JPH0829038A - Heating and cooling device - Google Patents

Heating and cooling device

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Publication number
JPH0829038A
JPH0829038A JP18672194A JP18672194A JPH0829038A JP H0829038 A JPH0829038 A JP H0829038A JP 18672194 A JP18672194 A JP 18672194A JP 18672194 A JP18672194 A JP 18672194A JP H0829038 A JPH0829038 A JP H0829038A
Authority
JP
Japan
Prior art keywords
refrigerant
tank
ejector
cooling
heating
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP18672194A
Other languages
Japanese (ja)
Other versions
JP3210997B2 (en
Inventor
Takayuki Morii
高之 森井
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.)
TLV Co Ltd
Original Assignee
TLV Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by TLV Co Ltd filed Critical TLV Co Ltd
Priority to JP18672194A priority Critical patent/JP3210997B2/en
Publication of JPH0829038A publication Critical patent/JPH0829038A/en
Application granted granted Critical
Publication of JP3210997B2 publication Critical patent/JP3210997B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

PURPOSE:To obtain a heating and cooling device capable of maintaining the temperature of evaporating and cooling with a high accuracy by preventing the change of concentration of a refrigerant and capable of effecting heating treatment also. CONSTITUTION:A steam pipe 16 is connected to the jacket unit 5 of a reaction oven 21. The ejector 9 of a combination pump 22 is connected to the jacket unit 5. A first tank reserving a refrigerant, and a second tank 2 reserving cooling water, are arranged. The ejector 9, the tanks 1, 2 and a circulation pump 30 are communicated with each other. A supplemental water supplying passage 8 and the ejector 9 are connected to the first tank 1.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、被熱処理物を冷却した
りあるいは加熱するものに関し、特に熱交換室内を減圧
状態にして供給した冷媒でもって被冷却物を気化冷却す
ると共に、加熱処理もできるものに関する。具体的に
は、各種反応を行う反応釜や食品、医療品や合成繊維等
の加熱冷却装置に関する。これらの被熱処理物は少しの
温度変化によって熱損傷を起こす場合が多くあり、従っ
て、温度を精度良く維持する必要があった。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a device for cooling or heating an object to be heat-treated, and more particularly to evaporating and cooling the object to be cooled with a refrigerant supplied in a decompressed state of a heat exchange chamber and performing heat treatment. Regarding what you can do. Specifically, it relates to a reactor for performing various reactions, a heating / cooling device for foods, medical products, synthetic fibers and the like. These heat-treated objects often cause thermal damage due to slight changes in temperature, and therefore it was necessary to maintain the temperature with high accuracy.

【0002】[0002]

【従来の技術】従来の冷媒による気化冷却装置として
は、例えば特開平5−106953号公報に示されたも
のがある。これは、エゼクタとタンクと循環ポンプを組
み合わせた組み合わせポンプと、エゼクタと連通した熱
交換室と、組み合わせポンプ内を循環する冷媒液を熱交
換室に供給する冷媒液供給通路とから成るもので、冷媒
を用いることにより急冷を行うことができ、被熱処理物
の熱損傷を防止することができるものである。
2. Description of the Related Art As a conventional evaporative cooling device using a refrigerant, there is one shown in, for example, Japanese Patent Laid-Open No. 106953/1993. This consists of a combination pump that combines an ejector, a tank, and a circulation pump, a heat exchange chamber that communicates with the ejector, and a refrigerant liquid supply passage that supplies the refrigerant liquid circulating in the combination pump to the heat exchange chamber. By using a refrigerant, rapid cooling can be performed and heat damage to the heat-treated object can be prevented.

