JPH03100332A - Apparatus and method for generating electric power - Google Patents

Apparatus and method for generating electric power

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Publication number
JPH03100332A
JPH03100332A JP23587889A JP23587889A JPH03100332A JP H03100332 A JPH03100332 A JP H03100332A JP 23587889 A JP23587889 A JP 23587889A JP 23587889 A JP23587889 A JP 23587889A JP H03100332 A JPH03100332 A JP H03100332A
Authority
JP
Japan
Prior art keywords
hydrogen
turbine
heat exchanger
generator
gas generator
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
JP23587889A
Other languages
Japanese (ja)
Inventor
George A Coffinberry
ジョージ・アルバート・コフィンベリィ
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.)
General Electric Co
Original Assignee
General Electric Co
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 General Electric Co filed Critical General Electric Co
Priority to JP23587889A priority Critical patent/JPH03100332A/en
Publication of JPH03100332A publication Critical patent/JPH03100332A/en
Pending legal-status Critical Current

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Abstract

PURPOSE: To prevent the discharge of water into space by providing a gas generator for burning hydrogen and oxygen, a turbine generator, a hydrogen transporting means for feeding hydrogen to the gas generator and to a gas turbine and an oxygen transporting means for feeding oxygen to the gas generator. CONSTITUTION: A generator 10 includes a gas generator 12 for burning hydrogen and oxygen to produce hot exhaust gas containing steam. It also includes a turbine generator 14 having a turbine 16 for creating electricity by the rotation of the generator 18. The turbine 16 is driven with hydrogen heated by heat exchange with exhaust gas of the generator 12 in a second heat exchanger 20. Almost all steam in the exhaust gas is condensed into water by a condenser 22 and cooled by heat exchange with oxygen transported to the generator 12 in a first heat exchanger 23. At least part of water is driven by a turbo pump 24 and used to cool the generator 12, and unused (remaining) water 25 is fed through an entrance pressure control valve 26 to a reservoir 28.

Description

【発明の詳細な説明】 この発明は一般に発電に関し、特に宇宙環境での発電装
置および方法に関する。
DETAILED DESCRIPTION OF THE INVENTION This invention relates generally to power generation, and more particularly to power generation apparatus and methods in a space environment.

発明の背景 (ロケット、宇宙ステーション、衛星などを含む)宇宙
船用に発電を行なうことのできる現存の装置は成る用途
によっては不適当なことがある。
BACKGROUND OF THE INVENTION Existing devices capable of generating electricity for spacecraft (including rockets, space stations, satellites, etc.) may be unsuitable for some applications.

電池や太陽エネルギー装置は寸法および重量を大きくし
ない限り大量(即ち約1kW以上)の電気を供給できな
い。ガス発生機で駆動するタービン発電機で電気を発電
すると必ず水を宇宙空間に排出することになる。
Batteries and solar energy devices cannot provide large amounts of electricity (ie, more than about 1 kW) without increasing their size and weight. When electricity is generated using a turbine generator driven by a gas generator, water is inevitably ejected into space.

将来の宇宙空間での活動では、宇宙空間に水を排出する
ことなく大量の電気を供給できる発電装置が必要になる
と予4pjされている。たとえば、地球軌道の宇宙ステ
ーションでの無重力での製作活動には大量の電気を必要
とするが、宇宙ステーションの発電装置の副生物として
水が宇宙空間に放出されると、宇宙ステーションに搭載
した天候監視カメラの性能が劣化するおそれがある。
It is predicted that future activities in outer space will require power generation devices that can supply large amounts of electricity without emitting water into outer space. For example, production activities in zero gravity on a space station in Earth orbit require large amounts of electricity, but when water is released into space as a byproduct of the space station's power generating equipment, The performance of the surveillance camera may deteriorate.

発明の要旨 この発明の目的は宇宙環境で大量の電気を発電する装置
および方法を提供することにある。
SUMMARY OF THE INVENTION It is an object of this invention to provide an apparatus and method for generating large amounts of electricity in a space environment.

この発明の別の目的は原子力の代替手段の形式で電気を
発電することにある。
Another object of the invention is to generate electricity in the form of an alternative to nuclear power.

この発明の他の目的は宇宙空間に水を放出せずに電気を
得ることにある。
Another object of this invention is to obtain electricity without releasing water into space.

