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JPH0744805B2 - Method for adjusting hydrogen pressure of hydrogen-cooled rotating electric machine - Google Patents
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JPH0744805B2 - Method for adjusting hydrogen pressure of hydrogen-cooled rotating electric machine - Google Patents

Method for adjusting hydrogen pressure of hydrogen-cooled rotating electric machine

Info

Publication number
JPH0744805B2
JPH0744805B2 JP60133416A JP13341685A JPH0744805B2 JP H0744805 B2 JPH0744805 B2 JP H0744805B2 JP 60133416 A JP60133416 A JP 60133416A JP 13341685 A JP13341685 A JP 13341685A JP H0744805 B2 JPH0744805 B2 JP H0744805B2
Authority
JP
Japan
Prior art keywords
hydrogen
pressure
hydrogen gas
machine
electric machine
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.)
Expired - Lifetime
Application number
JP60133416A
Other languages
Japanese (ja)
Other versions
JPS61293132A (en
Inventor
幹夫 熊谷
裕 渡辺
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.)
Toshiba Corp
Original Assignee
Toshiba Corp
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 Toshiba Corp filed Critical Toshiba Corp
Priority to JP60133416A priority Critical patent/JPH0744805B2/en
Publication of JPS61293132A publication Critical patent/JPS61293132A/en
Publication of JPH0744805B2 publication Critical patent/JPH0744805B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Description

【発明の詳細な説明】 〔発明の技術分野〕 本発明は水素冷却回転電機において、特に水素貯蔵合金
を用いて機内の水素ガス圧力を負荷変動に応じて調整可
能にした水素冷却回転電機の水素圧力調整方法に関す
る。
Description: TECHNICAL FIELD OF THE INVENTION The present invention relates to a hydrogen-cooled rotary electric machine, and more particularly to a hydrogen-cooled rotary electric machine in which the hydrogen gas pressure in the machine can be adjusted according to the load variation by using a hydrogen storage alloy. Regarding pressure adjustment method.

〔発明の技術的背景とその問題点〕[Technical background of the invention and its problems]

回転電機、例えばタービン発電機においてはその冷却媒
体として水素ガスを用いたものがある。この場合、機内
の水素ガスはタービン発電機の単機容量が上がるに従っ
てその熱容量、即ち(比重量)×(比熱)を増加して冷
却効果を上げる必要があり、特に大容量機では機内の水
素ガス圧力を例えば5.2atmにしているものもある。
Some rotating electrical machines, such as turbine generators, use hydrogen gas as a cooling medium. In this case, it is necessary to increase the heat capacity of the hydrogen gas inside the machine as the unit capacity of the turbine generator increases, that is, (specific weight) × (specific heat) to improve the cooling effect. Some have a pressure of, for example, 5.2 atm.

しかるに、近年タービン発電機の使用は多用化し、常に
100%負荷だけでなく部分負荷で使用されることがあ
る。この部分負荷時は発電機の電気損が少なく、冷却上
水素ガス圧を5.2atmのままにしておく必要がない。部分
負荷時に機内の水素ガス圧力を5.2atmのままにしておく
と、回転子の風損,ファン動力が100%負荷時と変わら
ないため、発電機の効率が低下する。そこで、このよう
な場合には機内の水素ガス圧力を下げることにより回転
子の風損,ファン動力が減少し、部分負荷時の発電機の
効率を向上させることができる。また、水素圧力を負荷
の如何にかかわらず、一定にしておくと、部分負荷時は
過冷却になり、負荷に応じたヒートサイクルが回転電機
構成部品、例えば絶縁物などにかかるが、負荷に応じて
水素圧力を変えると回転電機の温度が常に一定となり、
回転電機の寿命が増すメリットもある。
However, in recent years, the use of turbine generators has become more frequent and
It may be used at partial load as well as 100% load. During this partial load, there is little electric loss in the generator, and it is not necessary to keep the hydrogen gas pressure at 5.2 atm for cooling. If the hydrogen gas pressure inside the machine is kept at 5.2 atm during partial load, rotor windage loss and fan power will be the same as at 100% load, resulting in reduced generator efficiency. Therefore, in such a case, by lowering the hydrogen gas pressure inside the machine, windage of the rotor and fan power are reduced, and the efficiency of the generator under partial load can be improved. Also, if the hydrogen pressure is kept constant regardless of the load, it will be supercooled during partial load, and the heat cycle depending on the load will be applied to the rotating electrical machine components, such as insulators, but depending on the load. If the hydrogen pressure is changed by
There is also an advantage that the life of the rotating electric machine is increased.

そこで、従来では機内の水素ガスを負荷の変動に応じて
大気に放出したり、高圧の水素ガスボンベより再注入し
たりして回転電機の機内の水素ガス圧力を調整するよう
にしていた。しかしこの方式は水素ガスの注入や放出の
ための操作が繁雑であると共に水素ガスを取扱う上で安
全対策を十分に施しておく必要があり、また水素ガスの
消耗量が多大なものとなるため、エネルギーの有効利用
と言う観点から見ても問題がある。
Therefore, conventionally, the hydrogen gas pressure inside the machine has been adjusted by discharging the hydrogen gas inside the machine to the atmosphere according to the change in the load or by reinjecting it from a high-pressure hydrogen gas cylinder. However, in this method, the operations for injecting and releasing hydrogen gas are complicated, and it is necessary to take sufficient safety measures in handling hydrogen gas, and the consumption of hydrogen gas will be enormous. However, there is a problem from the viewpoint of effective use of energy.

また、かかる問題を解決するものとして、例えば実開昭
55−12720号公報に記載された発明のようにタービン発
電機の機内の水素ガス圧力を負荷の変動に応じて圧力調
整制御機構により調整できるようにしたものがある。
Moreover, as a means for solving such a problem, for example,
There is an invention in which the hydrogen gas pressure inside the turbine generator can be adjusted by a pressure adjustment control mechanism according to the fluctuation of the load, as in the invention described in Japanese Patent No. 55-12720.

第10図はこのような従来の水素冷却タービン発電機にお
ける水素ガス圧力調整系を示すものである。すなわち、
第10図に示すように外部負荷系統に接続されたタービン
発電機31において、その機内32には水素ガスボンベ33に
充填された水素ガスが圧力調整弁34を介して供給可能に
してあり、また機内の水素ガス圧力の調整制御系として
は機内に圧力調整弁35を介して連通するレリーフ水素リ
ザーブ室36、このリザーブ室36の容積を調整して機内32
の水素ガスを流出入させるピストン37、このピストン37
を駆動するピストン駆動機構38及びタービン発電機31の
出力により負荷の大きさを検出しその負荷変動に応じて
ピストン駆動機構38に駆動指令を与えると共に圧力調整
弁35に対しては開閉指令を与える負荷追従制御機構39か
ら構成されている。
FIG. 10 shows a hydrogen gas pressure adjusting system in such a conventional hydrogen-cooled turbine generator. That is,
In a turbine generator 31 connected to an external load system as shown in FIG. 10, hydrogen gas filled in a hydrogen gas cylinder 33 can be supplied to the inside 32 of the turbine generator 31 through a pressure adjusting valve 34, and As a control system for adjusting the hydrogen gas pressure of, the relief hydrogen reserve chamber 36 communicating with the inside of the aircraft through the pressure regulating valve 35, the volume of this reserve chamber 36 is adjusted and the inside of the aircraft 32
This piston 37 that allows the hydrogen gas of
The magnitude of the load is detected by the outputs of the piston drive mechanism 38 and the turbine generator 31 that drive the engine, and a drive command is given to the piston drive mechanism 38 according to the load fluctuation and an opening / closing command is given to the pressure regulating valve 35. It is composed of a load following control mechanism 39.