【0003】[0003]

【本発明が解決しようとする課題】上記従来のもので
は、時間の経過と共に冷媒の濃度が変化することによ
り、気化冷却の温度を精度良く維持することができない
問題があった。通常、冷媒は水等により希釈して所望の
濃度にして使用するのであるが、使用期間を経ると共に
水が蒸発して冷媒の濃度が濃くなったり、あるいは反対
に水が混入して冷媒の濃度が薄くなったりしてしまうた
めである。冷媒の濃度が変化すると、同じ圧力状態であ
っても冷媒の気化温度あるいは気化量が変化して気化冷
却の温度も変化してしまうのである。
The above-mentioned conventional device has a problem that the temperature of the evaporative cooling cannot be accurately maintained because the concentration of the refrigerant changes with the passage of time. Usually, the refrigerant is diluted with water etc. to a desired concentration and used, but over the period of use, water evaporates and the concentration of the refrigerant becomes thicker, or conversely water is mixed and the concentration of the refrigerant becomes The reason is that it becomes thin. When the concentration of the refrigerant changes, the vaporization temperature or vaporization amount of the refrigerant changes even under the same pressure state, and the temperature of vaporization cooling also changes.

【0004】また上記従来のものでは、気化冷却に変え
て加熱処理を行うことができない問題があった。反応釜
や食品等においては冷却と加熱を交互に行なわなければ
ならない場合が多々あるのである。
Further, in the above-mentioned conventional one, there is a problem that the heat treatment cannot be performed in place of the evaporative cooling. In many cases, it is necessary to alternately cool and heat the reaction kettle and food.

【0005】従って本発明の技術的課題は、気化冷却と
共に加熱処理ができ、且つ、冷媒の濃度の変化を防止し
て気化冷却の温度を精度良く維持することのできる加熱
冷却装置を得ることである。
Therefore, a technical object of the present invention is to obtain a heating / cooling device which can perform heat treatment together with evaporative cooling, and can prevent the change in the concentration of the refrigerant and maintain the evaporative cooling temperature with high accuracy. is there.

【0006】[0006]

【課題を解決する為の手段】本発明の加熱冷却装置の構
成は次の通りである。エゼクタとタンクと循環ポンプを
組み合わせた組み合わせポンプと、該エゼクタと連通し
た熱交換室と、組み合わせポンプ内を循環する冷媒液を
上記熱交換室に供給する冷媒液供給通路とから成るもの
において、タンクとして冷媒を溜置く第1のタンクと冷
却水を溜置く第2のタンクを設け、該第1のタンクに補
給水供給通路または減圧吸引手段を設けると共に、上記
熱交換室に加熱流体供給通路を接続したものである。
The constitution of the heating / cooling device of the present invention is as follows. A tank comprising a combination pump combining an ejector, a tank, and a circulation pump, a heat exchange chamber communicating with the ejector, and a refrigerant liquid supply passage for supplying a refrigerant liquid circulating in the combination pump to the heat exchange chamber. A first tank for storing the refrigerant and a second tank for storing the cooling water are provided, a makeup water supply passage or a decompression suction means is provided in the first tank, and a heating fluid supply passage is provided in the heat exchange chamber. It is connected.

【0007】[0007]

【作用】冷媒を溜置く第1のタンクに補給水供給通路ま
たは減圧吸引手段を設けたことにより、冷媒の濃度が濃
くなれば補給水供給通路から水を補給することによって
冷媒濃度を薄めて所望の濃度とすることができ、反対に
冷媒の濃度が薄くなると減圧吸引手段により冷媒中の水
分を減圧吸引することによって冷媒濃度を濃くすること
ができる。
By providing the make-up water supply passage or the decompression suction means in the first tank for storing the refrigerant, if the concentration of the refrigerant becomes high, the water is replenished from the make-up water supply passage to dilute the refrigerant concentration to a desired value. On the contrary, when the concentration of the refrigerant becomes low, the decompression suction unit decompresses the water in the refrigerant under reduced pressure to increase the concentration of the refrigerant.

【0008】熱交換室に加熱流体供給通路を接続したこ
とにより、気化冷却に変えて加熱流体を供給して被熱処
理物を加熱処理することもできる。
By connecting the heating fluid supply passage to the heat exchange chamber, it is possible to heat the object to be heat treated by supplying the heating fluid instead of evaporative cooling.

