JPH0515774A - Heating and cooling apparatus - Google Patents
Heating and cooling apparatusInfo
- Publication number
- JPH0515774A JPH0515774A JP3201284A JP20128491A JPH0515774A JP H0515774 A JPH0515774 A JP H0515774A JP 3201284 A JP3201284 A JP 3201284A JP 20128491 A JP20128491 A JP 20128491A JP H0515774 A JPH0515774 A JP H0515774A
- Authority
- JP
- Japan
- Prior art keywords
- heating
- steam
- ejector
- cooling
- cooling water
- 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
Landscapes
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、加熱と冷却を1つの装
置で行う加熱冷却装置に関し、特に、加熱冷却室を吸引
手段によって低圧状態に維持し、100度前後の温度で
加熱と冷却を行う加熱冷却装置に関する。具体的には、
各種反応を行う反応釜の加熱冷却装置、食品等の加熱冷
却装置等として利用されるものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a heating / cooling apparatus for performing heating and cooling by a single apparatus, and more particularly, a heating / cooling chamber is maintained at a low pressure by suction means so that heating and cooling can be performed at a temperature of about 100 degrees. The present invention relates to a heating / cooling device. In particular,
It is used as a heating / cooling device for a reaction kettle that performs various reactions, a heating / cooling device for food, etc.
【0002】[0002]
【従来の技術】従来の反応釜の加熱冷却装置として、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、反応釜の流体室に加熱蒸気と、冷却水とし
ての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、加熱蒸気ある
いは冷却用の組合せポンプからの吐出水を供給して、反
応釜を加熱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ることにより、100度
以下の温度で加熱冷却することができる。2. Description of the Related Art As a conventional heating and cooling device for a reaction kettle, there is one disclosed in Japanese Patent Laid-Open No. 1-315336. This is a combination pump that combines an ejector, a tank, and a pump, a switching valve means that can supply heated steam to the fluid chamber of the reaction vessel, and a part of the discharge water of the combination pump as cooling water, and passes through the inside of the ejector. A temperature control unit for controlling the temperature of the fluid is provided, and heating water is supplied to the fluid chamber of the reaction vessel or discharge water from a combination pump for cooling to heat and cool the reaction vessel. The suction force generated in the ejector, that is, the degree of pressure reduction, becomes a saturation pressure with respect to the temperature of the fluid passing through the ejector, so the degree of pressure reduction in the ejector is increased,
By increasing the degree of pressure reduction in the cooling chamber, heating and cooling can be performed at a temperature of 100 degrees or less.
【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、減圧度合を充分に高めることができず、比較的低温
例えば20度とか30度の温度で加熱冷却することがで
きない問題があった。エゼクタで発生する減圧度は、そ
こを通過する冷却水の温度に対する飽和圧力までしか高
めることができないためである。冷却水として一般的に
は地下水等の工業用水が用いられるが、この温度は通常
25度程度であり、加熱のために供給される蒸気や、被
冷却物からの熱等によって、せいぜい50度程度の温度
までしか下げることができないのである。The above-mentioned conventional devices have a problem that the degree of pressure reduction cannot be sufficiently increased and heating and cooling cannot be carried out at a relatively low temperature, for example, a temperature of 20 degrees or 30 degrees. This is because the degree of pressure reduction generated at the ejector can be increased only up to the saturation pressure with respect to the temperature of the cooling water passing therethrough. Industrial water such as groundwater is generally used as cooling water, but this temperature is usually about 25 degrees, and at most about 50 degrees due to steam supplied for heating and heat from the object to be cooled. It can only be reduced to the temperature of.
【0004】従って本発明の技術的課題は、50度程度
以下の温度でも加熱や冷却を行うことのできる加熱冷却
装置を得ることである。Therefore, a technical object of the present invention is to obtain a heating / cooling device capable of heating and cooling even at a temperature of about 50 ° C. or lower.
