JPH048828A - Gas turbine cogeneration system - Google Patents

Gas turbine cogeneration system

Info

Publication number
JPH048828A
JPH048828A JP10750890A JP10750890A JPH048828A JP H048828 A JPH048828 A JP H048828A JP 10750890 A JP10750890 A JP 10750890A JP 10750890 A JP10750890 A JP 10750890A JP H048828 A JPH048828 A JP H048828A
Authority
JP
Japan
Prior art keywords
steam
gas turbine
waste heat
high pressure
turbine
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
JP10750890A
Other languages
Japanese (ja)
Inventor
Takeshi Suzuki
剛 鈴木
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.)
Mitsui Engineering and Shipbuilding Co Ltd
Original Assignee
Mitsui Engineering and Shipbuilding 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 Mitsui Engineering and Shipbuilding Co Ltd filed Critical Mitsui Engineering and Shipbuilding Co Ltd
Priority to JP10750890A priority Critical patent/JPH048828A/en
Publication of JPH048828A publication Critical patent/JPH048828A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/14Combined heat and power generation [CHP]

Landscapes

  • Engine Equipment That Uses Special Cycles (AREA)

Abstract

PURPOSE:To generate and collect steam much more by generating steam by heat collected from air compressed by a gas turbine compressor and collecting this steam by a steam ejector in which waste heat from the gas turbine is utilized. CONSTITUTION:A gas turbine 1 rotates a turbine 3 by combustion gas created by a combustor 2. Also, a waste heat boiler 9 connected to a turbine 3 heats water W fed from a supply source by using the exhaust gas G discharged from the gas turbine 1 and generates high pressure steam Sh. Further, the high pressure steam Sh is supplied to a high pressure process apparatus 10. In this case, an evaporator 11 is connected to the upper 7A side of a middle cooler 7, and a steam is generated by heat taken from air compressed by a compressor 4 on the first stage. On the other hand, the generated low pressure steam Sl is collected by a steam ejector 12 whose power source is a part of the high pressure steam Sh to be supplied to a low pressure process apparatus 13 as steam for miscellaneous use.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、電力と蒸気とを出力するガスタービンコージ
ェネレーションシステムに関する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a gas turbine cogeneration system that outputs electric power and steam.

より詳しくは、より多くの蒸気を回収できるガスタービ
ンコージェネレーションシステムに関する。
More specifically, the present invention relates to a gas turbine cogeneration system that can recover more steam.

〔従来の技術〕[Conventional technology]

近年、着目されているコージェネレーションシステムで
使用されている主機関としては、ガスエンジン、ディー
ゼルエンジン及びガスタービンなどがある。前述したガ
スエンジンとディーゼルエンジンとは、ともに発電効率
が高いが、ガスタービンを主機関とするコージェネレー
ションシステムは電力のほかに、ガスタービンからの廃
熱を利用した廃熱ボイラによって蒸気が得られることか
ら有用視されている。
Main engines used in cogeneration systems that have been attracting attention in recent years include gas engines, diesel engines, and gas turbines. Both the gas engine and diesel engine mentioned above have high power generation efficiency, but in a cogeneration system that uses a gas turbine as the main engine, in addition to electricity, steam is obtained from a waste heat boiler that uses waste heat from the gas turbine. Therefore, it is considered useful.

しかし、一般に、コージェネレーションシステムより発
生させる蒸気圧力はgatg以上とされているが、例え
ば蒸気吸収式2重効用冷凍機等の特別なユーティリティ
ーがない場合は、本来、必要もない高圧の蒸気を供給す
るコージェネレーションシステムは不合理である。すな
わち、従来のコージェネレーションシステムは、8at
gもある高圧の蒸気を減圧して末端の低圧プロセス機器
へ供給している場合が多い。
However, in general, the steam pressure generated by a cogeneration system is said to be higher than GATG, but if there is no special utility such as a steam absorption double-effect refrigerator, high-pressure steam that is not originally needed can be supplied. A cogeneration system that does this is unreasonable. In other words, the conventional cogeneration system has 8at
In many cases, high-pressure steam with a pressure of up to 300 g is reduced in pressure and supplied to low-pressure process equipment at the end.

〔発明の解決しようとする課題〕[Problem to be solved by the invention]

本発明は、コージェネレーションシステムにおいて、そ
の蒸気をさらに多く回収するとともに、その蒸気を利用
するプロセス機器の各用途に応じた圧力の蒸気を供給で
きる対応性に冨んだガスタービンコージェネレーション
システムを提供することにある。
The present invention provides a highly adaptable gas turbine cogeneration system that can recover even more steam and supply steam at pressures appropriate for each use of process equipment that utilizes the steam. It's about doing.

