JP2013040735A - Heating device by low-pressure steam - Google Patents

Heating device by low-pressure steam Download PDF

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JP2013040735A
JP2013040735A JP2011179043A JP2011179043A JP2013040735A JP 2013040735 A JP2013040735 A JP 2013040735A JP 2011179043 A JP2011179043 A JP 2011179043A JP 2011179043 A JP2011179043 A JP 2011179043A JP 2013040735 A JP2013040735 A JP 2013040735A
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steam
low
pressure
heating
heat exchanger
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JP5822599B2 (en
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Yoshiyasu Fujiwara
良康 藤原
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TLV Co Ltd
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Abstract

PROBLEM TO BE SOLVED: To provide a heating device by low-pressure steam, which does not use a boiler.SOLUTION: A heat exchanger 1 accommodating a heated object and a steam supply tube 3 which supplies heating steam from a condenser 9 of a heat pump 6 filling a heat medium in a closed loop by an evaporator 7, a compressor 8, the condenser 9, and a steam trap 10 to a jacket part 2 of the heat exchanger 1 are connected, a suction means 4 for sucking fluid in the jacket part 2 is connected to the jacket part 2 of the heat exchanger, and by keeping the inside of the jacket part 2 by the suction means 4 to the level of atmospheric pressure or a low-pressure state at atmospheric pressure or below, the heated object is heated by low-pressure steam. Heating steam from the condenser 9 of the heat pump 6 is supplied to the jacket part 2 of the heat exchanger 1, fluid in the jacket part 2 is sucked by the suction means 4 to keep the inside of the jacket part 2 to the level of atmospheric pressure or at a low-pressure state at atmospheric pressure or below, so that the heating device by the low-pressure steam, which does not use the boiler can be provided.

Description

本発明は、熱交換器内の被加熱物を熱交換器の加熱部からの低圧蒸気で加熱するものに関し、特にその低圧蒸気温度が100度C程度の比較的低温の場合に適した低圧蒸気による加熱装置に関する。 The present invention relates to heating an object to be heated in a heat exchanger with low-pressure steam from a heating section of the heat exchanger, and particularly suitable for a case where the low-pressure steam temperature is a relatively low temperature of about 100 ° C. Relates to a heating device.

従来の低圧蒸気による加熱装置は、例えば特許文献1に示されている。これは、被加熱物を収容する熱交換器の加熱部に、ボイラーからの加熱用の蒸気を供給する蒸気供給管を接続するとともに、加熱部内の流体を吸引する吸引手段を接続し、吸引手段で加熱部内を大気圧程度又は大気圧以下の低圧状態に維持することにより被加熱物を低圧蒸気により加熱するものである。 A conventional heating apparatus using low-pressure steam is disclosed in Patent Document 1, for example. This is connected to a heating unit of a heat exchanger that accommodates an object to be heated, a steam supply pipe that supplies steam for heating from a boiler, and a suction unit that sucks a fluid in the heating unit, and a suction unit Thus, the object to be heated is heated with low-pressure steam by maintaining the inside of the heating section at a low pressure state of about atmospheric pressure or below atmospheric pressure.

特開2003−80003号公報JP 2003-80003 A

上記従来の低圧蒸気による加熱装置は、加熱用の蒸気としてボイラーからの蒸気を利用するものであるので、ボイラー設備のない大学等の実験室においては、この低圧蒸気による加熱装置を利用できない問題点があった。 The conventional low-pressure steam heating device uses steam from a boiler as heating steam, so that this low-pressure steam heating device cannot be used in a laboratory such as a university without a boiler facility. was there.

解決しようとする課題は、ボイラーを用いない低圧蒸気による加熱装置を提供することである。 The problem to be solved is to provide a low pressure steam heating device that does not use a boiler.

本発明は、被加熱物を収容する熱交換器の加熱部に、蒸発器、圧縮機、凝縮器、膨張機による閉ループ内に熱媒体を充填したヒートポンプの凝縮器からの加熱用の蒸気を供給する蒸気供給管を接続するとともに、加熱部内の流体を吸引する吸引手段を接続し、吸引手段で加熱部内を大気圧程度又は大気圧以下の低圧状態に維持することにより被加熱物を低圧蒸気により加熱することを特徴とするものである。 The present invention supplies heating steam from a condenser of a heat pump in which a heating medium is filled in a closed loop of an evaporator, a compressor, a condenser, and an expander to a heating section of a heat exchanger that accommodates an object to be heated. And a suction means for sucking the fluid in the heating part is connected, and the heated part is maintained at a low pressure state of about atmospheric pressure or lower than atmospheric pressure by the suction means, so that the object to be heated is made of low-pressure steam. It is characterized by heating.