【0009】[0009]

【実施例】図示の実施例を詳細に説明する。本実施例に
おいては、加熱冷却装置として反応釜を用いた例を示
す。熱交換室としてのジャケット部5を備えた反応釜2
1と、組み合わせポンプ22と第1のタンク1と第2の
タンク2と、補給水供給通路8と減圧吸引手段としての
エゼクタ9、及び、加熱流体供給通路としての蒸気管1
6とで加熱冷却装置を構成する。蒸気管16には圧力制
御弁61と開閉弁62を取り付ける。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The illustrated embodiment will be described in detail. In this embodiment, an example in which a reaction kettle is used as the heating / cooling device is shown. Reactor 2 with jacket 5 as heat exchange chamber
1, a combination pump 22, a first tank 1, a second tank 2, a makeup water supply passage 8, an ejector 9 as a decompression suction means, and a steam pipe 1 as a heating fluid supply passage.
6 and 6 constitute a heating / cooling device. A pressure control valve 61 and an opening / closing valve 62 are attached to the steam pipe 16.

【0010】組み合わせポンプ22は循環ポンプ30と
エゼクタ9、及び、第1のタンク1と第2のタンク2と
で構成する。タンク1,2と循環ポンプ30の吸込側を
接続し、循環ポンプ30の吐出側をエゼクタ9のノズル
33に接続し、エゼクタ9のディフュ―ザ34をタンク
1,2の上部空間に弁3,4を介して接続した構成のも
のであり、エゼクタ9とジャケット部5とが弁10を介
して接続されている。この組み合わせポンプ22は、循
環ポンプ30の作動によりタンク1または2内の流体を
エゼクタ9に供給して吸引作用させ、タンク1または2
に戻すようになっている。また、循環ポンプ30から吐
出された流体の一部は、弁11からジャケット部5へ供
給されるようになっている。
The combination pump 22 comprises a circulation pump 30, an ejector 9, and a first tank 1 and a second tank 2. The tanks 1 and 2 are connected to the suction side of the circulation pump 30, the discharge side of the circulation pump 30 is connected to the nozzle 33 of the ejector 9, and the diffuser 34 of the ejector 9 is connected to the upper space of the tanks 1 and 2 by the valve 3, 4 and the ejector 9 and the jacket portion 5 are connected via the valve 10. The combination pump 22 supplies the fluid in the tank 1 or 2 to the ejector 9 by the operation of the circulation pump 30 to cause the ejector 9 to perform suction action, and
It is supposed to return to. A part of the fluid discharged from the circulation pump 30 is supplied from the valve 11 to the jacket portion 5.

【0011】第1のタンク1内には冷媒を溜置く。冷媒
は従来より用いられているものを冷却温度に応じて濃度
と共に適宜選定するものとする。第1のタンク1の上部
に補給水供給通路8を接続すると共に、弁6と管路7を
介してエゼクタ9のノズル33と接続する。第1のタン
ク1内の下部にタンク内の冷媒を冷却するための冷却手
段28を設ける。冷却手段28は、タンク1内に設けた
螺旋状の冷却パイプ18と、冷却流体を供給する弁12
とで構成する。冷却流体としては、被冷却物の温度にも
よるが、水や冷媒や更に低温冷媒等を用いることができ
る。第1のタンク1の下部と循環ポンプ30とを管路2
0と弁59により接続する。
Refrigerant is stored in the first tank 1. As the refrigerant, one conventionally used together with the concentration should be appropriately selected according to the cooling temperature. The makeup water supply passage 8 is connected to the upper portion of the first tank 1, and is connected to the nozzle 33 of the ejector 9 via the valve 6 and the pipe 7. Cooling means 28 for cooling the refrigerant in the tank is provided in the lower part of the first tank 1. The cooling means 28 includes a spiral cooling pipe 18 provided in the tank 1 and a valve 12 for supplying a cooling fluid.
It consists of and. As the cooling fluid, water, a refrigerant, a low temperature refrigerant, or the like can be used, depending on the temperature of the object to be cooled. The lower part of the first tank 1 and the circulation pump 30 are connected to each other through the conduit 2
0 and valve 59 are connected.

