JPH0823456B2 - Absorption heat source device - Google Patents
Absorption heat source deviceInfo
- Publication number
- JPH0823456B2 JPH0823456B2 JP2144119A JP14411990A JPH0823456B2 JP H0823456 B2 JPH0823456 B2 JP H0823456B2 JP 2144119 A JP2144119 A JP 2144119A JP 14411990 A JP14411990 A JP 14411990A JP H0823456 B2 JPH0823456 B2 JP H0823456B2
- Authority
- JP
- Japan
- Prior art keywords
- liquid
- surfactant
- refrigerant vapor
- condenser
- transfer pipe
- 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
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- Sorption Type Refrigeration Machines (AREA)
Description
【発明の詳細な説明】 産業上の利用分野 本発明は吸収式熱源装置に関するものである。Description: FIELD OF THE INVENTION The present invention relates to an absorption heat source device.
従来の技術 従来、吸収式冷凍機、吸収式ヒートポンプなどの吸収
式熱源装置は、冷媒(例えば水)を蒸発させる蒸発器
と、この蒸発器で蒸発された冷媒蒸気を吸収液(倒えば
臭化リチウム水溶液)に吸収する吸収器と、この吸収器
で冷媒蒸気を吸収して濃度が薄くなった稀吸収液を加熱
する再生器と、この再生器で加熱されて液体から分離さ
れた冷媒蒸気を凝縮させる凝縮器と、上記再生器で冷媒
蒸気が分離されて薄くなった濃吸収液を吸収器に送る濃
吸収液移送管と、途中に溶液ポンプを有して上記吸収器
で薄くなった稀吸収液を再生器に送る稀吸収液移送管と
から構成されている。そして、この構成において、例え
ば冷凍サイクルを行う場合、冷媒の蒸発→吸収→再生→
凝縮というサイクルが行われていた。また、暖房サイク
ルを行う場合、再生器を作動させて外部からの熱媒を再
生器に導いて加熱していた。2. Description of the Related Art Conventionally, an absorption heat source device such as an absorption refrigerator or an absorption heat pump has an evaporator that evaporates a refrigerant (for example, water), and a refrigerant vapor that is evaporated by the evaporator as an absorbing liquid (bromination if it falls down). Lithium aqueous solution), an absorber, a regenerator that absorbs the refrigerant vapor in this absorber and heats the diluted absorption liquid that has become thin, and a refrigerant vapor that is heated in this regenerator and separated from the liquid. A condenser for condensing, a concentrated absorbent transfer pipe for sending the concentrated absorbent that has become thin due to the separation of the refrigerant vapor in the regenerator to the absorber, and a solution pump on the way It is composed of a rare absorbent transfer pipe for sending the absorbent to the regenerator. Then, in this configuration, for example, when performing a refrigeration cycle, evaporation of refrigerant → absorption → regeneration →
There was a cycle of condensation. Further, when performing the heating cycle, the regenerator is operated to guide the heat medium from the outside to the regenerator to heat it.
発明が解決しようとする課題 ところで、上記従来の構成によると、吸収液の吸収効
率が悪く、最近、吸収液に界面活性剤を使用することが
考えられている。しかし、上記従来の構成において、界
面活性剤を使用した場合、界面活性剤の沸点は吸収液よ
りも低く、したがって再生器で吸収液を加熱した場合、
先に界面活性剤が蒸発して凝縮器に入り、そして凝縮器
を介して蒸発器に導かれ、界面活性剤が蒸発器内に滞留
してしまうという問題が生じる。DISCLOSURE OF THE INVENTION Problems to be Solved by the Invention By the way, according to the above-described conventional configuration, the absorption efficiency of the absorbing liquid is poor, and recently, it has been considered to use a surfactant in the absorbing liquid. However, in the above conventional configuration, when a surfactant is used, the boiling point of the surfactant is lower than that of the absorbing liquid, and therefore, when the absorbing liquid is heated by the regenerator,
First, the surfactant evaporates and enters the condenser, and is guided to the evaporator through the condenser, which causes a problem that the surfactant stays in the evaporator.
