JPH06241634A - Evaporation cooling device - Google Patents

Evaporation cooling device

Info

Publication number
JPH06241634A
JPH06241634A JP5014293A JP5014293A JPH06241634A JP H06241634 A JPH06241634 A JP H06241634A JP 5014293 A JP5014293 A JP 5014293A JP 5014293 A JP5014293 A JP 5014293A JP H06241634 A JPH06241634 A JP H06241634A
Authority
JP
Japan
Prior art keywords
cooling liquid
cooling
heat exchanger
cooled
amount
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
JP5014293A
Other languages
Japanese (ja)
Other versions
JP2802472B2 (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 JP5050142A priority Critical patent/JP2802472B2/en
Publication of JPH06241634A publication Critical patent/JPH06241634A/en
Application granted granted Critical
Publication of JP2802472B2 publication Critical patent/JP2802472B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PURPOSE:To obtain an evaporation type cooling device, capable of changing quickly without delay when the cooling degree of the device is to be changed. CONSTITUTION:A passage 2, through which material to be cooled is passed, is formed in a flat plate type heat exchanger 1. A plurality of cooling liquid supplying ports 3, 4, 5, 6, 7, 8, 9, 10 are provided around the outer periphery of the heat exchanger l. Respective cooling liquid supplying ports 3, 4, 5, 6, 7, 8, 9, 10 are connected to a cooling liquid pipe through valves 11, 12, 13, 14, 15, 16, 17, 18. The amount, pressure and direction of cooling liquid for the heat exchanger 1 is controlled to regulate the thickness of cooling liquid film, formed on the outer surface of the heat exchanger 1, and control the cooling degree of the cooling liquid.

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、冷却室内に供給した冷
却水を蒸発気化させることにより被冷却物を気化冷却す
るものに関する。具体的には、各種反応を行う反応釜の
冷却装置、食品や医薬品や紙・パルプや繊維等の気化冷
却装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an object for evaporative cooling of an object to be cooled by evaporating cooling water supplied into a cooling chamber. Specifically, the present invention relates to a cooling device for a reaction kettle that performs various reactions, and a vaporization cooling device for foods, pharmaceuticals, paper / pulp, fibers and the like.

【0002】[0002]

【従来の技術】従来の反応釜の冷却装置として、例えば
特開平4−180829号公報に示されたものがある。
これは、冷却容器に接して冷却用流体室を形成し、この
流体室に冷却水を供給する冷却水供給管を接続すると共
に、流体室を真空ポンプと接続し、冷却容器の外壁に隙
間を介して気液分離機能高分子膜を設けたもので、冷却
容器の外壁と気液分離機能高分子膜との間に冷却液を供
給することによって、冷却容器の全周に均一な水膜を形
成して気化冷却することにより、冷却ムラを防止して、
製品の品質を一定に維持することができるものである。
2. Description of the Related Art As a conventional reactor cooling device, for example, there is one disclosed in Japanese Patent Laid-Open No. 4-180829.
This forms a cooling fluid chamber in contact with the cooling container, connects a cooling water supply pipe for supplying cooling water to the fluid chamber, connects the fluid chamber to a vacuum pump, and forms a gap on the outer wall of the cooling container. By providing a gas-liquid separation functional polymer membrane through the cooling liquid, by supplying the cooling liquid between the outer wall of the cooling container and the gas-liquid separation functional polymer film, a uniform water film around the entire circumference of the cooling container. By forming and evaporative cooling, prevent uneven cooling,
The quality of the product can be kept constant.

【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、気化冷却の度合、すなわち、伝達熱量を変化させる
場合に時間遅れを生じる問題があった。これは、真空ポ
ンプを操作して流体室の真空度を変化させるか、供給す
る冷却液の液温を変えることによって伝達熱量を変化さ
せるためである。真空ポンプの操作から実際に流体室の
真空度が変化するまでに所定の時間を要すると共に、冷
却液温の調節から実際に流体室の液温が変化するまでに
時間を要して遅れを生じるのである。
The above-mentioned conventional device has a problem that a time delay occurs when the degree of evaporative cooling, that is, the amount of transferred heat is changed. This is because the transferred heat amount is changed by operating the vacuum pump to change the degree of vacuum of the fluid chamber or changing the liquid temperature of the cooling liquid to be supplied. It takes a certain amount of time from the operation of the vacuum pump to the actual change in the degree of vacuum in the fluid chamber, and there is a delay from the adjustment of the cooling liquid temperature to the actual change in the fluid chamber temperature. Of.