【0012】第1のタンク1内の上部には、蒸気管16
を分岐して弁55と管路56を介して接続した蒸気加熱
管23を設ける。蒸気加熱管23の出口側は弁14と管
路15を介してエゼクタ9のノズル33と接続する。こ
の蒸気加熱管23はタンク1内の冷媒を加熱して水分を
蒸発させる場合に用いるものである。
At the top of the first tank 1, a steam pipe 16
Is provided and the steam heating pipe 23 connected to the valve 55 via the pipe 56 is provided. The outlet side of the steam heating pipe 23 is connected to the nozzle 33 of the ejector 9 via the valve 14 and the pipe 15. The steam heating pipe 23 is used when the refrigerant in the tank 1 is heated to evaporate water.

【0013】第2のタンク2内には冷却水を溜置く。タ
ンク2の上部に弁57を介して冷却水供給通路58を接
続する。タンク2の下部は管路32と弁60を介して循
環ポンプ30と接続する。
Cooling water is stored in the second tank 2. A cooling water supply passage 58 is connected to the upper portion of the tank 2 via a valve 57. The lower part of the tank 2 is connected to the circulation pump 30 via a pipe 32 and a valve 60.

【0014】第1のタンク1に冷媒そのものを補給する
ための冷媒補給管50を弁51を介して連通する。これ
は装置からの洩れ等により冷媒が減少した場合に補給を
行うためのものである。
A refrigerant supply pipe 50 for supplying the refrigerant itself to the first tank 1 is connected via a valve 51. This is for replenishing when the refrigerant decreases due to leakage from the device.

【0015】次に作用を説明する。反応釜21を冷却す
る場合、即ちジャケット部5で気化冷却を行う場合、弁
59,3,11を開弁し弁60,4を閉弁し循環ポンプ
30を駆動して第1のタンク1内の冷媒をエゼクタ9に
供給する。エゼクタ9部で生じる吸引力により、ジャケ
ット部5内も減圧状態となり、供給された冷媒は反応釜
21の熱により気化し、反応釜21を気化冷却する。気
化した冷媒の蒸気及び気化しきれなかった冷媒は弁10
を通り、エゼクタ9に吸引され弁3を経て第1のタンク
1に至る。
Next, the operation will be described. When the reaction vessel 21 is cooled, that is, when evaporative cooling is performed by the jacket portion 5, the valves 59, 3 and 11 are opened, the valves 60 and 4 are closed, and the circulation pump 30 is driven to drive the inside of the first tank 1. The refrigerant is supplied to the ejector 9. Due to the suction force generated in the ejector 9 part, the inside of the jacket part 5 is also in a depressurized state, and the supplied refrigerant is vaporized by the heat of the reaction kettle 21 and evaporatively cools the reaction kettle 21. The vapor of the vaporized refrigerant and the refrigerant that has not been vaporized are stored in the valve 10
Through the ejector 9 to the first tank 1 through the valve 3.

【0016】タンク1に至った冷媒液は、弁12から供
給される冷却流体によって冷却され所望温度となって循
環ポンプ30に吸引される。冷媒液の温度は冷却流体供
給量または温度を調節することによりコントロ―ルする
ことができる。
The refrigerant liquid reaching the tank 1 is cooled by the cooling fluid supplied from the valve 12 to reach a desired temperature and is sucked into the circulation pump 30. The temperature of the refrigerant liquid can be controlled by adjusting the cooling fluid supply amount or temperature.