〔課題を解決するための手段〕[Means to solve the problem]

すなわち、本発明のガスタービンコージェネレーション
システムは、ガスタービンに、該ガスタービンのコンプ
レッサーで圧縮した空気から回収した熱により蒸気を発
生させる蒸発器を併設すると共に、前記ガスタービンの
廃熱を利用した廃熱ボイラで発生した高圧蒸気の一部を
動力源とする蒸気エゼクタ−によって前記蒸発器の蒸気
を回収するようにしたことを特徴とするものである。
That is, in the gas turbine cogeneration system of the present invention, a gas turbine is provided with an evaporator that generates steam using heat recovered from air compressed by a compressor of the gas turbine, and the waste heat of the gas turbine is utilized. The present invention is characterized in that the steam of the evaporator is recovered by a steam ejector whose power source is a portion of the high-pressure steam generated in the waste heat boiler.

〔実施例〕〔Example〕

以下、図面を参照して本発明の実施例について説明する
Embodiments of the present invention will be described below with reference to the drawings.

図において、■はガスタービンであり、燃焼器2で生成
した燃焼ガスによってタービン3を回転するようになっ
ている。タービン3は同軸上に高低2段のコンプレッサ
ー4,5および発電機6を有している。また、2つのコ
ンプレッサー4.5の間には中間冷却器7が設けられ、
その中間冷却器7の下段7B側には冷却塔8が接続され
ている。
In the figure, ■ is a gas turbine, and a turbine 3 is rotated by combustion gas generated in a combustor 2. The turbine 3 has compressors 4 and 5 in two stages, high and low, and a generator 6 on the same axis. Furthermore, an intercooler 7 is provided between the two compressors 4.5,
A cooling tower 8 is connected to the lower stage 7B side of the intercooler 7.

前述したタービン3に接続された廃熱ボイラ9は、ガス
タービン1から排出された排ガスGを用いて供給源から
供給される水Wを加熱し、高圧蒸気shを発生するよう
になっている。廃熱ボイラ9で発生した高圧蒸気shは
蒸気吸収式2重効用冷凍機のような高圧プロセス機器1
0に供給される。
The waste heat boiler 9 connected to the turbine 3 described above uses the exhaust gas G discharged from the gas turbine 1 to heat water W supplied from a supply source to generate high-pressure steam sh. The high-pressure steam sh generated in the waste heat boiler 9 is used in high-pressure process equipment 1 such as a steam absorption double-effect refrigerator.
0.

他方、前述した中間冷却器7の上段7A側には、蒸発器
11が接続している。この蒸発器11は1段目のコンプ
レッサー4で圧縮された空気から奪った熱によって蒸気
を発生するようになっている。この蒸発器11で発生し
た低圧蒸気SRは廃熱ボイラ9で発生した高圧蒸気sh
の一部を動力源とする蒸気エゼクタ−12によって低圧
蒸気SZとして回収され、給湯、乾燥、加熱等の雑用蒸
気として低圧プロセス機器13に供給される。なお、図
中、14.15はポンプである。
On the other hand, an evaporator 11 is connected to the upper stage 7A side of the intercooler 7 mentioned above. This evaporator 11 is designed to generate steam using the heat taken from the air compressed by the first stage compressor 4. The low pressure steam SR generated in this evaporator 11 is the high pressure steam sh generated in the waste heat boiler 9.
is recovered as low-pressure steam SZ by a steam ejector 12 using part of the steam as a power source, and is supplied to low-pressure process equipment 13 as miscellaneous steam for hot water supply, drying, heating, etc. In addition, in the figure, 14 and 15 are pumps.

このガスタービンコージェネレーションシステムでは、
廃熱ボイラ9で発生する高圧蒸気Shを圧力を10au
gとし、その高圧蒸気shの大部分を高圧のまま高圧プ
ロセス機器10へ供給し、その一部を使って蒸発器11
から汲み上げた低圧蒸気SEの圧力を4atgとしてい
るが、用途及び負荷に応じて各蒸気のフローを切換える
システム構成にでき、極めて対応性に冨むシステムを実
現できる。
In this gas turbine cogeneration system,
The pressure of the high pressure steam Sh generated in the waste heat boiler 9 is 10au.
g, most of the high-pressure steam sh is supplied to the high-pressure process equipment 10 at high pressure, and a part of it is used to feed the evaporator 11.
Although the pressure of the low-pressure steam SE pumped from the system is set at 4 atg, the system configuration can be configured to switch the flow of each steam depending on the application and load, making it possible to realize a system with extremely high adaptability.

なお、エゼクタ−は部分負荷性能が良くないので、部分
負荷運転の多い用途には、エゼクタ−本数を増やし、エ
ゼクタ−の作動本数を制御することによって部分負荷に
対応するようにすると良い。
Note that ejectors do not have good partial load performance, so for applications where partial load operation is frequent, it is better to increase the number of ejectors and control the number of operating ejectors to cope with partial loads.

