JPH0477224B2 - - Google Patents
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- Publication number
- JPH0477224B2 JPH0477224B2 JP2154887A JP2154887A JPH0477224B2 JP H0477224 B2 JPH0477224 B2 JP H0477224B2 JP 2154887 A JP2154887 A JP 2154887A JP 2154887 A JP2154887 A JP 2154887A JP H0477224 B2 JPH0477224 B2 JP H0477224B2
- Authority
- JP
- Japan
- Prior art keywords
- heat
- wall surface
- workpiece
- cooling
- temperature
- 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
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- Devices That Are Associated With Refrigeration Equipment (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
- Devices For Use In Laboratory Experiments (AREA)
Description
【発明の詳細な説明】
産業上の利用分野
本発明は容器等の被処理物保持体の壁面を介し
て壁面内の被処理物を冷却する冷却装置に関す
る。DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to a cooling device for cooling a workpiece within a wall surface of a workpiece holder such as a container through a wall surface of the workpiece holder.
従来の技術
容器に保有された被処理物を所定温度あるいは
所定温度以下に冷却したり、化学反応、溶解、希
釈等の、化学的物理的操作によつて被処理物から
発生する熱量を除去して、被処理物の温度を一定
にコントロールする操作が各種工業において広く
行われている。BACKGROUND TECHNOLOGY Heat generated from the processed material is removed by cooling the processed material held in a container to a predetermined temperature or below a predetermined temperature, or through chemical and physical operations such as chemical reaction, dissolution, and dilution. Therefore, operations for controlling the temperature of a processed material to a constant level are widely practiced in various industries.
この場合、冷却あるいは除熱の方法として、容
器周囲に設けたジヤケツトや容器内部に設けたコ
イル等の熱交換装置に、容器内の被処理物の温度
より低い温度の熱媒体(被処理物の温度や冷却温
度に応じて、有機冷媒、無機冷媒、冷水、冷却
水、温水、水蒸気、有機熱媒体等の各種熱媒体の
うち、目的に合致した種類が選ばれる。)を容器
外部の熱媒体設備によつて供給し、高温の容器内
被処理物から低温の熱媒体への熱移動により、容
器内被処理物の温度を下げることが一般に行われ
ている。さらに一定の所定温度にコントロールす
る場合には、容器内被処理物の温度を測定し、こ
の測定値と前記所定温度との差に応じて、前記熱
媒体の温度、流量、圧力等を調整することにより
容器内被処理物の温度を一定にする方法が通常行
われている。 In this case, as a cooling or heat removal method, a heat exchanger such as a jacket installed around the container or a coil installed inside the container is used as a heat medium (heat transfer device) whose temperature is lower than the temperature of the object to be processed inside the container. Depending on the temperature and cooling temperature, a type of heat medium that matches the purpose is selected from among various heat media such as organic refrigerant, inorganic refrigerant, chilled water, cooling water, hot water, steam, and organic heat medium.) is used as a heat medium outside the container. Generally, the temperature of the object to be processed in the container is lowered by supplying the object through equipment and transferring heat from the high temperature object to be processed in the container to a low-temperature heat medium. Furthermore, when controlling the temperature to a constant predetermined temperature, the temperature of the object to be processed in the container is measured, and the temperature, flow rate, pressure, etc. of the heat medium are adjusted according to the difference between this measured value and the predetermined temperature. A method is generally used in which the temperature of the object to be processed in the container is kept constant.
しかしながら、このような冷却方法は、いずれ
も被処理物と熱媒体の温度差に基づく、顕熱の利
用による冷却であるため、応答が遅く、激しい発
熱を伴う化学反応の除熱などの目的には対応でき
ないといつた本質的な欠点がある。(凝縮性蒸気
を熱媒体にすれば、加熱時は潜熱の利用になる
が、冷却時は潜熱が利用できない。)また熱媒体
設備として、熱媒の種類に応じて温水ボイラー、
熱媒ボイラー、冷却設備、冷凍設備や熱媒のタン
ク類、配管類等種々の付帯設備が必要であり、熱
媒体の保有量が多くなつて熱媒体の熱容量が大き
くなり、熱媒体自体の温度変更の応答性が悪いと
いつた欠点もある。 However, all of these cooling methods use sensible heat based on the temperature difference between the object to be processed and the heat medium, so the response is slow and they are not suitable for purposes such as heat removal from chemical reactions that generate intense heat. It has an essential drawback that it cannot be addressed. (If condensable steam is used as a heat medium, latent heat will be used when heating, but latent heat cannot be used when cooling.) Also, depending on the type of heat medium, hot water boilers, hot water boilers,
Various auxiliary equipment such as heat medium boilers, cooling equipment, refrigeration equipment, heat medium tanks, piping, etc. are required, and as the amount of heat medium held increases, the heat capacity of the heat medium increases, and the temperature of the heat medium itself increases. It also has the drawback of poor responsiveness to changes.