したがって、このような構成のタービン発電機の水素ガ
ス圧力調整系において、通常は圧力調整弁34によって水
素ガスボンベ33の圧力を減圧して一定になるように制御
され、また負荷変動がある時は負荷追従制御機構39から
の指令に基いてピストン37を駆動してリザーブ室36の容
積を調整すると共に圧力調整弁35の開度を制御すること
によりタービン発電機32の機内水素ガス圧力を負荷変動
に応じて調整することができる。
Therefore, in the hydrogen gas pressure adjusting system of the turbine generator having such a configuration, the pressure of the hydrogen gas cylinder 33 is normally controlled by the pressure adjusting valve 34 so that the pressure is controlled to be constant, and when the load fluctuates, the load is changed. Drive the piston 37 based on the command from the tracking control mechanism 39 to adjust the volume of the reserve chamber 36 and control the opening degree of the pressure adjustment valve 35 to change the hydrogen gas pressure in the turbine generator 32 to the load fluctuation. It can be adjusted accordingly.

しかし、かかるタービン発電機の水素ガス圧力調整系で
はリザーブ室36の容積をリザーブ室内周面を摺動するピ
ストン37より調整するようにしているため、このピスト
ン37とリザーブ室内周面との間のシールが十分なされて
いないと機内と連通している側の高圧状態にある水素ガ
スが大気状態にあるピストン背部側へリークして爆発に
つながる恐れがある。
However, in the hydrogen gas pressure adjusting system of such a turbine generator, the volume of the reserve chamber 36 is adjusted by the piston 37 that slides on the peripheral surface of the reserve chamber, so that the volume between the piston 37 and the peripheral surface of the reserve chamber is adjusted. If the seal is not sufficient, the high-pressure hydrogen gas on the side communicating with the inside of the machine may leak to the back side of the piston in the atmospheric state, leading to an explosion.

そこで、最近では前述したようなレリーフ水素リザーブ
室及びこのリザーブ室の容積を調整するピストン等の駆
動装置を用いずに機内の水素ガス圧力を簡便に、しかも
水素ガスの消耗をなくして調整可能な水素貯蔵合金の使
用が考えられている。
Therefore, recently, the hydrogen gas pressure in the machine can be easily adjusted without using the relief hydrogen reserve chamber and the drive device such as a piston for adjusting the volume of the reserve chamber as described above, and the consumption of hydrogen gas can be eliminated. The use of hydrogen storage alloys is being considered.

この水素貯蔵合金は水素を非常によく吸収する性質を有
するチタンやメッシュメタルなどの金属原子を組合わせ
たもので、温度を下げるか圧力を上げると水素ガスを吸
収して発熱し、逆に温度を上げるか圧力を下げると吸収
した水素ガスを放出して周囲から熱をうばう性質があ
り、また送込む水素ガスの圧力値によって合金自体の温
度も変化し、逆に合金自体の温度を変えることによって
発生する水素ガスの圧力も異なるという相関関係を有し
ているものである。
This hydrogen storage alloy is a combination of metal atoms such as titanium and mesh metal, which have the property of absorbing hydrogen very well.When the temperature is lowered or the pressure is raised, hydrogen gas is absorbed and heat is generated. If the temperature is raised or the pressure is lowered, the absorbed hydrogen gas is released and heat is absorbed from the surroundings.Also, the temperature of the alloy itself changes depending on the pressure value of the hydrogen gas sent in, and conversely the temperature of the alloy itself is changed. There is a correlation that the pressure of hydrogen gas generated by is also different.

第7図は水素貯蔵合金の特性例を示すものである。すな
わち、水素貯蔵合金の特性は第7図に示すように中央に
ほぼ平坦部を持つ右上がりの特性で、この特性の左側の
右上がり部分は水素貯蔵合金の結晶隙間に水素原子が入
る水素の固溶段階、中央の平坦部は水素化反応による金
属水素化物の形成段階、特性右側の右上がり部分はすべ
ての金属が水素化してさらに格子間に水素が過飽和に入
る過飽和固溶段階である。
FIG. 7 shows a characteristic example of a hydrogen storage alloy. That is, as shown in Fig. 7, the characteristics of the hydrogen storage alloy are upward-sloping characteristics with a substantially flat portion in the center. The upward-sloping portion on the left side of this characteristic is the hydrogen The solid solution stage, the flat part in the center is the stage of forming metal hydride by hydrogenation reaction, and the rising part on the right side of the characteristic is the supersaturated solid solution stage in which all the metals are hydrogenated and hydrogen is supersaturated between the lattices.

この中で最も水素を吸収するのは水素化合物形成段階
で、ほぼ一定の圧力で反応が進ことからこの部分を平衡
部と言い、その圧力を平衡圧力と言う。この平衡圧力は
水素貯蔵合金の温度によって異なり、また水素貯蔵合金
の種類によっても異なる。この平衡圧力と温度の関係の
一例を示すと第8図の通りである。
Of these, hydrogen is most absorbed in the hydrogen compound formation stage, and since the reaction proceeds at a substantially constant pressure, this portion is called an equilibrium portion, and that pressure is called an equilibrium pressure. This equilibrium pressure depends on the temperature of the hydrogen storage alloy and also on the type of hydrogen storage alloy. An example of the relationship between the equilibrium pressure and the temperature is shown in FIG.

このような特性を有する水素貯蔵合金を密閉容器内に入
れて加熱冷却すると、容器内の水素ガス圧力は次式のよ
うに変化する。
When a hydrogen storage alloy having such characteristics is placed in a closed container and heated and cooled, the hydrogen gas pressure in the container changes as shown in the following equation.

容器の容積をV(m3),容器内の初期圧力P0(Kg/c
m2),水素貯蔵合金の水素含有能力k(m3/Kg大気圧換
算)とし、水素ガスを吸収、放出のために十分な冷却、
加熱を行なうと容器内の圧力Pは P=P0±KM/V ここで、+は放出、−は吸収の場合を示す。
The volume of the container is V (m 3 ), the initial pressure in the container P 0 (Kg / c
m 2 ), hydrogen content capacity of hydrogen storage alloy k (m 3 / Kg atmospheric pressure conversion), sufficient cooling to absorb and release hydrogen gas,
When heating is performed, the pressure P in the container is P = P 0 ± KM / V, where + indicates release and − indicates absorption.

以上述べたような水素貯蔵合金の特性を利用すれば静止
形にして回転電機内の水素圧力を調整することができる
が、この場合水素貯蔵合金を加熱、冷却する必要があ
る。この水素貯蔵合金を加熱、冷却するにあたっては、
できれば回転電機で用いられている冷却媒体の排熱を利
用することが可能であればエネルギ的には有利である。
By utilizing the characteristics of the hydrogen storage alloy as described above, the hydrogen pressure in the rotating electric machine can be adjusted to a stationary type, but in this case, it is necessary to heat and cool the hydrogen storage alloy. In heating and cooling this hydrogen storage alloy,
If possible, it is advantageous in terms of energy if the exhaust heat of the cooling medium used in the rotating electric machine can be utilized.

そこで、回転電機の負荷が大きい時は水素貯蔵合金を加
熱して水素ガスを放出させることにより機内圧力を高
め、また負荷が減った時は水素貯蔵合金を冷却して水素
ガスを吸着させることにより機内圧力を低下すれば良い
が、その場合負荷の変動に応じて温度変化する回転電機
の冷却媒体である固定子巻線冷却水を用いることが考え
られる。
Therefore, when the load on the rotating electrical machine is large, the hydrogen storage alloy is heated to release hydrogen gas to increase the internal pressure of the machine, and when the load is reduced, the hydrogen storage alloy is cooled to adsorb hydrogen gas. It suffices to reduce the internal pressure of the machine, but in that case, it is conceivable to use the stator winding cooling water which is the cooling medium of the rotating electric machine, the temperature of which changes according to the change of load.

