JPH0953802A - Heating/cooling device using heat medium - Google Patents

Heating/cooling device using heat medium

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Publication number
JPH0953802A
JPH0953802A JP22732995A JP22732995A JPH0953802A JP H0953802 A JPH0953802 A JP H0953802A JP 22732995 A JP22732995 A JP 22732995A JP 22732995 A JP22732995 A JP 22732995A JP H0953802 A JPH0953802 A JP H0953802A
Authority
JP
Japan
Prior art keywords
heat medium
heating
heat
medium
supply pipe
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.)
Pending
Application number
JP22732995A
Other languages
Japanese (ja)
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 JP22732995A priority Critical patent/JPH0953802A/en
Publication of JPH0953802A publication Critical patent/JPH0953802A/en
Pending legal-status Critical Current

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Abstract

PROBLEM TO BE SOLVED: To provide a wide-range heating/cooling device using a heat medium. SOLUTION: A boiler 1 for a heat medium is connected to a jacket part 6 of a reaction boiler 2 through a hot fluid pipe 11. A cold fluid pipe 5 is connected to the jacket part 6. The jacket part 6 is connected to an ejector 20 of a vacuum pump means 7 through a line 16. The vacuum pump means 7 comprises the ejector 20, a heat-exchange tank 21, a circulation pump 22, and a connection line 23 therebetween.

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、熱媒体によって被熱交
換物を加熱したり冷却するものに関し、石油化学工業や
合成繊維工業、あるいは、合成樹脂工業等の各種加熱や
冷却工程に使用される熱媒体による加熱冷却装置に関す
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to heating or cooling a heat exchange object with a heat medium, and is used in various heating and cooling processes in the petrochemical industry, synthetic fiber industry, synthetic resin industry and the like. The present invention relates to a heating / cooling device using a heat medium.

【0002】[0002]

【従来技術】従来の加熱冷却装置の例としては、例えば
特公平5−34054号公報に示されているような装置
が用いられていた。これは、反応釜を加熱したり冷却す
るもので、反応釜の流体室に加熱用の蒸気と冷却用の水
を切換えて供給できるようにすると共に、当該流体室を
エゼクタとタンクと循環ポンプとから成る真空ポンプ手
段に接続したものであり、蒸気の潜熱でもって反応釜を
加熱したり、水の蒸発潜熱により反応釜を冷却すること
ができるものである。
2. Description of the Related Art As an example of a conventional heating / cooling device, a device as disclosed in Japanese Patent Publication No. 5-34054 has been used. This heats or cools the reaction kettle so that steam for heating and water for cooling can be switched and supplied to the fluid chamber of the reaction kettle, and the fluid chamber can be connected to an ejector, a tank, and a circulation pump. It is connected to a vacuum pump means composed of, and is capable of heating the reaction kettle by the latent heat of steam and cooling the reaction kettle by the latent heat of vaporization of water.

【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
装置を用いた場合、加熱や冷却の温度が限られた値とな
り、従って、限られた被加熱物や被冷却物しか熱交換処
理ができない問題があった。これは、加熱冷却流体とし
て水を蒸発させた蒸気や冷却水を用いているために、そ
の蒸気温度や蒸発温度が所定の限られた値となってしま
うためである。
When the above-mentioned conventional heating / cooling device is used, the heating or cooling temperature has a limited value, so that only a limited object to be heated or object to be cooled can be heat-exchanged. There was a problem I couldn't do. This is because steam or cooling water obtained by evaporating water is used as the heating / cooling fluid, so that the steam temperature or the evaporation temperature becomes a predetermined limited value.

【0004】従って本発明の技術的課題は、広い温度範
囲で加熱したり冷却する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 in a wide temperature range.