【0004】例えば反応釜においては、反応の過程にお
いて温度を精度良く調節する必要があり、時間遅れを生
じると反応物が劣化したり、損傷したりする恐れがあ
る。
For example, in a reaction vessel, it is necessary to accurately adjust the temperature in the course of the reaction, and if a time delay occurs, the reaction product may be deteriorated or damaged.

【0005】従って本発明の技術的課題は、時間遅れを
生じることなく気化冷却の度合すなわち伝達熱量を制御
することができるようにして、冷却温度を精度良く調節
することができる気化冷却装置を得ることである。
Therefore, a technical object of the present invention is to obtain an evaporative cooling device capable of controlling the cooling temperature with high accuracy by making it possible to control the degree of evaporative cooling, that is, the amount of heat transferred, without causing a time delay. That is.

【0006】[0006]

【課題を解決する為の手段】本発明の気化冷却装置の構
成は次の通りである。被冷却物に冷却液を供給して、冷
却液の気化熱によって被冷却物を冷却するものにおい
て、冷却液を供給する冷却液供給口を形成し、該冷却液
供給口から供給する冷却液の圧力や流量や方向等を制御
して、被冷却物表面に形成される冷却液膜の膜厚を調整
することにより被冷却物からの冷却熱量をコントロ―ル
するものである。
The structure of the evaporative cooling apparatus of the present invention is as follows. In a system for supplying a cooling liquid to an object to be cooled and cooling the object to be cooled by the heat of vaporization of the cooling liquid, a cooling liquid supply port for supplying the cooling liquid is formed, and the cooling liquid supplied from the cooling liquid supply port is The amount of cooling heat from the object to be cooled is controlled by controlling the pressure, the flow rate, the direction, etc. to adjust the film thickness of the cooling liquid film formed on the surface of the object to be cooled.

【0007】[0007]

【作用】冷却液供給口から被冷却物表面に冷却液が供給
され、この冷却液が被冷却物の熱を奪って蒸発気化する
ことにより、被冷却物が冷却される。被冷却物から冷却
液への伝達熱量は、被冷却物表面に形成される冷却液膜
の厚さによって変化する。すなわち、冷却液膜が比較的
薄い場合は冷却液の気化量も多くなり、伝達熱量も大き
くなって被冷却物はより冷却される。冷却液膜が厚くな
ると冷却液の気化量が少なくなり伝達熱量も小さなもの
となって被冷却物の冷却度合は低下する。従って、冷却
液供給口から供給される冷却液の圧力や流量や方向等を
制御することにより、被冷却物表面に形成される冷却液
膜の厚さを変化させることによって伝達熱量を制御する
ことができる。冷却液の圧力や流量や方向等を変えると
直ちに冷却液膜の厚さも変化することにより、時間遅れ
を生じることなく冷却度合を変化させることができる。
The cooling liquid is supplied from the cooling liquid supply port to the surface of the object to be cooled, and the cooling liquid removes heat from the object to be cooled and evaporates and vaporizes, whereby the object to be cooled is cooled. The amount of heat transferred from the object to be cooled to the cooling liquid changes depending on the thickness of the cooling liquid film formed on the surface of the object to be cooled. That is, when the cooling liquid film is relatively thin, the amount of vaporization of the cooling liquid is large and the amount of transferred heat is also large, so that the object to be cooled is further cooled. When the cooling liquid film becomes thick, the amount of vaporization of the cooling liquid becomes small and the amount of transferred heat becomes small, so that the cooling degree of the object to be cooled decreases. Therefore, by controlling the pressure, flow rate, direction, etc. of the cooling liquid supplied from the cooling liquid supply port, the amount of heat transferred can be controlled by changing the thickness of the cooling liquid film formed on the surface of the object to be cooled. You can Since the thickness of the cooling liquid film changes immediately when the pressure, flow rate, direction, etc. of the cooling liquid are changed, the cooling degree can be changed without causing a time delay.