一方、回転電機の負荷と水素ガス圧力の関係には許容圧
力というものがあり、負荷が減少した場合の電気損と減
圧された水素ガス冷却による回転電機の部材の温度上昇
が100%負荷時の温度上昇と同じであると言う条件から
許容水素ガス圧力が決定される。
On the other hand, there is an allowable pressure in the relationship between the load on the rotating electric machine and the hydrogen gas pressure.There is an electrical loss when the load decreases and the temperature rise of the member of the rotating electric machine due to reduced hydrogen gas cooling is 100% load. The allowable hydrogen gas pressure is determined from the condition that it is the same as the temperature rise.

したがって、水素貯蔵合金の加熱、冷却を回転電機の冷
却媒体の排熱を利用する場合には回転電機の負荷に対す
る許容水素圧力と負荷によって生じた冷却媒体の排熱温
度に対する水素貯蔵合金の水素平衡圧力が等しいと、そ
のまま排熱を利用して水素貯蔵合金を加熱,冷却すれ
ば、回転電機の負荷に応じた水素ガス圧力の調整を完全
に自動的に行なうことが可能である。
Therefore, when the exhaust heat of the cooling medium of the rotating electric machine is used for heating and cooling of the hydrogen storage alloy, the allowable hydrogen pressure for the load of the rotating electric machine and the hydrogen balance of the hydrogen storage alloy for the exhaust heat temperature of the cooling medium generated by the load. If the pressures are the same, the exhaust gas can be used as it is to heat and cool the hydrogen storage alloy to completely automatically adjust the hydrogen gas pressure according to the load of the rotating electric machine.

しかしながら、例えば固定子巻線冷却水の排熱を利用し
た場合、第9図に示すように水素貯蔵合金の特性
(a),(b),(c),(d)と負荷に対する排熱温
度と許容水素ガス圧力(A)の関係は一致していない。
また水素貯蔵合金は一般に粉末状で粒子と粒子との間に
水素ガスが存在し、熱伝導が固形状金属に比べて悪く、
冷却又は加熱してから水素貯蔵合金の水素平衡圧力にな
るまで、タイムラグがある。特に急激に負荷が上昇した
場合、水素ガス圧力の上昇遅れは回転電機の構成部材の
加熱につながるので、タイムラグは避けなければならな
い。
However, for example, when the exhaust heat of the stator winding cooling water is used, as shown in FIG. 9, the characteristics (a), (b), (c) and (d) of the hydrogen storage alloy and the exhaust heat temperature with respect to the load are used. And the allowable hydrogen gas pressure (A) do not match.
Further, the hydrogen storage alloy is generally powdery, and hydrogen gas is present between the particles, so that the heat conduction is worse than that of the solid metal,
There is a time lag from cooling or heating to the hydrogen equilibrium pressure of the hydrogen storage alloy. Especially when the load is rapidly increased, the delay in the increase of the hydrogen gas pressure leads to the heating of the components of the rotating electric machine, so a time lag must be avoided.

このように水素貯蔵合金を回転電機の水素ガス圧力調整
のために使用する場合には水素貯蔵合金の特性の不一致
とタイムラグが問題となる。
As described above, when the hydrogen storage alloy is used for adjusting the hydrogen gas pressure of the rotating electric machine, there are problems such as inconsistency in characteristics of the hydrogen storage alloy and time lag.

〔発明の目的〕[Object of the Invention]

本発明はこれらの問題を解決するためになされたもの
で、水素貯蔵合金の選択を容易にして冷却又は加熱して
から水素貯蔵合金が水素平衡圧力になるまでのタイムラ
グを少なくでき、負荷が急激に変化しても機内の水素ガ
スの圧力を速やかに調整することができる水素冷却回転
電機の水素圧力調整方法を提供することを目的とする。
The present invention has been made to solve these problems, and facilitates selection of a hydrogen storage alloy, and can reduce the time lag from cooling or heating to the hydrogen equilibrium pressure of the hydrogen storage alloy, resulting in a sharp load. It is an object of the present invention to provide a hydrogen pressure adjusting method for a hydrogen-cooled rotating electric machine that can quickly adjust the pressure of hydrogen gas inside the machine even when the temperature changes to.

〔発明の概要〕[Outline of Invention]

本発明はかかる目的を達成するため、水素ガスにより冷
却される回転電機の外部に、温度変化により水素ガスを
放出または吸着する水素貯蔵合金を収納したケースを設
け、このケースに回転電機の冷却媒体を導入する配管を
機内と連通させて接続すると共に機内の水素ガス循環系
に水素ガスを流出入する配管を接続してそれぞれの配管
の中途に弁を設ける構成とし、前記ケース内に形成され
た流通路に回転電機の冷却媒体を流出入せしめて前記水
素貯蔵合金を冷却又は加熱することにより機内水素ガス
圧力を負荷変動に応じて調整するに際し、前記水素貯蔵
合金として前記回転電機の冷却媒体の排出温度で水素平
衡圧力が機内の調整圧力最上限以上で且つ前記回転電機
の冷却媒体の供給温度で水素貯蔵合金の水素平衡圧力が
機内の調整圧力最下限以下である水素貯蔵合金を選定し
て前記ケース内のガス圧力を調整圧力最上限以上か最下
限以下にしておき、負荷の変動に応じて前記弁を開閉し
て水素ガスを機内へ放出又は機内の水素ガスを吸着せし
めて機内の水素ガス圧力を調整することを特徴とするも
のである。
In order to achieve such an object, the present invention provides a case storing a hydrogen storage alloy that releases or adsorbs hydrogen gas due to temperature change, outside the rotating electric machine cooled by hydrogen gas, and in this case, a cooling medium for the rotating electric machine. The pipe for introducing the is connected to the inside of the machine and connected to the hydrogen gas circulation system in the machine for connecting and disconnecting the hydrogen gas, and a valve is provided in the middle of each pipe, which is formed in the case. When adjusting the in-machine hydrogen gas pressure according to load fluctuations by flowing in and out the cooling medium of the rotating electrical machine to the flow passage and cooling or heating the hydrogen storage alloy, as the hydrogen storage alloy of the cooling medium of the rotating electrical machine At the discharge temperature, the hydrogen equilibrium pressure is equal to or higher than the upper limit of the regulated pressure inside the machine, and at the supply temperature of the cooling medium of the rotating electric machine, the hydrogen equilibrium pressure of the hydrogen storage alloy is the maximum regulated pressure inside the machine. A hydrogen storage alloy that is less than or equal to the limit and keeps the gas pressure in the case to be higher than or equal to the upper limit or lower than the lower limit of the regulated pressure, and opens or closes the valve according to the fluctuation of the load to release hydrogen gas into the aircraft or It is characterized in that the hydrogen gas in the machine is adsorbed to adjust the hydrogen gas pressure in the machine.

〔発明の実施例〕Example of Invention

以下本発明の一実施例を図面を参照して説明する。 An embodiment of the present invention will be described below with reference to the drawings.