そこで、本発明は上記課題を解消し得る吸収式熱源装
置を提供することを目的とする。Therefore, an object of the present invention is to provide an absorption heat source device that can solve the above problems.
課題を解決するための手段 上記課題を解決するため、本発明の吸収式熱源装置
は、冷媒を蒸発させる蒸発器と、この蒸発器で蒸発され
た冷媒蒸気を吸収液に吸収する吸収器と、この吸収器で
冷媒蒸気を吸収して濃度が薄くなった稀吸収液を加熱す
る再生器と、この再生器で加熱された気液混合状態の液
体から冷媒蒸気を分離する気液分離器と、この気液分離
器で分離された冷媒蒸気を凝縮させる凝縮器と、上記気
液分離器で冷媒蒸気が分離されて濃くなった濃吸収液を
吸収器に送る濃吸収液移送管と、途中に溶液ポンプを有
して上記吸収器で薄くなった稀吸収液を再生器に送る稀
吸収液移送管と、上記気液分離器で分離された冷媒蒸気
を凝縮器に移送する冷媒蒸気移送管と、上記凝縮器で凝
縮された冷媒液を上記蒸発器に移送する冷媒液移送管と
を具備した吸収式熱源装置において、上記冷媒蒸気移送
管途中に吸収液に添加された界面活性剤を凝縮させる界
面活性剤凝縮器を設けるとともに、上記稀吸収液移送管
の途中に、この界面活性剤凝縮器の伝熱管を介装して、
凝縮用の冷却熱源として稀吸収液を使用したものであ
る。Means for Solving the Problems In order to solve the above problems, the absorption heat source device of the present invention is an evaporator that evaporates a refrigerant, and an absorber that absorbs the refrigerant vapor evaporated in the evaporator into an absorption liquid, A regenerator that absorbs the refrigerant vapor in this absorber and heats the diluted absorption liquid that has become thin, and a gas-liquid separator that separates the refrigerant vapor from the liquid in a gas-liquid mixed state that is heated in this regenerator, A condenser for condensing the refrigerant vapor separated by this gas-liquid separator, a concentrated absorbent transfer pipe for sending the concentrated absorbent that has become thicker due to the refrigerant vapor separated by the gas-liquid separator to the absorber, and on the way A rare absorbent transfer pipe having a solution pump for sending the diluted absorbent diluted in the absorber to the regenerator, and a refrigerant vapor transfer pipe for transferring the refrigerant vapor separated by the gas-liquid separator to the condenser. , Refrigerant liquid transfer for transferring the refrigerant liquid condensed in the condenser to the evaporator In the absorption heat source device having a pipe, a surfactant condenser for condensing the surfactant added to the absorbing liquid is provided in the middle of the refrigerant vapor transfer pipe, and in the middle of the rare absorbent transfer pipe, Via the heat transfer tube of the surfactant condenser,
A rare absorption liquid is used as a cooling heat source for condensation.
作 用 上記の構成によると、気液分離器からの冷媒蒸気を凝
縮器に移送する冷媒蒸気移送管途中に界面活性剤凝縮器
が設けられているので、吸収液に界面活性剤が添加され
ていてもここで除去される。したがって、界面活性剤が
蒸発器内に滞留したり、あるいは蒸発器内に熱交換のた
めに導かれている他の熱媒に界面活性剤が混入するのを
防止することができる。Operation According to the above configuration, since the surfactant condenser is provided in the refrigerant vapor transfer pipe that transfers the refrigerant vapor from the gas-liquid separator to the condenser, the surfactant is added to the absorbing liquid. But it is removed here. Therefore, it is possible to prevent the surfactant from staying in the evaporator or from being mixed into another heat medium introduced into the evaporator for heat exchange.
実施例 以下、本発明の一実施例を第1図および第2図に基づ
き説明する。Embodiment An embodiment of the present invention will be described below with reference to FIGS. 1 and 2.
本実施例における吸収式熱源装置は、例えば室内機と
室外機とからなる冷暖房設備の室外機として使用される
ものについて説明する。The absorption heat source device according to the present embodiment will be described as one used as an outdoor unit of a cooling and heating facility including an indoor unit and an outdoor unit, for example.
