JPH1136817A - Power generation facilities - Google Patents

Power generation facilities

Info

Publication number
JPH1136817A
JPH1136817A JP19113297A JP19113297A JPH1136817A JP H1136817 A JPH1136817 A JP H1136817A JP 19113297 A JP19113297 A JP 19113297A JP 19113297 A JP19113297 A JP 19113297A JP H1136817 A JPH1136817 A JP H1136817A
Authority
JP
Japan
Prior art keywords
air
power generation
heat exchanger
expander
gas
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
Application number
JP19113297A
Other languages
Japanese (ja)
Other versions
JP3782552B2 (en
Inventor
Hidetoshi Aiki
英鋭 相木
Masaharu Watabe
正治 渡部
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries 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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP19113297A priority Critical patent/JP3782552B2/en
Publication of JPH1136817A publication Critical patent/JPH1136817A/en
Application granted granted Critical
Publication of JP3782552B2 publication Critical patent/JP3782552B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related 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
    • Y02E20/16Combined cycle power plant [CCPP], or combined cycle gas turbine [CCGT]
    • 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
    • Y02E20/16Combined cycle power plant [CCPP], or combined cycle gas turbine [CCGT]
    • Y02E20/18Integrated gasification combined cycle [IGCC], e.g. combined with carbon capture and storage [CCS]

Abstract

PROBLEM TO BE SOLVED: To generate electricity with no need for cleaning up generated gas even if fuel including corrosive constituent and ash content such as coals, heavy oil and the like, is being used. SOLUTION: Fuel 10 such as coals, heavy oil and the like is burnt out by a incinerator 2 so as to allow exhaust gas 11 out of the incinerator to be introduced to a ceramics heat exchanger 1. Air 6 is compressed by a gas turbine compressor 3, and let the heat of air 7 at its outlet port be exchanged with that of exhaust gas 11 out of the incinerator by the ceramis heat exchanger 1, so that air at high temperature can thereby be obtained. Air 8 is conducted to the expander 4 of a gas turbine so as to be expanded, so that power driving a generator 5 can thereby be obtained.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、石炭や重質油等、
腐食成分、灰分を多く含む燃料を用いることのできる発
電設備に関する。
TECHNICAL FIELD The present invention relates to a method for producing coal, heavy oil, etc.
The present invention relates to a power generation facility that can use a fuel containing a large amount of corrosive components and ash.

【0002】[0002]

【従来の技術】従来の発電設備として、石炭や重質油を
ガス化した燃料をガスタービンで燃焼させるようにした
複合発電設備があり、その系統を図4に示してあり、以
下それについて説明する。
2. Description of the Related Art As a conventional power generation facility, there is a combined power generation facility in which fuel obtained by gasifying coal or heavy oil is burned by a gas turbine, and its system is shown in FIG. I do.

【0003】図4において、25はガス化炉、27は熱
交換器である。28はフィルタ、31は脱硫装置で、こ
れらはガス化ガスに対するクリーンアップシステムを構
成している。29はガスタービン30の燃焼器、13は
排熱回収ボイラを示し、5は発電機、15は蒸気タービ
ンを示している。
In FIG. 4, reference numeral 25 denotes a gasification furnace, and 27 denotes a heat exchanger. 28 is a filter and 31 is a desulfurization device, which constitutes a cleanup system for gasified gas. 29 denotes a combustor of the gas turbine 30, 13 denotes an exhaust heat recovery boiler, 5 denotes a generator, and 15 denotes a steam turbine.

【0004】このような構成を有する図4の発電設備に
おいて、燃料10が空気23と共にガス化炉25に投入
される。ガス化炉25で生成されたガス化ガス26は熱
交換器27に導かれて冷却されたのち、フィルタ28、
脱硫装置31で除塵と脱硫が行われてクリーンガスとな
ってガスタービン30の燃焼器29へ供給される。
[0004] In the power generation equipment of FIG. 4 having such a configuration, the fuel 10 is charged into the gasification furnace 25 together with the air 23. The gasification gas 26 generated in the gasification furnace 25 is guided to a heat exchanger 27 and cooled, and then filtered,
Dust removal and desulfurization are performed in the desulfurization device 31 to be supplied as a clean gas to the combustor 29 of the gas turbine 30.