上記のような欠点を改善して応答を早くするた
めに、冷却時には加熱時とは別の冷却用熱媒体を
前記ジヤケツトあるいはコイル等の熱交換器に供
給したり、あるいは加熱時はジヤケツトを使用
し、冷却時には容器内コイルを使用するといつた
ように、冷却時と加熱時で各々専用の加熱用およ
び冷却用の熱媒体設備を設けることが行われてい
る。また、容器内部の被処理物を容器外部に設置
した伝熱面積の大きい熱交換器に供給し、容器と
外部の熱交換器とのあいだで被処理物を循環する
ことによつて冷却、除熱することもしばしば行わ
れている。 In order to improve the above-mentioned drawbacks and speed up the response, it is possible to supply a cooling heat medium different from that used during heating to the heat exchanger such as the jacket or coil during cooling, or to use a jacket during heating. However, as in the case of using an in-vessel coil during cooling, dedicated heating and cooling heat medium facilities are provided for cooling and heating, respectively. In addition, the material to be processed inside the container is supplied to a heat exchanger with a large heat transfer area installed outside the container, and the material to be processed is cooled and removed by circulating between the container and the external heat exchanger. Heating is also often done.
しかしながら、この場合も冷却は顕熱の利用で
あり、温度差を大きくしたり、伝熱面積を多くし
て対応しているだけであつて、本質的な効率の悪
さを解決しているものではない。さらに高粘度液
の撹拌の場合のように、容器内にコイル等の熱交
換器を設置することが下可能であつたり、設置で
きたとしても充分な伝熱面積がとれないこともあ
る。また容器内被処理物の性状によつては外部に
循環することが不適当な場合もある。このように
冷却時の応答性を良くするために、伝熱面積を増
大しようとしても種々の制約条件から不可能であ
ることが多く、やはり、発熱量の大きい場合の除
熱や急冷などの目的には対応できないといつた欠
点がある。 However, in this case as well, cooling is the use of sensible heat, and this is only achieved by increasing the temperature difference or increasing the heat transfer area, and does not solve the inherent inefficiency. do not have. Furthermore, as in the case of stirring high viscosity liquids, it may be possible to install a heat exchanger such as a coil inside the container, or even if it is possible, a sufficient heat transfer area may not be available. Furthermore, depending on the nature of the material to be treated inside the container, it may be inappropriate to circulate the material to the outside. Even if we try to increase the heat transfer area in order to improve responsiveness during cooling, it is often impossible due to various constraints, and as expected, it is not possible to do so for purposes such as heat removal or rapid cooling when the amount of heat generated is large. There are some drawbacks that cannot be addressed.
発明が解決しようとする問題点
本発明は、凝縮性蒸気を熱媒体として例えば容
器内の温度を所定の温度にコントロールしたり、
所定温度以下にする際に必要となる冷却操作を、
凝縮した液が蒸発する際の蒸発潜熱を利用して、
極めて早い応答速度で行えるようにすることを目
的とする。Problems to be Solved by the Invention The present invention uses condensable steam as a heat medium to control the temperature inside a container to a predetermined temperature,
The cooling operation required to bring the temperature below a specified level,
Using the latent heat of vaporization when the condensed liquid evaporates,
The aim is to achieve extremely fast response speed.