第1図に示すように、この吸収式熱源装置は、冷媒を
蒸発させるとともに室内機(図示せず)からの熱源(例
えば水)を導いて両者の間で熱交換を行うすなわち熱媒
を冷却させる蒸発器1と、この蒸発器1で蒸発された冷
媒蒸気を連通部(例えば連通管)11を介して導入して吸
収液(例えば、臭化リチウムが使用されるとともに、そ
の吸収効率を高めるために界面活性剤が添加されてい
る)に吸収させる吸収器2と、この吸収器2で冷媒蒸気
を吸収して濃度が薄くなった稀吸収液を加熱する再生器
3と、この再生器3で加熱された気液混合状態の液体か
ら冷媒蒸気および界面活性剤の蒸気を分離させる気液分
離器4と、この気液分離器4で分離された冷媒蒸気を凝
縮させる空冷式の凝縮器5と、上記気液分離器4で冷媒
蒸気および界面活性剤の蒸気が分離されて濃くなった濃
吸収液を吸収器2に送る濃吸収液移送管12と、途中に溶
液ポンプ13を有して上記吸収器2で薄くなった稀吸収液
を再生器3に送る稀吸収液移送管14と、上記気液分離器
4で分離された冷媒蒸気および界面活性剤の蒸気を凝縮
器5側に移送する冷媒蒸気移送管15と、この冷媒蒸気移
送管15途中に設けられるとともに上記稀吸収液移送管14
途中に介装された伝熱管16を有して冷媒蒸気と一緒に蒸
発された界面活性剤の蒸気を凝縮させる界面活性剤凝縮
器17と、途中に冷媒ポンプ18を有するとともに上記凝縮
器5で凝縮された冷媒液を上記蒸発器1に移送する冷媒
液移送管19と、上記界面活性剤凝縮器17内で凝縮された
界面活性剤を濃吸収液吸収管12内に戻す界面活性剤戻し
管20と、上記濃吸収液移送管12と稀吸収液移送管14との
間に設けられて濃吸収液の持つ熱を稀吸収液に与えて熱
回収を行う熱交換器21とが具備されている。As shown in FIG. 1, this absorption heat source device evaporates a refrigerant and guides a heat source (for example, water) from an indoor unit (not shown) to perform heat exchange between the two, that is, to cool a heat medium. The evaporator 1 to be introduced and the refrigerant vapor evaporated in the evaporator 1 are introduced through the communication part (for example, communication pipe) 11 to use an absorbing liquid (for example, lithium bromide and improve its absorption efficiency). (For which a surfactant has been added in order to absorb it), a regenerator 3 that absorbs the refrigerant vapor in the absorber 2 and heats the dilute absorption liquid that has become thin, and this regenerator 3 A gas-liquid separator 4 that separates a refrigerant vapor and a surfactant vapor from a liquid in a gas-liquid mixed state that has been heated in step 1, and an air-cooled condenser 5 that condenses the refrigerant vapor separated in the gas-liquid separator 4. And refrigerant vapor and surfactant in the gas-liquid separator 4 The concentrated absorbent transfer pipe 12 for sending the concentrated absorbent, which has become thicker due to the separation of the vapor, to the absorber 2, and the solution pump 13 on the way, and the diluted absorbent thinned in the absorber 2 is supplied to the regenerator 3. The rare absorption liquid transfer pipe 14 to be sent, the refrigerant vapor transfer pipe 15 for transferring the refrigerant vapor and the surfactant vapor separated by the gas-liquid separator 4 to the condenser 5 side, and the refrigerant vapor transfer pipe 15 The rare absorbent transfer pipe 14 provided
A surfactant condenser 17 for condensing the vapor of the surfactant vaporized together with the refrigerant vapor by having a heat transfer tube 16 interposed on the way, and a refrigerant pump 18 on the way, and the condenser 5 A refrigerant liquid transfer pipe 19 for transferring the condensed refrigerant liquid to the evaporator 1, and a surfactant return pipe for returning the surfactant condensed in the surfactant condenser 17 into the concentrated absorbent absorbing pipe 12. 20 and a heat exchanger 21 provided between the concentrated absorption liquid transfer pipe 12 and the rare absorption liquid transfer pipe 14 for performing heat recovery by giving the heat of the concentrated absorption liquid to the rare absorption liquid. There is.