【0005】燃焼器29では、別途供給される空気24
によって上記ガス化ガスが燃焼し、ガスタービン30が
駆動される。ガスタービン30は発電機5を駆動し、ガ
スタービン30の燃焼ガス32は排熱回収ボイラ13へ
導入される。
[0005] In the combustor 29, separately supplied air 24
As a result, the gasified gas is burned, and the gas turbine 30 is driven. The gas turbine 30 drives the generator 5, and the combustion gas 32 of the gas turbine 30 is introduced into the exhaust heat recovery boiler 13.

【0006】排熱回収ボイラ13で発生する蒸気により
蒸気タービン15が駆動され、発電機5を駆動して発電
を行い、排熱回収ボイラ13の燃焼ガス32は煙突17
から放出される。
The steam generated by the heat recovery steam generator 13 drives the steam turbine 15 to drive the generator 5 to generate electric power.
Released from

【0007】[0007]

【発明が解決しようとする課題】石炭や重質油は腐食成
分と灰分を多く含む燃料であり、ガスタービンに直接導
いて燃焼することができないため、前記したように従来
のガス化複合発電設備では、それらの燃料をガス化し、
ガス化ガスをフィルタ28と脱硫装置31を有するクリ
ーンアップシステムに通してガスタービンに導く構成と
しており、システムが複雑となっていた。
As described above, coal and heavy oil are fuels containing a large amount of corrosive components and ash, and cannot be directly guided to a gas turbine for combustion. Then, gasify those fuels,
The configuration is such that the gasified gas is led to the gas turbine through a cleanup system having the filter 28 and the desulfurization device 31, and the system is complicated.

【0008】本発明は、石炭や重質油等の腐食成分、灰
分を多く含む燃料を用いながらも、生成ガスのクリーン
アップシステムを必要とせずに発電可能な発電設備を提
供することを課題としている。
[0008] It is an object of the present invention to provide a power generation facility capable of generating power without using a cleanup system for generated gas while using a fuel containing a large amount of corrosive components and ash, such as coal and heavy oil. I have.

【0009】[0009]

【課題を解決するための手段】本発明は、前記課題を解
決するため、次の構成をもつ発電設備を提供する。すな
わち、本発明による発電設備は空気圧縮機と、同空気圧
縮機と同軸で回転する空気膨張機および発電機と、燃焼
炉と、熱交換器とを備える。
The present invention, in order to solve the above-mentioned problems, provides a power generation facility having the following configuration. That is, the power generation equipment according to the present invention includes an air compressor, an air expander and a generator rotating coaxially with the air compressor, a combustion furnace, and a heat exchanger.

【0010】そして前記空気圧縮機の出口空気を前記熱
交換器で加熱して前記空気膨張機へ送給するとともに、
同空気膨張機の出口空気と燃料とを前記燃焼炉に送給し
て燃焼させる。同燃焼炉の排ガスは前記熱交換器へ送給
して前記空気圧縮機の出口空気と熱交換させるように構
成する。
[0010] The outlet air of the air compressor is heated by the heat exchanger and sent to the air expander.
The outlet air and fuel of the air expander are fed to the combustion furnace and burned. Exhaust gas from the combustion furnace is sent to the heat exchanger to exchange heat with outlet air of the air compressor.

【0011】本発明による発電設備は前記した構成を有
しており、石炭や重質油などの腐食成分、灰分を多く含
む燃料は独立した燃焼炉で燃焼させ、その燃焼生成ガス
を熱交換器に導いて空気と熱交換させその高温化した空
気を空気膨張機に導いて仕事をさせる。
[0011] The power generation equipment according to the present invention has the above-described configuration, and a fuel containing a large amount of corrosive components such as coal and heavy oil and ash is burned in an independent combustion furnace, and the combustion product gas is converted into a heat exchanger. And heat exchange with the air, and the heated air is guided to an air expander for work.