【0005】[0005]

【課題を解決するための手段】上記の技術的課題を解決
するために講じた本発明の技術的手段は、熱交換器の一
次側に加熱流体供給管と冷却流体供給管を接続し、熱交
換器の二次側に真空ポンプ手段を接続して、熱交換器内
の被熱交換物を加熱したり冷却するものにおいて、加熱
冷却流体を熱媒体とし、当該熱媒体を蒸気化する熱媒体
蒸気発生部を配置して上記加熱流体供給管に接続すると
共に、上記冷却流体供給管に液体状の熱媒体を供給する
液体状熱媒体供給部を接続したものである。
The technical means of the present invention taken to solve the above-mentioned technical problem is to connect a heating fluid supply pipe and a cooling fluid supply pipe to the primary side of a heat exchanger, A heating medium, in which a heating / cooling fluid is used as a heat medium and the heat medium is vaporized by connecting a vacuum pump means to the secondary side of the exchanger to heat or cool the heat exchange object in the heat exchanger. A vapor generating unit is arranged and connected to the heating fluid supply pipe, and a liquid heat medium supply unit for supplying a liquid heat medium is connected to the cooling fluid supply pipe.

【0006】[0006]

【作用】熱媒体蒸気によって被熱交換物を加熱し、ま
た、液体状の熱媒体の蒸発潜熱によって被熱交換物を冷
却することにより、水蒸気の潜熱と水の蒸発潜熱による
加熱冷却と比較して、より高温度までの加熱や冷却を行
うことができる。
[Operation] By heating the heat exchange object by the heat medium vapor and cooling the heat exchange object by the latent heat of vaporization of the liquid heat medium, compared with the heating and cooling by the latent heat of water vapor and the latent heat of vaporization of water. Therefore, heating or cooling to a higher temperature can be performed.

【0007】熱媒体は様々な種類のものが市販され用い
られているが、通常の水を沸騰させた水蒸気よりも圧力
が低くて温度が高いものが一般的である。例えば水の場
合、水銀柱で約95ミリの真空圧力の状態で約50度C
の水蒸気となるのであるが、ある熱媒体の場合は同じ圧
力状態の場合で約200度Cの高温蒸気となる。
Various types of heat mediums are commercially available and used, but those having a lower pressure and a higher temperature are generally used as compared with ordinary steam obtained by boiling water. For example, in the case of water, the pressure is approximately 50 degrees C under a vacuum pressure of approximately 95 mm of mercury.
However, in the case of a certain heat medium, it becomes a high temperature steam of about 200 ° C. under the same pressure condition.

【0008】[0008]

【実施例】上記の技術的手段の具体例を示す実施例を説
明する(図1参照)。本実施例においては熱交換器とし
て反応釜2を用いた例を示す。熱媒体蒸気発生部として
の熱媒体用ボイラ―1と反応釜2のジャケット部6とを
加熱流体供給管11を介して接続すると共に、ジャケッ
ト部6に冷却流体供給管5を接続し、ジャケット部6の
下部を真空ポンプ手段7と連設し、真空ポンプ手段7を
タンク3と循環ポンプ4を介して熱媒体用ボイラ―1と
接続して、熱媒体による加熱冷却装置を構成する。
EXAMPLE An example showing a concrete example of the above technical means will be described (see FIG. 1). In this embodiment, an example in which the reaction kettle 2 is used as the heat exchanger is shown. The heating medium boiler-1 as the heating medium vapor generating section and the jacket section 6 of the reaction vessel 2 are connected via the heating fluid supply pipe 11, and the cooling fluid supply tube 5 is connected to the jacket section 6 to form the jacket section. The lower part of 6 is connected to the vacuum pump means 7, and the vacuum pump means 7 is connected to the heat medium boiler 1 via the tank 3 and the circulation pump 4 to form a heating and cooling device by the heat medium.

【0009】熱媒体用ボイラ―1と反応釜2の間の加熱
流体供給管11に、圧力調整弁8と気液分離器9と圧力
センサ―10を取り付ける。圧力調整弁8は、圧力セン
サ―10で検出した加熱流体供給管11内の熱媒体蒸気
圧力を所定値に調整するものであり、気液分離器9は加
熱流体供給管11内の熱媒体蒸気と液体を分離し、分離
した熱媒体蒸気だけを反応釜2のジャケット部6へ供給
し、液体をその下部に設けたスチ―ムトラップ12から
排出するものである。気液分離器9としては、衝突式や
遠心式やフィルタ―式等のものを用いることができる。
A pressure regulating valve 8, a gas-liquid separator 9 and a pressure sensor 10 are attached to a heating fluid supply pipe 11 between the heating medium boiler 1 and the reaction vessel 2. The pressure adjusting valve 8 is for adjusting the heat medium vapor pressure in the heating fluid supply pipe 11 detected by the pressure sensor 10 to a predetermined value, and the gas-liquid separator 9 is the heat medium vapor in the heating fluid supply pipe 11. And the liquid are separated, only the separated heat medium vapor is supplied to the jacket portion 6 of the reaction kettle 2, and the liquid is discharged from the steam trap 12 provided in the lower portion thereof. The gas-liquid separator 9 may be of a collision type, a centrifugal type, a filter type, or the like.