本発明は、ヒートポンプの凝縮器からの加熱用の蒸気を熱交換器の加熱部に供給し、加熱部内の流体を吸引手段で吸引して加熱部内を大気圧程度又は大気圧以下の低圧状態に維持することにより、ボイラーを用いない低圧蒸気による加熱装置を提供できるという優れた効果を生じる。 The present invention supplies the heating steam from the condenser of the heat pump to the heating part of the heat exchanger, sucks the fluid in the heating part with the suction means, and puts the inside of the heating part into a low pressure state of about atmospheric pressure or less than atmospheric pressure. By maintaining, an excellent effect that a heating device using low-pressure steam without using a boiler can be provided is produced.

本発明の実施の形態に係わる低圧蒸気による加熱装置の概略構成図である。It is a schematic block diagram of the heating apparatus by the low pressure steam concerning embodiment of this invention.

以下、本発明の実施の形態について、図1を参照して説明する。被加熱物を収容する熱交換器1の外周に一体に熱交換器の加熱部としてのジャケット部2を設け、このジャケット部2へ加熱用の蒸気供給管3と吸引手段4を接続する。熱交換器1は円筒タンク状で内部に図示しない被加熱物を収容し、側方外周の全周を覆うジャケット部2を一体に設けたものである。ジャケット部2の上方に蒸気供給管3を接続し、蒸気供給管3に圧力制御弁5を配置する。蒸気供給管3はヒートポンプ6の凝縮器9からの加熱用の蒸気を熱交換器1のジャケット部2に供給する。 Hereinafter, an embodiment of the present invention will be described with reference to FIG. A jacket portion 2 as a heating portion of the heat exchanger is integrally provided on the outer periphery of the heat exchanger 1 that accommodates an object to be heated, and the heating steam supply pipe 3 and the suction means 4 are connected to the jacket portion 2. The heat exchanger 1 has a cylindrical tank shape and accommodates an object to be heated (not shown) therein, and is integrally provided with a jacket portion 2 that covers the entire outer periphery of the side. A steam supply pipe 3 is connected above the jacket portion 2, and a pressure control valve 5 is disposed in the steam supply pipe 3. The steam supply pipe 3 supplies the steam for heating from the condenser 9 of the heat pump 6 to the jacket portion 2 of the heat exchanger 1.

ヒートポンプ6は、熱媒体を高温熱源と熱交換させ熱媒体を蒸発させる蒸発器7と、蒸発器7で蒸発させた熱媒体を圧縮する圧縮機8と、圧縮機8で圧縮された熱媒体を低温熱源と熱交換させ熱媒体を凝縮させる凝縮器9と、凝縮器9で凝縮させた熱媒体を膨張させて蒸発器7に供給する膨張機としてのスチームトラップ10から構成する。蒸発器7には蒸発器7に高温熱源を供給する高温熱源供給管11が接続され、凝縮器9には凝縮器9に低温熱源を供給する低温熱源供給管12が接続される。低温熱源供給管12は吸引手段4の循環路21から分岐している。ヒートポンプ6では、蒸発器7にて熱媒体が蒸発し、気相となった熱媒体が圧縮機8を通して凝縮器9に移動する。凝縮器9に移動した気相の熱媒体は凝縮器9にて液相に凝縮され、液相の熱媒体がスチームトラップ10を通して蒸発器6に戻る。高温熱源供給管11から蒸発器7に供給された高温熱源は、蒸発器7にて液相の熱媒体と熱交換され低温熱源として低温熱源導出管13から導出され、吸引手段4の循環路21を分岐して低温熱源供給管12から凝縮器9に供給された低温熱源は、凝縮器9にて気相の熱媒体と熱交換され蒸気として蒸気供給管3からジャケット部2に供給される。 The heat pump 6 includes an evaporator 7 that exchanges heat with a high-temperature heat source to evaporate the heat medium, a compressor 8 that compresses the heat medium evaporated by the evaporator 7, and a heat medium that is compressed by the compressor 8. It comprises a condenser 9 that exchanges heat with a low-temperature heat source and condenses the heat medium, and a steam trap 10 as an expander that expands the heat medium condensed in the condenser 9 and supplies it to the evaporator 7. A high temperature heat source supply pipe 11 that supplies a high temperature heat source to the evaporator 7 is connected to the evaporator 7, and a low temperature heat source supply pipe 12 that supplies a low temperature heat source to the condenser 9 is connected to the condenser 9. The low temperature heat source supply pipe 12 branches from the circulation path 21 of the suction means 4. In the heat pump 6, the heat medium evaporates in the evaporator 7, and the heat medium that has become a gas phase moves to the condenser 9 through the compressor 8. The gas phase heat medium that has moved to the condenser 9 is condensed into a liquid phase by the condenser 9, and the liquid phase heat medium returns to the evaporator 6 through the steam trap 10. The high temperature heat source supplied to the evaporator 7 from the high temperature heat source supply pipe 11 is exchanged with the liquid phase heat medium in the evaporator 7 and is led out from the low temperature heat source outlet pipe 13 as a low temperature heat source. The low-temperature heat source supplied from the low-temperature heat source supply pipe 12 to the condenser 9 is subjected to heat exchange with the gas phase heat medium in the condenser 9 and supplied as steam to the jacket portion 2 from the vapor supply pipe 3.