問題点を解決するための手段
本発明は、被処理物保持体壁面に接する凝縮性
蒸気相中に設けた、蒸気を凝縮させるための熱交
換装置と、前記熱交換装置によつて凝縮した凝縮
液を集液し整流するための集液整流装置と集液整
流した前記凝縮液を流下させる壁面を備える被処
理物保持体とからなり、集液整流した前記凝縮液
を前記壁面に極力均一に膜状または滴状にして流
下させ、前記凝縮液が前記壁面を介して被処理物
保持体内の被処理物の保有する熱量によつて蒸発
する際の蒸発潜熱を利用して、前記被処理物を冷
却するようになしたことを特徴とする冷却装置に
関する。なおこの場合凝縮性蒸気中の不凝縮性ガ
スは極力排除することがより効果的である。Means for Solving the Problems The present invention provides a heat exchange device for condensing vapor provided in a condensable vapor phase in contact with a wall surface of a workpiece holder, and a heat exchange device for condensing vapor condensed by the heat exchange device. It consists of a liquid collecting and rectifying device for collecting and rectifying the liquid, and a processing object holder having a wall surface through which the collected and rectified condensed liquid flows down, and the collected and rectified condensed liquid is distributed as uniformly as possible on the wall surface. The object to be processed is caused to flow down in the form of a film or drops, and the latent heat of evaporation when the condensed liquid evaporates through the wall surface due to the amount of heat held by the object to be processed in the object holder is used to cool the object to be processed. The present invention relates to a cooling device characterized in that it is configured to cool. In this case, it is more effective to eliminate as much non-condensable gas as possible from the condensable vapor.
ここで「集液整流装置」とは、凝縮した凝縮液
を集液し、その流れを一定方向(ここでは被処理
物保持体壁面の方向)へ向けるための集液および
流れ誘導装置をいう。以下同じ。 Here, the term "liquid collection and rectification device" refers to a liquid collection and flow guiding device that collects condensed liquid and directs the flow in a certain direction (in this case, the direction of the wall surface of the object holder). same as below.
具体的には、ジヤケツト付容器において、水蒸
気等の凝縮性蒸気をジヤケツト室に供給して容器
内部の被処理物を加熱しているような場合に、本
発明の熱交換装置および集液整流装置をジヤケツ
ト室内に組み込むと、加熱時のみならず冷却時も
潜熱を利用できるため、応答が極めて早く、発熱
量の大きい化学反応、溶解、希釈等の諸操作や急
冷操作に適している。この場合、前記熱交換装置
はパイプ類をジヤケツト室内の容器本体壁周囲に
コイル状に巻回して設置したコイル式熱交換器
に、外部から冷却用熱媒体を供給すればよく、前
記集液整流装置は、たとえば平板や波板等の板状
物を、前記コイル式熱交換器のコイルのパイプに
沿つてパイプ下部に設置し、さらに容器本体の壁
面に向かつて傾斜をつけると共に、容器本体壁面
との間に微少の隙間を保ち、パイプ表面で凝縮し
て落下する凝縮液を集めて容器本体壁面をほぼ均
一に膜状または滴状に流下するようにすればよ
い。このとき、板状の集液整流装置は、凝縮液が
円周方向に流れて、容器本体壁面を均一に流れな
くなるのを防ぐために、ピツチの小さい液板状や
折板状の凹凸のある板を用いるのがよい。また凝
縮液が流下する容器本体の壁面をグラインダーや
サンドブラストで荒らしたり、縦すじを入れた
り、ナシ地模様にするとより効果的である。 Specifically, in a container with a jacket, when condensable steam such as water vapor is supplied to the jacket chamber to heat the object to be treated inside the container, the heat exchange device and the liquid collecting and rectifying device of the present invention can be used. When installed in the jacket chamber, latent heat can be used not only during heating but also during cooling, so the response is extremely fast and it is suitable for various operations such as chemical reactions, melting, dilution, etc. that generate a large amount of heat, and quenching operations. In this case, the heat exchange device may be configured by supplying a cooling heat medium from the outside to a coil-type heat exchanger installed by winding pipes around the container body wall in a jacket chamber, and The device installs a plate-shaped object, such as a flat plate or a corrugated plate, along the pipe of the coil of the coil type heat exchanger at the bottom of the pipe, and further slopes it toward the wall surface of the container body. A small gap may be maintained between the pipe and the condensate that condenses on the pipe surface and falls so that it flows almost uniformly down the wall surface of the container body in the form of a film or drops. At this time, the plate-shaped liquid collecting and rectifying device is a plate-like liquid plate with a small pitch or a folded plate-like uneven plate in order to prevent the condensed liquid from flowing in the circumferential direction and not flowing uniformly on the wall surface of the main body of the container. It is better to use It is also more effective to roughen the wall surface of the container body through which the condensate flows down with a grinder or sandblast, add vertical lines, or create a pear pattern.
