JPS63189763A - Heating-cooling vessel - Google Patents

Heating-cooling vessel

Info

Publication number
JPS63189763A
JPS63189763A JP62021549A JP2154987A JPS63189763A JP S63189763 A JPS63189763 A JP S63189763A JP 62021549 A JP62021549 A JP 62021549A JP 2154987 A JP2154987 A JP 2154987A JP S63189763 A JPS63189763 A JP S63189763A
Authority
JP
Japan
Prior art keywords
heat
container
heating
cooling
liquid
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
JP62021549A
Other languages
Japanese (ja)
Other versions
JPH0477225B2 (en
Inventor
沖野 育郎
中谷 安廣
牧野 和彦
良夫 北野
幸三 岡本
成之 弘田
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.)
Kanegafuchi Chemical Industry Co Ltd
Tokuden Co Ltd Kyoto
Original Assignee
Kanegafuchi Chemical Industry Co Ltd
Tokuden Co Ltd Kyoto
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 Kanegafuchi Chemical Industry Co Ltd, Tokuden Co Ltd Kyoto filed Critical Kanegafuchi Chemical Industry Co Ltd
Priority to JP62021549A priority Critical patent/JPS63189763A/en
Publication of JPS63189763A publication Critical patent/JPS63189763A/en
Publication of JPH0477225B2 publication Critical patent/JPH0477225B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Devices That Are Associated With Refrigeration Equipment (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
  • Heat-Pump Type And Storage Water Heaters (AREA)
  • Devices For Use In Laboratory Experiments (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 産業上皇且且分立 本発明は加熱−冷却容器に係り、特に、加熱時・冷却時
ともに潜熱を利用することにより、加熱・冷却の応答を
極めて早くした加熱−冷却容器に関する。
[Detailed Description of the Invention] The present invention relates to a heating/cooling container, and in particular, to a heating/cooling container that has an extremely quick heating/cooling response by utilizing latent heat during both heating and cooling. Regarding.

l米■肢玉 化学反応操作や溶解・希釈操作をはじめとする種々の操
作において、容器内部に保有されている被処理物を所定
温度まで昇温した後、化学反応熱や溶解熱、希釈熱、結
晶化熱のような、容器内部の被処理物から発生する熱量
を除去しながら、前記被処理物の温度を所定温度に維持
したり、所定温度で処理した後、容器内部の被処理物の
温度を降温して次工程に移るといった操作が頻繁に行わ
れている。
In various operations such as chemical reaction operations and dissolution/dilution operations, after the material to be processed held inside the container is heated to a predetermined temperature, heat of chemical reaction, heat of dissolution, and heat of dilution are released. , while removing the amount of heat generated from the processed material inside the container, such as heat of crystallization, the temperature of the processed material is maintained at a predetermined temperature, or after processing at a predetermined temperature, the processed material inside the container is removed. Operations such as lowering the temperature and moving on to the next process are frequently performed.

上記操作を行う方法として、容器本体の周囲に設けたジ
ャケットや容器内部に設けたコイル式等の熱交換装置に
、容器外部で発生させた温水、水蒸気、有機熱媒体等の
熱媒体を供給し、この熱媒体の流量、圧力、温度等を調
整することによって、容器内の被処理物を加熱したり、
所定温度に維持したり、冷却したりすることが一般に行
われている。
As a method for performing the above operation, a heat medium such as hot water, steam, or organic heat medium generated outside the container is supplied to a heat exchange device such as a jacket provided around the container body or a coil type installed inside the container. By adjusting the flow rate, pressure, temperature, etc. of this heat medium, the object to be processed in the container can be heated,
It is generally practiced to maintain a predetermined temperature or cool it.

しかるに、この方法では加熱と冷却の切替えが遅く、応
答性が悪いため、加熱用と冷却用の2種類の熱媒体を用
意して、加熱時と冷却時で熱媒体を切り替えて使用する
ことも行われているが、加熱用熱媒体と冷却用熱媒体の
入れ替えにかなりの時間を要し、必ずしも応答性は良く
なく、特に頻繁に加熱と冷却を繰り返す必要がある場合
には通用できない。
However, with this method, the switching between heating and cooling is slow and the response is poor, so it is also possible to prepare two types of heat medium, one for heating and one for cooling, and switch between them for heating and cooling. However, it takes a considerable amount of time to replace the heat medium for heating and the heat medium for cooling, and the responsiveness is not always good, so it is not applicable especially when heating and cooling need to be repeated frequently.

