JP3013070B2 - Heating and cooling device - Google Patents

Heating and cooling device

Info

Publication number
JP3013070B2
JP3013070B2 JP5281707A JP28170793A JP3013070B2 JP 3013070 B2 JP3013070 B2 JP 3013070B2 JP 5281707 A JP5281707 A JP 5281707A JP 28170793 A JP28170793 A JP 28170793A JP 3013070 B2 JP3013070 B2 JP 3013070B2
Authority
JP
Japan
Prior art keywords
cooling
heating
steam
chamber
cooling chamber
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
Application number
JP5281707A
Other languages
Japanese (ja)
Other versions
JPH07108167A (en
Inventor
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 JP5281707A priority Critical patent/JP3013070B2/en
Publication of JPH07108167A publication Critical patent/JPH07108167A/en
Application granted granted Critical
Publication of JP3013070B2 publication Critical patent/JP3013070B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は熱交換器内の被加熱冷却
物を加熱したり冷却するものに関し、特にその温度が3
0度Cから100度C程度の比較的低温の場合に適した
加熱冷却装置に関する。具体的には重合反応に用いられ
る各種反応釜や食品の蒸溜装置、濃縮装置、及び、殺菌
装置等の加熱冷却に用いるものである。これらの場合の
被熱処理物は少しの温度上昇によって熱損傷を生じてし
まう場合が多く、加熱冷却の温度を精度良く維持する必
要があった。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a device for heating and cooling a material to be heated in a heat exchanger, and more particularly to a device for heating and cooling a material to be cooled.
The present invention relates to a heating and cooling device suitable for a relatively low temperature of about 0 ° C. to 100 ° C. More specifically, it is used for heating and cooling various kinds of reaction pots used for the polymerization reaction, a distilling device for food, a concentrating device, a sterilizing device, and the like. In these cases, the heat-treated material often causes thermal damage due to a slight rise in temperature, and it is necessary to accurately maintain the heating and cooling temperatures.

【0002】[0002]

【従来技術】従来の熱損傷を防止する加熱冷却装置とし
て例えば反応釜の例が特開平3−127625号公報に
示されたものが用いられていた。これは、反応釜の外壁
に多孔質状部材を微小な隙間を介して設けることによ
り、多孔質状部材によって加熱蒸気の過度の供給が防止
され、被加熱物の熱損傷を防止しながら加熱を行なうこ
とができるもと共に、冷却時においても反応釜の外壁全
体に均一に冷却水を供給することができ、反応釜全体を
均一に冷却することができるものである。
2. Description of the Related Art As a conventional heating and cooling apparatus for preventing thermal damage, for example, a reaction vessel shown in Japanese Patent Application Laid-Open No. 3-127625 has been used. This is because, by providing a porous member on the outer wall of the reactor via a minute gap, excessive supply of heating steam is prevented by the porous member, and heating is performed while preventing heat damage to the object to be heated. In addition to this, the cooling water can be uniformly supplied to the entire outer wall of the reactor even during cooling, and the entire reactor can be uniformly cooled.

【0003】[0003]

【本発明が解決しようとする課題】上記従来の加熱冷却
装置は、使用開始の初期の段階においては精度良く加熱
冷却温度を維持することができるが、長期間の使用を経
ると精度良く温度を維持することが困難となってしまう
問題があった。これは、多孔質状部材を介して加熱蒸気
や冷却水を供給しているために、長期間使用している内
に多孔質状部材が詰ってしまい、精度良く温度を維持す
ることができなくなってしまうためである。一般の加熱
用蒸気や冷却水においてはスケ―ル等の異物が混入して
いると共に、配管や装置等で発生した酸化物などが混入
しており、詰りを生じてしまうのである。
The above-mentioned conventional heating and cooling apparatus can maintain the heating and cooling temperature with high accuracy in the initial stage of the start of use, but can accurately maintain the temperature after long-term use. There was a problem that it was difficult to maintain. This is because heating steam or cooling water is supplied through the porous member, so that the porous member is clogged during long-term use, and the temperature cannot be maintained accurately. This is because In general, steam and cooling water contain foreign substances such as scales, and oxides generated in pipes and devices, and the like, resulting in clogging.

