JPH04338231A - Decompressed vaporization cooler - Google Patents
Decompressed vaporization coolerInfo
- Publication number
- JPH04338231A JPH04338231A JP14092791A JP14092791A JPH04338231A JP H04338231 A JPH04338231 A JP H04338231A JP 14092791 A JP14092791 A JP 14092791A JP 14092791 A JP14092791 A JP 14092791A JP H04338231 A JPH04338231 A JP H04338231A
- Authority
- JP
- Japan
- Prior art keywords
- ejector
- tank
- pump
- cooling water
- 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.)
- Granted
Links
- 238000009834 vaporization Methods 0.000 title abstract description 6
- 230000008016 vaporization Effects 0.000 title abstract description 6
- 238000001816 cooling Methods 0.000 claims abstract description 29
- 239000000498 cooling water Substances 0.000 claims abstract description 26
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 13
- 238000006243 chemical reaction Methods 0.000 abstract description 12
- 239000012530 fluid Substances 0.000 description 20
- 230000006837 decompression Effects 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 230000007423 decrease Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 101100298225 Caenorhabditis elegans pot-2 gene Proteins 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000001934 delay Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
Description
【0001】0001
【産業上の利用分野】本発明は、冷却室内を減圧状態に
して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、食品等の気化冷却
装置等に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a system for evaporative cooling of objects to be cooled by reducing the pressure within a cooling chamber. Specifically, the present invention relates to a cooling device for a reaction vessel in which various reactions are carried out, an evaporative cooling device for foods, etc.
【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1−315336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ポンプを組合せた組合せポ
ンプと、反応釜の流体室に組合せポンプの吐出水の一部
を供給できる切替え弁手段と、エゼクタ内を通過する流
体の温度を制御する温度制御部とから成り、反応釜の流
体室に、冷却用の組合せポンプからの吐出水を供給して
、反応釜を気化冷却するものである。エゼクタで生じる
吸引力即ち減圧度は、エゼクタを通過する流体の温度に
対する飽和圧力となるために、エゼクタでの減圧度を高
め、ひいては冷却室の減圧度を高めて、気化冷却をより
促進するためには、温度制御部によりエゼクタ内を通過
する流体の温度を低下せしめることによりできる。2. Description of the Related Art A conventional cooling device for a reaction vessel is disclosed in, for example, Japanese Unexamined Patent Publication No. 1-315336. This consists of a combination pump that combines an ejector, a tank, and a pump, a switching valve that can supply part of the water discharged from the combination pump to the fluid chamber of the reaction vessel, and a temperature control that controls the temperature of the fluid passing through the ejector. The reactor is evaporatively cooled by supplying water discharged from a cooling combination pump to the fluid chamber of the reactor. The suction force, that is, the degree of reduced pressure generated in the ejector becomes the saturation pressure for the temperature of the fluid passing through the ejector, increasing the degree of reduced pressure in the ejector, which in turn increases the degree of reduced pressure in the cooling chamber to further promote evaporative cooling. This can be achieved by lowering the temperature of the fluid passing through the ejector using a temperature control section.
【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
、減圧度を変化させ、気化冷却の度合を変化させる場合
に時間遅れを生じる問題があった。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。この時間遅れの原因は、エゼクタを通
過する流体の温度を速やかに変化させることができない
ためである。即ち、上記従来のものでは、温度制御部か
ら冷却水をタンクに供給し、タンク内の流体の温度が低
下して初めてエゼクタを通過する流体の温度も低下する
ため、タンク内の水温を調節するために時間がかかり、
遅れを生じるのである。[Problems to be Solved by the Invention] The above-mentioned conventional method has the problem of a time delay occurring when changing the degree of pressure reduction and changing the degree of evaporative cooling. In the reaction vessel,
It is necessary to precisely control the temperature during the reaction process, and if a time delay occurs, the reactants may deteriorate or be damaged. This time delay is caused by the inability to quickly change the temperature of the fluid passing through the ejector. That is, in the conventional system described above, cooling water is supplied to the tank from the temperature control section, and only after the temperature of the fluid in the tank decreases will the temperature of the fluid passing through the ejector also decrease, so the water temperature in the tank is adjusted. It takes time to
This causes delays.
【0004】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、気化冷却の度合即ち冷却温度の変更を
行うことのできる減圧気化冷却装置を得ることである。[0004] Accordingly, the technical object of the present invention is to provide a reduced pressure evaporative cooling device that can change the degree of evaporative cooling, that is, the cooling temperature, without causing a time delay.
