JP2761698B2 - Evaporative cooling device - Google Patents
Evaporative cooling deviceInfo
- Publication number
- JP2761698B2 JP2761698B2 JP5014493A JP5014493A JP2761698B2 JP 2761698 B2 JP2761698 B2 JP 2761698B2 JP 5014493 A JP5014493 A JP 5014493A JP 5014493 A JP5014493 A JP 5014493A JP 2761698 B2 JP2761698 B2 JP 2761698B2
- Authority
- JP
- Japan
- Prior art keywords
- cooling
- gas
- cooled
- liquid separation
- functional polymer
- 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 - Fee Related
Links
- 238000001816 cooling Methods 0.000 title claims description 31
- 239000000110 cooling liquid Substances 0.000 claims description 23
- 239000007788 liquid Substances 0.000 claims description 23
- 238000000926 separation method Methods 0.000 claims description 22
- 229920001002 functional polymer Polymers 0.000 claims description 20
- 230000008016 vaporization Effects 0.000 claims description 8
- 238000009834 vaporization Methods 0.000 claims description 6
- 239000012528 membrane Substances 0.000 description 12
- 239000012530 fluid Substances 0.000 description 6
- 238000006243 chemical reaction Methods 0.000 description 5
- 239000000498 cooling water Substances 0.000 description 4
- 239000002826 coolant Substances 0.000 description 3
- 238000001704 evaporation Methods 0.000 description 3
- 229920005597 polymer membrane Polymers 0.000 description 2
- 239000012809 cooling fluid Substances 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 229920006254 polymer film Polymers 0.000 description 1
- -1 pulp Substances 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Description
【0001】[0001]
【産業上の利用分野】本発明は、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 apparatus for vaporizing and cooling an object to be cooled by evaporating supplied cooling water. Specifically, a cooling device for a reaction vessel for performing various reactions,
The present invention relates to 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 cooling device for a reaction vessel, there is, for example, one disclosed in Japanese Patent Application Laid-Open No. 4-180829.
In this method, a cooling fluid chamber is formed in contact with the cooling vessel, a cooling water supply pipe for supplying cooling water is connected to the fluid chamber, and the fluid chamber is connected to a vacuum pump, and a gap is formed in an outer wall of the cooling vessel. Gas-liquid separation functional polymer membrane is provided through the cooling water supply between the outer wall of the cooling vessel and the gas-liquid separation functional polymer membrane to form a uniform water film all around the cooling vessel. By forming and vaporizing and cooling, cooling unevenness is prevented,
Product quality 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。In the above-described conventional apparatus, there is a problem that a time delay occurs when the degree of evaporative cooling, that is, the amount of heat transfer is changed. This is because the amount of heat transferred is changed by operating the vacuum pump to change the degree of vacuum in the fluid chamber or by changing the temperature of the supplied cooling liquid. It takes a predetermined time from the operation of the vacuum pump to the actual change in the degree of vacuum of the fluid chamber, and a delay occurs from the adjustment of the coolant temperature to the actual change of the fluid temperature in the fluid chamber. It is.
【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 control the temperature in the course of the reaction, and if a time delay occurs, the reactants 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。Accordingly, it is an object of the present invention to provide a vaporization cooling apparatus capable of controlling the degree of vaporization cooling, that is, the amount of heat transferred without causing a time delay, and capable of accurately adjusting the cooling temperature. 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。被冷却物表面と隙間を介して気液
分離機能高分子膜を配置し、該被冷却物表面と気液分離
機能高分子膜の間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、気液分離機
能高分子膜を被冷却物表面に対して移動可能に設けたも
のである。The constitution of the evaporative cooling device of the present invention is as follows. A gas-liquid separation functional polymer film is arranged via a gap with the surface of the object to be cooled, and a cooling liquid is supplied between the surface of the object to be cooled and the gas-liquid separation functional polymer film. In the cooling of the cooling object, a gas-liquid separation functional polymer film is provided so as to be movable with respect to the surface of the cooling object.