【0004】また上記従来の加熱冷却装置では、加熱か
ら冷却あるいは冷却から加熱へと切り換える場合に比較
的長時間を要し、速やかに切り換えることができない問
題があった。これは、流体室へ蒸気と冷却水を交互に供
給するために、その交換に時間を要するためである。
In addition, the conventional heating / cooling apparatus has a problem in that switching from heating to cooling or from cooling to heating requires a relatively long time and cannot be performed quickly. This is because it takes time to exchange the steam and the cooling water to the fluid chamber alternately.

【0005】従って本発明の技術的課題は、長期間の使
用においても精度良く加熱冷却の温度を維持することが
できると共に、加熱と冷却の切り換えを速やかに行なう
ことができる加熱冷却装置を得ることである。
Accordingly, it is an object of the present invention to provide a heating / cooling apparatus which can maintain a heating / cooling temperature with high accuracy even during long-term use and can quickly switch between heating and cooling. It is.

【0006】[0006]

【課題を解決する為の手段】本発明の蒸気加熱装置の構
成は次の通りである。熱交換器と、該熱交換器のほぼ全
周を覆う蒸気室と、該蒸気室に弁を介して加熱蒸気を供
給する蒸気管とから成るものにおいて、熱交換器と蒸気
室との間に冷却室を形成し、該冷却室に弁を介して冷却
液供給管と温水供給管を接続すると共に、冷却室を減圧
状態に維持する吸引手段を接続したものである。
The structure of the steam heating apparatus according to the present invention is as follows. A heat exchanger, a steam chamber covering almost the entire circumference of the heat exchanger, and a steam pipe for supplying heating steam to the steam chamber via a valve, wherein a heat pipe is provided between the heat exchanger and the steam chamber. A cooling chamber is formed, a cooling liquid supply pipe and a hot water supply pipe are connected to the cooling chamber via a valve, and suction means for maintaining the cooling chamber in a reduced pressure state is connected.

【0007】[0007]

【作用】熱交換器と蒸気室との間に冷却室を形成したこ
とにより、熱交換器はこの冷却室を介して蒸気室の蒸気
によって加熱される。冷却室に冷却液を供給せずに空気
のみが滞留していると、蒸気室の蒸気の熱はこの空気層
を介して伝達される。従って、100度C以上の温度の
蒸気、すなわち大気圧以上の圧力の蒸気を供給しても、
100度C以下の低温度で加熱することができる。ま
た、冷却室を吸引手段で減圧することにより、更に熱伝
達量は少なくなって低温度で加熱することができる。
With the cooling chamber formed between the heat exchanger and the steam chamber, the heat exchanger is heated by the steam in the steam chamber via the cooling chamber. If only the air stays without supplying the cooling liquid to the cooling chamber, the heat of the steam in the steam chamber is transmitted through the air layer. Therefore, even if steam at a temperature of 100 ° C. or higher, that is, steam at a pressure higher than the atmospheric pressure is supplied,
It can be heated at a low temperature of 100 ° C. or less. Further, by reducing the pressure in the cooling chamber by the suction means, the heat transfer amount is further reduced, and the cooling chamber can be heated at a low temperature.

【0008】加熱から冷却へ切り換える場合は、蒸気室
への蒸気の供給を停止し、冷却室に冷却液供給管から冷
却液を供給することにより行なうことができる。また、
吸引手段で冷却室を減圧状態とすることにより、冷却液
の蒸発を促進して熱交換器を蒸発潜熱によって気化冷却
することができる。
When switching from heating to cooling, the supply of steam to the steam chamber is stopped, and the cooling liquid is supplied to the cooling chamber from a cooling liquid supply pipe. Also,
By setting the cooling chamber in a reduced pressure state by the suction means, the evaporation of the cooling liquid is promoted, and the heat exchanger can be vaporized and cooled by the latent heat of evaporation.

【0009】再度冷却から加熱に切り換える場合、冷却
室への冷却液の供給を停止すると共に、温水供給管から
温水を冷却室に供給し、続いて蒸気室に加熱蒸気を供給
することにより、速やかに加熱へと切り換えることがで
きる。
When switching from cooling to heating again, the supply of the cooling liquid to the cooling chamber is stopped, hot water is supplied from the hot water supply pipe to the cooling chamber, and then the heating steam is supplied to the steam chamber, so that the steam is quickly supplied. Can be switched to heating.