なお、この熱交換器21は界面活性剤戻し管20の接続箇
所よりも上流側に配置されており、また上記界面活性剤
戻し管20の濃吸収液移送管12への接続箇所は、熱交換器
21よりも下流側の比較的温度が低い箇所とされている。The heat exchanger 21 is arranged upstream of the connection point of the surfactant return pipe 20, and the connection point of the surfactant return pipe 20 to the concentrated absorbent transfer pipe 12 is heat exchange. vessel
It is said that the temperature is relatively lower on the downstream side than 21.
上記構成により例えば冷房運転が行われる場合、蒸発
器1で蒸発された冷媒蒸気は吸収器2に導かれ、ここで
界面活性剤が添加された吸収液に効率良く吸収される。
冷媒蒸気を吸収して濃度が薄くなった稀吸収液は再生器
3に導かれて加熱される。なお、この再生器3では、界
面活性剤も加熱されるため、冷媒蒸気とともに界面活性
剤の蒸気も発生する。したがって、気液分離器4で分離
された冷媒蒸気には、界面活性剤の蒸気も含まれてお
り、これらの蒸気は界面活性剤凝縮器17内に導かれ、こ
こで稀吸収液によって冷却される。この界面活性剤凝縮
器17では、第2図に示すように、冷媒すなわち水の凝縮
温度C点よりも高い温度B点で凝縮させるようにしてい
るため、この時の界面活性剤の濃度はA点となり、水の
濃度は非常に薄くなる。したがって、界面活性剤の濃度
が濃い状態となり、界面活性剤の回収を充分に行うこと
ができる。With the above configuration, for example, when the cooling operation is performed, the refrigerant vapor evaporated in the evaporator 1 is guided to the absorber 2 where it is efficiently absorbed by the absorbent to which the surfactant has been added.
The rare absorption liquid, which has absorbed the refrigerant vapor and becomes thin in concentration, is guided to the regenerator 3 and heated. In the regenerator 3, since the surfactant is also heated, the vapor of the surfactant is generated together with the refrigerant vapor. Therefore, the refrigerant vapor separated by the gas-liquid separator 4 also contains the vapor of the surfactant, and these vapors are guided into the surfactant condenser 17 where they are cooled by the rare absorption liquid. It In the surfactant condenser 17, as shown in FIG. 2, the refrigerant, that is, water is condensed at a temperature B point higher than the condensation point C. Therefore, the concentration of the surfactant at this time is A. It becomes a point, and the concentration of water becomes very thin. Therefore, the concentration of the surfactant becomes high, and the surfactant can be sufficiently recovered.
そして、界面活性剤が除去された冷媒蒸気は凝縮器5
内に入りここで凝縮されて冷媒液となり、冷媒液移送管
19を介して蒸発器1に循環移送される。一方、界面活性
剤凝縮器17で凝縮された界面活性剤は、界面活性剤戻し
管20を介して気液分離器4からの濃吸収液移送管12途中
に混入されて循環使用される。The refrigerant vapor from which the surfactant has been removed is condensed by the condenser 5
Enters inside and is condensed here to become a refrigerant liquid, and the refrigerant liquid transfer pipe
It is circulated and transferred to the evaporator 1 via 19. On the other hand, the surfactant condensed in the surfactant condenser 17 is mixed with the concentrated absorbent transfer pipe 12 from the gas-liquid separator 4 through the surfactant return pipe 20 and is circulated.
このように、界面活性剤が界面活性剤凝縮器17で回収
されるため、運転につれて界面活性剤が室内機との熱交
換用の熱媒に混入するのを防止することができるととも
に、界面活性剤の濃度が薄くなるのを防止することがで
きる。In this way, since the surfactant is recovered by the surfactant condenser 17, it is possible to prevent the surfactant from being mixed in the heat medium for heat exchange with the indoor unit as the operation proceeds, and the surfactant It is possible to prevent the concentration of the agent from decreasing.