第1の態様によれば、この発明の発電装置は、水素と酸
素とを燃焼させるガス発生機と、タービン発電機と、水
素をガス発生機の入口領域に送るとともに、水素をター
ビン発電機のタービンに送る水素輸送手段と、酸素をガ
ス発生機の入口領域に送る酸素輸送手段とを備える。こ
の装置は、ガス発生機の高熱の(蒸気を含む)ガス排気
とタービン発電機のタービンに送られる水素との間で熱
を交換する機構も含む。この装置はさらに、排気をター
ビンへ送られる水素と熱交換した後排気の蒸気の略全て
を水に凝縮する手段を含む。この装置はさらに、凝縮水
の少なくとも一部をガス発生機の燃焼領域に送り、凝縮
水の残りを貯蔵する手段を含む。
According to a first aspect, the power generation device of the present invention includes a gas generator that burns hydrogen and oxygen, a turbine generator, and a turbine generator that sends hydrogen to an inlet area of the gas generator. A means for transporting hydrogen to the turbine and a means for transporting oxygen to the inlet region of the gas generator are provided. The device also includes a mechanism for exchanging heat between the hot (steam-containing) gas exhaust of the gas generator and the hydrogen that is sent to the turbine of the turbine generator. The apparatus further includes means for condensing substantially all of the exhaust steam into water after exchanging heat with the exhaust gas with hydrogen that is directed to the turbine. The apparatus further includes means for delivering at least a portion of the condensate to the combustion zone of the gas generator and storing the remainder of the condensate.

別の態様によれば、この発明の発電装置は、水素と酸素
を燃焼させるガス発生機と、タービン発電機と、復水器
と、熱交換器と、槽と、輸送手段とを備える。輸送手段
は、酸素をガス発生機の入口領域に送る輸送手段と、水
素を復水器に送る輸送手段とを含む。輸送手段はさらに
、水素を復水器とガス発生機の入口領域間、復水器と熱
交換器間、そして熱交換器とタービン発電機のタービン
間で移送する水素輸送手段を含む。輸送手段はさらに、
排気をガス発生機の排気出口と熱交換器間、熱交換器と
復水器間、復水器とガス発生機の燃焼領域間、そして復
水器と検量で移送する排気輸送手段を含む。
According to another aspect, the power generation device of the present invention includes a gas generator that burns hydrogen and oxygen, a turbine generator, a condenser, a heat exchanger, a tank, and a transportation means. The transport means includes a transport means for delivering oxygen to the inlet area of the gas generator and a transport means for transporting hydrogen to the condenser. The transport means further includes a hydrogen transport means for transporting hydrogen between the condenser and the inlet region of the gas generator, between the condenser and the heat exchanger, and between the heat exchanger and the turbine of the turbine generator. In addition, the means of transportation
It includes an exhaust transport means for transporting the exhaust gas between the gas generator exhaust outlet and the heat exchanger, between the heat exchanger and the condenser, between the condenser and the combustion area of the gas generator, and between the condenser and the metering.

更に別の態様によれば、この発明の発電装置は、水素と
酸素を燃焼させるガス発生機と、タービン発電機と、復
水器と、第1及び第2熱交換器と、槽と、輸送手段とを
備える。輸送手段は、酸素を第1熱交換器に送る手段と
、水素を復水器に送る手段とを含む。輸送手段はさらに
、水素を復水器とガス発生機の入口領域間、復水器と第
2熱交換器間、そして第2熱交換器とタービン発電機の
タービン間で移送する水素輸送手段を含む。輸送手段は
更に、酸素を第1熱交換器とガス発生機の入口領域間で
移送する酸素輸送手段を含む。輸送手段はそのほかに、
排気をガス発生機の排気出口と第2熱交換器間、第2熱
交換器と復水器間、復水器と第1熱交換器間、第1熱交
換器とガス発生機の燃焼領域間、そして第1熱交換器と
検量で移送する排気輸送手段を含む。
According to yet another aspect, the power generation device of the present invention includes a gas generator that burns hydrogen and oxygen, a turbine generator, a condenser, first and second heat exchangers, a tank, and a transporter. and means. The transport means includes means for transporting oxygen to the first heat exchanger and means for transporting hydrogen to the condenser. The transport means further includes a hydrogen transport means for transporting hydrogen between the condenser and the inlet region of the gas generator, between the condenser and the second heat exchanger, and between the second heat exchanger and the turbine of the turbine generator. include. The transport means further includes an oxygen transport means for transporting oxygen between the first heat exchanger and the inlet region of the gas generator. In addition, the means of transportation are
The exhaust gas is routed between the exhaust outlet of the gas generator and the second heat exchanger, between the second heat exchanger and the condenser, between the condenser and the first heat exchanger, and between the first heat exchanger and the combustion area of the gas generator. and an exhaust conveying means for calibrating the exhaust gas between the first heat exchanger and the first heat exchanger.

更に別の態様では、本発明の発電方法によれば、水素と
酸素をガス発生機の入口領域に送ってガス発生機の排気
出口から蒸気を含む高熱排気ガスを生成し、水素をター
ビン発電機のタービンに送る。
In yet another aspect, the power generation method of the present invention provides hydrogen and oxygen to the inlet region of the gas generator to produce hot exhaust gas containing steam from the exhaust outlet of the gas generator, and the hydrogen to the turbine generator. turbine.

