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JP2013154267A - Low-pressure steam heating apparatus - Google Patents

Low-pressure steam heating apparatus Download PDF

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Publication number
JP2013154267A
JP2013154267A JP2012014995A JP2012014995A JP2013154267A JP 2013154267 A JP2013154267 A JP 2013154267A JP 2012014995 A JP2012014995 A JP 2012014995A JP 2012014995 A JP2012014995 A JP 2012014995A JP 2013154267 A JP2013154267 A JP 2013154267A
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steam
heat
heating
pump
vacuum pump
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JP2013154267A5 (en
JP5852452B2 (en
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Takayuki Morii
高之 森井
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TLV Co Ltd
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TLV Co Ltd
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Abstract

PROBLEM TO BE SOLVED: To provide a low-pressure steam heating apparatus allowing reduction of the amount of cooling water.SOLUTION: A steam supply pipe 8 for heating is connected to a jacket portion 2 of a reactor 1. A combination vacuum pump 4 is connected to the lower part of the jacket portion 2. The combination vacuum pump 4 is composed of a circulation pump 14, an ejector 10 and a circulation water tank 13. A heat pump 3 is composed of a compressor 5, a condenser 6, a steam trap 9 and an evaporator 13. Because the circulation water in the circulation water tank 13 of the combination vacuum pump 4 is cooled in an evaporation pipe 21 of the heat pump 3, the combination vacuum pump 4 does not require replenishment of fresh cooling water, allowing the reduction of the amount of cooling water used in the combination vacuum pump 4.

Description

本発明は、熱交換室で被熱交換物を低圧蒸気によって加熱する低圧蒸気加熱装置に関する。   The present invention relates to a low-pressure steam heating apparatus that heats a heat exchange object with low-pressure steam in a heat exchange chamber.

蒸気加熱装置は、熱交換室に熱交換流体供給管と吸引手段を接続して、熱交換流体供給管から加熱用の蒸気を熱交換室へ供給することによって、蒸気で被加熱物を加熱することができるものである。  The steam heating apparatus heats an object to be heated with steam by connecting a heat exchange fluid supply pipe and suction means to the heat exchange chamber and supplying steam for heating from the heat exchange fluid supply pipe to the heat exchange chamber. It is something that can be done.

特許第3170669号公報Japanese Patent No. 3170669

上記従来の蒸気加熱装置においては、タンク内の循環水の温度を所定値に維持するために冷却流体供給管から多量の冷却水を供給しなければならない問題があった。  The conventional steam heating apparatus has a problem that a large amount of cooling water must be supplied from the cooling fluid supply pipe in order to maintain the temperature of the circulating water in the tank at a predetermined value.

本発明が解決しようとする課題は、タンク内へ供給する冷却水の量を少なくすることのできる低圧蒸気加熱装置を提供することである。  The problem to be solved by the present invention is to provide a low-pressure steam heating device capable of reducing the amount of cooling water supplied into the tank.

本発明は、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と、当該ヒートポンプの凝縮器で熱交換器の加熱部に蒸気を供給する蒸気供給管を熱媒体と熱交換して加熱し、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て、当該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と共に、ヒートポンプの蒸発器で吸引手段を循環する循環液体を熱媒体と熱交換して冷却するものである。  The present invention includes a heat exchanger that accommodates an object to be heated, a heat pump filled with a heat medium in a closed loop of an evaporator, a compressor, a condenser, and an expander, and a heating unit of the heat exchanger using the condenser of the heat pump. The steam supply pipe for supplying steam to the heating medium is heated by exchanging heat with the heat medium, and a suction means for sucking the fluid in the heating section is connected to the heating section of the heat exchanger, and the inside of the heating section is about atmospheric pressure by the suction means. Or while maintaining the low pressure state below atmospheric pressure, the circulating liquid circulating through the suction means is cooled by exchanging heat with the heat medium in the evaporator of the heat pump.

本発明の低圧蒸気加熱装置は、ヒートポンプの蒸発器で吸引手段を循環する循環液体を熱媒体と熱交換して冷却することにより、少量の循環液体としての冷却水をヒートポンプで所定温度まで冷却し、繰り返して使用することができ、必要とする冷却流体の量を少なくすることができる。  The low-pressure steam heating device of the present invention cools a small amount of circulating water as a circulating liquid to a predetermined temperature with a heat pump by cooling the circulating liquid circulating through the suction means with a heat pump and cooling it with a heat medium. Can be used repeatedly, and the amount of cooling fluid required can be reduced.