【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。加熱冷却室を有する熱交換器
と、加熱冷却室に蒸気と冷却水を供給する管路と、加熱
冷却室と連通した吸引手段とから成るものにおいて、吸
引手段として蒸気エゼクタを配置し、上記蒸気供給管路
と蒸気エゼクタのノズル部を接続し、蒸気エゼクタの吸
込室と加熱冷却室を連通したものである。The structure of the reduced pressure evaporative cooling apparatus of the present invention is as follows. A heat exchanger having a heating / cooling chamber, a pipeline for supplying steam and cooling water to the heating / cooling chamber, and a suction means communicating with the heating / cooling chamber, wherein a steam ejector is arranged as the suction means, The supply pipe line and the nozzle portion of the steam ejector are connected, and the suction chamber of the steam ejector and the heating / cooling chamber are communicated with each other.
【0006】[0006]
【作用】吸引手段として蒸気エゼクタを用い、加熱用の
蒸気によって減圧状態を作り出すことにより、冷却水の
温度に関係なく高い減圧度合を維持することができる。
従って、気化冷却室も高い減圧状態となり、50度以下
の低温度でも加熱や冷却を行うことができる。By using a steam ejector as the suction means and creating a depressurized state by the steam for heating, a high degree of depressurization can be maintained regardless of the temperature of the cooling water.
Therefore, the vaporization cooling chamber is also in a highly depressurized state, and heating and cooling can be performed even at a low temperature of 50 ° C. or less.
【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、熱交換器としてジャケット式の反応釜を用い
た例を示す。 加熱冷却室としてのジャケット部を備え
た反応釜21と、エゼクタ22と、蒸気供給管2と、冷
却水供給管3とで加熱冷却装置を構成する。反応釜21
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6、製品出口7、撹拌器8を備え、ジャケ
ット部5には蒸気供給口9と、冷却水供給口10と流体
排出口12,13を設けてある。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The illustrated embodiment will be described in detail. In this example, a jacket-type reaction vessel is used as the heat exchanger. A heating / cooling device is constituted by the reaction vessel 21 having a jacket as a heating / cooling chamber, the ejector 22, the steam supply pipe 2, and the cooling water supply pipe 3. Reaction kettle 21
Has a jacket portion 5 formed over substantially the entire circumference and is provided with a raw material inlet 6, a product outlet 7, and an agitator 8. The jacket portion 5 has a steam supply port 9, a cooling water supply port 10, and a fluid discharge port 12, 13 is provided.
【0008】蒸気供給管2に圧力調節弁23を介して蒸
気供給口9と連通する。蒸気供給管2はまた自動弁24
を介してエゼクタ22のノズル25と連通する。エゼク
タ22に流体吸込室28,29を設けて、ジャケット部
5の流体排出口12,13と接続する。エゼクタ22の
二次側には液体と蒸気を分離するセパレ―タ30を連通
する。セパレ―タ30の下部はスチ―ムトラップ31と
接続し、上部は三方切替え弁32と接続する。三方切替
え弁32には分離した蒸気の排気管35と別途の蒸気使
用機器に供給する管36とを接続する。The steam supply pipe 2 is connected to the steam supply port 9 via a pressure control valve 23. The steam supply pipe 2 also has an automatic valve 24.
Through the nozzle 25 of the ejector 22. Fluid ejecting chambers 28 and 29 are provided in the ejector 22 and are connected to the fluid outlets 12 and 13 of the jacket portion 5. A separator 30 for separating liquid and vapor is connected to the secondary side of the ejector 22. The lower part of the separator 30 is connected to the steam trap 31, and the upper part is connected to the three-way switching valve 32. To the three-way switching valve 32, a separated steam exhaust pipe 35 and a pipe 36 for supplying a separate steam-using device are connected.
【0009】冷却水供給管3は自動弁50を介して冷却
水供給口10と接続する。参照番号51,52はそれぞ
れ自動弁を示し、同じく参照番号53は、ノズル25に
供給される蒸気中のドレンを排除するためのスチ―ムト
ラップである。The cooling water supply pipe 3 is connected to the cooling water supply port 10 via an automatic valve 50. Reference numerals 51 and 52 denote automatic valves, respectively, and reference numeral 53 is a steam trap for eliminating drain in the vapor supplied to the nozzle 25.