【0010】[0010]

【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、熱交換器として反応釜1を用いた例を示す。
反応釜1と蒸気室としてのジャケット部2と、ジャケッ
ト部2と反応釜1との間に形成した冷却室3とで加熱冷
却装置を構成する。ジャケット部2には弁4を介して蒸
気管5を接続する。
BRIEF DESCRIPTION OF THE DRAWINGS FIG. In this embodiment, an example in which the reactor 1 is used as a heat exchanger will be described.
The heating and cooling device is constituted by the reactor 1 and the jacket 2 as a steam chamber, and the cooling chamber 3 formed between the jacket 2 and the reactor 1. A steam pipe 5 is connected to the jacket 2 via a valve 4.

【0011】熱交換器としての反応釜1は、従来のもの
と同様に加熱冷却対象の被熱処理物入口6と被熱処理物
出口7と撹拌器8とを有している。ジャケット部2の下
部には加熱を行なった蒸気が凝縮して復水となり排出さ
れる復水出口9が設けてある。
The reactor 1 as a heat exchanger has an inlet 6 to be heated and cooled, an outlet 7 to be heated and a stirrer 8 as in the conventional reactor. A condensate outlet 9 is provided at a lower portion of the jacket portion 2 to condense the heated steam to be condensed and discharged.

【0012】反応釜1のほぼ全周を覆うジャケット部2
の内側に形成した冷却室3は、上部に弁10を介して冷
却液供給管11と接続すると共に、同じく弁39を介し
て温水供給管40を接続する。また、冷却室3の下部に
は水排出口12を設けて管21を介してエゼクタ―式真
空ポンプ22と接続する。また、ジャケット部2下部の
復水排出口9もスチ―ムトラップ13を介してエゼクタ
―式真空ポンプ22と接続する。
A jacket 2 covering almost the entire circumference of the reaction vessel 1
The cooling chamber 3 formed inside is connected to the coolant supply pipe 11 via a valve 10 at the upper part, and also connected to a hot water supply pipe 40 via a valve 39. A water outlet 12 is provided at the lower part of the cooling chamber 3 and connected to an ejector-type vacuum pump 22 through a pipe 21. The condensate discharge port 9 at the lower part of the jacket 2 is also connected to an ejector type vacuum pump 22 via a steam trap 13.

【0013】エゼクタ―真空ポンプ22は、ノズル部2
3とディフュ―ザ24から成るエゼクタ―25と、タン
ク26と、渦巻きポンプ27とで構成する。タンク26
の下部と渦巻きポンプ27の吸込み口を接続し吐出口を
エゼクタ―25のノズル部23と接続する。エゼクタ―
式真空ポンプ22はタンク26内の流体を渦巻きポンプ
27で循環してノズル部23へ通過させることにより、
ノズル部23で吸引力を生じるものである。渦巻きポン
プ27の吐出口と連設する循環路に弁28を介して余剰
液排出通路29を接続する。また本実施例においては、
循環路に弁35を介して通路36を冷却室3の上部と接
続する。タンク26には、内部の液位を検出するための
液位センサ―30,31と、液温を検出する温度センサ
―32を取り付けると共に、上部には冷却液供給管11
から分岐した供給管33を接続する。
The ejector-vacuum pump 22 includes a nozzle 2
It comprises an ejector 25 consisting of a diffuser 3 and a diffuser 24, a tank 26, and a spiral pump 27. Tank 26
Is connected to the suction port of the spiral pump 27, and the discharge port is connected to the nozzle portion 23 of the ejector 25. Ejector
The type vacuum pump 22 circulates the fluid in the tank 26 by the vortex pump 27 and passes the fluid to the nozzle 23,
The suction force is generated in the nozzle portion 23. A surplus liquid discharge passage 29 is connected via a valve 28 to a circulation passage connected to the discharge port of the volute pump 27. In the present embodiment,
The passage 36 is connected to the upper part of the cooling chamber 3 via a valve 35 in the circulation path. The tank 26 is provided with liquid level sensors 30 and 31 for detecting the internal liquid level and a temperature sensor 32 for detecting the liquid temperature.
Is connected to the supply pipe 33 branched from.