さらに、ガス発生機の排気とタービン発電機のタービン
に送られる水素との間で熱を交換し、上記排気がタービ
ン発電機のタービンへ送られる水素と熱交換した後排気
から全ての蒸気を水に凝縮する。さらに、凝縮水の少な
くとも一部を上記ガス発生機の燃焼領域に送り、そして
凝縮水の残りを貯蔵する。
Furthermore, heat is exchanged between the exhaust gas of the gas generator and the hydrogen sent to the turbine of the turbine generator, and after the exhaust gas exchanges heat with the hydrogen sent to the turbine of the turbine generator, all the steam is removed from the exhaust gas into water. condensed into. Furthermore, at least a portion of the condensed water is sent to the combustion zone of the gas generator and the remainder of the condensed water is stored.

更に別の態様では、本願発明の発電方法は上の段落に記
載した態様と同じであるが、水素と酸素をガス発生機の
入口領域に送ってガス発生機の排気出口から蒸気を含む
高熱排気ガスを生成する工程の代りに、水素と酸素の化
学量論的混合物をガス発生機の入口領域に送ってガス発
生機の排気出口から蒸気排気を生成する。
In yet another embodiment, the power generation method of the present invention is the same as the embodiment described in the paragraph above, but with hydrogen and oxygen being directed into the inlet region of the gas generator and hot exhaust gas containing steam from the exhaust outlet of the gas generator. As an alternative to the step of producing gas, a stoichiometric mixture of hydrogen and oxygen is sent to the inlet region of the gas generator to produce steam exhaust from the gas generator's exhaust outlet.

この発明にはたくさんの効果と利点がある。タービン発
電機を用いることから、大量の電気が得られる。ガス発
生機を用いることから、原子力エネルギーの代替手段が
得られる。閉じた水サイクルでの運転であるので宇宙空
間への水の放出を回避できる。化学量論的水素−酸素混
合物を用いると燃料利用効率がよい。ガス発生機に水を
注入してガス発生機を冷却することができる。
This invention has many effects and advantages. A large amount of electricity can be obtained by using a turbine generator. The use of gas generators provides an alternative to nuclear energy. Since it operates in a closed water cycle, the release of water into space can be avoided. The use of stoichiometric hydrogen-oxygen mixtures provides good fuel utilization efficiency. Water can be injected into the gas generator to cool it.

具体的な構成 第1図に示すように、この発明の発電装置10は、水素
と酸素を燃焼させて蒸気を含む(好ましくは蒸気のみの
)高熱排気ガスを生成するガス発生機12を備える。簡
単に説明すると、この装置10は、発電機18を回転し
て電気をつくり出すタービン16を有するタービン発電
機14も含む。
Specific Configuration As shown in FIG. 1, a power generation device 10 of the present invention includes a gas generator 12 that burns hydrogen and oxygen to generate high-temperature exhaust gas containing steam (preferably only steam). Briefly, the apparatus 10 also includes a turbine generator 14 having a turbine 16 that rotates a generator 18 to produce electricity.

タービン16は、従来の装置で行なわれているようにガ
ス発生機12からの排気により駆動されるのではない。
Turbine 16 is not driven by exhaust gas from gas generator 12 as is done in conventional systems.

その代りに、第2熱交換器20でガス発生機の排気との
熱交換により加熱された水素によってタービン16は駆
動される。排気中の水蒸気の略全てを復水器22で水に
凝縮し、さらに第1熱交換器23でガス発生機12に運
ばれる酸素との熱交換により冷却する。この水の少なく
とも一部をターボポンプ24で駆動し、ガス発生機12
の冷却に用い、未使用の(残りの)水25を入口圧力調
整弁26を通して貯水槽28に送る。
Instead, the turbine 16 is driven by hydrogen heated by heat exchange with the exhaust gas of the gas generator in the second heat exchanger 20. Almost all of the water vapor in the exhaust gas is condensed into water in the condenser 22, and further cooled by heat exchange with oxygen carried to the gas generator 12 in the first heat exchanger 23. At least a portion of this water is driven by the turbo pump 24 and the gas generator 12
The unused (remaining) water 25 is sent to a water storage tank 28 through an inlet pressure regulating valve 26.