本発明の低圧蒸気加熱装置の実施例を示す構成図。The block diagram which shows the Example of the low pressure steam heating apparatus of this invention.

本発明は、ヒートポンプを設けたものであるが、このヒートポンプとしては、蒸発器と圧縮機と凝縮器と膨張機とそれらを接続する管路とで構成される従来周知のものを用いることができる。  The present invention is provided with a heat pump. As this heat pump, a conventionally known one constituted by an evaporator, a compressor, a condenser, an expander, and a pipe line connecting them can be used. .

本実施例においては、熱交換器として反応釜1のジャケット部2を用いた例を示す。反応釜1の内部に入れた図示しない被加熱物を、ジャケット部2に供給する加熱源としての加熱用蒸気によって加熱するものである。  In this embodiment, an example is shown in which the jacket portion 2 of the reaction kettle 1 is used as a heat exchanger. An object to be heated (not shown) put inside the reaction kettle 1 is heated by heating steam as a heating source supplied to the jacket portion 2.

反応釜1のほぼ全周にわたりジャケット部2を形成して、このジャケット部2に吸引手段としての組み合わせ真空ポンプ4と、加熱流体としての加熱用蒸気供給管8を接続する。  A jacket portion 2 is formed over substantially the entire circumference of the reaction kettle 1, and a combined vacuum pump 4 as a suction means and a heating steam supply pipe 8 as a heating fluid are connected to the jacket portion 2.

ジャケット部2の左側上部には、流量調節弁7を介在した加熱用蒸気供給管8を接続する。この加熱用蒸気供給管8から、所定圧力すなわち温度の加熱用蒸気が、ジャケット部2へ供給されることによって、反応釜1内の被加熱物を加熱することができるものである。   A heating steam supply pipe 8 with a flow rate adjusting valve 7 interposed is connected to the upper left portion of the jacket portion 2. The heating steam in the reaction kettle 1 can be heated by supplying heating steam having a predetermined pressure, that is, temperature from the heating steam supply pipe 8 to the jacket portion 2.

ジャケット部2の下方に排出管20を接続して、組み合わせ真空ポンプ4のエゼクタ10と接続する。排出管20には蒸気トラップ22を取り付け、蒸気トラップ22と並列にバイパス弁23を取り付ける。   A discharge pipe 20 is connected below the jacket portion 2 and connected to the ejector 10 of the combination vacuum pump 4. A steam trap 22 is attached to the discharge pipe 20, and a bypass valve 23 is attached in parallel with the steam trap 22.

組み合わせ真空ポンプ4を、エゼクタ10と、循環ポンプ14と循環水タンク13、並びに、循環水タンク13内に配置したヒートポンプ3の蒸発管21とで形成する。循環水タンク13の底部には、タンク13内の循環水を所望温度まで加熱することのできる電気ヒータ24を取り付ける。組み合わせ真空ポンプ4は、循環水タンク13内の循環水を循環ポンプ14からエゼクタ10へ吐出し、再度循環水タンク13へと循環するものであり、エゼクタ10に循環水が高速で吐出されることによってエゼクタ10内で吸引力を発生して、ジャケット部2下方の排出管20からジャケット部2内で蒸気が凝縮した復水を吸引し、循環水と混合して循環水タンク13へと流下するものである。   The combination vacuum pump 4 is formed by an ejector 10, a circulation pump 14, a circulation water tank 13, and an evaporation pipe 21 of the heat pump 3 disposed in the circulation water tank 13. An electric heater 24 capable of heating the circulating water in the tank 13 to a desired temperature is attached to the bottom of the circulating water tank 13. The combination vacuum pump 4 discharges the circulating water in the circulating water tank 13 from the circulating pump 14 to the ejector 10 and circulates it again to the circulating water tank 13, and the circulating water is discharged to the ejector 10 at a high speed. As a result, a suction force is generated in the ejector 10, the condensate in which the steam is condensed in the jacket portion 2 is sucked from the discharge pipe 20 below the jacket portion 2, mixed with the circulating water, and flows down to the circulating water tank 13. Is.

