JP2010266144A - Vaporization cooling device - Google Patents
Vaporization cooling device Download PDFInfo
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- JP2010266144A JP2010266144A JP2009118597A JP2009118597A JP2010266144A JP 2010266144 A JP2010266144 A JP 2010266144A JP 2009118597 A JP2009118597 A JP 2009118597A JP 2009118597 A JP2009118597 A JP 2009118597A JP 2010266144 A JP2010266144 A JP 2010266144A
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- heat exchange
- cooling water
- compressed air
- cooling
- exchange container
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Abstract
Description
本発明は、熱交換容器の内部を減圧状態にして、供給される冷却水で被熱交換物を冷却する気化冷却装置に関する。 The present invention relates to a vaporization cooling apparatus that cools an object to be heat-exchanged with cooling water supplied by reducing the inside of a heat exchange container.
従来の気化冷却装置は、気化冷却室に接続する冷却水供給管を、熱交換容器の外壁面の接線方向で且つ水平方向に接続したものであり、冷却水が熱交換容器の外壁面を旋回しながら流下することによって、冷却水の付着効果が向上して、冷却効率を高めることができるものである。 In the conventional evaporative cooling device, the cooling water supply pipe connected to the evaporative cooling chamber is connected in the tangential direction and the horizontal direction of the outer wall surface of the heat exchange vessel, and the cooling water swirls around the outer wall surface of the heat exchange vessel. While flowing down, the adhesion effect of the cooling water is improved and the cooling efficiency can be increased.
上記従来の気化冷却装置では、熱交換容器の熱交換面が水平状である場合に、供給した冷却水が熱交換面から瞬時に滴下してしまい、気化冷却を効率良く実施することができない問題があった。 In the above conventional evaporative cooling device, when the heat exchange surface of the heat exchange container is horizontal, the supplied cooling water drops instantaneously from the heat exchange surface, and evaporative cooling cannot be performed efficiently. was there.
解決しようとする問題点は、熱交換容器の熱交換面が水平状の場合であっても、効率良く気化冷却を行うことのできる気化冷却装置を得ることである。 The problem to be solved is to obtain an evaporative cooling device that can efficiently perform evaporative cooling even when the heat exchange surface of the heat exchange vessel is horizontal.
本発明は、熱交換容器へ弁を介して冷却水を供給すると共に、熱交換容器の内部を減圧状態に維持する吸引手段を接続して、熱交換容器の被熱交換物を冷却するものにおいて、熱交換容器の熱交換面を水平状に配置して、当該水平状の熱交換面の表面に対向して冷却水供給口と圧縮空気供給口を設けて、当該冷却水供給口と圧縮空気供給口から交互に冷却水と圧縮空気を熱交換面の表面に供給するものである。 The present invention supplies cooling water to a heat exchange container through a valve and connects a suction means for maintaining the inside of the heat exchange container in a reduced pressure state to cool a heat exchange object in the heat exchange container. The heat exchange surface of the heat exchange container is horizontally arranged, the cooling water supply port and the compressed air supply port are provided facing the surface of the horizontal heat exchange surface, and the cooling water supply port and the compressed air are provided. Cooling water and compressed air are alternately supplied from the supply port to the surface of the heat exchange surface.
本発明は、水平状の熱交換面の表面に、冷却水と圧縮空気を交互に供給することにより、熱交換面に供給された冷却水が、その後に供給される圧縮空気によって熱交換面から滴下しにくくなり、熱交換面で確実に熱交換することができる。また、圧縮空気を供給することで、冷却水の熱交換面での蒸発気化が促進されて、冷却効率を向上させることができる。 In the present invention, the cooling water and the compressed air are alternately supplied to the surface of the horizontal heat exchange surface, so that the cooling water supplied to the heat exchange surface is transferred from the heat exchange surface by the compressed air supplied thereafter. It becomes difficult to dripping, and heat exchange can be reliably performed on the heat exchange surface. Further, by supplying the compressed air, evaporation of the cooling water on the heat exchange surface is promoted, and the cooling efficiency can be improved.