また、濃吸収液からの稀吸収液への熱回収は界面活性
剤凝縮器17内を出た後で行われているため、界面活性剤
の凝縮熱も無駄にならず、したがって設備全体の熱効率
を向上させることができる。Further, the heat recovery from the concentrated absorption liquid to the rare absorption liquid is performed after leaving the inside of the surfactant condenser 17, so that the condensation heat of the surfactant is not wasted, and therefore the thermal efficiency of the entire facility is improved. Can be improved.
発明の効果 以上のように本発明の構成によると、気液分離器から
の冷媒蒸気を凝縮器に移送する冷媒蒸気移送管途中に界
面活性剤凝縮器を設けたので、吸収液に界面活性剤を添
加させても、界面活性剤が蒸発器内に滞留したり、ある
いは蒸発器内に熱交換のために導かれている他の熱媒に
界面活性剤が混入するのを防止することができる。As described above, according to the configuration of the present invention, since the surfactant condenser is provided in the middle of the refrigerant vapor transfer pipe that transfers the refrigerant vapor from the gas-liquid separator to the condenser, the surfactant is added to the absorbing liquid. Even if added, it is possible to prevent the surfactant from staying in the evaporator or from being mixed with other heat medium introduced into the evaporator for heat exchange. .
また、界面活性剤凝縮器の冷却熱源として、稀吸収液
を使用しているので、例えば強制的に凝縮させない場合
に比べて、その凝縮効果が大きい。Further, since the rare absorption liquid is used as the cooling heat source of the surfactant condenser, the condensation effect is large as compared with the case where the condensation is not forcedly conducted.
図面は本発明の一実施例を示すもので、第1図は吸収式
熱源装置の概略構成を示す図、第2図は水の沸点曲線お
よび界面活性剤の凝縮曲線を示すグラフ図である。 1……蒸発器、2……吸収器、3……再生器、4……気
液分離器、5……凝縮器、12……濃吸収液移送管、13…
…溶液ポンプ、14……稀吸収液移送管、15……冷媒蒸気
移送管、17……界面活性剤凝縮器、20……界面活性剤戻
し管、21……熱交換器。The drawings show one embodiment of the present invention. FIG. 1 is a diagram showing a schematic configuration of an absorption heat source device, and FIG. 2 is a graph showing a boiling point curve of water and a condensation curve of a surfactant. 1 ... Evaporator, 2 ... Absorber, 3 ... Regenerator, 4 ... Gas-liquid separator, 5 ... Condenser, 12 ... Concentrated absorbent transfer pipe, 13 ...
… Solution pump, 14 …… Diluted absorption liquid transfer pipe, 15 …… Refrigerant vapor transfer pipe, 17 …… Surfactant condenser, 20 …… Surfactant return pipe, 21 …… Heat exchanger.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 三宅 一幸 大阪府大阪市此花区西九条5丁目3番28号 日立造船株式会社内 (72)発明者 八木 崇晴 大阪府大阪市此花区西九条5丁目3番28号 日立造船株式会社内 (72)発明者 安部 春雄 大阪府大阪市此花区西九条5丁目3番28号 日立造船株式会社内 (72)発明者 古川 哲郎 大阪府大阪市此花区西九条5丁目3番28号 日立造船株式会社内 (72)発明者 梅田 辰彦 大阪府大阪市此花区西九条5丁目3番28号 日立造船株式会社内 (72)発明者 矢野 猛 大阪府大阪市此花区西九条5丁目3番28号 日立造船株式会社内 (56)参考文献 特開 平3−25258(JP,A) 特開 昭52−1552(JP,A) 特開 昭63−201460(JP,A) ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Kazuyuki Miyake 5-3 28 Nishi Kujo, Konohana-ku, Osaka City, Osaka Prefecture Hitachi Shipbuilding Co., Ltd. (72) Takaharu Yagi 5-9, Nishikujo, Konohana-ku, Osaka City, Osaka Prefecture Hitachi Shipbuilding Co., Ltd. 3-28 (72) Inventor Haruo Abe 5-3-8 Nishikujo, Konohana-ku, Osaka City, Osaka Prefecture (3) Hitachi Shipbuilding Co., Ltd. (72) Tetsuro Furukawa Nishikujo, Konohana-ku, Osaka City, Osaka Prefecture 5-3 28 Hitachi Shipbuilding Co., Ltd. (72) Inventor Tatsuhiko Umeda Nishikojo 5-3 28 Nishikojo, Konohana-ku, Osaka City Osaka Prefecture (72) Inventor Takeshi Yano Konohana-ku, Osaka City, Osaka Prefecture Nishikujo 5-chome 3-28 Hitachi Shipbuilding Co., Ltd. (56) Reference JP-A-3-25258 (JP, A) JP-A 52-1552 (JP, A) JP-A 63-201460 (JP, A) )