【0005】[0005]
【課題を解決する為の手段】本発明の減圧気化冷却装置
の構成は次の通りである。エゼクタとタンクとポンプを
組合せた組み合せポンプと、該エゼクタと連通した気化
冷却室と、上記タンクに冷却水を供給する冷却水供給通
路とから成る気化冷却装置において、タンクを複数個配
置し、それぞれのタンクに冷却水供給通路を接続すると
共に、弁手段を介してポンプと連通したものである。[Means for Solving the Problems] The structure of the reduced pressure evaporative cooling device of the present invention is as follows. In an evaporative cooling device consisting of a combination pump that combines an ejector, a tank, and a pump, an evaporative cooling chamber communicating with the ejector, and a cooling water supply passage that supplies cooling water to the tank, a plurality of tanks are arranged, and each A cooling water supply passage is connected to the tank and communicated with the pump via valve means.
【0006】[0006]
【作用】タンク内の流体をポンプによりエゼクタに供給
することにより、エゼクタ部で流体温度に応じた飽和圧
力となり、流体温度を100度以下とすることによって
大気圧以下の減圧状態とすることができる。エゼクタで
減圧状態となると連通した気化冷却室も減圧状態となり
、冷却水は気化して被冷却物を気化冷却する。熱を奪っ
て気化した蒸気はエゼクタに吸引され、1つのタンクに
至る。タンク内の冷却水により蒸気は液体化し、ポンプ
によってエゼクタに供給される。気化温度を変える場合
、即ち減圧度を変える場合、弁手段を操作して他方のタ
ンクとポンプを接続する。この他方のタンクには所望減
圧度に応じた温度の冷却水を貯溜しておくことにより、
エゼクタ部には必要とする温度の流体が速やかに供給さ
れ、所望の吸引力即ち減圧度を発生する。[Operation] By supplying the fluid in the tank to the ejector using a pump, the ejector section achieves a saturated pressure according to the fluid temperature, and by lowering the fluid temperature to 100 degrees or less, it is possible to create a reduced pressure state below atmospheric pressure. . When the pressure is reduced in the ejector, the communicating evaporative cooling chamber is also reduced in pressure, and the cooling water is vaporized to evaporatively cool the object to be cooled. The steam that has been vaporized by removing heat is sucked into the ejector and reaches one tank. The steam is liquefied by the cooling water in the tank and supplied to the ejector by a pump. When changing the vaporization temperature, that is, when changing the degree of pressure reduction, the valve means is operated to connect the other tank and the pump. By storing cooling water at a temperature corresponding to the desired degree of decompression in this other tank,
Fluid at the required temperature is quickly supplied to the ejector section to generate the desired suction force, that is, the degree of reduced pressure.
【0007】[0007]
【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反応釜を用いた例を示す
。気化冷却室としてのジャケット部を備えた反応釜21
と、組み合せポンプ22と、タンク1,2と、冷却水供
給通路28とで減圧気化冷却装置を構成する。反応釜2
1は、ほぼ全周にわたりジャケット部5を形成すると共
に、原料入口3、製品出口4、撹拌器6、被冷却物の温
度を検出する温度センサ―20を備え、ジャケット部5
には冷却水供給口5a,5bと流体排出口7を設けてあ
る。[Embodiment] The illustrated embodiment will be explained in detail. In this example, an example is shown in which a reaction vessel is used as the evaporative cooling device. Reaction vessel 21 equipped with a jacket section as a vaporization cooling chamber
, the combined pump 22, the tanks 1 and 2, and the cooling water supply passage 28 constitute a reduced pressure evaporation cooling device. Reaction pot 2
1 forms a jacket part 5 over almost the entire circumference, and is equipped with a raw material inlet 3, a product outlet 4, a stirrer 6, and a temperature sensor 20 for detecting the temperature of the object to be cooled.
Cooling water supply ports 5a, 5b and a fluid discharge port 7 are provided in the cooling water supply port 5a and 5b.
【0008】組合せポンプ22は、ポンプ30がタンク
1,2に吸込側を接続され吐出側をエゼクタ32のノズ
ル33に接続し、エゼクタ32のディフュ―ザ34が弁
51,52を介してタンク1,2の上部空間に接続され
た構成のものであり、エゼクタ32と反応釜21の流体
排出口7とが弁10とトラップ12を介して接続されて
いる。この組合せポンプ22は、ポンプ30の作動によ
りタンク1又は2内の水をエゼクタ32に供給して吸引
作用させ、タンク1又は2に戻すようになっている。In the combination pump 22, a pump 30 has a suction side connected to the tanks 1 and 2 and a discharge side connected to a nozzle 33 of an ejector 32, and a diffuser 34 of the ejector 32 connects the tank 1 through valves 51 and 52. , 2, and the ejector 32 and the fluid discharge port 7 of the reaction vessel 21 are connected via the valve 10 and the trap 12. This combination pump 22 is configured to supply the water in the tank 1 or 2 to the ejector 32 by operation of the pump 30, apply suction thereto, and return the water to the tank 1 or 2.