本発明は、熱交換面に冷却水と圧縮空気を供給口から供給するものであるが、この供給口は、共通の供給口から冷却水と圧縮空気を交互に供給することも、あるいは、別個の供給口からそれぞれの流体を交互に供給することもできる。 In the present invention, cooling water and compressed air are supplied to the heat exchange surface from the supply port. This supply port can alternately supply cooling water and compressed air from a common supply port, or separately. Each fluid can be alternately supplied from the supply port.
図1において、横長で直方体状の熱交換容器1と、この熱交換容器1の上端面に水平状に形成した熱交換面2と、熱交換面2の下方に取り付けた冷却水と圧縮空気の供給口24,25と、熱交換容器1の下方に連通したスチームトラップ4と吸引手段6とで気化冷却装置を構成する。なお、本実施例においては、気化冷却のみならず、加熱用の蒸気を蒸気供給管3から熱交換容器1へ供給することで、熱交換面2を加熱することもできる例を示す。 In FIG. 1, a horizontally long and rectangular parallelepiped heat exchange vessel 1, a heat exchange surface 2 formed horizontally on the upper end surface of the heat exchange vessel 1, and cooling water and compressed air attached below the heat exchange surface 2. The supply ports 24 and 25, the steam trap 4 communicating with the lower part of the heat exchange container 1, and the suction means 6 constitute a vaporization cooling device. In this embodiment, an example is shown in which the heat exchange surface 2 can be heated not only by evaporative cooling but also by supplying steam for heating from the steam supply pipe 3 to the heat exchange vessel 1.
蒸気供給管3には、熱交換容器1へ供給する蒸気の量を制御するための制御弁7を取り付ける。蒸気供給管3から熱交換容器1へ供給された加熱用の蒸気によって、熱交換面2を加熱するものである。 A control valve 7 for controlling the amount of steam supplied to the heat exchange container 1 is attached to the steam supply pipe 3. The heat exchange surface 2 is heated by the heating steam supplied from the steam supply pipe 3 to the heat exchange container 1.
熱交換容器1に冷却水を供給する冷却水供給管5を接続する。冷却水供給管5には自動弁27を介在して、熱交換容器1の下面の供給口24,25と接続する。自動弁27が開弁することにより、供給口24,25から熱交換面2へ冷却水が噴射されるものである。 A cooling water supply pipe 5 for supplying cooling water to the heat exchange vessel 1 is connected. The cooling water supply pipe 5 is connected to supply ports 24 and 25 on the lower surface of the heat exchange vessel 1 via an automatic valve 27. When the automatic valve 27 is opened, cooling water is injected from the supply ports 24 and 25 to the heat exchange surface 2.
熱交換容器1に圧縮空気を供給する圧縮空気供給管12を接続する。この圧縮空気供給管12にも自動弁16を介在して、供給口24,25と接続する。自動弁16が開弁することにより、供給口24,25から熱交換面2へ圧縮空気が噴射されるものである。 A compressed air supply pipe 12 that supplies compressed air to the heat exchange container 1 is connected. The compressed air supply pipe 12 is also connected to supply ports 24 and 25 via an automatic valve 16. When the automatic valve 16 is opened, compressed air is injected from the supply ports 24 and 25 to the heat exchange surface 2.
熱交換容器1の下端から管路8によりスチームトラップ4の入口側と接続する。スチームトラップ4と並列に開閉弁9を取り付ける。スチームトラップ4と開閉弁9の出口側は、吸引手段6を構成する液体エゼクタ13の吸込室10と接続する。 The lower end of the heat exchange vessel 1 is connected to the inlet side of the steam trap 4 by a pipe line 8. An on-off valve 9 is attached in parallel with the steam trap 4. The outlet side of the steam trap 4 and the on-off valve 9 is connected to the suction chamber 10 of the liquid ejector 13 constituting the suction means 6.
吸引手段6を、液体エゼクタ13と冷却水タンク14と循環ポンプ15とで構成する。循環ポンプ15の駆動によって冷却水タンク14内の冷却水を液体エゼクタ13へ供給することによって、吸込室10で所定の吸引力を発生するものである。 The suction means 6 includes a liquid ejector 13, a cooling water tank 14, and a circulation pump 15. By supplying the cooling water in the cooling water tank 14 to the liquid ejector 13 by driving the circulation pump 15, a predetermined suction force is generated in the suction chamber 10.