切替え時の対応を早くし、加熱と冷却の頻繁な切替えに
も応答できるようにするために、加熱用の熱交換装置と
冷却用の熱交換装置の二系統の熱交換装置を設置して、
加熱時には加熱用熱交換装置に加熱用熱媒体を供給し、
冷却時には冷却用熱交換装置に冷却用熱媒体を供給する
ことも一般的に行われている。たとえば加熱時にはジャ
ケットを使用して、冷却時には容器内部に設置したコイ
ル式熱交換器を使用したり、ジャケット室内の容器本体
外壁面に、半割りのパイプをコイル状に巻きつけて、加
熱時はジャケットを使用し、冷却時は半割りコイルを使
用するなどの例があるが、前者の方法は、コイル式熱交
換器表面での過冷却や、攪拌翼との関係などの容器の構
造上の理由で、容器内部に熱交換装置を設置できない場
合には適用できず、後者の方法は、伝熱面積が減少する
ため、伝熱面積が不足して必要な応答性が得られないこ
とがあるなどの欠点がある。
In order to respond quickly to changeovers and to be able to respond to frequent switching between heating and cooling, we installed two systems of heat exchange equipment: one for heating and one for cooling.
During heating, a heating medium is supplied to the heating heat exchange device,
During cooling, it is also common practice to supply a cooling heat medium to a cooling heat exchange device. For example, a jacket may be used for heating, a coil heat exchanger installed inside the container may be used for cooling, or a halved pipe may be wrapped in a coil around the outer wall of the container body inside the jacket chamber. There are examples of using a jacket and half-split coils for cooling, but the former method has problems with the structure of the container, such as supercooling on the surface of the coil heat exchanger and the relationship with the stirring blades. For some reason, it cannot be applied if a heat exchange device cannot be installed inside the container, and the latter method reduces the heat transfer area, so the heat transfer area may be insufficient and the necessary responsiveness may not be obtained. There are drawbacks such as.

さらに本質的な欠点として、上記いずれの方法によって
も、蒸気で加熱する場合以外は潜熱が利用できず、顕熱
しか利用できないため、加熱時に水蒸気や有機熱媒蒸気
の潜熱を利用している場合でも、冷却時には冷却用熱媒
体の顕熱を利用して冷却することになり、冷却速度が律
速になって容器全体の応答性が良くならないといったこ
とがある。この欠点を解決するために、冷却時の伝熱面
積を増大して冷却速度を加熱速度と同程度にしようとし
ても、加熱面積の数倍以上の伝熱面積が必要となって、
前述したような構造上の理由から実際には必要伝熱面積
を得られないことが多い。
A further fundamental drawback is that with any of the above methods, latent heat cannot be used except when heating with steam, and only sensible heat can be used. However, during cooling, the sensible heat of the cooling heat medium is used for cooling, and the cooling rate becomes rate-limiting, which may prevent the overall response of the container from improving. In order to solve this drawback, even if we try to increase the heat transfer area during cooling so that the cooling rate is on the same level as the heating rate, a heat transfer area that is several times larger than the heating area is required.
Due to the above-mentioned structural reasons, the required heat transfer area is often not actually obtained.

このように従来の加熱−冷却容器では、発熱量の大きい
化学反応や溶解用の容器として、あるいは急冷を必要と
される冷却容器として使用しようとしても、応答性の悪
さから通用できない場合も多い。
As described above, conventional heating-cooling containers are often not suitable for use as containers for chemical reactions or dissolution that generate a large amount of heat, or as cooling containers that require rapid cooling due to poor responsiveness.