【0012】その熱交換器を、セラミックス管製とした
り、或いは、例えばメタル温度650〜700℃以上の
領域部分をセラミックス管、600〜700℃以下はス
テンレス鋼、炭素鋼管を用いて構成し、高温腐食に強い
構造とすることによって、腐食成分、灰分を多く含む石
炭や重質油を用いても何らの問題を生じない発電設備と
なる。
The heat exchanger may be made of a ceramic tube, or may be made of, for example, a ceramic tube for a region having a metal temperature of 650 to 700 ° C. or higher, and a stainless steel or carbon steel tube for a metal temperature of 600 to 700 ° C. or lower. By providing a structure that is resistant to corrosion, a power generation facility that does not cause any problem even when coal or heavy oil containing a large amount of corrosive components and ash is used.

【0013】このように、本発明の発電設備では、例え
ば1300〜1600℃の高温燃焼ガスを用いて100
0℃以上の高温空気を生成させ、効率の良い発電を行わ
せることができる。
As described above, in the power generation equipment of the present invention, for example, a high-temperature combustion gas of 1300 to 1600 ° C.
High-temperature air of 0 ° C. or more can be generated, and efficient power generation can be performed.

【0014】本発明による発電設備では、熱交換器で空
気を加熱したあとの熱交換器出口排ガスを排熱回収ボイ
ラに導いて蒸気を発生させ蒸気発電サイクルを併設した
構成とすることにより更に高効率の発電設備とすること
ができる。
In the power generation equipment according to the present invention, the exhaust gas discharged from the heat exchanger after the air is heated by the heat exchanger is guided to the exhaust heat recovery boiler to generate steam, and the steam power generation cycle is additionally provided. An efficient power generation facility can be provided.

【0015】更にまた、本発明による発電設備では、空
気膨張機を出た空気のうち、燃焼炉に導かれる空気以外
の余剰分を、燃焼炉をバイパスさせて排熱回収ボイラや
燃料を燃焼させるボイラへ燃焼用空気として導いて有効
に活用するようにすることができる。
Still further, in the power generation equipment according to the present invention, of the air that has exited the air expander, an excess other than the air guided to the combustion furnace is caused to bypass the combustion furnace and burn the exhaust heat recovery boiler and the fuel. It can be guided to the boiler as combustion air and used effectively.

【0016】以上のように、本発明によれば、石炭や重
質油等の腐食成分、灰分を多く含む燃料を用いながら
も、生成ガスのクリーンアップシステムを必要とせずに
発電可能な発電設備が提供される。
As described above, according to the present invention, power generation equipment capable of generating power without using a cleanup system for generated gas while using a fuel containing a large amount of ash and corrosive components such as coal and heavy oil. Is provided.

【0017】[0017]

【発明の実施の形態】以下、本発明の発電設備を図1〜
図3に示した実施の形態に基づいて具体的に説明する。
なお、以下の各実施形態において、同一部分には同じ符
号を付し重複する説明は省略する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The power generation equipment of the present invention is shown in FIGS.
A specific description will be given based on the embodiment shown in FIG.
In the following embodiments, the same portions are denoted by the same reference numerals, and redundant description will be omitted.

【0018】(実施の第1形態)まず、図1に示した実
施の第1形態による発電設備について説明する。図1に
おいて、1はセラミックス熱交換器、2は燃焼炉であ
る。3はガスタービン圧縮機で、4はガスタービン膨張
機で、両者は同軸で回転する。
(First Embodiment) First, a power generation facility according to a first embodiment shown in FIG. 1 will be described. In FIG. 1, 1 is a ceramic heat exchanger, and 2 is a combustion furnace. 3 is a gas turbine compressor, 4 is a gas turbine expander, and both rotate coaxially.

【0019】ガスタービン圧縮機3は本発明にいう空気
圧縮機を構成し、ガスタービン膨張機4は本発明にいう
空気膨張機を構成する。5は発電機で、ガスタービン膨
張機4と同軸で回転する。
The gas turbine compressor 3 constitutes the air compressor of the present invention, and the gas turbine expander 4 constitutes the air expander of the present invention. A generator 5 rotates coaxially with the gas turbine expander 4.