ヒートポンプ3を、圧縮機5と凝縮器6と膨張機としての蒸気トラップ9、及び、循環水タンク13がその作用を発揮する蒸発器13とで構成して、それぞれの機器を連通する循環路11で連通する。 The heat pump 3 includes a compressor 5, a condenser 6, a steam trap 9 as an expander, and an evaporator 13 in which a circulating water tank 13 exerts its action, and a circulation path 11 that communicates each device. Communicate with

循環ポンプ14の吐出側を分岐して凝縮器6へ循環水の一部を供給する循環水供給管12を接続する。循環水供給管12は、凝縮器6内の水位を制御する水位制御弁15を介在して、凝縮器6内でヒートポンプ3の循環路11と熱交換して加熱されることによって蒸気供給管16で蒸気となり、加熱用蒸気供給管8からジャケット部2へその蒸気を供給する。ジャケット部2へ供給された蒸気によって、反応釜1内の被加熱物を加熱するものである。  A circulating water supply pipe 12 for branching the discharge side of the circulation pump 14 and supplying a part of the circulating water to the condenser 6 is connected. The circulating water supply pipe 12 is heated by exchanging heat with the circulation path 11 of the heat pump 3 in the condenser 6 via a water level control valve 15 that controls the water level in the condenser 6. And the steam is supplied from the heating steam supply pipe 8 to the jacket portion 2. An object to be heated in the reaction kettle 1 is heated by the steam supplied to the jacket portion 2.

凝縮器6で蒸気供給管16内の循環水と熱交換して熱を奪われた循環路11内の熱媒体は、凝縮して液体となり、膨張機としての蒸気トラップ9を通過する間に膨張して気体となって蒸発器13へ流下する。蒸発器13内の蒸発管21で循環水の熱を奪って昇温した熱媒体は、圧縮機5で圧縮されて更に昇温して凝縮器6へと送られる。 The heat medium in the circulation path 11 deprived of heat by exchanging heat with the circulating water in the steam supply pipe 16 by the condenser 6 is condensed to become a liquid and expands while passing through the steam trap 9 as an expander. The gas then flows down to the evaporator 13. The heat medium that has been heated by removing heat from the circulating water in the evaporator 13 in the evaporator 13 is compressed by the compressor 5, further heated, and sent to the condenser 6.

蒸発器13すなわち循環水タンク13内の循環水は、蒸発管21で熱を奪われて冷却される。このように、循環水が冷却されることによって、新たな冷却水を補給する必要がなく、組み合わせ真空ポンプ4で使用する冷却水の量を少なくすることができる。   The evaporator 13, that is, the circulating water in the circulating water tank 13 is cooled by removing heat from the evaporation pipe 21. In this way, the circulating water is cooled, so that it is not necessary to supply new cooling water, and the amount of cooling water used in the combination vacuum pump 4 can be reduced.

循環水タンク13内に循環水を所望温度まで加熱することのできる電気ヒータ24を取り付けたことによって、循環水供給管12から凝縮器6へと供給される循環水の温度を任意にコントロールすることができ、ヒートポンプ3の制御と相俟って、加熱用蒸気供給管8からジャケット部2へ供給する蒸気の温度も任意にコントロールすることができ、蒸気ボイラ等の蒸気発生源を別途設置する必要がなくなる。  The temperature of the circulating water supplied from the circulating water supply pipe 12 to the condenser 6 can be arbitrarily controlled by attaching an electric heater 24 capable of heating the circulating water to a desired temperature in the circulating water tank 13. In combination with the control of the heat pump 3, the temperature of the steam supplied from the heating steam supply pipe 8 to the jacket part 2 can be arbitrarily controlled, and a steam generation source such as a steam boiler must be separately installed. Disappears.

本発明は、蒸気ボイラ等の蒸気発生源を別途設置することなく、熱交換室で被熱交換物を低圧蒸気によって加熱する低圧蒸気加熱装置として利用することができる。 INDUSTRIAL APPLICABILITY The present invention can be used as a low pressure steam heating apparatus that heats a heat exchange object with low pressure steam in a heat exchange chamber without separately installing a steam generation source such as a steam boiler.