また、設備的には、熱媒体を供給するためには、温水ボ
イラー、蒸気ボイラー、熱媒ボイラー等のボイラーが必
要となり、特に有機熱媒体を使用する場合には、容器専
用の熱媒ボイラーが必要となることが多い。さらに容器
とボイラーを接続する配管やパルプ類、保温、タンク類
等が必要となり、しかもボイラー、配管類、タンク類等
の付帯設備は、一般に容器本体よりもはるかに大型で、
多額の設備投資と広い設置場所を必要とし、また保守点
検が欠かせず、法規制を受けるなど繁雑で不都合な点が
多い。加熱用と冷却用の二種類の熱媒体を用意する場合
は、さらに繁雑になることはいうまでもない。
In addition, in terms of equipment, a boiler such as a hot water boiler, steam boiler, or heat medium boiler is required to supply the heat medium, and especially when using an organic heat medium, a heat medium boiler dedicated to the container is required. It is often necessary. Furthermore, piping, pulp, heat insulation, tanks, etc. that connect the container and boiler are required, and additional equipment such as boilers, piping, and tanks are generally much larger than the container itself.
It requires a large amount of capital investment and a large installation space, requires maintenance and inspection, is subject to legal regulations, and has many complicated and inconvenient points. Needless to say, the process becomes even more complicated when two types of heat medium are prepared, one for heating and one for cooling.

上記欠点のうち、設備的な問題点を解決して、コンパク
トでしかも潜熱を利用して効率的に加熱する容器として
、容器本体の周囲に設けたジャケット室に液溜部を設け
、容器の一部に設置した電磁誘導発熱機構によって、前
記液溜部に封入した気液二相の熱媒体を加熱して蒸発さ
せ、この蒸発した熱媒体の潜熱の授受によって、容器内
の被処理物を加熱する容器が提案されている。
Among the above drawbacks, in order to solve the equipment problems and create a compact container that efficiently heats using latent heat, a liquid reservoir is provided in the jacket chamber provided around the container body. An electromagnetic induction heating mechanism installed in the chamber heats and evaporates the gas-liquid two-phase heating medium sealed in the liquid reservoir, and the object to be processed in the container is heated by giving and receiving latent heat of the evaporated heating medium. Containers have been proposed.

しかしながら、この場合でも、冷却時の上記欠点を解決
できるものではなく、冷却用のコイル式熱交換器などを
設置しても、冷却時には潜熱が利用できないために冷却
速度が遅く、応答を良くしようとすれば加熱時の数倍以
上の伝熱面積が必要となり、上記したような過冷却や構
造上の理由から必要な伝熱面積が得られず、冷却時の伝
熱面積が不足して、発熱量の大きい化学反応や、急冷を
要する場合には、応答が遅くて適用できないといった欠
点がある。
However, even in this case, the above drawbacks during cooling cannot be solved; even if a coil heat exchanger is installed for cooling, the cooling speed is slow because latent heat cannot be used during cooling, and it is difficult to improve the response. If so, a heat transfer area several times larger than that for heating would be required, and due to the above-mentioned supercooling and structural reasons, the necessary heat transfer area could not be obtained, and the heat transfer area during cooling would be insufficient. The disadvantage is that the response is slow and it cannot be applied to chemical reactions that generate a large amount of heat or when rapid cooling is required.

B < ° しよ゛と るロ 占 本発明は容器の一部に設置した電磁誘導発熱機構によっ
て、熱媒体を蒸発させ、蒸発した熱媒体が前記容器本体
の外壁面で凝縮する際の潜熱の授受によって前記容器内
の被処理物を加熱する容器において、被処理物を冷却す
る場合にも、熱媒体が蒸発する際の潜熱の授受によって
冷却できるようにし、極めて応答の早い加熱・冷却が行
えるようにすることを目的とする。
The present invention evaporates a heat medium using an electromagnetic induction heating mechanism installed in a part of a container, and reduces the amount of latent heat generated when the evaporated heat medium condenses on the outer wall surface of the container body. In a container that heats the object to be processed in the container by transfer and reception, even when cooling the object, the object can be cooled by transfer of latent heat when the heat medium evaporates, and heating and cooling can be performed with an extremely quick response. The purpose is to do so.