【0017】第1のタンク1内の冷媒の濃度が濃くなっ
た場合は、補給水供給通路8から水を補給することによ
り冷媒濃度を薄くすることができ、あるいは、冷媒濃度
が所望値よりも薄くなると弁6を開弁してエゼクタ9の
吸引力により、タンク1内を減圧して水分が蒸発しやす
くすることによって水分を優先的に気化して吸引し、冷
媒濃度を濃くすることができる。この場合ディフュ―ザ
34を出た流体はタンク1へ戻すことなく、弁63から
系外へ排除する。通常、冷媒の蒸発温度は水よりも高い
ために、水分を優先的に蒸発させ吸引することができる
のである。
When the concentration of the refrigerant in the first tank 1 becomes high, the refrigerant concentration can be made low by replenishing water from the makeup water supply passage 8, or the refrigerant concentration is lower than a desired value. When the valve becomes thin, the valve 6 is opened and the suction force of the ejector 9 is used to reduce the pressure in the tank 1 to facilitate the evaporation of the water, whereby the water is preferentially vaporized and sucked, so that the refrigerant concentration can be increased. . In this case, the fluid discharged from the diffuser 34 is discharged from the valve 63 to the outside of the system without returning to the tank 1. Usually, since the evaporation temperature of the refrigerant is higher than that of water, the water can be preferentially evaporated and sucked.

【0018】タンク1内に設けた蒸気加熱管23に蒸気
を通過させて、冷媒液を加熱することにより、冷媒中の
水の蒸発を助長してエゼクタ9で吸引することができ
る。
By passing the steam through the steam heating pipe 23 provided in the tank 1 to heat the refrigerant liquid, evaporation of water in the refrigerant can be promoted and sucked by the ejector 9.

【0019】冷媒による気化冷却に変えて反応釜21を
加熱する場合は、弁59,3,11,14,6を閉弁し
弁4,62を開弁して蒸気管16から加熱蒸気をジャケ
ット部5へ供給すると共に、循環ポンプ30とエゼクタ
9と第2のタンク2とを連通させる。エゼクタ9には第
2のタンク2からの冷却水を供給することにより吸引力
を生じてジャケット部5内を減圧状態にし、100度C
前後の比較的低温度で反応釜21を加熱することができ
る。
When heating the reaction vessel 21 instead of evaporative cooling with a refrigerant, the valves 59, 3, 11, 14, 6 are closed and the valves 4, 62 are opened to jacket the heating steam from the steam pipe 16. The circulation pump 30, the ejector 9, and the second tank 2 are communicated with each other while being supplied to the unit 5. By supplying the cooling water from the second tank 2 to the ejector 9, a suction force is generated and the inside of the jacket portion 5 is depressurized to 100 ° C.
The reaction kettle 21 can be heated at a relatively low temperature before and after.

【0020】反応釜21を加熱して凝縮した蒸気の復水
は弁10を経てエゼクタ9に吸引され第2のタンク2へ
至る。蒸気で加熱する場合の温度は、ジャケット部5へ
供給する蒸気の圧力すなわち温度を圧力制御弁61で調
節すると共に、エゼクタ9の吸引力を通過する冷却水の
温度を調整することにより適宜行うことができる。
Condensed water of the steam which is heated and condensed in the reaction kettle 21 is sucked by the ejector 9 through the valve 10 and reaches the second tank 2. The temperature in the case of heating with steam is appropriately adjusted by adjusting the pressure of steam supplied to the jacket portion 5, that is, the temperature with the pressure control valve 61, and adjusting the temperature of the cooling water passing through the suction force of the ejector 9. You can

【0021】本実施例においては、減圧吸引手段として
組み合わせポンプ22のエゼクタ9を用いた例を示した
が、その他、組み合わせポンプ22以外の別途の吸引手
段を用いることもできる。
In this embodiment, the ejector 9 of the combination pump 22 is used as the decompression suction means, but other suction means other than the combination pump 22 may be used.