この装置は、さらに、(液体および/または気体を含む
)水素の輸送手段50a〜50e、(液体および/また
は気体を含む)酸素の輸送手段48a〜48b1および
(蒸気、飽和蒸気および/または水を含む)排気の輸送
手段60a〜60gを含む。このような輸送手段は、当
業者によく知られているように、バイブ(又は他の導管
)、マニホールド、ダクト、弁、その他の水素、酸素ま
たは排気を輸送するための部材から構成するのが好まし
い。また、前述した熱交換器および復水器はそれぞれ熱
を交換する手段および水に凝縮する手段であり、2つの
物質量での熱交換が物理的混合を伴なわない任意の形式
の熱交換器でよく、たとえば密な多重管を2組有する装
置、第1の物質が流れるハウジング内に第2の物質が通
る多重管が通過する装置などがある。
The device further comprises means for transporting hydrogen (including liquid and/or gas) 50a-50e, transport means for oxygen (including liquid and/or gas) 48a-48b1 and (steam, saturated steam and/or water). (including) exhaust transportation means 60a to 60g. Such vehicles may consist of vibrators (or other conduits), manifolds, ducts, valves, and other components for transporting hydrogen, oxygen, or exhaust air, as is well known to those skilled in the art. preferable. In addition, the heat exchanger and condenser described above are means for exchanging heat and means for condensing into water, respectively, and any type of heat exchanger in which heat exchange between two quantities of substances does not involve physical mixing. For example, there may be a device having two sets of close multiple tubes, or a device in which a multiple tube through which a second substance flows passes through a housing through which a first substance flows.

水素と酸素とを燃焼させるガス発生機12は、第2図に
詳細に示すように、大体ベル形の多孔質内壁36の内部
に、(水素および酸素を受は取る)入口領域30、(水
素および酸素を点火するとともに冷却水を受は取る)燃
焼領域32および排気出口34を含む。内壁36は大体
ベル形の不透過性外壁38で囲まれて、相互間に大体ベ
ル形のチャンネル40を画定する。この構造は、当業者
に従来の水素/酸素ロケットエンジンの代表的なものと
して知られている。従来のロケットエンジンでは水素を
チャンネルに導くことによりロケットエンジンを冷却し
、その後その水素を多孔質内壁に透過させているが、こ
の発明では、水を外壁38の水入口42からチャンネル
40に噴射することによりガス発生機12を冷却し、そ
の換水を多孔質内壁36から燃焼領域32へ透過させる
。内部に酸素入口管46が同心配置され固定された水素
入口管44が、ガス発生機12の内壁36および外壁3
8の両方を入口領域30付近で貫通している。水素およ
び酸素を燃焼領域32内で通常の点火手段(点火手段は
この発明を構成する要素ではないので図示せず)で点火
し、蒸気を含む高熱の排気ガスを生成する。水素および
酸素を化学量論的な比で供給するときには、蒸気しか生
成しない。
Gas generator 12 for combusting hydrogen and oxygen includes an inlet area 30 (for receiving and taking hydrogen and oxygen), an inlet area 30 (for receiving and taking hydrogen and and a combustion zone 32 (for igniting oxygen and receiving cooling water) and an exhaust outlet 34. Inner wall 36 is surrounded by a generally bell-shaped impermeable outer wall 38 to define a generally bell-shaped channel 40 therebetween. This structure is known to those skilled in the art as typical of conventional hydrogen/oxygen rocket engines. While conventional rocket engines cool the rocket engine by introducing hydrogen into the channels and then permeating the hydrogen through the porous inner wall, in the present invention water is injected into the channels 40 from the water inlet 42 in the outer wall 38. This cools the gas generator 12 and allows its exchange water to permeate through the porous inner wall 36 into the combustion zone 32 . A hydrogen inlet pipe 44 in which an oxygen inlet pipe 46 is concentrically arranged and fixed is connected to the inner wall 36 and the outer wall 3 of the gas generator 12.
8 near the entrance area 30. Hydrogen and oxygen are ignited within combustion zone 32 by conventional ignition means (ignition means are not part of this invention and are not shown) to produce hot exhaust gas containing steam. When hydrogen and oxygen are supplied in stoichiometric ratios, only steam is produced.

輸送手段48aは酸素を第1熱交換器23に運ぶための
ものである。酸素は、代表的なロケットエンジンで見ら
れるように、加圧された低温の液体酸素の形態とするの
が好ましい。酸素は加圧された酸素ガスとして第1熱交
換′523を田て、輸送手段48bは酸素を第1熱交換
器23からガス発生機12の入口領域の間を運ぶ。
The transport means 48a is for transporting oxygen to the first heat exchanger 23. Preferably, the oxygen is in the form of pressurized, cold liquid oxygen, as found in typical rocket engines. The oxygen passes through the first heat exchange '523 as pressurized oxygen gas, and the transport means 48b transports the oxygen between the first heat exchanger 23 and the inlet area of the gas generator 12.

輸送手段50aは水素を復水器22に運ぶためのもので
ある。水素は当業者であれば実現できる加圧された低温
のガスの形態とするのが好ましい。
The transportation means 50a is for transporting hydrogen to the condenser 22. Preferably, the hydrogen is in the form of a pressurized, cold gas, which can be realized by those skilled in the art.

水素はより高圧に加圧された暖かいガスとして復水器2
2を出て、輸送手段50bは水素を復水器22からガス
発生機12の入口領域の間を運ぶ。
Hydrogen is transferred to condenser 2 as warm gas pressurized to a higher pressure.
2, the transport means 50b transports the hydrogen between the condenser 22 and the inlet area of the gas generator 12.