−占  ゞ るための 本発明は、容器本体の周囲に、電磁誘導発熱機構によっ
て加熱される気液二相の熱媒体を封入した液溜部のある
ジャケット室を有する容器において、前記ジャケット室
内に熱交換装置と集液整流装置(熱交換装置に集液整流
機能を持たせてもよい)を設け、前記ジャケット室内の
蒸発した熱媒体を、前記熱交換装置によって凝縮させ、
この凝縮した熱媒体を前記集液整流装置(または熱交換
装置の集液整流機能)によって前記容器外壁面に極力均
一に膜状または滴状にして流下させ、前記凝縮熱媒体が
前記容器内の被処理物の保有する熱量によって蒸発する
際の潜熱の授受によって、前記容器内の被処理物を冷却
するようになしたことを特徴とする加熱−冷却容器に関
する。
- The present invention provides a container having a jacket chamber around the container body with a liquid reservoir portion containing a gas-liquid two-phase heating medium heated by an electromagnetic induction heating mechanism. A heat exchange device and a liquid collection and rectification device (the heat exchange device may have a liquid collection and rectification function) are provided, and the evaporated heat medium in the jacket chamber is condensed by the heat exchange device,
The condensed heat medium is made to flow down as uniformly as possible in the form of a film or droplets on the outer wall surface of the container by the liquid collection and rectification device (or the liquid collection and rectification function of the heat exchange device), and the condensed heat medium flows down into the container. The present invention relates to a heating/cooling container characterized in that the object to be processed in the container is cooled by transfer of latent heat when the object to be processed evaporates due to the amount of heat held by the object.

実施例 本発明の実施例を図面によって説明すると、気液二相の
熱媒体が、減圧封入された密閉ジャケット室2の内部の
蒸気相部7に、冷却用の熱交換装置8を設ける。この熱
交換装置8は本実施例ではフィン付パイプ9からなり、
これを加熱−冷却容器本体lの外壁部5の外周にコイル
状に巻回することによって設置する。このとき、フィン
付パイプ9と容器外壁面5が接触しないように、適当な
距離の隙間をおいて設置する。フィン付パイプ9には熱
媒蒸気を凝縮させるための冷却用熱媒体が供給されるよ
うになっており、12はその潜動用熱媒体の供給の出入
口である。
Embodiment An embodiment of the present invention will be described with reference to the drawings. A cooling heat exchange device 8 is provided in a vapor phase section 7 inside a sealed jacket chamber 2 in which a gas-liquid two-phase heat medium is sealed under reduced pressure. In this embodiment, this heat exchange device 8 consists of a finned pipe 9,
This is installed by winding it in a coil around the outer periphery of the outer wall portion 5 of the heating-cooling container main body l. At this time, the finned pipe 9 and the container outer wall surface 5 are installed with a gap of an appropriate distance so that they do not come into contact with each other. A cooling heat medium for condensing the heat medium vapor is supplied to the finned pipe 9, and 12 is an inlet/outlet for supplying the latent heat medium.

熱交換装置8に冷却用熱媒体を供給することによって、
熱交換装置8の表面で、ジャケット室2内部の加熱用熱
媒体の蒸気が凝縮されて液滴となって落下するが、その
凝縮液を集液し、集液した加熱用熱媒体の凝縮液を容器
外壁面5に均一に流下させるための集液整流装置10が
設置される。
By supplying the cooling heat medium to the heat exchange device 8,
On the surface of the heat exchange device 8, the vapor of the heating heat medium inside the jacket chamber 2 condenses and falls as droplets, and the condensed liquid is collected and the collected condensed liquid of the heating heat medium is A liquid collecting and rectifying device 10 is installed to uniformly flow down the liquid onto the outer wall surface 5 of the container.

この集液整流装置10は平板や波板等の板状物で構成さ
れ、本実施例のように、容器外壁の周囲にコイル状に巻
回したパイプからなる熱交換装置の場合には、パイプに
沿ってパイプ下部に螺旋状に巻回して設置するのが適当
であり、その場合、容器の円周方向に流れる凝縮液をせ
き止めて、容器外壁面5に均一に流下させるために、第
2図に示すようなせき止め用の突起物を設けたり、第3
図に示すような折板状のものや、第4図に示すような波
板状のものを用いるのがよい。
This liquid collecting and rectifying device 10 is composed of a plate-like object such as a flat plate or a corrugated plate. In the case of a heat exchange device consisting of a pipe wound in a coil around the outer wall of the container as in this embodiment, the pipe It is appropriate to install the condensate spirally around the lower part of the pipe along the circumferential direction of the container. Protrusions for damming as shown in the figure may be provided, or a third
It is preferable to use a folded plate shape as shown in the figure or a corrugated plate shape as shown in FIG.