1 反応釜
2 ジャケット部
3 ヒートポンプ
4 組み合わせ真空ポンプ
5 圧縮機
6 凝縮器
8 加熱用蒸気供給管
9 蒸気トラップ
10 エゼクタ
11 循環路
12 循環水供給管
13 蒸発器
16 蒸気供給管
20 排出管
21 蒸発管
22 蒸気トラップ
DESCRIPTION OF SYMBOLS 1 Reaction kettle 2 Jacket part 3 Heat pump 4 Combination vacuum pump 5 Compressor 6 Condenser 8 Steam supply pipe for heating 9 Steam trap 10 Ejector 11 Circulation path 12 Circulating water supply pipe 13 Evaporator 16 Steam supply pipe 20 Exhaust pipe 21 Evaporation pipe 22 Steam trap

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と、当該ヒートポンプの凝縮器で熱交換器の加熱部に蒸気を供給する蒸気供給管を熱媒体と熱交換して加熱し、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て、当該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と共に、ヒートポンプの蒸発器で吸引手段を循環する循環液体を熱媒体と熱交換して冷却することを特徴とする低圧蒸気加熱装置。 Steam is supplied to the heating section of the heat exchanger with a heat exchanger that contains the object to be heated, a heat pump that is filled with a heat medium in a closed loop by an evaporator, compressor, condenser, and expander. The steam supply pipe is heated by exchanging heat with the heat medium, and a suction means for sucking the fluid in the heating section is connected to the heating section of the heat exchanger, and the inside of the heating section is about atmospheric pressure or lower than the atmospheric pressure by the suction means. The low-pressure steam heating apparatus is characterized in that the circulating liquid circulating through the suction means is cooled by exchanging heat with the heat medium in the evaporator of the heat pump.
JP2012014995A 2012-01-27 2012-01-27 Low pressure steam heating device Active JP5852452B2 (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104089272A (en) * 2014-06-13 2014-10-08 云南能投有能科技股份有限公司 Two-stage deoxidized exhaust steam condensing device for heat-exchange mixed exhaust steam recovery of condensate water and desalted water
CN104085938A (en) * 2014-06-13 2014-10-08 云南能投有能科技股份有限公司 Condensate water and demineralized water indirect heat-exchange forced-mixing one-stage deoxygenization apparatus
CN104085939A (en) * 2014-06-13 2014-10-08 云南能投有能科技股份有限公司 Condensate water and demineralized water exhaust-steam recovery one-stage deoxygenization apparatus

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62288463A (en) * 1986-06-09 1987-12-15 東京都 Heat pump with auxiliary heater
JPH0979514A (en) * 1995-09-14 1997-03-28 Tlv Co Ltd Low-pressure steam heater by heating medium
JP2010164223A (en) * 2009-01-14 2010-07-29 Kobe Steel Ltd Steam generator

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62288463A (en) * 1986-06-09 1987-12-15 東京都 Heat pump with auxiliary heater
JPH0979514A (en) * 1995-09-14 1997-03-28 Tlv Co Ltd Low-pressure steam heater by heating medium
JP2010164223A (en) * 2009-01-14 2010-07-29 Kobe Steel Ltd Steam generator

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104089272A (en) * 2014-06-13 2014-10-08 云南能投有能科技股份有限公司 Two-stage deoxidized exhaust steam condensing device for heat-exchange mixed exhaust steam recovery of condensate water and desalted water
CN104085938A (en) * 2014-06-13 2014-10-08 云南能投有能科技股份有限公司 Condensate water and demineralized water indirect heat-exchange forced-mixing one-stage deoxygenization apparatus
CN104085939A (en) * 2014-06-13 2014-10-08 云南能投有能科技股份有限公司 Condensate water and demineralized water exhaust-steam recovery one-stage deoxygenization apparatus
CN104085938B (en) * 2014-06-13 2016-05-11 云南能投有能科技股份有限公司 Condensed water demineralized water indirect heat exchange Forced Mixing one-level deaerating plant
CN104085939B (en) * 2014-06-13 2016-05-11 云南能投有能科技股份有限公司 One-level deaerating plant is reclaimed in the exhaust steam of condensed water demineralized water

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