また、発熱ボイラー9の後流に温水発生器9゜を設け、
蒸発器11に導いてさらに低圧蒸気を発生させ、エネル
ギー効率を高めることも可能である。
In addition, a hot water generator 9° is installed downstream of the heat generating boiler 9,
It is also possible to further generate low-pressure steam by guiding it to the evaporator 11 to improve energy efficiency.

〔発明の効果〕〔Effect of the invention〕

上記のように、本発明は、ガスタービンに、該ガスター
ビンのコンプレッサーで圧縮した空気から回収した熱に
より蒸気を発生させる蒸発器を併設すると共に、前記ガ
スタービンの廃熱を利用した廃熱ボイラで発生した高圧
蒸気の一部を動力源とする蒸気エゼクタ−によって前記
蒸発器の蒸気を回収するようにしたので、蒸気をさらに
多く発生回収することができるようになった。また、そ
の蒸気を利用するプロセス機器の各用途に応じた圧力の
蒸気を供給できるので、非常に対応性に冨み、工業上、
非常に有用である。
As described above, the present invention provides a gas turbine with an evaporator that generates steam using heat recovered from air compressed by a compressor of the gas turbine, and a waste heat boiler that utilizes the waste heat of the gas turbine. Since the steam in the evaporator is recovered by a steam ejector powered by a portion of the high-pressure steam generated in the evaporator, even more steam can be generated and recovered. In addition, it is possible to supply steam at a pressure that matches the application of the process equipment that uses the steam, making it highly adaptable and suitable for industrial use.
Very useful.

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

図は本発明のガスタービンコージェネレーションシステ
ムの系統図である。 1・・・ガスタービン、4.5・・・コンプレッサー9
・・・廃熱ボイラ、11・・・蒸発器、12・・・エゼ
クター
The figure is a system diagram of the gas turbine cogeneration system of the present invention. 1... Gas turbine, 4.5... Compressor 9
...waste heat boiler, 11...evaporator, 12...ejector

Claims (1)

【特許請求の範囲】[Claims] ガスタービンに、該ガスタービンのコンプレッサーで圧
縮した空気から回収した熱により蒸気を発生させる蒸発
器を併設すると共に、前記ガスタービンの廃熱を利用し
た廃熱ボイラで発生した高圧蒸気の一部を動力源とする
蒸気エゼクターによって前記蒸発器の蒸気を回収するよ
うにしたガスタービンコージェネレーションシステム。
The gas turbine is equipped with an evaporator that generates steam using the heat recovered from the air compressed by the compressor of the gas turbine, and a part of the high-pressure steam generated in the waste heat boiler that utilizes the waste heat of the gas turbine is A gas turbine cogeneration system in which steam from the evaporator is recovered by a steam ejector serving as a power source.
JP10750890A 1990-04-25 1990-04-25 Gas turbine cogeneration system Pending JPH048828A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10750890A JPH048828A (en) 1990-04-25 1990-04-25 Gas turbine cogeneration system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10750890A JPH048828A (en) 1990-04-25 1990-04-25 Gas turbine cogeneration system

Publications (1)

Publication Number Publication Date
JPH048828A true JPH048828A (en) 1992-01-13

Family

ID=14460985

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10750890A Pending JPH048828A (en) 1990-04-25 1990-04-25 Gas turbine cogeneration system

Country Status (1)

Country Link
JP (1) JPH048828A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0597325A1 (en) * 1992-11-07 1994-05-18 Asea Brown Boveri Ag Method of compressor intercooling
EP0604718A3 (en) * 1992-12-30 1994-10-05 Texas Brine Corp Evaporative salt plant.
WO2005090861A1 (en) * 2004-03-18 2005-09-29 Sharp Kabushiki Kaisha Steam generator and steam cooker mounting it
US12407054B2 (en) 2020-03-25 2025-09-02 Lg Energy Solution, Ltd. Transfer jig configured to load battery pack in battery rack and battery pack loading method using the same

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0597325A1 (en) * 1992-11-07 1994-05-18 Asea Brown Boveri Ag Method of compressor intercooling
EP0604718A3 (en) * 1992-12-30 1994-10-05 Texas Brine Corp Evaporative salt plant.
WO2005090861A1 (en) * 2004-03-18 2005-09-29 Sharp Kabushiki Kaisha Steam generator and steam cooker mounting it
CN100507359C (en) 2004-03-18 2009-07-01 夏普株式会社 Steam generator and steam cooker mounting it
US12407054B2 (en) 2020-03-25 2025-09-02 Lg Energy Solution, Ltd. Transfer jig configured to load battery pack in battery rack and battery pack loading method using the same

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