第1図は本発明による水素冷却回転電機の水素圧力調整
装置の構成例を示すものである。第1図において、1は
回転電機、例えばタービン発電機の固定子フレームで、
その内周面には冷却水が流出入可能な中空導体からなる
固定子巻線2を備えた固定子鉄心3が取付けられると共
にその背部にガス通気空間部4が形成されている。5は
軸受に支承された回転子で、この回転子5には自己ファ
ン6が取付けられており、機内に大気圧以上の圧力で封
入された水素ガス7を強制循環させるためのものであ
る。また8a,8bは固定子巻線2の中空導体に冷却水を通
すためのヘッダーであり、これらヘッダー8a,8bには機
外に設けられた純水供給装置9が配管10a,10bを介して
接続されている。この純水供給装置9はタンク11,ポン
プ12,クーラ13及び図示しないイオン交換樹脂から構成
されている。一方、14は機外に設けられたケースで、こ
のケース14は筒体の周面のほぼ中央部に上部ヘッダー15
を有し、また内部には複数個の伝熱管16を筒体の長手方
向に沿って配設する共にこれら各伝熱管16相互間に形成
される管外スペースには粉末状の水素貯蔵合金17を充填
したものである。このようなケース14において、その筒
体の一方の開口部に固定子巻線2の冷却水流出側ヘッダ
ー8aと純水供給装置9のタンク11との間を結ぶ配管10a
の中途に接続された配管18aを接続すると共にこの配管1
8aとクーラ13の出口近傍の配管10bとの間を配管21によ
り接続し、また筒体の他方の開口部に冷却水を純水供給
装置9のタンク11へ戻す配管18bを接続して冷却水の一
部をバイパスするバイパス路を形成する。さらにケース
14に有する上部ヘッダー15にはダストや微粒子が機内へ
浮遊あるいは飛散しないようにするための通気性のフィ
ルタ19が設けられると共にこの部分を配管20を介して機
内のガス通気空間部4に連通させて接続し、水素貯蔵合
金17から放出または水素貯蔵合金17に吸着される水素ガ
スを機内との間で流通できるようになっている。さら
に、22a,22b,22cはケース14の一方の開口部に接続され
た冷却水バイパス路を形成する配管18a,この配管18aと
クーラ13の出口近傍の配管10bとを結ぶ配管21及び上部
ヘッダー15と機内とを結ぶ水素ガス流通路となる配管20
の適宜箇所にそれぞれ設けられた電磁弁である。
FIG. 1 shows an example of the configuration of a hydrogen pressure adjusting device for a hydrogen-cooled rotary electric machine according to the present invention. In FIG. 1, 1 is a rotating electric machine, for example, a stator frame of a turbine generator,
A stator core 3 having a stator winding 2 made of a hollow conductor through which cooling water can flow in and out is attached to the inner peripheral surface thereof, and a gas ventilation space 4 is formed in the back portion thereof. Reference numeral 5 denotes a rotor supported by bearings, and a self-fan 6 is attached to the rotor 5 for forcibly circulating the hydrogen gas 7 sealed in the machine at a pressure higher than atmospheric pressure. Further, 8a and 8b are headers for passing cooling water through the hollow conductors of the stator winding 2, and a pure water supply device 9 provided outside the machine is installed in these headers 8a and 8b via pipes 10a and 10b. It is connected. The pure water supply device 9 is composed of a tank 11, a pump 12, a cooler 13 and an ion exchange resin (not shown). On the other hand, 14 is a case provided outside the machine, and this case 14 has an upper header 15 at approximately the center of the peripheral surface of the cylindrical body.
In addition, a plurality of heat transfer tubes 16 are arranged inside along the longitudinal direction of the cylindrical body, and a powdery hydrogen storage alloy 17 is provided in the outer space formed between these heat transfer tubes 16. Is filled. In such a case 14, a pipe 10a connecting the cooling water outflow side header 8a of the stator winding 2 and the tank 11 of the pure water supply device 9 to one opening of the cylindrical body.
Connect the pipe 18a connected in the middle of the
8a and a pipe 10b in the vicinity of the outlet of the cooler 13 are connected by a pipe 21, and a pipe 18b for returning the cooling water to the tank 11 of the pure water supply device 9 is connected to the other opening of the cylindrical body for cooling water. Form a bypass path that bypasses a part of Further case
The upper header 15 of 14 is provided with a breathable filter 19 for preventing dust and particles from floating or scattering in the machine, and this portion is connected to the gas ventilation space 4 in the machine through the pipe 20. The hydrogen gas released from the hydrogen storage alloy 17 or adsorbed to the hydrogen storage alloy 17 can be flowed to and from the inside of the aircraft. Further, 22a, 22b and 22c are a pipe 18a forming a cooling water bypass passage connected to one opening of the case 14, a pipe 21 connecting the pipe 18a and a pipe 10b near the outlet of the cooler 13, and an upper header 15 Piping 20 that serves as a hydrogen gas flow passage that connects the
The solenoid valves are provided at appropriate places respectively.

このように構成された水素冷却タービン発電機の水素圧
力調整系において、ケース14内に充填された水素貯蔵合
金として例えば80°〜60℃の温度で水素平衡圧力が5.2K
g/cm2以上で、冷却水の低温側温度45°〜40℃で水素平
衡圧力が1.0Kg/cm2以下になるものが選択されているも
のとする。このような条件下において、今電磁弁22aが
開、電磁弁22b,22cが閉状態にあると冷却水は純粋供給
装置9のタンク11から固定子巻線2の中空導体に配管10
b,流入側ヘッダー8bを通して流入し、流出側ヘッダー8a
から配管10aを通して純水供給装置9のタンク11へ戻る
固定子巻線冷却水循環系により固定子巻線2が冷却さ
れ、この時固定子巻線冷却水は巻線の電機損による熱に
より昇温して排熱水となる。この排熱水はさらにバイパ
ス配管18a及び電磁弁22aを通ってケース14に流入し、こ
こで水素貯蔵合金17を加熱した後配管18bを通してタン
ク11に戻る。したがって、電磁弁22cは閉じているの
で、ケース14内は水素貯蔵合金17から発生する水素ガス
により排出熱水温度の水素平衡圧力にまで昇圧する。
In the hydrogen pressure adjusting system of the hydrogen-cooled turbine generator configured as described above, the hydrogen equilibrium pressure is 5.2 K at a temperature of 80 ° to 60 ° C., for example, as the hydrogen storage alloy filled in the case 14.
It is assumed that the hydrogen equilibrium pressure of 1.0 kg / cm 2 or less is selected at g / cm 2 or more and the cooling water low temperature side temperature of 45 ° to 40 ° C. Under such conditions, when the solenoid valve 22a is now open and the solenoid valves 22b and 22c are closed, the cooling water is piped from the tank 11 of the pure supply device 9 to the hollow conductor of the stator winding 2.
b, inflow through the inflow side header 8b, outflow side header 8a
To the tank 11 of the pure water supply device 9 through the pipe 10a. The stator winding cooling water circulation system cools the stator winding 2, and at this time, the stator winding cooling water is heated by heat due to electrical loss of the winding. It becomes waste heat water. The waste heat water further flows into the case 14 through the bypass pipe 18a and the solenoid valve 22a, where the hydrogen storage alloy 17 is heated and then returns to the tank 11 through the pipe 18b. Therefore, since the solenoid valve 22c is closed, the inside of the case 14 is boosted to the hydrogen equilibrium pressure of the exhaust hot water temperature by the hydrogen gas generated from the hydrogen storage alloy 17.

一方、電磁弁22aと22bを閉じ、電磁弁22cを開にする
と、ケース14にはクーラ13の出口から流出する低温の冷
却水が配管21を通して流入し、ケース14内の水素貯蔵合
金17を冷却してタンク11に戻る。したがって、この場合
はケース14内の水素ガスが水素貯蔵合金17に吸着される
ので、ケース14内の水素ガス圧力はその冷却水の温度の
水素平衡圧力にまで低下する。
On the other hand, when the solenoid valves 22a and 22b are closed and the solenoid valve 22c is opened, the low-temperature cooling water flowing out from the outlet of the cooler 13 flows into the case 14 through the pipe 21 and cools the hydrogen storage alloy 17 in the case 14. Then return to tank 11. Therefore, in this case, the hydrogen gas in the case 14 is adsorbed by the hydrogen storage alloy 17, and the hydrogen gas pressure in the case 14 drops to the hydrogen equilibrium pressure of the temperature of the cooling water.