【0010】ジャケット部6の右側には熱媒体補給管路
31とバルブ18を介して接続した冷却流体供給管5を
接続する。冷却流体供給管5から液体状の熱媒体をジャ
ケット部6へ供給するものである。
The cooling fluid supply pipe 5 connected to the heat medium supply pipe 31 via the valve 18 is connected to the right side of the jacket portion 6. A liquid heat medium is supplied from the cooling fluid supply pipe 5 to the jacket portion 6.

【0011】反応釜2の外周に配置したジャケット部6
の下部接続口13を、スチ―ムトラップ14とバイパス
バルブ15を並行に設けた管路16で、真空ポンプ手段
7のエゼクタ―20と接続する。また、気液分離器9の
スチ―ムトラップ12の出口も管路17を介してエゼク
タ―20と接続する。
A jacket portion 6 arranged on the outer periphery of the reaction kettle 2.
The lower connection port 13 is connected to the ejector 20 of the vacuum pump means 7 by a pipe line 16 in which a steam trap 14 and a bypass valve 15 are provided in parallel. Further, the outlet of the steam trap 12 of the gas-liquid separator 9 is also connected to the ejector 20 via the conduit 17.

【0012】真空ポンプ手段7は、エゼクタ―20と熱
交換タンク21と循環ポンプ22、及び、接続管路23
とで構成する。エゼクタ―20は、ノズル部25とディ
フュ―ザ部26で形成する。熱交換タンク21には、内
部に溜った熱媒体27を冷却するための冷却管28を調
節弁29を介して取り付けると共に、下部には熱媒体2
7の流体温度を検出するための温度センサ―30を取り
付け、図示はしていないが温度センサ―30と調節弁2
9を温度コントロ―ラ―を介して接続して、熱媒体27
の温度を所定値に維持できるようにする。熱交換タンク
21の上部には熱媒体を補給するための熱媒体補給管路
31をバルブ19を介して接続する。
The vacuum pump means 7 includes an ejector 20, a heat exchange tank 21, a circulation pump 22, and a connection conduit 23.
It consists of and. The ejector 20 is formed of a nozzle portion 25 and a diffuser portion 26. A cooling pipe 28 for cooling the heat medium 27 accumulated therein is attached to the heat exchange tank 21 via a control valve 29, and the heat medium 2 is provided in the lower portion.
A temperature sensor 30 for detecting the fluid temperature of 7 is attached, and although not shown, the temperature sensor 30 and the control valve 2
9 are connected via a temperature controller, and the heat medium 27
So that the temperature can be maintained at a predetermined value. A heat medium supply pipe line 31 for supplying a heat medium is connected to the upper part of the heat exchange tank 21 via a valve 19.

【0013】真空ポンプ手段7は、循環ポンプ22で熱
交換タンク21内の熱媒体27をエゼクタ―20中に循
環させて、エゼクタ―20のノズル部25で吸引力を発
生し、反応釜2のジャケット部6から熱媒体を吸引する
と共に、ジャケット部6内を所定の圧力状態に維持する
ものである。
The vacuum pump means 7 circulates the heat medium 27 in the heat exchange tank 21 through the ejector 20 by means of the circulation pump 22 to generate suction force at the nozzle portion 25 of the ejector 20, so that the reaction vessel 2 The heat medium is sucked from the jacket portion 6 and the inside of the jacket portion 6 is maintained at a predetermined pressure state.