【0009】冷却水供給通路28は、タンク1あるいは
2内の水温を制御するように設けたものであり、タンク
1又は2内に弁53,55,56を介して冷却水を供給
することによって制御するようになっている。タンク1
あるいは2には、それぞれの水位と流体温度を検出する
水位センサ―57,58,59,60と温度センサ―6
1,62を取り付ける。タンク1,2は弁手段8,9を
介してポンプ30と連通する。The cooling water supply passage 28 is provided to control the water temperature in the tank 1 or 2, and is controlled by supplying cooling water into the tank 1 or 2 through the valves 53, 55, 56. It is meant to be controlled. tank 1
Alternatively, 2 includes water level sensors 57, 58, 59, 60 and a temperature sensor 6 that detect the respective water levels and fluid temperatures.
Attach 1,62. Tanks 1,2 communicate with pump 30 via valve means 8,9.
【0010】冷却水供給通路28からジャケット部5に
弁63を介して冷却水供給管26を、取り付ける。A cooling water supply pipe 26 is attached from the cooling water supply passage 28 to the jacket portion 5 via a valve 63.
【0011】ポンプ30とエゼクタ32を接続する通路
の一部を分岐して余剰水排出弁25を取り付け、タンク
1及び2内の水位センサ―57,58,59,60から
の信号により、タンク1及び2内の水位を所定範囲に保
つようにする。各弁及びセンサ―は図示していないが制
御部と接続して集中制御できるようにすることもできる
。A part of the passage connecting the pump 30 and the ejector 32 is branched and an excess water discharge valve 25 is installed, and the water level sensor 57, 58, 59, 60 in the tanks 1 and 2 causes and 2 to maintain the water level within a predetermined range. Although not shown, each valve and sensor may be connected to a control unit for centralized control.
【0012】被冷却物を冷却する場合、即ちジャケット
部5で気化冷却を行う場合、冷却水供給通路28から弁
53,55を介してタンク1内に冷却水を供給すると共
に、弁63を介してジャケット部5にも冷却水を供給す
る。この場合弁9,52,56は閉じ、弁8,10,5
1は開いておく。ポンプ30によりタンク1内の流体は
エゼクタ32に至り吸引力を生じる。エゼクタ32の吸
引力により、ジャケット部5内も減圧状態となり、冷却
水は被冷却物の熱により気化し、被冷却物を冷却する。
気化した蒸気は弁10を通り、エゼクタ32に吸引され
タンク1に至る。When cooling the object to be cooled, that is, when performing evaporative cooling in the jacket section 5, cooling water is supplied from the cooling water supply passage 28 into the tank 1 through the valves 53 and 55, and at the same time, the cooling water is supplied through the valve 63. Cooling water is also supplied to the jacket part 5. In this case valves 9, 52, 56 are closed and valves 8, 10, 5
Leave 1 open. The fluid in the tank 1 reaches the ejector 32 by the pump 30 and generates a suction force. Due to the suction force of the ejector 32, the inside of the jacket portion 5 is also brought into a reduced pressure state, and the cooling water is vaporized by the heat of the object to be cooled, thereby cooling the object. The vaporized steam passes through the valve 10, is sucked into the ejector 32, and reaches the tank 1.
【0013】冷却度合を変えるために、ジャケット部5
内の減圧度を変える場合、あらかじめタンク2内に対応
した温度の流体を溜めておき、弁8,9,51,52を
操作することにより、タンク2の所望温度の流体をエゼ
クタ32に供給することによって速やかに変えることが
できる。[0013] In order to change the degree of cooling, the jacket part 5
When changing the degree of pressure reduction in the tank 2, fluid at the corresponding temperature is stored in the tank 2 in advance, and by operating the valves 8, 9, 51, and 52, the fluid at the desired temperature in the tank 2 is supplied to the ejector 32. This allows for quick changes.
【0014】本実施例においては、タンク1,2に対し
てポンプ30を1台用いた例を示したが、それぞれのタ
ンク1,2に、例えば流体の温度に適したポンプを複数
台設置することもできる。In this embodiment, one pump 30 is used for the tanks 1 and 2, but a plurality of pumps suitable for the temperature of the fluid may be installed in each tank 1 and 2, for example. You can also do that.