【0020】このように構成された図1の発電設備にお
いて、燃焼炉2には石炭や重質油などの燃料10とガス
タービン膨張機4から出る空気が供給されて燃焼し、燃
焼炉2よりの排ガス11はセラミックス熱交換器1に至
る。
In the power generation system of FIG. 1 configured as described above, the combustion furnace 2 is supplied with fuel 10 such as coal or heavy oil and air emitted from the gas turbine expander 4 and burns. Exhaust gas 11 reaches the ceramic heat exchanger 1.

【0021】セラミックス熱交換器1にてガスタービン
圧縮機3より供給された高圧の空気7を1000℃以上
に加熱し、その熱交換器1出口の空気8をガスタービン
膨張機4に供給、駆動する。これにより発電機5で発電
が行われる。ガスタービン膨張機4より排出される空気
9は余熱を利用し燃焼炉2で燃料10を燃焼する為の燃
焼用空気として利用される。
The high-pressure air 7 supplied from the gas turbine compressor 3 is heated to 1000 ° C. or higher in the ceramic heat exchanger 1, and the air 8 at the outlet of the heat exchanger 1 is supplied to the gas turbine expander 4 for driving. I do. As a result, power is generated by the generator 5. The air 9 discharged from the gas turbine expander 4 is used as combustion air for burning the fuel 10 in the combustion furnace 2 using residual heat.

【0022】(実施の第2形態)次に、図2に示した実
施の第2形態による発電設備について説明する。図2に
おいて、13は排熱回収ボイラを示し、セラミックス熱
交換器1を出た燃焼炉2の排ガス12が導かれる。
(Second Embodiment) Next, a power generation facility according to a second embodiment shown in FIG. 2 will be described. In FIG. 2, reference numeral 13 denotes an exhaust heat recovery boiler to which exhaust gas 12 from the combustion furnace 2 exiting the ceramic heat exchanger 1 is guided.

【0023】15は蒸気タービン、16は排煙処理設備
を示している。図2に示した発電設備は、図1に示した
発電設備に対し、その設備から出る燃焼炉排ガス12を
用いる排熱回収システムを付設した構成を有している。
Reference numeral 15 denotes a steam turbine, and 16 denotes a flue gas treatment facility. The power generation equipment illustrated in FIG. 2 has a configuration in which an exhaust heat recovery system that uses the combustion furnace exhaust gas 12 emitted from the power generation equipment illustrated in FIG. 1 is added to the power generation equipment illustrated in FIG.

【0024】図2の設備では、セラミックス熱交換器1
から出る燃焼炉排ガス12と、ガスタービン膨張機4か
ら出る排気(空気)のうち燃焼炉2に使用されない余剰
空気が過剰空気バイパス18を通して排熱回収ボイラ1
3へ供給される。排熱回収ボイラ13で発生した蒸気1
4は蒸気タービン15へ供給され発電機5を駆動して電
力を発生する。
In the equipment shown in FIG.
Of the combustion furnace exhaust gas 12 and exhaust air (air) exiting from the gas turbine expander 4 that are not used in the combustion furnace 2 are passed through the excess air bypass 18 to the exhaust heat recovery boiler 1.
3. Steam 1 generated in the heat recovery steam generator 13
4 is supplied to the steam turbine 15 to drive the generator 5 to generate electric power.

【0025】(実施の第3形態)次に、図3に示した実
施の第3形態による発電設備について説明する。図3に
おいて、21はダンパ、22は通常のボイラを示してい
る。図3に示す発電設備は、図2における排熱回収ボイ
ラ13に代えてボイラ22を設置したものである。ボイ
ラ22は従来のボイラであってよい。
(Third Embodiment) Next, a power generation facility according to a third embodiment shown in FIG. 3 will be described. In FIG. 3, reference numeral 21 denotes a damper, and 22 denotes a normal boiler. The power generation equipment shown in FIG. 3 is provided with a boiler 22 instead of the exhaust heat recovery boiler 13 in FIG. Boiler 22 may be a conventional boiler.