【0014】次に作用を説明する。反応釜1内の被加熱
物を例えば30度C程度の温度で加熱する場合は、弁1
0を開弁して冷却室3に冷却液を供給しながらエゼクタ
―式真空ポンプ22を駆動させて、冷却室3内を減圧状
態として、ジャケット部2に100度C以上の加熱蒸気
を供給することにより行なうことができる。加熱温度の
調節は、エゼクタ―式真空ポンプ22のノズル部23を
通過する流体の温度をタンク26内へ供給する冷却液の
量を調整して吸引力を制御することにより行なうことが
できると共に、供給蒸気の温度を弁4の開度を調整して
行なうことができる。
Next, the operation will be described. When heating the object to be heated in the reactor 1 at a temperature of, for example, about 30 ° C., the valve 1
By opening the valve 0 and driving the ejector type vacuum pump 22 while supplying the cooling liquid to the cooling chamber 3, the inside of the cooling chamber 3 is depressurized, and the heating steam of 100 ° C. or more is supplied to the jacket portion 2. It can be done by doing. The heating temperature can be adjusted by controlling the suction force by adjusting the amount of the cooling liquid supplied to the tank 26 with the temperature of the fluid passing through the nozzle portion 23 of the ejector-type vacuum pump 22, and The temperature of the supplied steam can be adjusted by adjusting the opening of the valve 4.

【0015】冷却室3内に供給された冷却液と、ジャケ
ット部2で加熱により生じた凝縮水としての復水は、管
21とスチ―ムトラップ13を経てエゼクタ―25に吸
引されタンク26に至る。
The cooling liquid supplied into the cooling chamber 3 and the condensed water as condensed water generated by heating in the jacket 2 are sucked by the ejector 25 through the pipe 21 and the steam trap 13 to reach the tank 26. .

【0016】反応釜1を冷却する場合は、弁4を閉じて
蒸気の供給を停止し、エゼクタ―式真空ポンプ22を駆
動させながら弁10を開弁して冷却液を冷却室3内へ供
給することにより、冷却室3内は減圧状態となり反応釜
1の熱を奪って冷却液が気化することによる蒸発潜熱で
もって反応釜1を冷却することができる。この場合、冷
却により気化した蒸気と冷却液の残りは管21を経てエ
ゼクタ―25に吸引される。
When the reactor 1 is cooled, the supply of steam is stopped by closing the valve 4 and the valve 10 is opened while the ejector-type vacuum pump 22 is driven to supply the cooling liquid into the cooling chamber 3. By doing so, the inside of the cooling chamber 3 is brought into a reduced pressure state, so that the heat of the reaction vessel 1 is taken out, and the reaction vessel 1 can be cooled with latent heat of evaporation caused by vaporization of the cooling liquid. In this case, the remainder of the vapor and the cooling liquid vaporized by the cooling are sucked into the ejector 25 through the pipe 21.

【0017】冷却から加熱へと切り換える場合、弁10
を閉じて冷却液の供給を停止し、弁39を開弁して温水
を冷却室3に供給すると共に、弁4を開弁して加熱蒸気
をジャケット部2へ供給することにより、温水の一部の
熱と蒸気の熱が直ちに反応釜1を加熱することとなっ
て、時間を要しない速やかな加熱への切り換えを行なう
ことができる。
When switching from cooling to heating, the valve 10
Is closed to stop the supply of the cooling liquid, and the valve 39 is opened to supply the hot water to the cooling chamber 3, and the valve 4 is opened to supply the heating steam to the jacket portion 2, so that one of the hot water is supplied. The heat of the section and the heat of the steam immediately heat the reaction vessel 1, so that it is possible to quickly switch to heating without requiring time.

【0018】本実施例においては、エゼクタ―式真空ポ
ンプ22を循環する流体の一部を、通路36を介して冷
却室3に供給することができるようにしたことにより、
加熱時に蒸気によって暖められた循環流体を、温水供給
管40からの温水に変えて、冷却室3へ供給することも
できる。
In this embodiment, a part of the fluid circulating in the ejector type vacuum pump 22 can be supplied to the cooling chamber 3 through the passage 36,
The circulating fluid heated by the steam at the time of heating can be supplied to the cooling chamber 3 instead of the hot water from the hot water supply pipe 40.

