス抽気
ラインと、前記高温改質器の他側と該ガスタービンの中
間段とを接続して該ガス抽気ラインから前記高温改質器
を通ったガスを該ガスタービンの中間段へ戻すガス戻し
ラインとを備えているから、前記低温改質器で十分に改
質されなかった改質燃料が前記高温改質器で十分に改質
され、したがって、改質効果による効率向上が図れる。
As described above, according to the present invention,
In a fuel reforming gas turbine power generator in which the reformer is a low temperature reformer, a high temperature reformer installed in the middle of a reforming fuel line for supplying the fuel reformed by the low temperature reformer to a combustor. And a gas extraction line that connects the intermediate stage of the gas turbine and one side of the high temperature reformer and extracts high temperature gas from the intermediate stage of the gas turbine and supplies the extracted high temperature reformer to the high temperature reformer. And a gas return line that connects the other side of the high-temperature reformer and the intermediate stage of the gas turbine and returns the gas that has passed through the high-temperature reformer from the gas extraction line to the intermediate stage of the gas turbine. Since it is provided, the reformed fuel that has not been sufficiently reformed in the low temperature reformer is sufficiently reformed in the high temperature reformer, and therefore the efficiency can be improved by the reforming effect.

【0014】また前記高温改質器の加熱源としては、ガ
スタービンの中間段からの抽気したガスを利用し、その
後は中間段に戻すので、設計の段階でその抽気個所を最
適な個所となるように選ぶことができ、したがって、改
質温度を最適な温度範囲にすることができ、改質による
効率向上効果が十分に得られる。
Further, as the heating source of the high temperature reformer, the gas extracted from the intermediate stage of the gas turbine is used and then returned to the intermediate stage, so that the extracted place is the optimum place in the design stage. Therefore, the reforming temperature can be set in the optimum temperature range, and the efficiency improving effect due to the reforming can be sufficiently obtained.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明の一実施例を示した説明図である。FIG. 1 is an explanatory diagram showing an embodiment of the present invention.

【図2】従来の技術の一例を示した説明図である。FIG. 2 is an explanatory diagram showing an example of a conventional technique.

【符号の説明】[Explanation of symbols]

1 原燃料ライン 2 低温改質器 6 蒸気ライン 7 改質燃料ライン 8 燃焼器 12 ガスタービン 13 タービン入口ライン 14 タービン排気ライン 15 発電機 18 高温改質器 19 タービン中間段抽気ライン 20 タービン中間段ガス戻しライン 21 タービン中間段の一部 22 タービン中間段の一部の直下流部 1 Raw Fuel Line 2 Low Temperature Reformer 6 Steam Line 7 Reformed Fuel Line 8 Combustor 12 Gas Turbine 13 Turbine Inlet Line 14 Turbine Exhaust Line 15 Generator 18 High Temperature Reformer 19 Turbine Intermediate Stage Extraction Line 20 Turbine Intermediate Stage Gas Return line 21 Part of intermediate turbine stage 22 Directly downstream part of intermediate turbine stage