ジャケット部2の下方に連通管14を介して、吸引手段4のエゼクタ15と接続する。連通管14にはスチームトラップ16と、そのバイパス弁17を並列に取り付ける。連通管14はその下端がエゼクタ15の吸引室18と接続する。吸引手段4はエゼクタ15とタンク19と循環ポンプ20を循環路21で接続して組み合わせたエゼクタ式組み合わせポンプで構成する。タンク19内に循環流体としての温水を所定量溜め置き、この温水を循環ホンプ20でエゼクタ15からタンク19へと循環させ、エゼクタ15の吸引作用により吸引室18に吸引力を発生させ、熱交換器1のジャケット部2内を所定の圧力状態としての大気圧や大気圧以下の負圧状態に維持する。タンク19には循環流体補給管22をバルブ23を介して接続し、循環流体排出管24をバルブ25を介して接続する。 The ejector 15 of the suction means 4 is connected to the lower portion of the jacket portion 2 through the communication pipe 14. A steam trap 16 and a bypass valve 17 are attached to the communication pipe 14 in parallel. The lower end of the communication pipe 14 is connected to the suction chamber 18 of the ejector 15. The suction means 4 is constituted by an ejector type combination pump in which an ejector 15, a tank 19 and a circulation pump 20 are connected by a circulation path 21. A predetermined amount of warm water as a circulating fluid is stored in the tank 19, and this warm water is circulated from the ejector 15 to the tank 19 by the circulation pump 20, and a suction force is generated in the suction chamber 18 by the suction action of the ejector 15 to exchange heat. The inside of the jacket portion 2 of the vessel 1 is maintained at an atmospheric pressure as a predetermined pressure state or a negative pressure state below the atmospheric pressure. A circulating fluid supply pipe 22 is connected to the tank 19 via a valve 23, and a circulating fluid discharge pipe 24 is connected via a valve 25.

エゼクタ15で生じる吸引力は、エゼクタ15内を流下する流体の温度に相当する飽和圧力となることから、循環流体補給管22から流体を補給して流体温度を適宜調節することにより、エゼクタ15の吸引力を任意に制御することができる。例えば、ジャケット部2内に80度Cの低温蒸気を供給して被加熱物を加熱する場合、エゼクタ15の吸引力が80度Cより僅かに低い温度における蒸気の飽和圧力に相当する圧力の吸引力となるように、循環流体の温度を調節することにより、所定の温度状態を維持することができる。熱交換器1内の被加熱物を加熱する場合、先ず、バイパス弁17を開弁すると共に、エゼクタ式組み合わせポンプ4を駆動してエゼクタ15の吸引力によってジャケット部2内を所定の低圧力状態とし、圧力制御弁5を通して所定圧力に制御された加熱用蒸気を蒸気供給管3からジャケット部2内に供給する。被加熱物を加熱して熱を奪われた蒸気は凝縮して復水となり、連通管14のスチームトラップ16又はバイパス弁17からエゼクタ15に吸引されタンク19に至る。 Since the suction force generated in the ejector 15 becomes a saturation pressure corresponding to the temperature of the fluid flowing down in the ejector 15, the fluid is replenished from the circulating fluid supply pipe 22 and the fluid temperature is appropriately adjusted, so that the ejector 15 The suction force can be arbitrarily controlled. For example, when a low-temperature steam of 80 ° C. is supplied into the jacket portion 2 to heat an object to be heated, suction of a pressure corresponding to the saturation pressure of the steam at a temperature where the suction force of the ejector 15 is slightly lower than 80 ° C. A predetermined temperature state can be maintained by adjusting the temperature of the circulating fluid so as to be a force. When the object to be heated in the heat exchanger 1 is heated, first, the bypass valve 17 is opened, the ejector-type combination pump 4 is driven, and the inside of the jacket portion 2 is in a predetermined low pressure state by the suction force of the ejector 15. Then, the steam for heating controlled to a predetermined pressure is supplied from the steam supply pipe 3 into the jacket portion 2 through the pressure control valve 5. Steam deprived of heat by heating the object to be heated is condensed and becomes condensed water, and is sucked into the ejector 15 from the steam trap 16 or the bypass valve 17 of the communication pipe 14 and reaches the tank 19.