ガス発生機を始動するには、ロケットエンジン技術でよ
く知られているように、追加の弁および配管により水素
および酸素をトーチ点火装置(全て図示せず)に導く。
To start the gas generator, additional valves and piping direct hydrogen and oxygen to a torch igniter (all not shown), as is well known in rocket engine technology.

輸送手段50cは水素を復水器22から第2熱交換器2
0に運ぶためのものである。水素は高圧に加圧された高
メジlのガスとして第2熱交換器20を出て、輸送手段
50dは水素を第2熱交換器20からタービン16の間
を運び、こうしてタービン発電機14を駆動して電気を
発生する。このような輸送手段50dは、第2熱交換器
20から2つの弁54および56に分岐する管52とし
、方の弁54を管58によりタービン16に接続し、第
2の弁56を(59aで)宇宙空間に排気する構成とす
るのが好ましい。タービン16から出てくる使用済み水
素も59bで宇宙空間に排気する。
The transportation means 50c transports hydrogen from the condenser 22 to the second heat exchanger 2.
This is to bring it to 0. The hydrogen exits the second heat exchanger 20 as a highly pressurized, high-method gas, and the transport means 50d transports the hydrogen from the second heat exchanger 20 between the turbine 16 and the turbine generator 14. Drive to generate electricity. Such a transportation means 50d has a pipe 52 branching from the second heat exchanger 20 into two valves 54 and 56, one valve 54 is connected to the turbine 16 by a pipe 58, and the second valve 56 is connected to the turbine 16 (59a). ) It is preferable to have a configuration that exhausts the air into outer space. The used hydrogen coming out of the turbine 16 is also exhausted into space at 59b.

輸送手段60a、60bおよび60cは、ガス発生機の
排気を排気出口34から第2熱交換器20へ、第2熱交
換器20から復水器22へ、そして復水器22から第1
熱交換器23へ運ぶためのものである。第2熱交換器2
0に入るときには全て蒸気である排気は、第2熱交換器
20を出たり、復水器22に入る時には飽和水蒸気、そ
して復水器22を出たり第1熱交換″ri23に入る時
には熱湯であるのが好ましい。
The transport means 60a, 60b and 60c transport the exhaust gas of the gas generator from the exhaust outlet 34 to the second heat exchanger 20, from the second heat exchanger 20 to the condenser 22, and from the condenser 22 to the first
It is for conveying to the heat exchanger 23. Second heat exchanger 2
The exhaust gas, which is all steam when it enters zero, is saturated steam when it exits the second heat exchanger 20 and enters the condenser 22, and hot water when it exits the condenser 22 and enters the first heat exchanger RI23. It is preferable to have one.

輸送手段60dおよび60eは低温の水排出物を第1熱
交換器23からターボポンプ24のポンプ部分62へ、
そしてターボポンプ24からガス発生機12の燃焼領域
へ運ぶためのものである。
The transport means 60d and 60e transport the cold water effluent from the first heat exchanger 23 to the pump section 62 of the turbo pump 24;
The gas is then transported from the turbo pump 24 to the combustion region of the gas generator 12.

ターボポンプ24を駆動するために、水素を復水器22
からターボポンプ24のタービン部分64へ運ぶための
輸送手段50eが設けられている。
Hydrogen is transferred to the condenser 22 to drive the turbo pump 24.
A transport means 50e is provided for transporting the fuel from the turbo pump 24 to the turbine section 64 of the turbo pump 24.

タービン64から出てくる使用済の水素は(65で)宇
宙空間に排出される。輸送手段60fおよび60gは、
低温の水排出物を第1熱交換器23から貯水槽28の入
口圧力調節弁26へ、そして入口圧力調節弁26から貯
水槽28へ運ぶためのものである。入口圧力調節弁26
の設定により、排出水のどの程度の部分を貯水槽28に
送り、どの程度の部分をガス発生機12の燃焼領域に噴
射するかが決まる。
The spent hydrogen exiting the turbine 64 is discharged (at 65) into space. The transportation means 60f and 60g are
It is for conveying the cold water effluent from the first heat exchanger 23 to the inlet pressure regulating valve 26 of the water tank 28 and from the inlet pressure regulating valve 26 to the water tank 28 . Inlet pressure control valve 26
The setting determines how much of the waste water is sent to the water storage tank 28 and how much of the waste water is injected into the combustion region of the gas generator 12.

この発明の発電方法では、水素および酸素をガス発生機
12の入口領域30に輸送し、ガス発生機12の排気出
口34から蒸気を含む高熱排気ガスを生成する。この方
法ではほかに、水素をタービン発電機14のタービン1
6に運び、排気とタービン16に運ばれる水素との間で
熱を交換する。
In the power generation method of the present invention, hydrogen and oxygen are transported to the inlet region 30 of the gas generator 12, and high-temperature exhaust gas containing steam is produced from the exhaust outlet 34 of the gas generator 12. In addition, in this method, hydrogen is transferred to the turbine 1 of the turbine generator 14.
6 to exchange heat between the exhaust gas and the hydrogen transported to turbine 16.