【0014】真空ポンプ手段7の接続管路23の一部を
分岐して管路32を接続し、循環熱媒体の一部が管路3
3からタンク3へ供給されるようにすると共に、更に管
路35を接続して循環熱媒体の一部を加熱流体供給管1
1中で気液分離器9の一次側に注入する。管路35によ
り、圧力調整弁8で圧力調整された熱媒体蒸気が過熱蒸
気となった場合でも、循環熱媒体の一部を注入して気液
分離部9で熱交換させることにより、飽和温度の蒸気と
することができるものである。
A part of the connecting pipe line 23 of the vacuum pump means 7 is branched to connect the pipe line 32, and a part of the circulating heat medium is supplied to the pipe line 3.
3 is supplied to the tank 3, and a pipe 35 is further connected so that a part of the circulating heat medium is supplied to the heating fluid supply pipe 1.
It is injected into the primary side of the gas-liquid separator 9 in 1. Even when the heat transfer medium whose pressure is adjusted by the pressure adjusting valve 8 by the pipe line 35 becomes superheated steam, a part of the circulating heat transfer medium is injected and heat is exchanged in the gas-liquid separation unit 9 to obtain the saturation temperature. It can be steam.

【0015】管路32を更に分岐して管路36とバルブ
37とを介して冷却流体供給管5と接続する。真空ホン
プ手段7を循環している液体状の熱媒体の一部を、管路
36から冷却流体供給管5を経て反応釜2のジャケット
部6へ供給することができるものである。本実施例にお
いては、管路36と熱媒体補給管路31とで液体状熱媒
体供給部を形成する。
The pipe 32 is further branched and connected to the cooling fluid supply pipe 5 via the pipe 36 and the valve 37. A part of the liquid heat medium circulating in the vacuum homping means 7 can be supplied to the jacket portion 6 of the reaction vessel 2 from the pipe line 36 through the cooling fluid supply pipe 5. In the present embodiment, the conduit 36 and the heat medium supply conduit 31 form a liquid heat medium supply unit.

【0016】次に作用を説明する。反応釜2を加熱する
場合は、熱媒体用ボイラ―1で発生させた熱媒体蒸気
を、圧力調整弁8を経て圧力調整してジャケット部6に
供給する。ジャケット部6内は、真空ポンプ手段7のエ
ゼクタ―20の吸引力により予め所定の低圧状態となっ
ており、ジャケット部6に供給された熱媒体蒸気は、所
定の圧力すなわち蒸気温度となって反応釜2内の被加熱
物を加熱する。加熱して熱を奪われた熱媒体蒸気は凝縮
して液体となり、スチ―ムトラップ14を経てエゼクタ
―20に吸引され、熱交換タンク21に至る。
Next, the operation will be described. When heating the reaction kettle 2, the heat medium vapor generated in the heat medium boiler-1 is pressure-adjusted via the pressure regulating valve 8 and supplied to the jacket portion 6. The inside of the jacket portion 6 is in a predetermined low pressure state due to the suction force of the ejector 20 of the vacuum pump means 7, and the heat medium vapor supplied to the jacket portion 6 becomes a predetermined pressure, that is, the vapor temperature and reacts. The object to be heated in the kettle 2 is heated. The heat medium vapor that has been heated and deprived of heat condenses into a liquid, is sucked by the ejector 20 through the steam trap 14, and reaches the heat exchange tank 21.

【0017】熱交換タンク21内の熱媒体27は、冷却
管28で所定温度まで冷却されて循環ポンプ22でエゼ
クタ―20へ供給され、再度ジャケット部6内の熱媒体
を吸引する。エゼクタ―20で生じる吸引力は、エゼク
タ―20内を通過する熱媒体の温度によって決まるため
に、熱交換タンク21内の熱媒体27の液温を適宜調節
することにより、エゼクタ―20の吸引力すなわち減圧
度合を制御することができる。エゼクタ―20の吸引力
を制御することにより、ジャケット部6内の圧力状態を
制御することができ、大気圧以下の負圧状態から、大気
圧以上の正圧状態までジャケット部6内の圧力を制御す
ることができ、対応関係にある蒸気温度も同様に制御す
ることができる。
The heat medium 27 in the heat exchange tank 21 is cooled to a predetermined temperature by the cooling pipe 28 and supplied to the ejector 20 by the circulation pump 22 to suck the heat medium in the jacket portion 6 again. Since the suction force generated in the ejector 20 is determined by the temperature of the heat medium passing through the ejector 20, the suction force of the ejector 20 can be adjusted by appropriately adjusting the liquid temperature of the heat medium 27 in the heat exchange tank 21. That is, the degree of pressure reduction can be controlled. By controlling the suction force of the ejector 20, the pressure state inside the jacket portion 6 can be controlled, and the pressure inside the jacket portion 6 can be changed from a negative pressure state below atmospheric pressure to a positive pressure state above atmospheric pressure. It can be controlled, and corresponding steam temperatures can be controlled as well.