本発明は、熱交換器内の被加熱物を熱交換器の加熱部からの低圧蒸気で加熱する低圧蒸気による加熱装置に利用することができる。   INDUSTRIAL APPLICATION This invention can be utilized for the heating apparatus by the low pressure steam which heats the to-be-heated object in a heat exchanger with the low pressure steam from the heating part of a heat exchanger.

1 熱交換器
2 ジャケット部
3 蒸気供給管
4 吸引手段
5 圧力制御弁
6 ヒートポンプ
7 蒸発器
8 圧縮機
9 凝縮器
10 スチームトラップ
11 高温熱源供給管
12 低温熱源供給管
13 低温熱源導出管
14 連通管
15 エゼクタ
16 スチームトラップ
17 バイパス弁
18 吸引室
19 タンク
20 循環ホンプ
DESCRIPTION OF SYMBOLS 1 Heat exchanger 2 Jacket part 3 Steam supply pipe 4 Suction means 5 Pressure control valve 6 Heat pump 7 Evaporator 8 Compressor 9 Condenser 10 Steam trap 11 High temperature heat source supply pipe 12 Low temperature heat source supply pipe 13 Low temperature heat source derivation pipe 14 Communication pipe 15 Ejector 16 Steam trap 17 Bypass valve 18 Suction chamber 19 Tank 20 Circulation pump

Claims (1)

被加熱物を収容する熱交換器と、蒸発器、圧縮機、凝縮器、膨張機による閉ループ内に熱媒体を充填したヒートポンプの凝縮器からの加熱用の蒸気を熱交換器の加熱部に供給する蒸気供給管を接続するとともに、熱交換器の加熱部に加熱部内の流体を吸引する吸引手段を接続し、吸引手段で加熱部内を大気圧程度又は大気圧以下の低圧状態に維持することにより被加熱物を低圧蒸気により加熱することを特徴とする低圧蒸気による加熱装置。 Supplying steam for heating from the heat exchanger containing the object to be heated and the condenser of the heat pump filled with the heat medium in the closed loop by the evaporator, compressor, condenser, and expander to the heating section of the heat exchanger By connecting a steam supply pipe to the heating section of the heat exchanger and a suction means for sucking the fluid in the heating section, and maintaining the inside of the heating section at a low pressure state of about atmospheric pressure or lower than atmospheric pressure by the suction means. A heating apparatus using low-pressure steam, wherein an object to be heated is heated by low-pressure steam.
JP2011179043A 2011-08-18 2011-08-18 Heating device using low pressure steam Active JP5822599B2 (en)

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WO2015021760A1 (en) * 2013-08-12 2015-02-19 天津市万泽电子系统控制技术有限公司 Turbonator-based cooled water treatment system
CN104848284A (en) * 2015-04-09 2015-08-19 宜诺珐玛(天津)科技有限公司 Steam condensation water heat recovery method and device

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CN110748873B (en) * 2019-10-08 2021-04-16 河南理工大学 Exhaust steam heat regeneration system of power plant

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Publication number Priority date Publication date Assignee Title
WO2015021760A1 (en) * 2013-08-12 2015-02-19 天津市万泽电子系统控制技术有限公司 Turbonator-based cooled water treatment system
CN104848284A (en) * 2015-04-09 2015-08-19 宜诺珐玛(天津)科技有限公司 Steam condensation water heat recovery method and device
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