さらに、排気がタービン16へ運ばれる水素と熱交換を
終えたあとこの排気からの蒸気の略合てを水に凝縮し、
凝縮水の少なくとも一部をガス発生機12の燃焼領域3
2に運び、そして凝縮水の残りを貯蔵する。水素と酸素
との略化学口論的混合物をガス発生機12の入口領域3
oに供給して、ガス発生機の排気出口34がら略蒸気の
排気を生成するのか好ましい。
Furthermore, after the exhaust gas has completed heat exchange with the hydrogen carried to the turbine 16, substantially all of the steam from the exhaust gas is condensed into water;
At least a portion of the condensed water is transferred to the combustion zone 3 of the gas generator 12.
2 and store the remainder of the condensate. A substantially stoichiometric mixture of hydrogen and oxygen is introduced into the inlet region 3 of the gas generator 12.
Preferably, the gas is supplied to the gas generator to produce a substantially steam exhaust from the exhaust outlet 34 of the gas generator.

なお、排気中に第1熱交換器23の後でもガスが残るよ
うにこの発電装置を運転する場合には、適宜の設計とし
て、第1熱交換器23がらの全排気物を入口圧力調節弁
26および貯水槽28に輸送することかできる。その場
合、貯水槽28に、ガス分離器(主として蒸気からなる
排気に水素を生成するように装置を運転する場合には水
素分離器)およびガスを宇宙空間に排出する排気口を設
ける(ともに図示せず)。そして水を貯水槽28からタ
ーボポンプ24のポンプ部分62に運ぶ輸送手段(図示
せず)を設ける。この発明の発電装置の作用は当業者で
あれば以上の説明がら理解できるはずである。装置の制
御(水素および酸素の供給条件、入口圧力調節弁26の
設定、タービン発電機タービン16の水素入口弁54お
よびバイパス弁56の設定など)については説明しない
が、それはこの発明を構成する要素ではなく、そのよう
な1り御は当業者の通常の技術の範囲内で行なうことが
できる。
In addition, when operating this power generation device so that gas remains in the exhaust gas even after the first heat exchanger 23, as an appropriate design, all the exhaust gas from the first heat exchanger 23 is removed from the inlet pressure regulating valve. 26 and a water storage tank 28. In that case, the water storage tank 28 is provided with a gas separator (a hydrogen separator if the device is operated to generate hydrogen from exhaust gas mainly consisting of steam) and an exhaust port for discharging the gas into space (both shown in the figure). (not shown). A transport means (not shown) is then provided for conveying water from the reservoir 28 to the pump section 62 of the turbo pump 24. Those skilled in the art should be able to understand the operation of the power generation device of the present invention from the above explanation. Control of the device (hydrogen and oxygen supply conditions, settings of the inlet pressure control valve 26, settings of the hydrogen inlet valve 54 and bypass valve 56 of the turbine generator turbine 16, etc.) will not be described, but is an element constituting the present invention. Rather, such control is within the ordinary skill of those skilled in the art.

以−し、この発明のいくつかの好適な実施例を例示の目
的で説明した。これらは発明を記載した通りの形態に限
定しようとするものではなく、上述した教示に照らして
色々な変更や改変が可能である。
Several preferred embodiments of the invention have been described for purposes of illustration. It is not intended to be exhaustive or to limit the invention to the precise form described, and many modifications and variations are possible in light of the above teachings.

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

第1図はこの発明の発電装置の概略図、第2図は第1図
に示したガス発生機の縦断面図である。 主な符号の説明 10:発電装置、    12:ガス発生機、14:タ
ービン発電機、16:タービン、18:発電機、   
 20:第2熱交換器、22:復水器、    23:
第1熱交換器、:ターボポンプ、 :貯水槽、 :燃焼領域、 :内壁、 :外壁、 :水素入口管、 :酸素輸送手段、 54:管、 :排気輸送手段。 :圧力調節弁、 二人目領域、 :排気出口、 二チャンネル、 :水入口、 :酸素入口管、 :水素輸送手段、 56:弁
FIG. 1 is a schematic diagram of the power generating apparatus of the present invention, and FIG. 2 is a longitudinal sectional view of the gas generator shown in FIG. 1. Explanation of main symbols 10: Power generator, 12: Gas generator, 14: Turbine generator, 16: Turbine, 18: Generator,
20: Second heat exchanger, 22: Condenser, 23:
1st heat exchanger, :turbo pump, :water tank, :combustion area, :inner wall, :outer wall, :hydrogen inlet pipe, :oxygen transport means, 54:pipe, :exhaust transport means. :Pressure control valve, 2nd person area, :Exhaust outlet, 2 channels, :Water inlet, :Oxygen inlet pipe, :Hydrogen transport means, 56:Valve