【0008】[0008]

【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、気化冷却装置として平板状の熱交換器を用い
た例を示す。 平板状の熱交換器1の内部に被冷却物の
通路2を形成する。被冷却物は通路2内を下方から上方
へ通過できるものである。熱交換器1の両側外表面に冷
却液を供給する複数の冷却液供給口3,4,5,6,
7,8,9,10を配置する。それぞれの供給口は図示
はしていないがノズル状に形成することが望ましい。そ
れぞれの供給口3,4,5,6,7,8,9,10はバ
ルブ11,12,13,14,15,16,17,18
を介して冷却液管と接続する。冷却液供給口3,4は熱
交換器1に対して鉛直上方より下方へ冷却液を供給す
る。供給口5,6は熱交換器1に対して斜め上方から冷
却液を供給する。同じく供給口7,8は水平方向から供
給し、供給口9,10は斜め下方から供給する。それぞ
れのバルブ11,12,13,14,15,16,1
7,18は全開と全閉ができると共に弁開度を調節する
ことができるものが、冷却液の圧力や流量や方向等を制
御するためには望ましい。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The illustrated embodiment will be described in detail. In this embodiment, a flat plate heat exchanger is used as the evaporative cooling device. A passage 2 for an object to be cooled is formed inside a flat plate heat exchanger 1. The object to be cooled can pass through the passage 2 from the lower side to the upper side. A plurality of cooling liquid supply ports 3, 4, 5, 6, for supplying the cooling liquid to both outer surfaces of the heat exchanger 1.
7, 8, 9, 10 are arranged. Although not shown, each supply port is preferably formed in a nozzle shape. The respective supply ports 3, 4, 5, 6, 7, 8, 9, 10 are valves 11, 12, 13, 14, 15, 16, 17, 18, respectively.
To the cooling liquid pipe. The cooling liquid supply ports 3 and 4 supply the cooling liquid to the heat exchanger 1 from vertically above to below. The supply ports 5 and 6 supply the cooling liquid to the heat exchanger 1 obliquely from above. Similarly, the supply ports 7 and 8 supply from the horizontal direction, and the supply ports 9 and 10 supply from diagonally below. Each valve 11, 12, 13, 14, 15, 16, 1
It is desirable that the valves 7 and 18 can be fully opened and closed and the valve opening can be adjusted in order to control the pressure, flow rate, direction, etc. of the cooling liquid.

【0009】熱交換器1を気化冷却して通路2内の被冷
却物を冷却するには、それぞれの冷却液供給口3,4,
5,6,7,8,9,10から冷却液を熱交換器1に供
給する。熱交換器1上に位置する冷却液は通路2内の被
冷却物の熱を奪って気化することにより被冷却物を冷却
する。気化した蒸気は大気中に放散する。熱交換器1の
伝達熱量を変える場合は、熱交換器1上に形成される冷
却液膜の厚さを変えることにより時間遅れを生じること
なく行うことができる。冷却液膜の厚さの変更はそれぞ
れのバルブ11,12,13,14,15,16,1
7,18の開閉やあるいは弁開度の調節により冷却液の
圧力や流量や方向等を変化させることによって行うこと
ができる。
In order to evaporatively cool the heat exchanger 1 to cool the object to be cooled in the passage 2, the respective cooling liquid supply ports 3, 4,
Coolant is supplied to the heat exchanger 1 from 5, 6, 7, 8, 9, and 10. The cooling liquid located on the heat exchanger 1 absorbs heat of the object to be cooled in the passage 2 and vaporizes to cool the object to be cooled. The vaporized vapor diffuses into the atmosphere. The amount of heat transferred to the heat exchanger 1 can be changed without changing the thickness of the cooling liquid film formed on the heat exchanger 1 without causing a time delay. The thickness of the cooling liquid film can be changed by changing the respective valves 11, 12, 13, 14, 15, 16, 1.
This can be done by changing the pressure, flow rate, direction, etc. of the cooling liquid by opening / closing 7, 18 or adjusting the valve opening.

【0010】本実施例においては、気化冷却装置として
平板状の熱交換器1を用いた例を示したが、熱交換器と
しては平板状に限られるものではなく例えば円筒状やロ
―ル状、あるいは、円錐状や角状等従来周知の熱交換器
を用いることができる。また、被冷却物が流下するもの
でなく、所定量の被冷却物を収容して間欠的に冷却する
熱交換器を用いることもできる。
In this embodiment, the flat heat exchanger 1 is used as the evaporative cooling device. However, the heat exchanger is not limited to the flat heat exchanger, and may be, for example, a cylinder or a roll. Alternatively, a conventionally known heat exchanger such as a conical shape or a rectangular shape can be used. Further, it is also possible to use a heat exchanger that accommodates a predetermined amount of the object to be cooled and cools it intermittently, instead of the object to be cooled flowing down.