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 原燃料に水蒸気を導入して該燃料を改質
する改質器と、該改質器で改質された燃料を燃焼器へ供
給する改質燃料ラインと、該燃焼器で発生した燃焼ガス
を駆動源として導入して発電機を回転駆動するガスター
ビンとを有し、かつ、前記改質器が低温改質器である発
電装置において、前記改質燃料ラインの途中に設置され
た高温改質器を備え、しかも、該ガスタービンの中間段
と前記高温改質器の一側とを接続して該ガスタービンの
中間段から高温ガスを抽気して前記高温改質器に供給す
るガス抽気ラインと、前記高温改質器の他側と該ガスタ
ービンの中間段とを接続して該ガス抽気ラインから前記
高温改質器を通ったガスを該ガスタービンの中間段へ戻
すガス戻しラインとを備えていることを特徴とする、燃
料改質形ガスタービン発電装置。
1. A reformer for introducing steam into a raw fuel to reform the fuel, a reforming fuel line for supplying the fuel reformed by the reformer to a combustor, and the combustor. A power generator having a gas turbine that introduces the generated combustion gas as a drive source to drive a generator to rotate, and the reformer is a low-temperature reformer, and is installed in the middle of the reforming fuel line. And a high temperature reformer which is connected to an intermediate stage of the gas turbine and one side of the high temperature reformer to extract high temperature gas from the intermediate stage of the gas turbine to the high temperature reformer. The gas extraction line to be supplied is connected to the other side of the high temperature reformer and the intermediate stage of the gas turbine, and the gas passing through the high temperature reformer from the gas extraction line is returned to the intermediate stage of the gas turbine. A fuel reforming type gas turbine, which is equipped with a gas return line. Power generator.
【請求項2】 ガス抽気ラインがガスタービンの中間段
の一部に接続され、ガス戻しラインが該ガスタービンの
中間段の前記一部の直下流部に接続されている請求項1
記載の燃料改質形ガスタービン発電装置。
2. The gas extraction line is connected to a part of an intermediate stage of the gas turbine, and the gas return line is connected to a part of the intermediate stage of the gas turbine, just downstream of the part.
The fuel reforming type gas turbine power generator described.
【請求項3】 ガスタービンに供給される燃焼ガスの温
度が900ないし1600°Cであり、低温改質器に供
給されるタービン排気ガスの温度が約600°Cである
ようにしている請求項1または2記載の燃料改質形ガス
タービン発電装置。
3. The temperature of the combustion gas supplied to the gas turbine is 900 to 1600 ° C., and the temperature of the turbine exhaust gas supplied to the low temperature reformer is about 600 ° C. 1. The fuel reforming type gas turbine power generator according to 1 or 2.
JP13814692A 1992-05-29 1992-05-29 Fuel reforming type gas turbine power generator Pending JPH05332167A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13814692A JPH05332167A (en) 1992-05-29 1992-05-29 Fuel reforming type gas turbine power generator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13814692A JPH05332167A (en) 1992-05-29 1992-05-29 Fuel reforming type gas turbine power generator

Publications (1)

Publication Number Publication Date
JPH05332167A true JPH05332167A (en) 1993-12-14

Family

ID=15215086

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13814692A Pending JPH05332167A (en) 1992-05-29 1992-05-29 Fuel reforming type gas turbine power generator

Country Status (1)

Country Link
JP (1) JPH05332167A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6014863A (en) * 1996-05-28 2000-01-18 Hitachi, Ltd. Waste processing system and fuel reformer used in the waste processing system
FR2783014A1 (en) * 1998-09-04 2000-03-10 Toshiba Kk TURBINE SYSTEM AND METHOD FOR PRODUCING ENERGY
US6058856A (en) * 1996-05-28 2000-05-09 Hitachi, Ltd. Waste processing system and fuel reformer used in the waste processing system
US6282902B1 (en) 1997-10-28 2001-09-04 Hitachi, Ltd. Waste processing system and fuel reformer used in the waste processing system
JP2005220007A (en) * 2004-01-09 2005-08-18 Hitachi Ltd Reforming furnace system
US7707837B2 (en) 2004-01-09 2010-05-04 Hitachi, Ltd. Steam reforming system

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6014863A (en) * 1996-05-28 2000-01-18 Hitachi, Ltd. Waste processing system and fuel reformer used in the waste processing system
US6058856A (en) * 1996-05-28 2000-05-09 Hitachi, Ltd. Waste processing system and fuel reformer used in the waste processing system
US6282902B1 (en) 1997-10-28 2001-09-04 Hitachi, Ltd. Waste processing system and fuel reformer used in the waste processing system
US6442938B2 (en) 1997-10-28 2002-09-03 Hitachi, Ltd. Waste processing system and fuel reformer used in the waste processing system
US6688106B2 (en) 1997-10-28 2004-02-10 Hitachi, Ltd. Waste processing system and fuel reformer used in the waste processing system
FR2783014A1 (en) * 1998-09-04 2000-03-10 Toshiba Kk TURBINE SYSTEM AND METHOD FOR PRODUCING ENERGY
US6338239B1 (en) 1998-09-04 2002-01-15 Kabushiki Kaisha Toshiba Turbine system having a reformer and method thereof
JP2005220007A (en) * 2004-01-09 2005-08-18 Hitachi Ltd Reforming furnace system
US7707837B2 (en) 2004-01-09 2010-05-04 Hitachi, Ltd. Steam reforming system

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