【0010】反応釜21を加熱する場合は、圧力調節弁
23と自動弁24を開弁して、ジャケット部5とエゼク
タ22に蒸気を供給する。エゼクタ22の吸引力によ
り、ジャケット部5内は減圧状態になると共に、圧力調
節弁23の開度を絞ることによって、ジャケット部5内
の蒸気は大気圧以下となり、100度以下の温度とな
る。自動弁24の開度を調節してノズル25への供給蒸
気量を増やすことにより、エゼクタ22での減圧度合は
高まり、ジャケット部5内の蒸気温度を50度程度以下
とすることができる。反応釜21を加熱して生じたドレ
ンは流体排出口12からエゼクタ22に吸引され、残余
の蒸気は流体排出口13から同じくエゼクタ22に吸引
される。エゼクタ22に吸引されたドレンと蒸気は、セ
パレ―タ30で分離され、ドレンはスチ―ムトラップ3
1を経て系外に排出され、蒸気は三方弁32を経て、系
外に排除されるか、別途蒸気使用機器に供給される。When heating the reaction kettle 21, the pressure control valve 23 and the automatic valve 24 are opened to supply steam to the jacket 5 and the ejector 22. By the suction force of the ejector 22, the inside of the jacket portion 5 is depressurized, and the opening of the pressure control valve 23 is narrowed, so that the vapor in the jacket portion 5 becomes atmospheric pressure or less and the temperature becomes 100 degrees or less. By adjusting the opening degree of the automatic valve 24 and increasing the amount of steam supplied to the nozzle 25, the degree of pressure reduction in the ejector 22 is increased, and the steam temperature in the jacket portion 5 can be set to about 50 degrees or less. Drain generated by heating the reaction kettle 21 is sucked into the ejector 22 from the fluid outlet 12, and the remaining vapor is sucked into the ejector 22 from the fluid outlet 13 as well. The drain and the vapor sucked into the ejector 22 are separated by the separator 30, and the drain is the steam trap 3
After being discharged to the outside of the system via 1, the steam is discharged to the outside of the system via the three-way valve 32, or is separately supplied to a steam using device.
【0011】反応釜21を冷却する場合、圧力調節弁2
3を閉じてジャケット部5への蒸気の供給を停止し、弁
50を開弁してジャケット部5に冷却水を供給する。ジ
ャケット部5内はエゼクタ22により減圧状態となって
おり、供給された冷却水は、被冷却物としての反応釜2
1の熱によりただちに気化し、その蒸発潜熱により反応
釜21を冷却する。冷却により生じた気化蒸気と一部残
った冷却水はエゼクタ22に吸引され、冷却水はスチ―
ムトラップ31より、気化蒸気は排気管35より系外に
排出される。When the reaction vessel 21 is cooled, the pressure control valve 2
3 is closed to stop the supply of steam to the jacket 5, and the valve 50 is opened to supply cooling water to the jacket 5. The inside of the jacket portion 5 is depressurized by the ejector 22, and the supplied cooling water is the reaction kettle 2 serving as the object to be cooled.
The heat of 1 immediately evaporates and the latent heat of vaporization cools the reaction vessel 21. The vaporized steam generated by cooling and the partially remaining cooling water are sucked into the ejector 22, and the cooling water is steamed.
The vaporized vapor is exhausted from the mutrap 31 through the exhaust pipe 35 to the outside of the system.
【0012】本実施例においては、エゼクタ22を1台
用いた例を示したが、流体排出口12,13にそれぞれ
エゼクタを接続することもできる。In this embodiment, an example in which one ejector 22 is used is shown, but ejectors can be connected to the fluid discharge ports 12 and 13, respectively.
【0013】[0013]
【発明の効果】冷却水の水温に関係なく、蒸気エゼクタ
によって高い減圧状態を作り出すことができ、50度程
度以下の比較的低温度の加熱冷却を行うことができる。EFFECTS OF THE INVENTION A high depressurized state can be created by a steam ejector regardless of the temperature of cooling water, and heating and cooling at a relatively low temperature of about 50 degrees or less can be performed.
【図1】本発明の加熱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 heating / cooling device of the present invention.