【0007】[0007]
【作用】供給された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
表面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、移動可能に設けた気液分離機能高分子膜を移動
して被冷却物表面との間の距離を変えることにより、被
冷却物表面に形成される冷却液膜の厚さも変化すること
によって伝達熱量を制御することができる。気液分離機
能高分子膜は、液体を通過させることがなく気体は通過
させることができる微小な通孔を多数有した高分子膜で
あり、冷却液は被冷却物表面との間に保持されると共
に、気化蒸気は膜を通過することができものである。こ
のように気液分離機能高分子膜の位置を変えることによ
り直ちに冷却液膜の厚さも変化することとなり、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 supplied removes the heat of the cooling object and evaporates to cool the cooling object. The amount of heat transferred from the surface of 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 increases, and the amount of transmitted heat also increases, thereby cooling the object to be cooled. When the cooling liquid film becomes thicker, the amount of vaporization of the cooling liquid is reduced and the amount of transferred heat is also reduced, so that the degree of cooling of the object to be cooled is reduced.
Therefore, the thickness of the cooling liquid film formed on the surface of the object to be cooled is also changed by moving the gas-liquid separation functional polymer film movably provided to change the distance from the surface of the object to be cooled. The amount of heat transferred can be controlled. The gas-liquid separation functional polymer membrane is a polymer membrane having a large number of small through holes that allow gas to pass without passing liquid, and the cooling liquid is held between the surface of the object to be cooled. At the same time, the vaporized vapor can pass through the membrane. By changing the position of the gas-liquid separation functional polymer film in this way, the thickness of the cooling liquid film also changes immediately, and the degree of cooling can be changed without 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の内部に被冷却対象
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の外表面に隙
間3を介して気液分離機能高分子膜4を配置する。気液
分離機能高分子膜4は、一端部5が取付け具6を介して
電動モ―タ7の回転軸8と結合させる。回転軸8の回転
により取付け具6が左右に移動することによって気液分
離機能高分子膜4も熱交換器1に対して移動することが
できるものである。気液分離機能高分子膜4の下端9は
支持棒10を介して支持台11によって摺動自在に支持
される。気液分離機能高分子膜4は、本実施例のように
モ―タで移動することもできるし、あるいは、手動で移
動することができるようにすることもできる。気液分離
機能高分子膜4の上部の隙間に冷却液を供給する冷却液
供給口12配置する。冷却液供給口12は、その下端部
をノズル状に形成すると共に、バルブ13を介して冷却
液管14と接続する。バルブ13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望ましい。BRIEF DESCRIPTION OF THE DRAWINGS FIG. In the present embodiment, an example in which a flat heat exchanger is used as the evaporative cooling device will be described. A passage 2 for an object to be cooled is formed inside a flat heat exchanger 1. The object to be cooled can pass through the passage 2 from below to above. A gas-liquid separation functional polymer membrane 4 is disposed on the outer surface of the heat exchanger 1 via a gap 3. One end 5 of the gas-liquid separation functional polymer membrane 4 is connected to a rotating shaft 8 of an electric motor 7 via a fixture 6. The gas-liquid separation functional polymer membrane 4 can also move with respect to the heat exchanger 1 by moving the fixture 6 right and left by the rotation of the rotation shaft 8. A lower end 9 of the gas-liquid separation functional polymer membrane 4 is slidably supported by a support base 11 via a support rod 10. The gas-liquid separation functional polymer membrane 4 can be moved by a motor as in this embodiment, or can be moved manually. A cooling liquid supply port 12 for supplying a cooling liquid is arranged in a gap above the gas-liquid separation functional polymer film 4. The cooling liquid supply port 12 has a lower end formed in a nozzle shape, and is connected to a cooling liquid pipe 14 via a valve 13. It is desirable that the valve 13 can be fully opened and fully closed and can adjust the valve opening.