本実施例の場合は第2図に示すような集液整流板11を
使用し、フィン付パイプ9の直下にフィン付パイプ9に
沿って螺旋状に巻回して設置している。さらにこの集液
整流板11はフィン付パイプ9から落下した凝縮液滴を
容器外壁面5に流下させるために、外壁面5に対して適
当な傾斜角度をつけて設置されている。また容器外壁面
5と集液整流板11とは0.5鰭程度の隙間を設けて、
集液整流した凝縮液がこの隙間から容器外壁面5の壁面
上を膜状あるいは滴状に均一に流下するようにしている
In the case of this embodiment, a liquid collecting rectifying plate 11 as shown in FIG. 2 is used, and is installed directly below the finned pipe 9 so as to be spirally wound along the finned pipe 9. Further, the liquid collection rectifying plate 11 is installed at an appropriate inclination angle with respect to the outer wall surface 5 of the container in order to cause the condensed droplets that have fallen from the finned pipe 9 to flow down onto the outer wall surface 5 of the container. Further, a gap of about 0.5 fin is provided between the container outer wall surface 5 and the liquid collecting rectifier plate 11.
The collected and rectified condensed liquid is made to flow down uniformly from this gap onto the wall surface of the outer wall surface 5 of the container in the form of a film or drops.

以上の構成において、電磁誘導発熱機構15を駆動する
と、電流が誘起し、ジュール熱が発生してジャケット室
2内の液溜部6の液相の熱媒体が加熱されて蒸発する。
In the above configuration, when the electromagnetic induction heating mechanism 15 is driven, a current is induced, Joule heat is generated, and the liquid phase heat medium in the liquid reservoir 6 in the jacket chamber 2 is heated and evaporated.

この蒸発した熱媒蒸気は容器本体の外壁面5に接触して
凝縮し、その際、凝縮潜熱を放出して容器内部の被処理
物4を加熱する。凝縮した熱媒体は再び液溜部6にもど
って再度蒸発する。これを繰り返して容器内部の被処理
物4を所定温度に加熱する。
The evaporated heat medium vapor comes into contact with the outer wall surface 5 of the container body and condenses, releasing latent heat of condensation to heat the object 4 inside the container. The condensed heat medium returns to the liquid reservoir 6 and evaporates again. This is repeated to heat the object 4 inside the container to a predetermined temperature.

次に反応熱や溶解熱などのような、容器内部の被処理物
4から発生する熱量を除去して、所定温度に維持したり
、次工程の操作を行うために容器内の被処理物4の温度
を下げる場合には、ジャケット室2内のフィン付バイブ
9に冷却用熱媒体を供給すればよい。冷却用熱媒体が供
給される・と、直ちにジャケット室2内の熱媒体蒸気が
フィン付バイブ9の表面で凝縮し落下して集液整流板1
1によって集液され、容器外壁面5と集液整流板11と
の隙間から、容器外壁面5に沿ってほぼ均一に、膜状あ
るいは滴状になって流下する。流下中に凝縮液は、容器
内部の高温の被処理物4から受ける熱によって蒸発し、
その際蒸発潜熱を被処理物から奪うため、被処理物4の
温度は極めて速やかに低下する。
Next, the amount of heat generated from the processed material 4 inside the container, such as heat of reaction and heat of dissolution, is removed to maintain it at a predetermined temperature or to perform the next process operation. In order to lower the temperature, a cooling heat medium may be supplied to the finned vibrator 9 in the jacket chamber 2. When the cooling heat medium is supplied, the heat medium vapor in the jacket chamber 2 immediately condenses on the surface of the finned vibrator 9 and falls to the liquid collecting rectifier plate 1.
The liquid is collected by the container outer wall 5 and flows down almost uniformly along the container outer wall 5 in the form of a film or drops from the gap between the container outer wall 5 and the liquid collecting rectifying plate 11. While flowing down, the condensed liquid is evaporated by the heat received from the high-temperature processing object 4 inside the container,
At this time, the latent heat of vaporization is taken away from the object to be processed, so the temperature of the object to be processed 4 drops extremely quickly.