本発明の冷却装置を利用して保持体内の被処理
物を加熱しようとするときには、熱交換装置の冷
却用コイルに冷却用熱媒体の供給を停止し、ジヤ
ケツト室に加熱した凝縮性蒸気を吹き込めばよ
い。そうすると凝縮性蒸気は伝熱面となした被処
理物保持体壁面で凝縮し、凝縮潜熱によつて被処
理物を加熱することができる。 When attempting to heat the object to be processed in the holder using the cooling device of the present invention, the supply of the cooling heat medium to the cooling coil of the heat exchange device must be stopped, and heated condensable steam must be blown into the jacket chamber. Bye. Then, the condensable vapor condenses on the wall surface of the workpiece holder, which serves as a heat transfer surface, and the workpiece can be heated by the latent heat of condensation.
実施例
本発明の実施例を第1図によつて説明すると、
容器本体1の外周に設けたジヤケツト室2の内部
に、冷却用の熱交換装置6を設ける。この熱交換
装置6はたとえばパイプ7からなり、これを容器
本体外壁面5の外周にコイル状に巻回して設置す
る。このときパイプ7と外壁面5が接触しないよ
うに、適当な隙間をあけて設置する。パイプ7に
は凝縮性蒸気を凝縮させるための冷却用熱媒体が
供給されるようになつており、10はその供給の
出入口である。パイプ7の直下には凝縮液を集め
て容器本体外壁面5に流下させるための集液整流
装置8を設置する。この集液整流装置8はたとえ
ば波板9からなり、パイプ7に沿つてパイプ下部
に螺旋状に巻回して設置する。この波板9は集液
した凝縮液を容器本体外壁面5に流下させるため
に、外壁面5に対して適当な傾斜をつけ、さらに
波板9は容器本体外壁面5に対し、微少な隙間を
保つて設置する。Embodiment An embodiment of the present invention will be explained with reference to FIG.
A cooling heat exchange device 6 is provided inside a jacket chamber 2 provided on the outer periphery of the container body 1. The heat exchange device 6 is composed of, for example, a pipe 7, which is wound around the outer periphery of the outer wall surface 5 of the container body in a coiled manner. At this time, the pipe 7 and the outer wall surface 5 are installed with an appropriate gap so that they do not come into contact with each other. A cooling heat medium for condensing condensable steam is supplied to the pipe 7, and 10 is an inlet and an inlet for the supply. Immediately below the pipe 7, a liquid collecting and rectifying device 8 is installed to collect the condensed liquid and cause it to flow down onto the outer wall surface 5 of the container body. The liquid collecting and rectifying device 8 is made of, for example, a corrugated plate 9, and is installed in a spiral manner along the pipe 7 at the lower part of the pipe. The corrugated plate 9 has an appropriate slope with respect to the outer wall surface 5 in order to allow the collected condensate to flow down to the outer wall surface 5 of the container body. Maintain and install.
以上の構成において、ジヤケツト室2には凝縮
性蒸気として水蒸気が供給されており(ジヤケツ
ト室内の不凝縮性ガスを極力排除するために、あ
らかじめジヤケツト室を水蒸気でブローしておく
方がよい)、容器内部の被処理物4を加熱あるい
は所定温度に保持している。ここで被処理物4を
冷却したり、反応熱や溶解熱などのような被処理
物4から発生する熱量を除去する場合にはパイプ
7に水などの冷却用熱媒体を供給する。水を供給
すればジヤケツト室2内の水蒸気は直ちにパイプ
7の表面で凝縮し、落下して波板9によつて集液
され、波板9と容器本体外壁面5との隙間から外
壁面5に沿つてほぼ均一に膜状または滴状になつ
て流下する。流下中に凝縮液は容器内部の高温の
被処理物4から受ける熱によつて蒸発し、その際
蒸発潜熱を被処理物4から奪い、被処理物4の温
度は極めて速やかに低下する。このとき、水蒸気
は供給を停止するのではなく、水蒸気が凝縮して
壁面をほぼ均一に濡らすのに必要な程度の量を供
給する必要がある。実際的には、反応温度のコン
トロールのように、発生熱を除去するような場合
は、水蒸気の供給量を変更することなく、パイプ
7に水を供給すれば直ちに被処理物4の温度は低
下する。 In the above configuration, water vapor is supplied to the jacket chamber 2 as condensable steam (in order to eliminate as much non-condensable gas as possible within the jacket chamber, it is better to blow the jacket chamber with steam in advance), The object to be processed 4 inside the container is heated or maintained at a predetermined temperature. Here, when cooling the object 4 to be processed or removing heat generated from the object 4 such as reaction heat or heat of dissolution, a cooling heat medium such as water is supplied to the pipe 7 . When water is supplied, the water vapor in the jacket chamber 2 immediately condenses on the surface of the pipe 7, falls down and is collected by the corrugated plate 9, and flows through the gap between the corrugated plate 9 and the outer wall surface 5 of the container body into the outer wall surface 5. The water flows down almost uniformly in the form of a film or droplets. While flowing down, the condensed liquid is evaporated by the heat received from the high temperature workpiece 4 inside the container, and at this time, the latent heat of vaporization is taken away from the workpiece 4, and the temperature of the workpiece 4 drops extremely quickly. At this time, rather than stopping the supply of water vapor, it is necessary to supply the amount necessary for the water vapor to condense and wet the wall surface almost uniformly. In practice, when removing generated heat such as controlling the reaction temperature, the temperature of the material to be treated 4 immediately decreases by supplying water to the pipe 7 without changing the amount of water vapor supplied. do.