2 蒸気供給管 3 冷却水供給管 5 ジャケット部 12,13 流体排出口 22 エゼクタ 23 圧力調節弁 25 ノズル 30 セパレ―タ 2 Steam supply pipe 3 Cooling water supply pipe 5 Jacket part 12, 13 Fluid discharge port 22 Ejector 23 Pressure control valve 25 Nozzle 30 Separator
Claims (1)
却室に蒸気と冷却水を供給する管路と、加熱冷却室と連
通した吸引手段とから成るものにおいて、吸引手段とし
て蒸気エゼクタを配置し、上記蒸気供給管路と蒸気エゼ
クタのノズル部を接続し、蒸気エゼクタの吸込室と加熱
冷却室を連通した加熱冷却装置。Claim: What is claimed is: 1. A heat exchanger comprising a heating / cooling chamber, a pipeline for supplying steam and cooling water to the heating / cooling chamber, and a suction means communicating with the heating / cooling chamber. A heating / cooling device in which a steam ejector is arranged as a suction means, the above-mentioned steam supply pipe line and a nozzle portion of the steam ejector are connected, and a suction chamber of the steam ejector and a heating / cooling chamber are communicated with each other.
Priority Applications (13)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP20128491A JP2724776B2 (en) | 1991-07-15 | 1991-07-15 | Heating and cooling device |
AU11427/92A AU635457B2 (en) | 1991-04-15 | 1992-03-05 | Reduced pressure heat treating device |
US07/848,286 US5209284A (en) | 1991-04-15 | 1992-03-09 | Reduced pressure heat treating device |
DE69200056T DE69200056T2 (en) | 1991-04-15 | 1992-03-19 | Heat treatment device with reduced pressure. |
EP92302380A EP0509646B1 (en) | 1991-04-15 | 1992-03-19 | Reduced pressure heat treating device |
DK92302380.8T DK0509646T3 (en) | 1991-04-15 | 1992-03-19 | Heat treatment device with reduced pressure |
ES92302380T ES2052404T3 (en) | 1991-04-15 | 1992-03-19 | HEAT TREATMENT DEVICE. |
KR1019920005277A KR960010656B1 (en) | 1991-04-15 | 1992-03-30 | Reduced pressure heat treating device |
CN92102343A CN1034633C (en) | 1991-04-15 | 1992-04-02 | Reduced pressure heat treating device |
CA002065507A CA2065507C (en) | 1991-04-15 | 1992-04-07 | Reduced pressure heat treating device |
NO921469A NO301188B1 (en) | 1991-04-15 | 1992-04-13 | Device for heat treatment under reduced pressure |
BR929201370A BR9201370A (en) | 1991-04-15 | 1992-04-14 | REDUCED PRESSURE THERMAL TREATMENT APPLIANCE |
HK98100785A HK1001825A1 (en) | 1991-05-15 | 1998-02-04 | Reduced pressure heat treating device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP20128491A JP2724776B2 (en) | 1991-07-15 | 1991-07-15 | Heating and cooling device |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0515774A true JPH0515774A (en) | 1993-01-26 |
JP2724776B2 JP2724776B2 (en) | 1998-03-09 |
Family
ID=16438423
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP20128491A Expired - Fee Related JP2724776B2 (en) | 1991-04-15 | 1991-07-15 | Heating and cooling device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2724776B2 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6593031B1 (en) | 1999-08-13 | 2003-07-15 | Hitachi Maxell, Ltd. | Nickel metal-hydride cell |
JP2013202468A (en) * | 2012-03-28 | 2013-10-07 | Tlv Co Ltd | Low-pressure vapor heating apparatus |
-
1991
- 1991-07-15 JP JP20128491A patent/JP2724776B2/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6593031B1 (en) | 1999-08-13 | 2003-07-15 | Hitachi Maxell, Ltd. | Nickel metal-hydride cell |
JP2013202468A (en) * | 2012-03-28 | 2013-10-07 | Tlv Co Ltd | Low-pressure vapor heating apparatus |
Also Published As
Publication number | Publication date |
---|---|
JP2724776B2 (en) | 1998-03-09 |
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