再び加熱する場合は、フィン付バイブ9への冷却用熱媒
体の供給を止めればよ(、容器内の被処理物4はジャケ
ット室2内の熱媒体蒸気によって速やかに加熱される。
If you want to heat it up again, just stop supplying the cooling heat medium to the finned vibrator 9 (the workpiece 4 in the container is quickly heated by the heat medium vapor in the jacket chamber 2).

なお、実際的には、冷却用熱媒体の供給の開始および停
止は、容器内の被処理物4の温度を検出して自動的にコ
ントロールされる。さらに被処理物4の冷却温度幅を太
き(とる必要のある場合には、被処理物4の温度低下に
応じて、電磁誘導発熱機構の印加電圧や周波数をコント
ロールしてジャケット室2内の熱媒体への供給熱量を減
少させている。
Note that, in practice, the start and stop of the supply of the cooling heat medium is automatically controlled by detecting the temperature of the object to be processed 4 in the container. Furthermore, if it is necessary to widen the cooling temperature range of the workpiece 4, the voltage and frequency applied to the electromagnetic induction heating mechanism are controlled according to the decrease in the temperature of the workpiece 4. The amount of heat supplied to the heat medium is reduced.

発1廊B九栗 以上詳述したように、本発明によれば、電磁誘導発熱機
構と、気液二相の熱媒体を封入したジャケット室を備え
た容器において、前記ジャケット室内に、冷却用の熱交
換装置と、集液整流装置(熱交換装置に集液整流機能を
持たせてもよい)を設けて、前記熱交換装置によって凝
縮した、前記ジャケット室内の熱媒体の凝縮液を、前記
容器の外壁面に極力均一に膜状または滴状にして流下さ
せ、流下中の前記凝縮液が前記容器内部の被処理物の保
有する熱量によって蒸発する際に奪う潜熱によって、前
記被処理物を冷却することができる。
As detailed above, according to the present invention, in a container equipped with an electromagnetic induction heating mechanism and a jacket chamber in which a gas-liquid two-phase heat medium is enclosed, a cooling device is provided in the jacket chamber. A heat exchange device and a liquid collection rectification device (the heat exchange device may have a liquid collection and rectification function) are provided, and the condensed liquid of the heat medium in the jacket chamber condensed by the heat exchange device is The object to be processed is caused to flow down as uniformly as possible in the form of a film or drops on the outer wall surface of the container, and the object to be processed is absorbed by the latent heat taken away when the flowing condensate evaporates due to the amount of heat held by the object to be processed inside the container. Can be cooled.

このように加熱・冷却とも潜熱を利用しているため、極
めて迅速な加熱および冷却ができ、しかも加熱中に熱交
換装置に冷却用熱媒体を供給すれば直ちに容器内の被処
理物の冷却を開始し、冷却用熱媒体の供給を停止すれば
直ちに加熱状態にもどるため、加熱と冷却の切り替えが
早く、極めて応答性の良い加熱−冷却容器となる。従っ
て激しい発熱を伴う反応の反応装置や、加熱状態から急
速に冷却する場合の容器として使用でき、さらに容器の
一部に設置した電磁誘導発熱機構を加熱源としているた
め、水蒸気ボイラーや熱媒ボイラーによって、容器外部
から熱媒蒸気を供給している場合に比して、はるかにコ
ンパクトな加熱−冷却容器であるといった効果を有する
Since latent heat is used for both heating and cooling, extremely rapid heating and cooling are possible, and if a cooling heat medium is supplied to the heat exchanger during heating, the object to be processed in the container can be immediately cooled. As soon as the heating starts and the supply of the cooling heat medium is stopped, it returns to the heating state, so switching between heating and cooling is quick, resulting in a heating-cooling container with extremely good responsiveness. Therefore, it can be used as a reactor for reactions that generate intense heat, or as a container for rapid cooling from a heated state.Furthermore, since the heating source is an electromagnetic induction heating mechanism installed in a part of the container, it can be used as a steam boiler or heat medium boiler. This has the effect of making the heating/cooling container much more compact than a case where heat medium vapor is supplied from outside the container.