第2図は、被処理物を連続的に潜熱によつて冷
却することができる本発明の他の実施例を示す。
この実施例においては、被処理物保持体1は二重
管構造となつており、被処理物4は該二重管の環
状空隙内を連続的に流れるようになつている。冷
却用のコイル状パイプ7および該パイプ下方に設
けた螺旋状に巻回した波板9は二重管の両側に設
置される。この実施例も第1図の実施例と同じ原
理に従つてジヤケツト室2へ供給された凝縮性蒸
気が冷却用パイプ7の表面で凝縮し、集液整流用
の波板9によつて誘導されて二重管1の壁面5に
沿つて流下する間に被処理物4から受ける熱によ
つて再び蒸発し、その際蒸発潜熱を被処理物から
奪う。 FIG. 2 shows another embodiment of the invention in which the workpiece can be continuously cooled by latent heat.
In this embodiment, the object to be treated holder 1 has a double tube structure, and the object to be treated 4 flows continuously within the annular gap of the double tube. A cooling coiled pipe 7 and a spirally wound corrugated plate 9 provided below the pipe are installed on both sides of the double pipe. In this embodiment, condensable steam supplied to the jacket chamber 2 condenses on the surface of the cooling pipe 7 and is guided by the corrugated plate 9 for liquid collection and rectification according to the same principle as the embodiment shown in FIG. While flowing down along the wall surface 5 of the double tube 1, it is evaporated again by the heat received from the object to be treated 4, and at this time, the latent heat of vaporization is taken away from the object to be treated.
第2図の実施例は、被処理物を反応装置などの
温度制御用熱媒として使用する場合など、被処理
物を急冷する場合、あるいは頻繁に温度を変える
場合に有利である。 The embodiment shown in FIG. 2 is advantageous when the object to be treated is used as a heating medium for temperature control in a reaction device or the like, when the object to be treated is rapidly cooled, or when the temperature is frequently changed.
発明の効果
以上詳述したように、本発明によれば凝縮性蒸
気を熱媒体として、被処理物の温度をコントロー
ルするため、あるいは所定温度以下にするために
冷却する際に、凝縮性蒸気相中に蒸気を凝縮させ
るための熱交換装置と、熱交換装置下部に凝縮し
た凝縮液を集液し整流するための集液整流装置を
設けて、前記凝縮液を被処理物保持体外壁面に極
力均一に膜状または滴状にして流下させ、前記凝
縮液が被処理物の保有する熱量によつて蒸発する
際の蒸発潜熱を利用して被処理物を冷却すること
ができるようにしたことによつて、前記保持体内
の被処理物を迅速に冷却することができるといつ
た効果を有する。Effects of the Invention As described in detail above, according to the present invention, when cooling a workpiece to control the temperature of the object to be treated or to lower it to a predetermined temperature using condensable steam as a heat medium, the condensable vapor phase A heat exchange device for condensing steam inside the heat exchange device, and a liquid collection and rectification device for collecting and rectifying the condensed liquid at the bottom of the heat exchange device are installed to direct the condensed liquid to the outer wall surface of the object holder as much as possible. The object to be processed can be cooled using the latent heat of evaporation when the condensed liquid evaporates due to the amount of heat held by the object to be processed by causing the condensate to flow down uniformly in the form of a film or drops. Therefore, there is an effect that the object to be processed inside the holding body can be cooled quickly.