Claims (1)
蒸発された冷媒蒸気を吸収液に吸収する吸収器と、この
吸収器で冷媒蒸気を吸収して濃度が薄くなった稀吸収液
を加熱する再生器と、この再生器で加熱された気液混合
状態の液体から冷媒蒸気を分離する気液分離器と、この
気液分離器で分離された冷媒蒸気を凝縮させる凝縮器
と、上記気液分離器で冷媒蒸気が分離されて濃くなった
濃吸収液を吸収器に送る濃吸収液移送管と、途中に溶液
ポンプを有して上記吸収器で薄くなった稀吸収液を再生
器に送る稀吸収液移送管と、上記気液分離器で分離され
た冷媒蒸気を凝縮器に移送する冷媒蒸気移送管と、上記
凝縮器で凝縮された冷媒液を上記蒸発器に移送する冷媒
液移送管とを具備した吸収式熱源装置において、上記冷
媒蒸気移送管途中に吸収液に添加された界面活性剤を凝
縮させる界面活性剤凝縮器を設けるとともに、上記稀吸
収液移送管の途中に、この界面活性剤凝縮器の伝熱管を
介装して、凝縮用の冷却熱源として稀吸収液を使用した
ことを特徴とする吸収式熱源装置。1. An evaporator for evaporating a refrigerant, an absorber for absorbing a refrigerant vapor evaporated by the evaporator into an absorbing liquid, and a rare absorbing liquid having a thin concentration by absorbing the refrigerant vapor by the absorber. A regenerator for heating, a gas-liquid separator for separating the refrigerant vapor from the liquid in a gas-liquid mixed state heated by the regenerator, and a condenser for condensing the refrigerant vapor separated by the gas-liquid separator, The concentrated absorbent transfer pipe that sends the concentrated absorbent that has become thicker due to the separation of the refrigerant vapor in the gas-liquid separator to the absorber and the solution pump in the middle to regenerate the diluted absorbent that has become thinner in the absorber. Absorption liquid transfer pipe for sending to the condenser, refrigerant vapor transfer pipe for transferring the refrigerant vapor separated by the gas-liquid separator to the condenser, and refrigerant for transferring the refrigerant liquid condensed by the condenser to the evaporator In an absorption heat source device equipped with a liquid transfer pipe, in the middle of the refrigerant vapor transfer pipe A surfactant condenser for condensing the surfactant added to the collected liquid is provided, and a heat transfer pipe of this surfactant condenser is provided in the middle of the dilute absorption liquid transfer pipe to cool it for condensation. An absorption type heat source device characterized by using a dilute absorption liquid as a heat source.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2144119A JPH0823456B2 (en) | 1990-05-31 | 1990-05-31 | Absorption heat source device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2144119A JPH0823456B2 (en) | 1990-05-31 | 1990-05-31 | Absorption heat source device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0436556A JPH0436556A (en) | 1992-02-06 |
| JPH0823456B2 true JPH0823456B2 (en) | 1996-03-06 |
Family
ID=15354637
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2144119A Expired - Lifetime JPH0823456B2 (en) | 1990-05-31 | 1990-05-31 | Absorption heat source device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0823456B2 (en) |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2695923B2 (en) * | 1989-06-23 | 1998-01-14 | 東京瓦斯株式会社 | Air-cooled absorption chiller / heater |
-
1990
- 1990-05-31 JP JP2144119A patent/JPH0823456B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0436556A (en) | 1992-02-06 |
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