【0022】[0022]

【発明の効果】冷媒を溜置く第1のタンクに補給水供給
通路または減圧吸引手段を設けて、冷媒の濃度が濃くな
れば水を補給して冷媒濃度を薄め、反対に冷媒濃度が薄
くなれば冷媒中の水分を減圧吸引手段で吸引して冷媒濃
度を濃くすることにより、冷媒の濃度の変化を防止する
ことができ、従って、気化冷却の温度を精度良く維持す
ることができる。
The first tank for storing the refrigerant is provided with a makeup water supply passage or a decompression suction means so that when the concentration of the refrigerant becomes thicker, water is replenished to dilute the refrigerant concentration, and conversely the refrigerant concentration becomes thinner. For example, it is possible to prevent the change in the concentration of the refrigerant by sucking the water in the refrigerant with the decompression suction means to increase the concentration of the refrigerant, and therefore, it is possible to maintain the temperature of the evaporative cooling with high accuracy.

【0023】冷媒中の水分を減圧吸引手段で減圧して吸
引することにより、冷媒の温度を必要以上に高くするこ
とがなく、従って、高温になると変質しやすい冷媒であ
っても低温度の状態で水分を除去することができる。
By depressurizing and sucking the water in the refrigerant by the depressurizing suction means, the temperature of the refrigerant is not raised more than necessary, and therefore, even if the refrigerant is liable to be deteriorated at a high temperature, it is in a low temperature state. Water can be removed with.

【0024】熱交換室に加熱流体供給通路を接続したこ
とにより、冷媒による気化冷却に変えて被熱処理物を加
熱処理することもできる。
By connecting the heating fluid supply passage to the heat exchange chamber, it is possible to heat the object to be heat-treated in place of evaporative cooling with a refrigerant.

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

【図1】本発明の加熱冷却装置の実施例の構成図であ
る。
FIG. 1 is a configuration diagram of an embodiment of a heating / cooling device of the present invention.

【符号の説明】[Explanation of symbols]

1 第1のタンク 2 第2のタンク 5 ジャケット部 8 補給水供給通路 9 エゼクタ 16 蒸気管 18 冷却パイプ 21 反応釜 22 組み合わせポンプ 23 蒸気加熱管 30 循環ポンプ 1 1st tank 2 2nd tank 5 Jacket part 8 Makeup water supply passage 9 Ejector 16 Steam pipe 18 Cooling pipe 21 Reactor pot 22 Combined pump 23 Steam heating pipe 30 Circulation pump

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 エゼクタとタンクと循環ポンプを組み合
わせた組み合わせポンプと、該エゼクタと連通した熱交
換室と、組み合わせポンプ内を循環する冷媒液を上記熱
交換室に供給する冷媒液供給通路とから成るものにおい
て、タンクとして冷媒を溜置く第1のタンクと冷却水を
溜置く第2のタンクを設け、該第1のタンクに補給水供
給通路または減圧吸引手段を設けると共に、上記熱交換
室に加熱流体供給通路を接続したことを特徴とする加熱
冷却装置。
1. A combination pump including an ejector, a tank, and a circulation pump, a heat exchange chamber communicating with the ejector, and a refrigerant liquid supply passage for supplying a refrigerant liquid circulating in the combination pump to the heat exchange chamber. According to the present invention, a first tank for storing refrigerant as a tank and a second tank for storing cooling water are provided, and a makeup water supply passage or a vacuum suction means is provided in the first tank, and the heat exchange chamber is provided with A heating / cooling device characterized in that a heating fluid supply passage is connected.
JP18672194A 1994-07-15 1994-07-15 Heating and cooling device Expired - Fee Related JP3210997B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18672194A JP3210997B2 (en) 1994-07-15 1994-07-15 Heating and cooling device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18672194A JP3210997B2 (en) 1994-07-15 1994-07-15 Heating and cooling device

Publications (2)

Publication Number Publication Date
JPH0829038A true JPH0829038A (en) 1996-02-02
JP3210997B2 JP3210997B2 (en) 2001-09-25

Family

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Family Applications (1)

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JP18672194A Expired - Fee Related JP3210997B2 (en) 1994-07-15 1994-07-15 Heating and cooling device

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JP (1) JP3210997B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6482141B1 (en) 2001-07-25 2002-11-19 Spencer Johnston Company Flexible end supporting arrangement for direct drive adjustable spreader rolls

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JP3210997B2 (en) 2001-09-25

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