実際的には、水蒸気などの凝縮性蒸気を熱媒体
として使用している場合に、前述した熱交換装置
および集液整流装置をジヤケツト内に組み込むこ
とにより、加熱時のみならず冷却時にも潜熱を利
用することができ、しかも前記熱交換装置に水な
どの冷却用熱媒体を通せば、凝縮性蒸気は直ちに
凝縮し、被処理物保持体外壁面を流下してその中
の被処理物から蒸発潜熱を奪うため、熱的応答が
極めて早い装置となり、発熱量の大きい化学反応
などの温度コントロール装置として適用できると
いつた効果を有する。 In practice, when condensable steam such as water vapor is used as a heat medium, by incorporating the heat exchange device and liquid collection rectifier described above into the jacket, latent heat can be absorbed not only during heating but also during cooling. If a cooling heat medium such as water is passed through the heat exchange device, the condensable vapor will immediately condense, flow down the outer wall surface of the object holder, and absorb the latent heat of vaporization from the object therein. Since the device takes away the heat, it becomes a device with an extremely quick thermal response, and has the advantage that it can be applied as a temperature control device for chemical reactions that generate a large amount of heat.
第1図および第2図は本発明の実施例を示す縦
断面図である。
1は容器本体、2はジヤケツト室、4は被処理
物、6は熱交換装置、8は集液整流装置、11は
ジヤケツト室への凝縮性蒸気の供給の出入口であ
る。
1 and 2 are longitudinal sectional views showing an embodiment of the present invention. 1 is a container body, 2 is a jacket chamber, 4 is an object to be treated, 6 is a heat exchange device, 8 is a liquid collecting and rectifying device, and 11 is an inlet/outlet for supplying condensable steam to the jacket chamber.
Claims (1)
と、 前記被処理物保持体の壁面に接して設けられた
ジヤケツト室と、 前記ジヤケツト室内へ凝縮性蒸気を供給するた
めの手段と、 前記ジヤケツト室内に設けられ、凝縮性蒸気を
凝縮させるための熱交換装置と、 前記熱交換装置によつて凝集した凝縮液を集液
し、集液した凝縮液が前記被処理物保持体の壁面
に沿つて流下するように集液した凝縮液の流れを
前記壁面へ指向させるための流れ誘導装置を備
え、 前記凝縮液を前記壁面に膜状または滴状にして
流下させ、前記凝縮液が、前記壁面を介して被処
理物保持体内の被処理物の保有する熱量によつて
蒸発する際に、前記被処理物から奪う蒸発潜熱に
よつて前記被処理物を冷却するようになしたこと
を特徴とする冷却装置。[Scope of Claims] 1. A workpiece holder having a wall surface serving as a heat transfer surface, a jacket chamber provided in contact with the wall surface of the workpiece holder, and supplying condensable steam into the jacket chamber. a heat exchange device provided in the jacket chamber for condensing the condensable vapor; a device for collecting condensate that has coagulated by the heat exchange device; A flow guide device is provided for directing the flow of the collected condensate flowing down along the wall surface of the processing object holder toward the wall surface, and the condensate liquid is caused to flow down the wall surface in the form of a film or droplets. , when the condensed liquid evaporates via the wall surface by the amount of heat held by the workpiece in the workpiece holder, the workpiece is cooled by the latent heat of vaporization taken away from the workpiece. A cooling device characterized by the following.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2154887A JPS63189762A (en) | 1987-01-30 | 1987-01-30 | Cooling device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2154887A JPS63189762A (en) | 1987-01-30 | 1987-01-30 | Cooling device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS63189762A JPS63189762A (en) | 1988-08-05 |
| JPH0477224B2 true JPH0477224B2 (en) | 1992-12-07 |
Family
ID=12058040
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2154887A Granted JPS63189762A (en) | 1987-01-30 | 1987-01-30 | Cooling device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS63189762A (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH04203875A (en) * | 1990-11-30 | 1992-07-24 | Kajimoto Kikai Kogyo Kk | Cooling and heating tank |
| JP2006308187A (en) * | 2005-04-28 | 2006-11-09 | Tlv Co Ltd | Vaporization cooling device |
| JP2008096062A (en) * | 2006-10-13 | 2008-04-24 | Tlv Co Ltd | Evaporative cooling device |
| JP4897435B2 (en) * | 2006-11-15 | 2012-03-14 | 株式会社テイエルブイ | Evaporative cooling device |
-
1987
- 1987-01-30 JP JP2154887A patent/JPS63189762A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS63189762A (en) | 1988-08-05 |
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