【0019】[0019]

【発明の効果】本発明によれば、熱交換器と蒸気室との
間に冷却室を形成したことにより、被加熱物はこの冷却
室を介して加熱されることとなり過度に加熱されること
がなく熱損傷を生じることがないと共に、低温度で加熱
することができる。また、従来技術のように多孔質状部
材を介することがないために詰りを生じることがなく、
従って、長期に渡って精度良く加熱温度を維持すること
ができる。
According to the present invention, since the cooling chamber is formed between the heat exchanger and the steam chamber, the object to be heated is heated via the cooling chamber, and is thereby excessively heated. No heat damage occurs, and heating can be performed at a low temperature. Also, there is no clogging because there is no intervening porous member as in the prior art,
Therefore, the heating temperature can be accurately maintained over a long period of time.

【0020】本発明によれば、冷却室に温水供給管を接
続したことにより、冷却から加熱へ切り換える場合に、
前もって温水を冷却室に供給することができ、時間を要
せず速やかに加熱へと切り換えることができる。
According to the present invention, by connecting the hot water supply pipe to the cooling chamber, when switching from cooling to heating,
Hot water can be supplied to the cooling chamber in advance, and switching to heating can be quickly performed without requiring time.

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

【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.

【符号の説明】[Explanation of symbols]

1 反応釜 2 ジャケット部 3 冷却室 5 蒸気管 11 冷却液供給管 13 スチ―ムトラップ 22 エゼクタ―式真空ポンプ 23 ノズル部 25 エゼクタ― 26 タンク 27 渦巻きポンプ 40 温水供給管 REFERENCE SIGNS LIST 1 reaction vessel 2 jacket part 3 cooling chamber 5 steam pipe 11 cooling liquid supply pipe 13 steam trap 22 ejector type vacuum pump 23 nozzle part 25 ejector 26 tank 27 spiral pump 40 hot water supply pipe

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 熱交換器と、該熱交換器のほぼ全周を覆
う蒸気室と、該蒸気室に弁を介して加熱蒸気を供給する
蒸気管とから成るものにおいて、熱交換器と蒸気室との
間に冷却室を形成し、該冷却室に弁を介して冷却液供給
管と温水供給管を接続すると共に、冷却室を減圧状態に
維持する吸引手段を接続したことを特徴とする加熱冷却
装置。
1. A heat exchanger comprising: a heat exchanger; a steam chamber covering substantially the entire circumference of the heat exchanger; and a steam pipe for supplying heating steam to the steam chamber via a valve. A cooling chamber is formed between the cooling chamber and the cooling chamber, a cooling liquid supply pipe and a hot water supply pipe are connected to the cooling chamber via a valve, and suction means for maintaining the cooling chamber in a reduced pressure state is connected. Heating and cooling equipment.
JP5281707A 1993-10-15 1993-10-15 Heating and cooling device Expired - Fee Related JP3013070B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5281707A JP3013070B2 (en) 1993-10-15 1993-10-15 Heating and cooling device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5281707A JP3013070B2 (en) 1993-10-15 1993-10-15 Heating and cooling device

Publications (2)

Publication Number Publication Date
JPH07108167A JPH07108167A (en) 1995-04-25
JP3013070B2 true JP3013070B2 (en) 2000-02-28

Family

ID=17642864

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5281707A Expired - Fee Related JP3013070B2 (en) 1993-10-15 1993-10-15 Heating and cooling device

Country Status (1)

Country Link
JP (1) JP3013070B2 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5047426B2 (en) * 2001-04-13 2012-10-10 株式会社テイエルブイ Steam heating device
JP5047425B2 (en) * 2001-04-13 2012-10-10 株式会社テイエルブイ Steam heating device
CN102580656A (en) * 2012-02-22 2012-07-18 南通诚信氨基酸有限公司 Reaction kettle improvement device for production of glycylglutamine dipeptide
CN113430090B (en) * 2021-07-22 2024-03-15 上海太太乐食品有限公司 Edible vinegar sterilization device and edible vinegar sterilization method

Also Published As

Publication number Publication date
JPH07108167A (en) 1995-04-25

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