【0011】また本実施例においては、冷却液の気化蒸
気が大気中に放散する例を示したが、熱交換器の外周を
室状に区画してその室内に冷却液を供給すると共に、気
化蒸気を室と連通した吸引ポンプにより吸引して所定場
所に排除することもできる。
In this embodiment, the vaporized vapor of the cooling liquid is diffused into the atmosphere, but the outer periphery of the heat exchanger is divided into chambers and the cooling liquid is supplied into the chamber and vaporized. It is also possible to suck the vapor into a predetermined place by sucking it with a suction pump that communicates with the chamber.

【0012】[0012]

【発明の効果】本発明は次のような効果を奏する。冷却
液供給口から供給される冷却液の圧力や流量や方向等を
変化させることにより、冷却液膜の厚さを調節して時間
遅れを生じることなく伝達熱量を変化させることがで
き、被冷却物の劣化や損傷を防止して精度良く冷却する
ことができる。
The present invention has the following effects. By changing the pressure, flow rate, direction, etc. of the cooling liquid supplied from the cooling liquid supply port, it is possible to adjust the thickness of the cooling liquid film and change the amount of heat transferred without causing a time delay. It is possible to prevent deterioration and damage of the object and to cool it with high accuracy.

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

【図1】本発明の気化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 an evaporative cooling device of the present invention.

【符号の説明】[Explanation of symbols]

1 熱交換器 2 通路 3,4,5,6,7,8,9,10 冷却液供給口 1 heat exchanger 2 passages 3, 4, 5, 6, 7, 8, 9, 10 cooling liquid supply port

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 被冷却物に冷却液を供給して、冷却液の
気化熱によって被冷却物を冷却するものにおいて、冷却
液を供給する冷却液供給口を形成し、該冷却液供給口か
ら供給する冷却液の圧力や流量や方向等を制御して、被
冷却物表面に形成される冷却液膜の膜厚を調整すること
により被冷却物からの冷却熱量をコントロ―ルすること
を特徴とする気化冷却装置。
1. A cooling liquid supply port for supplying a cooling liquid, wherein the cooling liquid is supplied to a cooling target to cool the cooling target by heat of vaporization of the cooling liquid. Controlling the amount of cooling heat from the object to be cooled by controlling the pressure, flow rate, direction, etc. of the supplied cooling liquid to adjust the film thickness of the cooling liquid film formed on the surface of the object to be cooled. Evaporative cooling device.
JP5050142A 1993-02-15 1993-02-15 Evaporative cooling device Expired - Fee Related JP2802472B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5050142A JP2802472B2 (en) 1993-02-15 1993-02-15 Evaporative cooling device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5050142A JP2802472B2 (en) 1993-02-15 1993-02-15 Evaporative cooling device

Publications (2)

Publication Number Publication Date
JPH06241634A true JPH06241634A (en) 1994-09-02
JP2802472B2 JP2802472B2 (en) 1998-09-24

Family

ID=12850914

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5050142A Expired - Fee Related JP2802472B2 (en) 1993-02-15 1993-02-15 Evaporative cooling device

Country Status (1)

Country Link
JP (1) JP2802472B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002206834A (en) * 2000-12-28 2002-07-26 Seibu Giken Co Ltd Indirect evaporative cooling device
JP2011137630A (en) * 2011-02-22 2011-07-14 Sekisui Chem Co Ltd Cooling method of structure, cooling device, and structure including the cooling device

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH05164443A (en) * 1991-12-13 1993-06-29 Tlv Co Ltd Reduced pressure gasification cooling device

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH05164443A (en) * 1991-12-13 1993-06-29 Tlv Co Ltd Reduced pressure gasification cooling device

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002206834A (en) * 2000-12-28 2002-07-26 Seibu Giken Co Ltd Indirect evaporative cooling device
JP2011137630A (en) * 2011-02-22 2011-07-14 Sekisui Chem Co Ltd Cooling method of structure, cooling device, and structure including the cooling device

Also Published As

Publication number Publication date
JP2802472B2 (en) 1998-09-24

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