ここで、第2図に示す負荷パターンに基いてその具体的
な作用を説明する。
Here, the specific operation will be described based on the load pattern shown in FIG.

第2図において、夜間(D−A間に示す)のように低負
荷の場合には第1図の電磁弁22aを開にし、電磁弁22b,2
2cを閉状態にしておく。このようにすれば、前述したよ
うに固定子巻線2の冷却水流出側ヘッダー8aから流出す
る排熱水がケース14内を通して純水供給装置9のタンク
11へ流れることにより、ケース14内に充填された水素貯
蔵合金17が暖められ、水素貯蔵合金17から再生する水素
ガスによりケース14内は100%負荷時の回転電機の許容
水素圧力5.2atm以上になる。このような状態にある時、
朝方(A−B間を示す)になり、負荷が上昇するとその
負荷に応じて電磁弁22cの開度を調節するとケース14か
ら水素ガスが配管20を通して機内へ放出される。したが
って、機内の水素ガス圧力は負荷に対する許容水素ガス
圧力まで上昇する。尚、電磁弁22cは必要な時のみ開い
て常時は閉じられている。
In Fig. 2, when the load is low at night (shown between D and A), the solenoid valve 22a in Fig. 1 is opened and the solenoid valves 22b, 2
Keep 2c closed. With this configuration, as described above, the exhaust heat water flowing out from the cooling water outflow side header 8a of the stator winding 2 passes through the case 14 and the tank of the pure water supply device 9
By flowing to 11, the hydrogen storage alloy 17 filled in the case 14 is warmed, and the hydrogen gas regenerated from the hydrogen storage alloy 17 causes the inside of the case 14 to have an allowable hydrogen pressure of 5.2 atm or more of the rotating electric machine at 100% load. Become. When in this state,
When it becomes the morning (between A and B) and the load increases, the opening degree of the solenoid valve 22c is adjusted according to the load and hydrogen gas is discharged from the case 14 through the pipe 20 into the machine. Therefore, the hydrogen gas pressure inside the machine rises to the allowable hydrogen gas pressure for the load. The solenoid valve 22c is opened only when necessary and is normally closed.

負荷上昇が完了し、負荷が安定するB点に達すると電磁
弁22a,22cを閉じ、電磁弁22bを開としてケース14にクー
ラ13から流出する低温の冷却水が流入する。したがっ
て、ケース14内の水素貯蔵合金17が冷却されるので、ケ
ース14内の水素ガス圧力は1.0Kg/cm2以下になり、夕方
の負荷減少時に備える。
When the load rise is completed and the load reaches the point B where the load is stabilized, the solenoid valves 22a and 22c are closed, the solenoid valve 22b is opened, and the low temperature cooling water flowing out from the cooler 13 flows into the case 14. Therefore, since the hydrogen storage alloy 17 in the case 14 is cooled, the hydrogen gas pressure in the case 14 becomes 1.0 Kg / cm 2 or less, and prepares for the load reduction in the evening.

夕方になり、図示C−D間のように負荷の減少時にはそ
の時の負荷に応じて電磁弁19cを開にすると共にその開
度を調節して機内の水素ガスをケース14内に流入して水
素貯蔵合金17に吸着させ、負荷に対する許容水素ガス圧
力に調整する。そして負荷の減少が完了し、負荷が安定
する図示D点に達した時点で今度は逆に電磁弁22aを開
き、電磁弁22b,22cを閉じて熱交換器14に固定子巻線2
の冷却水流出側ヘッダー8aから流出する排熱水を前述同
様にケース14に流入してケース14内の水素貯蔵合金17を
加熱し、ケース14内の水素ガス圧を5.2Kg/cm2以上にし
ておき、朝方の負荷上昇に備える。
In the evening, when the load is reduced as shown in the figure between C and D, the solenoid valve 19c is opened according to the load at that time and the opening is adjusted to allow the hydrogen gas in the machine to flow into the case 14 so that the hydrogen gas is discharged. Adsorb on the storage alloy 17 and adjust to the allowable hydrogen gas pressure for the load. Then, when the load reduction is completed and the load reaches the point D shown in the figure where it stabilizes, the solenoid valve 22a is opened in reverse, the solenoid valves 22b and 22c are closed, and the stator winding 2 is attached to the heat exchanger 14.
Exhaust heat water that flows out from the cooling water outflow side header 8a flows into the case 14 in the same manner as described above to heat the hydrogen storage alloy 17 in the case 14, and the hydrogen gas pressure in the case 14 is set to 5.2 Kg / cm 2 or more. Be prepared for a load increase in the morning.

以上述べたように本実施例によれば、水素貯蔵合金17の
特性は80°〜60℃で水素平衡圧力が5.2Kg/cm2以上、45
°〜40℃で水素平衡圧力が1.0Kg/cm2以下と条件が緩や
かで、水素貯蔵合金の選択が容易となり、まや水素貯蔵
合金は粉末状であるため熱電導が悪く、加熱、冷却が開
始されてから所定の圧力になるまでのタイムラグがあっ
たが、あらかじめ負荷の安定した時点で次の負荷対応に
備えるようにしているので、負荷の変動に対して圧力調
整が速やかに行なうことが可能となる。また、水素貯蔵
合金の加熱は固定子巻線冷却後の排熱水を使用している
のでエネルギー的にも極めて有利である。さらに、水素
貯蔵合金は粉末状であるためケース14から水素ガスを放
出する際、機内に粉塵となって侵入し電気的耐電圧を劣
化させる恐れがあるが、ケース14の上部ヘッダー15にフ
イルタ19が設けられているので、その心配がなく、信頼
性を向上させることができる。
As described above, according to the present embodiment, the characteristics of the hydrogen storage alloy 17 are that the hydrogen equilibrium pressure is not less than 5.2 Kg / cm 2 at 80 ° to 60 ° C., 45
The hydrogen equilibrium pressure is 1.0Kg / cm 2 or less at ° -40 ° C, which makes the selection of hydrogen storage alloy easy, and since the hydrogen storage alloy is in powder form, it has poor thermal conductivity and starts heating and cooling. There was a time lag from when the load was adjusted to the prescribed pressure, but since the load is ready for the next load when the load stabilizes, it is possible to quickly adjust the pressure for load fluctuations. Becomes Further, since the hydrogen storage alloy is heated by using the waste heat water after cooling the stator winding, it is extremely advantageous in terms of energy. Further, since the hydrogen storage alloy is in powder form, when hydrogen gas is released from the case 14, there is a risk that it will enter the machine as dust and deteriorate the electrical withstand voltage. Is provided, the reliability can be improved without the concern.

勿論、負荷に応じて機内の水素ガス圧力を調整するよう
にしているので、部分負荷時の風損やファン動力が減っ
て回転電機の効率が向上すると共に回転電機構成部材の
ヒートサイクルが少なくなるので、回転電機の寿命が長
くなり、信頼性も増すことになる。また、水素ガス圧力
の調整が水素ガスの消耗なしで可能となり、回転電機の
定期点検時にはすべての水素ガスを大気に放出するこな
く、水素貯蔵合金に回収することができるので、エネル
ギの有効利用を図ることができる。
Of course, since the hydrogen gas pressure inside the machine is adjusted according to the load, wind loss and fan power during partial load are reduced, the efficiency of the rotary electric machine is improved, and the heat cycle of the rotary electric machine constituent members is reduced. Therefore, the life of the rotating electric machine is extended and the reliability is increased. In addition, the hydrogen gas pressure can be adjusted without exhaustion of hydrogen gas, and all hydrogen gas can be recovered in the hydrogen storage alloy without being released to the atmosphere during periodic inspection of rotating electric machines, so effective use of energy is possible. Can be achieved.

次に本発明の他の実施例をについて説明する。Next, another embodiment of the present invention will be described.