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

第1図は本発明の実施例を示す縦断面図、第2図、第3
図および第4図は集液整流装置の形状の一例を示す図面
である。 1は加熱−冷却容器本体、2はジャケット室、4は被処
理物、6はジャケット室内熱媒体液溜部、7はジャケッ
ト室内熱媒体蒸気相部、8は熱交換装置、10は集液整
流装置、13は誘導コイル、14は鉄心、15は電磁誘
導発熱機構、16は被処理物払い出しパルプである。
FIG. 1 is a vertical sectional view showing an embodiment of the present invention, FIG.
FIG. 4 and FIG. 4 are drawings showing an example of the shape of the liquid collecting and rectifying device. 1 is a heating-cooling container main body, 2 is a jacket chamber, 4 is a workpiece, 6 is a heat medium liquid reservoir in the jacket interior, 7 is a heat medium vapor phase part in the jacket interior, 8 is a heat exchange device, 10 is a liquid collection rectifier In the apparatus, 13 is an induction coil, 14 is an iron core, 15 is an electromagnetic induction heating mechanism, and 16 is a pulp to be treated.

Claims (1)

【特許請求の範囲】 容器の一部に設置された、誘導コイルを備えた電磁誘導
発熱機構と、 前記電磁誘導発熱機構によって加熱される気液二相の熱
媒体を封入した液溜部を有する、前記容器本体の周囲に
設けたジャケット室と、 前記ジャケット室内に設けた、蒸発した前記熱媒体を凝
縮させるための熱交換装置および該交換装置によって凝
縮した前記熱媒体を集液し整流して前記容器本体の外壁
面に流下させるための集液整流装置、または凝縮機能と
共に集液整流機能を有する熱交換装置、とからなり、 前記容器本体の内部に保有された被処理物を加熱する場
合には、前記電磁誘導発熱機構によって加熱されて蒸発
した、前記熱媒体の潜熱の授受によって加熱し、 前記被処理物を冷却する場合には、前記電磁誘導発熱機
構によって加熱されて蒸発した前記熱媒体を、前記熱交
換装置によって凝縮し、この凝縮した熱媒体を、前記集
液整流装置または前記熱交換装置の集液整流機能によっ
て、前記容器本体の外壁面に膜状または滴状にして流下
させ、凝縮した前記熱媒体が前記容器内の前記被処理物
の保有している熱量によって蒸発する際の潜熱の授受に
よって冷却するようになしたことを特徴とする加熱−冷
却容器。
[Scope of Claims] An electromagnetic induction heating mechanism equipped with an induction coil installed in a part of the container, and a liquid reservoir sealed with a gas-liquid two-phase heating medium heated by the electromagnetic induction heating mechanism. , a jacket chamber provided around the container body, a heat exchange device provided in the jacket chamber for condensing the evaporated heat medium, and collecting and rectifying the heat medium condensed by the exchange device. A liquid collecting and rectifying device for causing the liquid to flow down onto the outer wall surface of the container body, or a heat exchange device having a liquid collecting and rectifying function as well as a condensing function, when heating the object held inside the container body. In the case of heating and receiving the latent heat of the heating medium that has been heated and evaporated by the electromagnetic induction heating mechanism, and when cooling the object, the heat that has been heated and evaporated by the electromagnetic induction heating mechanism is heated. The medium is condensed by the heat exchange device, and the condensed heat medium flows down on the outer wall surface of the container body in the form of a film or drops by the liquid collection and rectification device or the liquid collection and rectification function of the heat exchange device. A heating-cooling container characterized in that the condensed heat medium is cooled by giving and receiving latent heat when it evaporates due to the amount of heat held by the object to be treated in the container.
JP62021549A 1987-01-30 1987-01-30 Heating-cooling vessel Granted JPS63189763A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62021549A JPS63189763A (en) 1987-01-30 1987-01-30 Heating-cooling vessel

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62021549A JPS63189763A (en) 1987-01-30 1987-01-30 Heating-cooling vessel

Publications (2)