【0026】すなわち、この図3に示した発電設備で
は、セラミックス熱交換器1を出た排ガス12をボイラ
22の火炉に投入し熱回収を計るものである。また、ガ
スタービン膨張機4からの余剰空気が過剰空気バイパス
18を経てボイラ22の火炉へバーナ部から排気再熱用
の燃焼空気として投入される。
That is, in the power generation equipment shown in FIG. 3, the exhaust gas 12 exiting the ceramic heat exchanger 1 is charged into the furnace of the boiler 22 to recover heat. Excess air from the gas turbine expander 4 is supplied to the furnace of the boiler 22 via the excess air bypass 18 from the burner as combustion air for reheating exhaust gas.

【0027】[0027]

【発明の効果】以上説明したように、本発明による燃焼
設備は独立した燃焼炉で燃料を燃焼し、その燃焼炉で生
成した排ガスにより空気を加熱し、その加熱空気を空気
膨張機に供給して動力を取り出す。
As described above, the combustion equipment according to the present invention burns fuel in an independent combustion furnace, heats air with exhaust gas generated in the combustion furnace, and supplies the heated air to an air expander. To remove the power.

【0028】従って、従来の技術である石炭ガス化複合
発電あるいは重質油複合発電システムにおいて必要とし
ていたようなガス化ガスからフィルタ及び脱硫装置を用
いて腐食成分、灰分を除去する、所謂、クリーンアップ
システムを本発明の発電設備では必要としない。
Therefore, the so-called clean, which removes corrosive components and ash from the gasified gas as required in the conventional integrated coal gasification combined cycle or heavy oil combined cycle system using a filter and a desulfurization apparatus, is called a clean technique. No up system is required in the power plant of the present invention.

【0029】本発明では、駆動用の気体は空気を用いて
おり、駆動系統の信頼性に優れる。これはまた、熱源と
しての燃焼器用の燃料に左右されないため、石炭、重質
油をはじめ多様な燃料が可能である。
In the present invention, the driving gas uses air, and the driving system is excellent in reliability. This is also independent of the fuel for the combustor as a heat source, so that various fuels such as coal and heavy oil are possible.

【0030】更にまた、本発明の発電設備では、熱交換
器を出た燃焼炉排ガスを排熱回収ボイラや通常のボイラ
に導く構成とすることにより熱効率の高い設備とするこ
とができる。
Furthermore, in the power generation equipment of the present invention, the equipment having high thermal efficiency can be provided by introducing the combustion furnace exhaust gas exiting the heat exchanger to a waste heat recovery boiler or a normal boiler.

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

【図1】本発明の実施の第1態様に係る発電設備の構成
を示す系統図。
FIG. 1 is a system diagram showing a configuration of a power generation facility according to a first embodiment of the present invention.

【図2】本発明の実施の第2態様に係る発電設備の構成
を示す系統図。
FIG. 2 is a system diagram showing a configuration of a power generation facility according to a second embodiment of the present invention.

【図3】本発明の実施の第3態様に係る発電設備の構成
を示す系統図。
FIG. 3 is a system diagram showing a configuration of a power generation facility according to a third embodiment of the present invention.

【図4】従来の石炭、重質油ガス化複合発電設備の構成
を示す系統図。
FIG. 4 is a system diagram showing a configuration of a conventional combined power plant for coal and heavy oil gasification.

【符号の説明】[Explanation of symbols]

1 セラミックス熱交換器 2 燃焼炉 3 ガスタービン圧縮機 4 ガスタービン膨張機 5 発電機 6 空気(圧縮機入口) 7 空気(圧縮機出口) 8 空気(熱交出口) 9 空気(膨張機出口) 10 燃料 11 燃焼炉排ガス(熱交換器入口) 12 燃焼炉排ガス(熱交換器出口) 13 排熱回収ボイラ 14 蒸気 15 蒸気タービン 16 排煙処理設備 17 煙突 18 過剰空気バイパス 19 燃料 21 ダンパ 22 ボイラ Reference Signs List 1 ceramic heat exchanger 2 combustion furnace 3 gas turbine compressor 4 gas turbine expander 5 generator 6 air (compressor inlet) 7 air (compressor outlet) 8 air (heat exchange outlet) 9 air (expander outlet) 10 Fuel 11 Combustion furnace exhaust gas (heat exchanger inlet) 12 Combustion furnace exhaust gas (heat exchanger outlet) 13 Waste heat recovery boiler 14 Steam 15 Steam turbine 16 Smoke exhaust treatment equipment 17 Chimney 18 Excess air bypass 19 Fuel 21 Damper 22 Boiler