第3図は水素冷却回転電機の水素圧力調整系の他の構成
例を示すもので、第1図と同一部分には同一記号を付し
てその説明を省略し、ここでは異なる部分についてのみ
述べる。本実施例では第3図に示すように2個のケース
14A,14Bを設けると共にその筒体のそれぞれ一方の開口
部を冷却水流出側ヘッダー8aと純粋供給装置9のタンク
11間を結ぶ配管10aの中途に配管18a1,18a2を介して接続
すると共にその配管18a1,18a2の中途に電磁弁23,24を設
け、また他方の開口部に冷却水を純粋供給装置9のタン
ク11へ戻す配管18b1,18b2を接続し、さらにケース14A,1
4Bの一方の開口部近傍の配管18a1,18a2を分岐した分岐
管路の中途に電磁弁25,26を設けてこれらを共通に接続
し、その共通接続部を配管21によりクーラ13の出口近傍
の配管10bに接続する。またケース14A,14Bの上部ヘッダ
ーをそれぞれ配管20a,20bにより機内に連通させて接続
すると共にこれら配管20a,20bの中途に電磁弁27,28をそ
れぞれ設け、さらに上部ヘッダー間を配管29により共通
に接続すると共にその中途に電磁弁30を設ける構成とす
るものである。
FIG. 3 shows another configuration example of the hydrogen pressure adjusting system of the hydrogen-cooled rotary electric machine. The same parts as those in FIG. 1 are designated by the same reference numerals and the description thereof will be omitted. Here, only different parts will be described. . In this embodiment, there are two cases as shown in FIG.
14A and 14B are provided, and one of the openings of the cylindrical body is provided with a cooling water outflow side header 8a and a tank of the pure supply device 9.
A solenoid valve 23, 24 is provided in the middle of the pipe 10a connecting the 11 through the pipes 18a1, 18a2, and solenoid valves 23, 24 are provided in the middle of the pipe 18a1, 18a2. Connect the pipes 18b1 and 18b2 to return to 11, and then connect the case 14A and 1
4B is provided with solenoid valves 25 and 26 in the middle of a branch pipe that branches the pipes 18a1 and 18a2 near one opening, and these are connected in common, and the common connection part is connected by a pipe 21 near the outlet of the cooler 13. Connect to pipe 10b. Further, the upper headers of the cases 14A and 14B are connected to the inside of the machine by communicating with the pipes 20a and 20b, respectively, and solenoid valves 27 and 28 are provided in the middle of these pipes 20a and 20b, respectively, and a pipe 29 is commonly used between the upper headers. The structure is such that the solenoid valve 30 is provided in the middle of the connection.

次に上記構成の作用を第4図に示す負荷パターンに基い
て説明する。
Next, the operation of the above configuration will be described based on the load pattern shown in FIG.

今、第4図において、朝方の図示E点では一方のケース
14Aが高圧状態にあり、他方のケース14Bが低圧状態にな
っているものとする。このような状態で朝,昼,夕の図
示E〜Fまでの負荷変動に対する圧力調整は次のように
して行なわれる。先ず、負荷上昇時はケース14A側の電
磁弁27を開放すると共にその開度を調節して水素ガスを
機内へ放出し機内の水素ガス圧力を高める。一方、負荷
減少時はケース14B側の電磁弁28を開放すると共にその
開度を調節して機内の水素ガスを吸着し、機内の水素ガ
ス圧力を減少させる。この場合、第1図の実施例と同様
に電磁弁23,26が開で、24,25が閉状態にあり、また電磁
弁30も閉じている。
Now, in FIG. 4, one case is shown at the point E in the morning.
It is assumed that 14A is in a high pressure state and the other case 14B is in a low pressure state. In such a state, pressure adjustment with respect to load changes from morning to afternoon to evening E to F is performed as follows. First, when the load is increased, the solenoid valve 27 on the case 14A side is opened and its opening is adjusted to release hydrogen gas into the machine to increase the hydrogen gas pressure in the machine. On the other hand, when the load is reduced, the solenoid valve 28 on the case 14B side is opened and the opening thereof is adjusted to adsorb the hydrogen gas in the machine to reduce the hydrogen gas pressure in the machine. In this case, as in the embodiment shown in FIG. 1, the solenoid valves 23 and 26 are open, 24 and 25 are closed, and the solenoid valve 30 is also closed.

以上のような日中の操作によりケース14Aは水素ガスを
ある量放出し、ケース14Bは機内の水素ガスを吸着して
いる。ここで、その状態を第5図に示す水素貯蔵合金の
特性曲線図を参照しながら説明する。即ち、ケース14A,
14B内の水素貯蔵合金中の水素量と水素平衡圧力との関
係を示す第5図において、今負荷が第4図のE点にある
とすれば、ケース14Aは第5図の点1にあり、負荷がF
点にあるとすれば水素ガスの放出で点2に移る。また、
ケース14Bは負荷がE点の時は点4にあり、F点の時は
水素ガスの吸収で点5に移る。負荷が第4図のF点を過
ぎて夜間に入り、低負荷で安定してきたらそのままにし
た状態で、電磁弁30を開いて熱交換器14A,14B相互間を
連通させ、水素貯蔵合金が充填されている室内で水素ガ
スが流出入できるようにする。この場合、電磁弁26,27
が閉じていることは勿論のことである。このようにする
と、第5図に示す水素貯蔵合金の特性曲線において、ケ
ース14A,14Bの水素ガス圧力は同じになり、その値はP
=(Pa+Pb)/2となる。つまり、ケース14Aは水素ガス
をケース14Bへ放出し、ケース14Bは水素ガスを吸着して
ケース14Aは点3へ、ケース14Bは点6へ移動する。した
がって、ケース14Aは水素ガスの含有量が少なくなり、
ケース14Bは水素ガスの含有量が多くなるので、水素含
有量では第4図に示す負荷パターンでE点の時点と全く
逆転する。この状態が平衡状態になったら電磁弁30を閉
じ、さらに電磁弁23,26を閉じる共に電磁弁24,25を開い
て水素貯蔵合金を加熱,冷却する冷却水の温度を逆にす
る。この場合、電磁弁25,27は閉状態にあることは勿論
である。このようにすれば、ケース14Aは低圧、ケース1
4Bは高圧状態になり、朝方の負荷変動に備えることにな
る。
Through the daytime operation as described above, the case 14A releases a certain amount of hydrogen gas, and the case 14B adsorbs the hydrogen gas inside the aircraft. Here, the state will be described with reference to the characteristic curve diagram of the hydrogen storage alloy shown in FIG. That is, case 14A,
In FIG. 5 showing the relationship between the amount of hydrogen in the hydrogen storage alloy in 14B and the hydrogen equilibrium pressure, if the load is now at point E in FIG. 4, then case 14A is at point 1 in FIG. , The load is F
If it is at a point, it moves to point 2 due to the release of hydrogen gas. Also,
Case 14B is located at point 4 when the load is at point E, and moves to point 5 when the load is at point F due to absorption of hydrogen gas. When the load has passed the point F in Fig. 4 and entered at night, and when it became stable at a low load, leave it as it is, open the solenoid valve 30 to communicate between the heat exchangers 14A and 14B, and fill the hydrogen storage alloy. Allow hydrogen gas to flow in and out of the room. In this case, solenoid valves 26, 27
Of course, is closed. By doing so, in the characteristic curve of the hydrogen storage alloy shown in FIG. 5, the hydrogen gas pressures in cases 14A and 14B are the same, and the value is P
= (Pa + Pb) / 2. That is, the case 14A releases hydrogen gas to the case 14B, the case 14B adsorbs hydrogen gas, and the case 14A moves to point 3 and the case 14B moves to point 6. Therefore, Case 14A has a low hydrogen gas content,
In case 14B, since the hydrogen gas content is large, the hydrogen content is completely opposite to the point E at the load pattern shown in FIG. When this state reaches an equilibrium state, the solenoid valve 30 is closed, the solenoid valves 23 and 26 are closed, and the solenoid valves 24 and 25 are opened to reverse the temperature of the cooling water for heating and cooling the hydrogen storage alloy. In this case, the solenoid valves 25 and 27 are, of course, in the closed state. In this way, case 14A is low pressure, case 1
4B will be in a high pressure state and will be prepared for load changes in the morning.