Claims (1)

【特許請求の範囲】 1、(a)水素と酸素を燃焼させて、蒸気を含む高熱排
気ガスを生成するガス発生機であって、入口領域、燃焼
領域および排気出口を含むガス発生機と、 (b)タービンを有するタービン発電機と、 (c)水素を上記ガス発生機の入口領域に 送るとともに、水素を上記タービンに送る水素輸送手段
と、 (d)酸素を上記ガス発生機の入口領域に 送る酸素輸送手段と、 (e)上記排気と上記タービンへ送られる 水素との間で熱交換を行なう手段と (f)上記排気が上記タービンへ送られる 水素と熱交換した後上記排気からの蒸気の略全てを水に
凝縮する手段と、 (g)上記凝縮水の少なくとも一部を上記 ガス発生機の燃焼領域に送り、凝縮水の残りを貯蔵する
手段とを備える発電装置。 2、(a)水素と酸素を燃焼させて蒸気を含む高熱排気
ガスを生成するガス発生機であって、入口領域、燃焼領
域および排気出口を含むガス発生機と、 (b)酸素を上記ガス発生機の入口領域に 送る酸素輸送手段と、 (c)復水器と、 (d)水素を上記復水器に送る輸送手段と (e)熱交換器と、 (f)タービンを有するタービン発電機と、 (h)水素を上記復水器から上記ガス発生 機の入口領域に、上記復水器から上記熱交換器に、そし
て上記熱交換器から上記タービンに送る水素輸送手段と (i)槽と、 (j)上記排気を上記排気出口から上記熱 交換器に、上記熱交換器から上記復水器に、上記復水器
から上記ガス発生機の燃焼領域に、そして上記復水器か
ら上記槽に送る排気輸送手段とを備える発電装置。 3、(a)水素と酸素を燃焼させて蒸気を含む高熱排気
ガスを生成するガス発生機であって、入口領域、燃焼領
域および排気出口を含むガス発生機と、 (b)第1熱交換器と、 (c)酸素を上記第1熱交換器に送る酸素輸送手段と、 (d)復水器と、 (e)水素を上記復水器に送る輸送手段と、 (f)第2熱交換器と、 (g)タービンを有するタービン発電機と、 (h)水素を上記復水器から上記ガス発生機の入口領域
に、上記復水器から上記第2熱交換器に、そして上記第
2熱交換器から上記タービンに送る水素輸送手段と、 (i)酸素を上記第1熱交換器から上記ガス発生機の入
口領域に送る酸素輸送手段と、 (j)槽と、 (k)上記排気を上記排気出口から上記第 2熱交換器に、上記第2熱交換器から上記復水器に、上
記復水器から上記第1熱交換器に、上記第1熱交換器か
ら上記ガス発生機の燃焼領域に、そして上記第1熱交換
器から上記槽に送る排気輸送手段とを備える発電装置。 4、上記第1熱交換器と上記ガス発生機の燃焼領域との
間の上記排気輸送手段がターボポンプを含み、上記装置
がさらに水素を上記復水器から上記ターボポンプに送る
水素輸送手段を含む請求項3に記載の装置。 5、上記槽が入口圧力調節弁を含み、上記第1熱交換器
と上記槽との間の上記排気輸送手段が上記排気を上記第
1熱交換器から上記入口圧力調節弁に送る排気輸送手段
を含む請求項4に記載の装置。 6、(a)水素と酸素をガス発生機の入口領域に送って
ガス発生機の排気出口から蒸気を含む高熱排気ガスを生
成し、 (b)水素をタービン発電機のタービンに 送り、 (c)上記排気と上記タービンに送られる水素との間で
熱を交換し、 (d)上記排気が上記タービンへ送られる水素と熱交換
した後上記排気からの蒸気の略全てを水に凝縮し、 (e)上記凝縮水の少なくとも一部を上記ガス発生機の
燃焼領域に送り、そして (f)凝縮水の残りを貯蔵する 工程を含む発電方法。 7、(a)水素と酸素の略化学量論的混合物をガス発生
機の入口領域に送ってガス発生機の排気出口から略蒸気
からなる排気を生成し、 (b)水素をタービン発電機のタービンに送り、 (c)上記排気と上記タービンに送られる水素との間で
熱を交換し、 (d)上記蒸気排気が上記タービンへ送られる水素と熱
交換した後上記蒸気排気の略全てを水に凝縮し、 (e)上記凝縮水の少なくとも一部を上記 ガス発生機の燃焼領域に送り、そして (f)凝縮水の残りを貯蔵する 工程を含む発電方法。
[Claims] 1. (a) A gas generator for combusting hydrogen and oxygen to produce high-temperature exhaust gas containing steam, the gas generator including an inlet region, a combustion region, and an exhaust outlet; (b) a turbine generator having a turbine; (c) hydrogen transport means for delivering hydrogen to an inlet region of said gas generator and for delivering hydrogen to said turbine; and (d) hydrogen transport means for delivering oxygen to an inlet region of said gas generator. (e) means for heat exchange between said exhaust gas and hydrogen directed to said turbine; and (f) means for carrying out heat exchange between said exhaust gas and hydrogen directed to said turbine; A power generating apparatus comprising: means for condensing substantially all of the steam into water; and (g) means for delivering at least a portion of the condensed water to a combustion region of the gas generator and storing the remainder of the condensed water. 2. (a) A gas generator for combusting hydrogen and oxygen to produce high-temperature exhaust gas containing steam, the gas generator including an inlet region, a combustion region, and an exhaust outlet; (c) a condenser; (d) a means of transport for hydrogen to said condenser; (e) a heat exchanger; and (f) a turbine generator. (h) means for transporting hydrogen from the condenser to the inlet region of the gas generator, from the condenser to the heat exchanger, and from the heat exchanger to the turbine; (i) (j) directing the exhaust gas from the exhaust outlet to the heat exchanger, from the heat exchanger to the condenser, from the condenser to the combustion zone of the gas generator, and from the condenser to the combustion zone of the gas generator; and a means for transporting exhaust gas to the tank. 3. (a) a gas generator that burns hydrogen and oxygen to produce high-temperature exhaust gas containing steam, the gas generator including an inlet region, a combustion region, and an exhaust outlet; (b) a first heat exchanger; (c) an oxygen transport means for transporting oxygen