【0015】本実施例においては、ポンプ30からエゼ
クタ32に至る通路を分岐して弁67を設けたことによ
り、ポンプ30の吐出水の一部を冷却水供給口5bから
ジャケット部5に供給して冷却することもできる。In this embodiment, by branching the passage from the pump 30 to the ejector 32 and providing a valve 67, a portion of the water discharged from the pump 30 is supplied to the jacket portion 5 from the cooling water supply port 5b. It can also be cooled down.
【0016】また本実施例においては、弁69を介して
加熱用の蒸気供給通路68を設けたことにより、減圧気
化冷却のみならず、減圧蒸気加熱あるいは正圧蒸気加熱
を行うこともできる。Furthermore, in this embodiment, by providing a heating steam supply passage 68 via a valve 69, not only vacuum vaporization cooling but also vacuum steam heating or positive pressure steam heating can be performed.
【0017】[0017]
【発明の効果】本発明は次のような効果を奏する。必要
とする減圧度に応じた温度の流体を他方のタンクに貯溜
しておくことにより、速やかにエゼクタの吸引力を変化
せしめることができ、減圧度即ち気化温度を変更する場
合に時間遅れを生じることがない。[Effects of the Invention] The present invention has the following effects. By storing fluid at a temperature corresponding to the required degree of decompression in the other tank, the suction force of the ejector can be changed quickly, causing a time delay when changing the degree of decompression, that is, the vaporization temperature. Never.
【図1】本発明の減圧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 a reduced pressure evaporative cooling device of the present invention.
1,2 タンク 5 ジャケット部 8,9 弁手段 21 反応釜 22 組合せポンプ 28 冷却水供給通路 30 ポンプ 32 エゼクタ 1,2 Tank 5 Jacket part 8,9 Valve means 21 Reaction pot 22 Combination pump 28 Cooling water supply passage 30 Pump 32 Ejector
Claims (1)
組合せポンプと、該エゼクタと連通した気化冷却室と、
上記タンクに冷却水を供給する冷却水供給通路とから成
る気化冷却装置において、タンクを複数個配置し、それ
ぞれのタンクに冷却水供給通路を接続すると共に、弁手
段を介してポンプと連通した減圧気化冷却装置。Claim 1: A combination pump that combines an ejector, a tank, and a pump, and an evaporative cooling chamber that communicates with the ejector.
In an evaporative cooling device comprising a cooling water supply passage for supplying cooling water to the tank, a plurality of tanks are arranged, a cooling water supply passage is connected to each tank, and a pressure reducing device is connected to a pump via a valve means. Evaporative cooling device.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP14092791A JP2724774B2 (en) | 1991-05-15 | 1991-05-15 | Decompression evaporative cooling equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP14092791A JP2724774B2 (en) | 1991-05-15 | 1991-05-15 | Decompression evaporative cooling equipment |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH04338231A true JPH04338231A (en) | 1992-11-25 |
JP2724774B2 JP2724774B2 (en) | 1998-03-09 |
Family
ID=15280054
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP14092791A Expired - Fee Related JP2724774B2 (en) | 1991-05-15 | 1991-05-15 | Decompression evaporative cooling equipment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2724774B2 (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0515773A (en) * | 1991-07-15 | 1993-01-26 | Tlv Co Ltd | Vacuum evaporation cooling apparatus |
JP2002306955A (en) * | 2001-04-13 | 2002-10-22 | Tlv Co Ltd | Steam heating apparatus |
JP2002306956A (en) * | 2001-04-13 | 2002-10-22 | Tlv Co Ltd | Steam heating apparatus |
JP2008224175A (en) * | 2007-03-15 | 2008-09-25 | Tlv Co Ltd | Heating and cooling device |
-
1991
- 1991-05-15 JP JP14092791A patent/JP2724774B2/en not_active Expired - Fee Related
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0515773A (en) * | 1991-07-15 | 1993-01-26 | Tlv Co Ltd | Vacuum evaporation cooling apparatus |
JP2002306955A (en) * | 2001-04-13 | 2002-10-22 | Tlv Co Ltd | Steam heating apparatus |
JP2002306956A (en) * | 2001-04-13 | 2002-10-22 | Tlv Co Ltd | Steam heating apparatus |
JP2008224175A (en) * | 2007-03-15 | 2008-09-25 | Tlv Co Ltd | Heating and cooling device |
Also Published As
Publication number | Publication date |
---|---|
JP2724774B2 (en) | 1998-03-09 |
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