尚、上記実施例において夜間の負荷が極めて低く、固定
子巻線冷却水の排熱温度が低い場合には水素貯蔵合金が
排熱温度で調整最上限圧力,例えば5.2Kg/cm2以上にな
らない場合には第6図に示すように冷却水排出側ヘッダ
ーに接続された配管10aに冷却水再加熱器31を設けて排
熱温度を上昇させることも考えられる。
In the above example, when the nighttime load is extremely low and the exhaust heat temperature of the stator winding cooling water is low, the hydrogen storage alloy does not reach the upper limit pressure adjusted by the exhaust heat temperature, for example, 5.2 Kg / cm 2 or more. In this case, it is possible to increase the exhaust heat temperature by providing a cooling water reheater 31 in the pipe 10a connected to the cooling water discharge side header as shown in FIG.

また、負荷パターンが昼夜とも極めて変動頻度が高い場
合には高圧状態にあるケース、低圧状態にあるケースを
予め切替える時間がないため、このような場合には高
圧,低圧ケースの対を2組用意して対応させるようにし
てもよい。
Also, if the load pattern changes extremely frequently both day and night, there is no time to switch between the high-voltage case and the low-voltage case beforehand. In such a case, prepare two pairs of high-voltage and low-voltage cases. You may make it correspond.

このようにケースを複数個(上記実施例では2個)備え
ることにより、負荷パターンが変わった時でも迅速に回
転電機の機内水素ガス圧を負荷に対応させて調整するこ
とが可能となる。
By providing a plurality of cases (two in the above embodiment) in this way, it is possible to quickly adjust the in-machine hydrogen gas pressure of the rotating electric machine according to the load even when the load pattern changes.

前述した第1図及び第3図に示す実施例では水素貯蔵合
金を冷却,加熱する媒体として固定子巻線冷却系を用い
る場合であるが、回転電機の冷却媒体である水素ガスを
用いるようにしてもよい。この場合、水素貯蔵合金の加
熱用としては機内に設けられている水素ガス冷却器の入
口よりも手前の温度の高い水素ガスをケースに導き、ま
た水素ガス冷却器の出口の温度の低い水素ガスを冷却用
としてケースに導くことにより実施することができる。
In the embodiment shown in FIGS. 1 and 3 described above, the stator winding cooling system is used as a medium for cooling and heating the hydrogen storage alloy. However, hydrogen gas, which is the cooling medium for the rotating electric machine, should be used. May be. In this case, for heating the hydrogen storage alloy, hydrogen gas with a higher temperature than the inlet of the hydrogen gas cooler installed inside the machine is introduced into the case, and hydrogen gas with a low temperature at the outlet of the hydrogen gas cooler is introduced. Can be carried out by introducing it into a case for cooling.

〔発明の効果〕〔The invention's effect〕

以上述べたように本発明では、水素ガスにより冷却され
る回転電機の外部に、温度変化により水素ガスを放出ま
たは吸着する水素貯蔵合金を収納したケースを設け、こ
のケースに回転電機の冷却媒体を導入する配管を機内と
連通させて接続すると共に機内の水素ガス循環系に対し
て水素ガスを流出入する配管を接続してそれぞれの配管
の中途に弁を設ける構成とし、前記ケース内に形成され
た流通路に回転電機の冷却媒体を流出入せしめて前記水
素貯蔵合金を冷却又は加熱することにより機内水素ガス
圧力を負荷変動に応じて調整するに際し、前記水素貯蔵
合金として前記回転電機の冷却媒体の排出温度で水素平
衡圧力が機内の調整圧力最上限以上で且つ前記回転電機
の冷却媒体の供給温度で水素貯蔵合金の水素平衡圧力が
機内の調整圧力最下限以下となる水素貯蔵合金を選定し
て前記ケース内のガス圧力を調整圧力最上限以上か最下
限以下にしておき、負荷の変動に応じて前記弁を開閉し
て水素ガスを機内へ放出又は機内の水素ガスを吸着せし
めて機内の水素ガス圧力を調整するようにしたものであ
る。したがって、水素貯蔵合金の選定条件は極めて緩や
かになるので、水素貯蔵合金の選択が容易になり、また
予め水素貯蔵合金を加熱又は冷却しておき、ケース内の
水素ガス圧力を調整圧力最上限以上又は最下限以下にな
るようにしてあるので、負荷が急激に変化しても機内の
水素ガス循環系に対して水素ガスを流出入する配管の中
途に設けられた電磁弁を開くことにより機内の水素ガス
圧力を速やかに調整することができる水素冷却回転電機
の水素圧力調整方法を提供することができる。
As described above, in the present invention, a case containing a hydrogen storage alloy that releases or adsorbs hydrogen gas due to temperature change is provided outside the rotating electric machine cooled by hydrogen gas, and the cooling medium for the rotating electric machine is provided in this case. The pipe to be introduced is connected to the inside of the machine so as to be connected to the hydrogen gas circulation system inside the machine, and the pipe for flowing the hydrogen gas into and out of the machine is connected to provide a valve in the middle of each pipe, which is formed in the case. When adjusting the in-machine hydrogen gas pressure according to load fluctuations by flowing the cooling medium of the rotating electric machine into and out of the flow passage to cool or heat the hydrogen storage alloy, the cooling medium of the rotating electric machine is used as the hydrogen storage alloy. The hydrogen equilibrium pressure at the exhaust temperature is equal to or higher than the maximum adjustment pressure inside the machine, and the hydrogen equilibrium pressure of the hydrogen storage alloy is at the adjustment pressure maximum inside the machine at the supply temperature of the cooling medium of the rotating electric machine. A hydrogen storage alloy below the limit is selected and the gas pressure in the case is kept above the adjustment upper limit or below the lower limit, and the hydrogen gas is released into the machine by opening or closing the valve according to the change in load. The hydrogen gas in the machine is adsorbed to adjust the hydrogen gas pressure in the machine. Therefore, the conditions for selecting the hydrogen storage alloy become extremely lenient, which facilitates the selection of the hydrogen storage alloy, and preheats or cools the hydrogen storage alloy to adjust the hydrogen gas pressure in the case to the adjusted pressure upper limit or higher. Or, since it is set to the lower limit or less, even if the load changes abruptly, the solenoid valve provided in the middle of the pipe for flowing hydrogen gas in and out of the hydrogen gas circulation system in the machine can be opened It is possible to provide a hydrogen pressure adjusting method for a hydrogen-cooled rotating electric machine that can quickly adjust the hydrogen gas pressure.