Publication Number Publication Date
JPS63189763A true JPS63189763A (en) 1988-08-05
JPH0477225B2 JPH0477225B2 (en) 1992-12-07

Family

ID=12058073

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62021549A Granted JPS63189763A (en) 1987-01-30 1987-01-30 Heating-cooling vessel

Country Status (1)

Country Link
JP (1) JPS63189763A (en)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH04290556A (en) * 1991-03-15 1992-10-15 Tlv Co Ltd Heating and cooling device
JPH04338242A (en) * 1991-05-15 1992-11-25 Tlv Co Ltd Heating/cooling device
JPH04338241A (en) * 1991-05-15 1992-11-25 Tlv Co Ltd Heating/cooling device
JP2006308185A (en) * 2005-04-28 2006-11-09 Tlv Co Ltd Evaporative cooling device
JP2008096062A (en) * 2006-10-13 2008-04-24 Tlv Co Ltd Evaporative cooling device
JP2011085329A (en) * 2009-10-16 2011-04-28 Tlv Co Ltd Heating-cooling device
JP2011085328A (en) * 2009-10-16 2011-04-28 Tlv Co Ltd Heating-cooling device
JP2011085327A (en) * 2009-10-16 2011-04-28 Tlv Co Ltd Heating-cooling device
CN111907682A (en) * 2020-07-29 2020-11-10 武汉第二船舶设计研究所(中国船舶重工集团公司第七一九研究所) Multi-unit integrated type ship cooler

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH04290556A (en) * 1991-03-15 1992-10-15 Tlv Co Ltd Heating and cooling device
JPH04338242A (en) * 1991-05-15 1992-11-25 Tlv Co Ltd Heating/cooling device
JPH04338241A (en) * 1991-05-15 1992-11-25 Tlv Co Ltd Heating/cooling device
JP2006308185A (en) * 2005-04-28 2006-11-09 Tlv Co Ltd Evaporative cooling device
JP2008096062A (en) * 2006-10-13 2008-04-24 Tlv Co Ltd Evaporative cooling device
JP2011085329A (en) * 2009-10-16 2011-04-28 Tlv Co Ltd Heating-cooling device
JP2011085328A (en) * 2009-10-16 2011-04-28 Tlv Co Ltd Heating-cooling device
JP2011085327A (en) * 2009-10-16 2011-04-28 Tlv Co Ltd Heating-cooling device
CN111907682A (en) * 2020-07-29 2020-11-10 武汉第二船舶设计研究所(中国船舶重工集团公司第七一九研究所) Multi-unit integrated type ship cooler
CN111907682B (en) * 2020-07-29 2021-10-12 武汉第二船舶设计研究所(中国船舶重工集团公司第七一九研究所) Multi-unit integrated type ship cooler

Also Published As

Publication number Publication date
JPH0477225B2 (en) 1992-12-07

Similar Documents

Publication Publication Date Title
JPS63189763A (en) Heating-cooling vessel
EP0057694B1 (en) Open cycle thermal boosting system
EP0182410A1 (en) Absorption heat pump
US4545217A (en) Steam generating and condensing apparatus
US5770019A (en) Apparatus for concentrating waste liquid
WO1991000760A1 (en) Process and apparatus for cooling a fluid
JPH0477224B2 (en)
JPH0714782Y2 (en) Heating and cooling container
JP2691382B2 (en) Heating and cooling device
JPH0133985Y2 (en)
JP2999080B2 (en) Waste liquid evaporator
SU1612199A1 (en) Heat exchange apparatus
JPH0761402B2 (en) Heating and cooling container
JPH09122635A (en) Apparatus for removing impurity in water
JP2814026B2 (en) Heating and cooling device
JPH02290478A (en) Direct contact type condenser and heat cycle apparatus using the same
JPH0761401B2 (en) Heating and cooling container
SU1177653A1 (en) Heat tube
SU616519A1 (en) Method of heat pipe operation
SU1270531A1 (en) Method of heat exchange between liquid and solid surface
SU1231026A1 (en) Device for granulating slag
SU822840A1 (en) Film-type heat mass exchange apparatus
SU1599032A1 (en) Evaporator
SU1386844A1 (en) Heat exchanging pipe
SU568808A1 (en) Heat exchanger