to the first heat exchanger; (d) a condenser; (e) a transport means for transporting hydrogen to the condenser; (f) a second heat exchanger; (g) a turbine generator having a turbine; (h) transferring hydrogen from the condenser to the inlet region of the gas generator, from the condenser to the second heat exchanger, and (i) an oxygen transport means for transporting oxygen from the first heat exchanger to the inlet region of the gas generator; (j) a tank; (k) a tank; The exhaust gas is passed from the exhaust outlet to the second heat exchanger, from the second heat exchanger to the condenser, from the condenser to the first heat exchanger, and from the first heat exchanger to the gas generation. a combustion zone of the machine and an exhaust transport means for conveying exhaust gas from the first heat exchanger to the tank. 4. The exhaust transport means between the first heat exchanger and the combustion region of the gas generator includes a turbo pump, and the device further includes a hydrogen transport means for transporting hydrogen from the condenser to the turbo pump. 4. The apparatus of claim 3, comprising: 5. The tank includes an inlet pressure regulating valve, and the exhaust transport means between the first heat exchanger and the tank sends the exhaust gas from the first heat exchanger to the inlet pressure regulating valve. 5. The apparatus of claim 4. 6. (a) delivering hydrogen and oxygen to the inlet region of the gas generator to produce hot exhaust gas containing steam from the exhaust outlet of the gas generator; (b) delivering hydrogen to the turbine of the turbine generator; (c) ) exchanging heat between the exhaust gas and hydrogen directed to the turbine; (d) condensing substantially all of the steam from the exhaust gas into water after the exhaust gas exchanges heat with hydrogen directed to the turbine; (e) directing at least a portion of the condensed water to a combustion zone of the gas generator; and (f) storing the remainder of the condensed water. 7. (a) delivering a substantially stoichiometric mixture of hydrogen and oxygen to the inlet region of the gas generator to produce an exhaust consisting substantially of steam from the gas generator's exhaust outlet; and (b) directing the hydrogen to the turbine generator. (c) exchanging heat between the exhaust gas and hydrogen sent to the turbine; and (d) converting substantially all of the steam exhaust after heat exchange with the hydrogen sent to the turbine. (e) directing at least a portion of the condensed water to a combustion zone of the gas generator; and (f) storing the remainder of the condensed water.
JP23587889A 1989-09-13 1989-09-13 Apparatus and method for generating electric power Pending JPH03100332A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP23587889A JPH03100332A (en) 1989-09-13 1989-09-13 Apparatus and method for generating electric power

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP23587889A JPH03100332A (en) 1989-09-13 1989-09-13 Apparatus and method for generating electric power

Publications (1)

Publication Number Publication Date
JPH03100332A true JPH03100332A (en) 1991-04-25

Family

ID=16992583

Family Applications (1)

Application Number Title Priority Date Filing Date
JP23587889A Pending JPH03100332A (en) 1989-09-13 1989-09-13 Apparatus and method for generating electric power

Country Status (1)

Country Link
JP (1) JPH03100332A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2021092224A (en) * 2019-12-03 2021-06-17 寛治 泉 Engine burning hydrogen and oxygen and also producing hydrogen and oxygen

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2021092224A (en) * 2019-12-03 2021-06-17 寛治 泉 Engine burning hydrogen and oxygen and also producing hydrogen and oxygen

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