【0018】熱媒体として例えば商品名でダウサムなる
ものを用いた場合、蒸気圧力を絶対圧で0.3キロとす
るとその蒸気温度は約210度Cとなり、1.1キロと
すると約260度Cとすることができ、蒸気圧力を制御
することによって、蒸気温度を制御することができるの
である。
When a heat medium called Dowsum is used as the heat medium, the steam temperature is about 210 ° C when the steam pressure is 0.3 kg in absolute pressure, and about 260 ° C when it is 1.1 km. The steam temperature can be controlled by controlling the steam pressure.

【0019】次に反応釜2を冷却する場合は、圧力調整
弁8を閉止して熱媒体蒸気の供給を停止すると共に、冷
却流体供給管5から液体状の熱媒体をジャケット部6へ
供給する。この場合、液体状の熱媒体は、熱媒体補給管
路31又は真空ポンプ手段7と接続した管路36のいず
れかから供給することができる。
Next, when the reaction kettle 2 is cooled, the pressure adjusting valve 8 is closed to stop the supply of the heat medium vapor and the liquid heat medium is supplied from the cooling fluid supply pipe 5 to the jacket portion 6. . In this case, the liquid heat medium can be supplied from either the heat medium supply pipe 31 or the pipe 36 connected to the vacuum pump means 7.

【0020】ジャケット部6へ供給された液体状の熱媒
体は、ジャケット部6内が真空ポンプ手段7によって所
定の減圧状態に維持されており、反応釜2の熱を奪って
ただちに蒸発することによりその蒸発潜熱でもって反応
釜2を冷却する。反応釜2を冷却して蒸発した熱媒体蒸
気と、蒸発しなかった液体状の熱媒体の一部は、スチ―
ムトラップ14とバルブ15を経てエゼクタ―25に吸
引され、熱交換タンク21に至り、再度所定温度に調整
される。
The liquid heat medium supplied to the jacket portion 6 is maintained in a predetermined depressurized state by the vacuum pump means 7 inside the jacket portion 6, and the heat of the reaction kettle 2 is taken to evaporate immediately. The reaction kettle 2 is cooled by the latent heat of vaporization. The heat medium vapor evaporated by cooling the reaction kettle 2 and a part of the liquid heat medium which has not evaporated are steamed.
It is sucked by the ejector 25 through the trap 14 and the valve 15, reaches the heat exchange tank 21, and is again adjusted to a predetermined temperature.

【0021】本実施例においては、熱交換器として反応
釜2を用いた例を示したが、その他の熱交換器、例えば
合成繊維や合成樹脂、あるいは、食料品や医療品等の熱
交換器としても用いることができるものである。
In this embodiment, the reaction vessel 2 is used as the heat exchanger, but other heat exchangers such as synthetic fibers and synthetic resins, heat exchangers for food and medical products, etc. Can also be used as.

【0022】本実施例においては、真空ポンプ手段7と
して、エゼクタ―20と熱交換タンク21と循環ポンプ
22から成るものを示したが、その他の例えば水封式や
回転式や往復式の真空ポンプを用いることもできる。
In this embodiment, the vacuum pump means 7 is composed of the ejector 20, the heat exchange tank 21 and the circulation pump 22. However, other vacuum pumps such as a water ring type, a rotary type or a reciprocating type vacuum pump. Can also be used.