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 空気圧縮機と、同空気圧縮機と同軸で回
転する空気膨張機および発電機と、燃焼炉と、熱交換器
とを備え、前記空気圧縮機の出口空気を前記熱交換器で
加熱して前記空気膨張機へ送給するとともに、同空気膨
張機の出口空気と燃料とを前記燃焼炉に送給して燃焼さ
せ、同燃焼炉の排ガスを前記熱交換器へ送給して前記空
気圧縮機の出口空気と熱交換させるように構成したこと
を特徴とする発電設備。
An air compressor, an air expander and a generator rotating coaxially with the air compressor, a combustion furnace, and a heat exchanger, wherein the outlet air of the air compressor is supplied to the heat exchanger. While heating in and sending to the air expander, outlet air and fuel of the air expander are sent to the combustion furnace for combustion, and the exhaust gas of the combustion furnace is sent to the heat exchanger. Characterized in that it is configured to exchange heat with outlet air of the air compressor.
【請求項2】 前記熱交換器の出口排ガスを排熱回収ボ
イラに送給して生成蒸気により発電する、蒸気発電サイ
クルを併設したことを特徴とする請求項1に記載の発電
設備。
2. The power generation equipment according to claim 1, further comprising a steam power generation cycle for feeding exhaust gas from the outlet of the heat exchanger to an exhaust heat recovery boiler to generate power using generated steam.
【請求項3】 前記空気膨張機の出口空気の一部を前記
燃焼炉をバイパスさせて前記排熱回収ボイラに送給する
ように構成したことを特徴とする請求項2に記載の発電
設備。
3. The power generation equipment according to claim 2, wherein a part of outlet air of the air expander is supplied to the exhaust heat recovery boiler by bypassing the combustion furnace.
【請求項4】 前記排熱回収ボイラに替えて燃料を燃焼
させるボイラを設置したことを特徴とする請求項3に記
載の発電設備。
4. The power generation equipment according to claim 3, wherein a boiler for burning fuel is installed in place of the exhaust heat recovery boiler.
JP19113297A 1997-07-16 1997-07-16 Power generation equipment Expired - Fee Related JP3782552B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP19113297A JP3782552B2 (en) 1997-07-16 1997-07-16 Power generation equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP19113297A JP3782552B2 (en) 1997-07-16 1997-07-16 Power generation equipment

Publications (2)

Publication Number Publication Date
JPH1136817A true JPH1136817A (en) 1999-02-09
JP3782552B2 JP3782552B2 (en) 2006-06-07

Family

ID=16269421

Family Applications (1)

Application Number Title Priority Date Filing Date
JP19113297A Expired - Fee Related JP3782552B2 (en) 1997-07-16 1997-07-16 Power generation equipment

Country Status (1)

Country Link
JP (1) JP3782552B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002156163A (en) * 2000-11-16 2002-05-31 Mitsubishi Heavy Ind Ltd Air conditioner
WO2012114367A1 (en) * 2011-02-21 2012-08-30 株式会社 日立製作所 Gas turbine system utilizing solar heat

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002156163A (en) * 2000-11-16 2002-05-31 Mitsubishi Heavy Ind Ltd Air conditioner
WO2012114367A1 (en) * 2011-02-21 2012-08-30 株式会社 日立製作所 Gas turbine system utilizing solar heat
JPWO2012114367A1 (en) * 2011-02-21 2014-07-07 株式会社日立製作所 Solar-powered gas turbine system

Also Published As

Publication number Publication date
JP3782552B2 (en) 2006-06-07

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