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

第1図は本発明方法を説明するための一実施例を示す水
素冷却回転電機の水素圧力調整系統の構成図、第2図は
同実施例の作用を説明するための回転電機の負荷パター
ン図、第3図は本発明の他の実施例を説明するための水
素冷却回転電機の水素圧力調整系統の構成図、第4図は
同実施例の作用を説明するための回転電機の負荷パター
ン図、第5図は第4図の負荷パターンに対する水素貯蔵
合金の水素ガスの吸着,放出の状態図、第6図は第3図
において熱交換器に固定子巻線冷却水を導入する冷却水
導入系の変形例を示す部分的な構成図、第7図及び第8
図は水素貯蔵合金の特性の一例を説明するための図、第
9図は水素貯蔵合金の特性と固定子巻線冷却水出口温度
と許容機内水素ガス圧力の関係図、第10図は従来のター
ビン発電機の水素圧力調整系を示す構成図である。 1……固定子フレーム、2……固定子巻線、3……固定
子鉄心、4……空間部、5……回転子、6……自己ファ
ン、7……水素ガス、8a,8b……ヘッダー、10a,10b……
配管、11……タンク、12……ポンプ、13……クーラ、1
4,14A,14B……ケース、15……ケースの上部ヘッダー、1
6……伝熱管、17……水素貯蔵合金、18a,18a1,18a2,18
b,18b1,18b2……配管、19……フイルタ、20,20a,20b…
…配管、22a〜22c,23〜30……電磁弁。
FIG. 1 is a block diagram of a hydrogen pressure adjusting system of a hydrogen-cooled rotary electric machine showing an embodiment for explaining the method of the present invention, and FIG. 2 is a load pattern diagram of the rotary electric machine for explaining the operation of the embodiment. 3 is a configuration diagram of a hydrogen pressure adjusting system of a hydrogen-cooled rotary electric machine for explaining another embodiment of the present invention, and FIG. 4 is a load pattern diagram of the rotary electric machine for explaining the operation of the embodiment. FIG. 5 is a state diagram of adsorption and release of hydrogen gas from the hydrogen storage alloy with respect to the load pattern of FIG. 4, and FIG. 6 is cooling water introduction for introducing stator winding cooling water to the heat exchanger in FIG. Partial configuration diagrams showing a modified example of the system, FIGS. 7 and 8
The figure is a diagram for explaining an example of the characteristics of the hydrogen storage alloy, FIG. 9 is a relationship diagram of the characteristics of the hydrogen storage alloy, the stator winding cooling water outlet temperature and the allowable hydrogen gas pressure in the machine, and FIG. It is a block diagram which shows the hydrogen pressure adjustment system of a turbine generator. 1 ... Stator frame, 2 ... Stator winding, 3 ... Stator core, 4 ... Space part, 5 ... Rotor, 6 ... Self fan, 7 ... Hydrogen gas, 8a, 8b ... … Header, 10a, 10b ……
Piping, 11 …… tank, 12 …… pump, 13 …… cooler, 1
4,14A, 14B …… Case, 15 …… Case top header, 1
6 ... Heat transfer tube, 17 ... Hydrogen storage alloy, 18a, 18a1,18a2,18
b, 18b1,18b2 …… Piping, 19 …… Filter, 20,20a, 20b…
… Piping, 22a-22c, 23-30 …… solenoid valve.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】水素ガスにより冷却される回転電機の外部
に、温度変化により水素ガスを放出または吸着する水素
貯蔵合金を収納したケースを設け、このケースに回転電
機の固定子巻線に冷却媒体を導入する配管を接続すると
共に機内の水素ガス循環系に対して水素ガスを流出入す
る配管を接続してそれぞれの配管の中途に弁を設ける構
成とし、前記ケース内に形成された流通路に回転電機の
固定子巻線を冷却する冷却媒体を流出入せしめて前記水
素貯蔵合金を冷却または加熱することにより機内水素ガ
ス圧力を負荷変動に応じて調整するに際して、前記水素
貯蔵合金として前記回転電機の固定子巻線より流出する
冷却媒体の排出温度で水素平衡圧力が機内の調整圧力最
上限以上で且つ前記回転電機の固定子巻線に流入する冷
却媒体の供給温度で水素貯蔵合金の水素平衡圧力が機内
の調整圧力最下限以下である水素貯蔵合金を選定して前
記ケース内のガス圧力を調整圧力最上限以上か最下限以
下にしておき、負荷の変動に応じて前記弁を開閉して水
素ガスを吸着せしめて機内の水素ガス圧力を調整するこ
とを特徴とする水素冷却回転電機の水素圧力調整方法。
1. A case in which a hydrogen storage alloy that releases or adsorbs hydrogen gas due to temperature changes is housed outside a rotating electric machine cooled by hydrogen gas, and a cooling medium is provided in a stator winding of the rotating electric machine in this case. In addition to connecting the piping for introducing the hydrogen gas circulation system in the machine to connect the piping for flowing in and out the hydrogen gas to provide a valve in the middle of each pipe, in the flow passage formed in the case When adjusting the in-machine hydrogen gas pressure according to load fluctuations by flowing in and out a cooling medium for cooling the stator windings of the rotating electric machine to cool or heat the hydrogen storing alloy, the rotating electric machine is used as the hydrogen storing alloy. Supply temperature of the cooling medium flowing into the stator winding of the rotating electric machine when the hydrogen equilibrium pressure is equal to or higher than the upper limit of the regulated pressure inside the machine at the discharge temperature of the cooling medium flowing out from Select a hydrogen storage alloy whose hydrogen equilibrium pressure of the hydrogen storage alloy is less than or equal to the adjustment pressure lower limit in the machine and keep the gas pressure in the case above the adjustment pressure upper limit or below the lower limit, depending on load fluctuations. A method for adjusting hydrogen pressure in a hydrogen-cooled rotating electric machine, comprising: opening and closing the valve to adsorb hydrogen gas to adjust the hydrogen gas pressure inside the machine.
【請求項2】機内の水素ガス循環系及び回転電機の固定
子巻線を冷却する冷却媒体の流出入系に接続されるケー
スは複数個設けられ、これらを高圧状態と低圧状態に分
けて負荷変動時に対応させるようにした特許請求の範囲
第1項記載の水素冷却回転電機の水素圧力調整方法。
2. A plurality of cases are provided which are connected to a hydrogen gas circulation system inside the machine and an inflow / outflow system of a cooling medium for cooling a stator winding of a rotary electric machine. The method for adjusting hydrogen pressure in a hydrogen-cooled rotary electric machine according to claim 1, wherein the method is adapted to cope with fluctuations.
JP60133416A 1985-06-19 1985-06-19 Method for adjusting hydrogen pressure of hydrogen-cooled rotating electric machine Expired - Lifetime JPH0744805B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60133416A JPH0744805B2 (en) 1985-06-19 1985-06-19 Method for adjusting hydrogen pressure of hydrogen-cooled rotating electric machine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60133416A JPH0744805B2 (en) 1985-06-19 1985-06-19 Method for adjusting hydrogen pressure of hydrogen-cooled rotating electric machine

Publications (2)

Publication Number Publication Date
JPS61293132A JPS61293132A (en) 1986-12-23
JPH0744805B2 true JPH0744805B2 (en) 1995-05-15

Family

ID=15104257

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60133416A Expired - Lifetime JPH0744805B2 (en) 1985-06-19 1985-06-19 Method for adjusting hydrogen pressure of hydrogen-cooled rotating electric machine

Country Status (1)

Country Link
JP (1) JPH0744805B2 (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5097669A (en) * 1991-02-11 1992-03-24 Westinghouse Electric Corp. Control of hydrogen cooler employed in power generators
ATE137621T1 (en) * 1992-11-04 1996-05-15 Siemens Ag DISCHARGE OF HYDROGEN FROM AN ELECTRIC MACHINE FILLED WITH HYDROGEN
JP4982119B2 (en) * 2006-06-29 2012-07-25 株式会社東芝 Rotating electric machine
DE102012022421A1 (en) * 2012-11-16 2014-05-22 Rwe Generation Se Method for cooling e.g. two-pole turbogenerator, with closed cooling gas circuit, involves controlling gas pressure within cooling gas circuit in dependence of actual operating point of direct current generator-electrical machine
US12261491B2 (en) * 2022-04-12 2025-03-25 Hamilton Sundstrand Corporation Aircraft electric motor

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57186948A (en) * 1981-05-13 1982-11-17 Hitachi Ltd Coolant supplier for electric rotary machine

Also Published As

Publication number Publication date
JPS61293132A (en) 1986-12-23

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