【0023】[0023]

【発明の効果】上記のように本発明によれば、加熱冷却
流体に熱媒体を用いることによって、より広い温度範囲
で被熱交換物を加熱したり冷却することができる。
As described above, according to the present invention, by using the heating medium as the heating / cooling fluid, it is possible to heat or cool the heat exchange object in a wider temperature range.

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

【図1】本発明の熱媒体による加熱冷却装置の実施例を
示す構成図である。
FIG. 1 is a configuration diagram showing an embodiment of a heating / cooling device using a heat medium according to the present invention.

【符号の説明】[Explanation of symbols]

1 熱媒体用ボイラ― 2 反応釜 6 ジャケット部 7 真空ポンプ手段 8 圧力調整弁 9 気液分離器 14 スチ―ムトラップ 20 エゼクタ― 21 熱交換タンク 22 循環ポンプ 27 熱媒体 31 熱媒体補給管路 36 管路 1 Boiler for heat medium 2 Reaction kettle 6 Jacket 7 Vacuum pump means 8 Pressure adjusting valve 9 Gas-liquid separator 14 Steam trap 20 Ejector 21 Heat exchange tank 22 Circulation pump 27 Heat medium 31 Heat medium supply line 36 Pipe Road

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 熱交換器の一次側に加熱流体供給管と冷
却流体供給管を接続し、熱交換器の二次側に真空ポンプ
手段を接続して、熱交換器内の被熱交換物を加熱したり
冷却するものにおいて、加熱冷却流体を熱媒体とし、当
該熱媒体を蒸気化する熱媒体蒸気発生部を配置して上記
加熱流体供給管に接続すると共に、上記冷却流体供給管
に液体状の熱媒体を供給する液体状熱媒体供給部を接続
したことを特徴とする熱媒体による加熱冷却装置。
1. A heat exchange object in the heat exchanger, wherein a heating fluid supply pipe and a cooling fluid supply pipe are connected to the primary side of the heat exchanger, and vacuum pump means is connected to the secondary side of the heat exchanger. Which heats or cools the heating medium, the heating medium is a heating medium, and a heating medium vapor generating part for vaporizing the heating medium is arranged and connected to the heating fluid supply pipe, and a liquid is supplied to the cooling fluid supply pipe. A heating / cooling device using a heat medium, characterized in that a liquid heat medium supply unit for supplying a heat medium in the shape of a liquid is connected.
JP22732995A 1995-08-11 1995-08-11 Heating/cooling device using heat medium Pending JPH0953802A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22732995A JPH0953802A (en) 1995-08-11 1995-08-11 Heating/cooling device using heat medium

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22732995A JPH0953802A (en) 1995-08-11 1995-08-11 Heating/cooling device using heat medium

Publications (1)

Publication Number Publication Date
JPH0953802A true JPH0953802A (en) 1997-02-25

Family

ID=16859108

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22732995A Pending JPH0953802A (en) 1995-08-11 1995-08-11 Heating/cooling device using heat medium

Country Status (1)

Country Link
JP (1) JPH0953802A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100376220B1 (en) * 1999-04-21 2003-03-15 서명희 Heating and cooling device by using a boiler
KR20030025949A (en) * 2003-02-24 2003-03-29 주식회사 옥토프라자 a boiler for both heating and cooling
JP2009168308A (en) * 2008-01-15 2009-07-30 Tlv Co Ltd Evaporative cooling apparatus
JP2012002405A (en) * 2010-06-15 2012-01-05 Tlv Co Ltd Decompressed steam heating device
KR101406481B1 (en) * 2013-01-28 2014-06-13 뉴젠에너지 주식회사 Vacuum cycle type steam boiler

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100376220B1 (en) * 1999-04-21 2003-03-15 서명희 Heating and cooling device by using a boiler
KR20030025949A (en) * 2003-02-24 2003-03-29 주식회사 옥토프라자 a boiler for both heating and cooling
JP2009168308A (en) * 2008-01-15 2009-07-30 Tlv Co Ltd Evaporative cooling apparatus
JP2012002405A (en) * 2010-06-15 2012-01-05 Tlv Co Ltd Decompressed steam heating device
KR101406481B1 (en) * 2013-01-28 2014-06-13 뉴젠에너지 주식회사 Vacuum cycle type steam boiler

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