【0009】熱交換器1を気化冷却して通路2内の被冷
却対象物を冷却するには、バルブ13を開弁させて冷却
液供給口12から冷却液を熱交換器1の表面と気液分離
機能高分子膜4との間に供給する。供給された冷却液は
通路2内の被冷却対象物の熱を奪って気化することによ
り被冷却対象物を冷却する。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、気液分
離機能高分子膜4を移動して熱交換器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。In order to cool the object to be cooled in the passage 2 by evaporating and cooling the heat exchanger 1, the valve 13 is opened and the cooling liquid is supplied from the cooling liquid supply port 12 to the surface of the heat exchanger 1. It is supplied to between the liquid separation function polymer membrane 4. The supplied cooling liquid cools the object to be cooled by removing the heat of the object to be cooled in the passage 2 and evaporating it. The vaporized vapor is released into the atmosphere. When changing the heat transfer amount of the heat exchanger 1, the gas-liquid separation functional polymer membrane 4 is moved to change the thickness of the cooling liquid film formed on the heat exchanger 1 without causing a time delay. be able to.
【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, an example is shown in which a flat heat exchanger 1 is used as the evaporative cooling device. However, the heat exchanger is not limited to a flat heat exchanger, and may be, for example, a cylindrical heat exchanger or a roll heat exchanger. Alternatively, a conventionally known heat exchanger having a conical shape or a square shape can be used. In addition, a heat exchanger that accommodates a predetermined amount of the object to be cooled and intermittently cools the object can be used instead of the object to be cooled.
【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。Further, in this embodiment, an example in which the vaporized vapor of the cooling liquid is diffused into the atmosphere has been shown. The vapor can be sucked by a suction pump communicating with the chamber and discharged to a predetermined place.
【0012】また本実施例においては、熱交換器1の片
側に気液分離機能高分子膜4を配置した例を示したがも
ちろん両側に配置することもできる。In this embodiment, an example is shown in which the gas-liquid separation functional polymer membrane 4 is arranged on one side of the heat exchanger 1, but it is needless to say that it can be arranged on both sides.
【0013】[0013]
【発明の効果】本発明は次のような効果を奏する。気液
分離機能高分子膜を被冷却物表面に対して移動させるこ
とにより冷却液膜の厚さを調節することができ、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る
こととなり、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. The thickness of the cooling liquid film can be adjusted by moving the gas-liquid separation function polymer film with respect to the surface of the object to be cooled, and the amount of heat transferred can be changed without a time delay. The object can be cooled with high precision while preventing deterioration and damage of the object.
【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.
1 熱交換器 2 通路 3 隙間 4 気液分離機能高分子膜 7 電動モ―タ 12 冷却液供給口 14 冷却液管 DESCRIPTION OF SYMBOLS 1 Heat exchanger 2 Passage 3 Gap 4 Gas-liquid separation functional polymer membrane 7 Electric motor 12 Coolant supply port 14 Coolant pipe
Claims (1)
能高分子膜を配置し、該被冷却物表面と気液分離機能高
分子膜の間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、気液分離機能高分
子膜を被冷却物表面に対して移動可能に設けたことを特
徴とする気化冷却装置。1. A gas-liquid separation functional polymer film is arranged through a gap between the surface of a cooling object and a gap, and a cooling liquid is supplied between the surface of the cooling object and the gas-liquid separation functional polymer film. An apparatus for cooling an object to be cooled by heat of vaporization, wherein a gas-liquid separation functional polymer film is provided movably with respect to the surface of the object to be cooled.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5014493A JP2761698B2 (en) | 1993-02-15 | 1993-02-15 | Evaporative cooling device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5014493A JP2761698B2 (en) | 1993-02-15 | 1993-02-15 | Evaporative cooling device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH06241636A JPH06241636A (en) | 1994-09-02 |
| JP2761698B2 true JP2761698B2 (en) | 1998-06-04 |
Family
ID=12850980
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP5014493A Expired - Fee Related JP2761698B2 (en) | 1993-02-15 | 1993-02-15 | Evaporative cooling device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2761698B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| AU1184900A (en) * | 1999-11-19 | 2001-06-04 | Seft Development Laboratory Co., Ltd. | Fluid cooling device |
-
1993
- 1993-02-15 JP JP5014493A patent/JP2761698B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH06241636A (en) | 1994-09-02 |
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