冷却水タンク14の上部に、冷却水供給管5を分岐した冷却水補給管30を接続すると共に、循環ポンプ15の吐出側の管路を分岐して余剰水排出管17を接続する。 A cooling water supply pipe 30 that branches the cooling water supply pipe 5 is connected to the upper part of the cooling water tank 14, and a surplus water discharge pipe 17 is connected by branching a discharge side pipe of the circulation pump 15.
熱交換面2を加熱する場合は、蒸気供給管3と制御弁7から熱交換容器1内へ所定量の蒸気を供給することによって、蒸気によって加熱される。加熱により凝縮した復水は、熱交換容器1下端の管路8からスチームトラップ4を通り、更に、液体エゼクタ13から冷却水タンク14へと至る。 When heating the heat exchange surface 2, the heat exchange surface 2 is heated by steam by supplying a predetermined amount of steam from the steam supply pipe 3 and the control valve 7 into the heat exchange container 1. Condensate condensed by heating passes from the pipe line 8 at the lower end of the heat exchange vessel 1 through the steam trap 4 and further from the liquid ejector 13 to the cooling water tank 14.
熱交換面2を冷却する場合は、冷却水供給管5の自動弁27を開弁して供給口24,25から熱交換面2の下表面へ所定量の冷却水を供給し、次いで、自動弁27を閉弁して、圧縮空気供給管12の自動弁16を開弁して供給口24,25から熱交換面2へ圧縮空気を供給することによって、熱交換面2の下面の冷却水が瞬時に滴下することがなく、熱交換面2の熱により冷却水が蒸発気化してその蒸発線熱でもって冷却することで、冷却効率を向上することができる。 When cooling the heat exchange surface 2, the automatic valve 27 of the cooling water supply pipe 5 is opened to supply a predetermined amount of cooling water from the supply ports 24 and 25 to the lower surface of the heat exchange surface 2. The valve 27 is closed, the automatic valve 16 of the compressed air supply pipe 12 is opened, and compressed air is supplied from the supply ports 24 and 25 to the heat exchange surface 2, thereby cooling water on the lower surface of the heat exchange surface 2. The cooling water evaporates by the heat of the heat exchange surface 2 and is cooled by the evaporation line heat, so that the cooling efficiency can be improved.
間接的な気化冷却を行うさまざまな気化冷却装置として適用できる。 It can be applied as various evaporative cooling devices that perform indirect evaporative cooling.
1 熱交換容器
2 熱交換面
5 冷却水供給管
6 吸引手段
10 吸込室
12 圧縮空気供給管
13 液体エゼクタ
14 冷却水タンク
15 循環ポンプ
24,25 供給口
DESCRIPTION OF SYMBOLS 1 Heat exchange container 2 Heat exchange surface 5 Cooling water supply pipe 6 Suction means 10 Suction chamber 12 Compressed air supply pipe 13 Liquid ejector 14 Cooling water tank 15 Circulation pump 24, 25 Supply port
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JP2009118597A JP5432588B2 (en) | 2009-05-15 | 2009-05-15 | Evaporative cooling device |
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JP2009118597A JP5432588B2 (en) | 2009-05-15 | 2009-05-15 | Evaporative cooling device |
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JP2010266144A true JP2010266144A (en) | 2010-11-25 |
JP5432588B2 JP5432588B2 (en) | 2014-03-05 |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103528261A (en) * | 2013-10-15 | 2014-01-22 | 上海交通大学 | Passive type organics jet refrigeration device |
Citations (7)
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JPH0361275U (en) * | 1989-10-13 | 1991-06-17 | ||
JPH0487737U (en) * | 1990-12-14 | 1992-07-30 | ||
JPH0526553A (en) * | 1991-07-15 | 1993-02-02 | Tlv Co Ltd | Vacuum gasification cooling device |
JPH0596229A (en) * | 1991-10-09 | 1993-04-20 | Fujitsu Ltd | Spin coating type resin liquid coating method |
JPH07163892A (en) * | 1993-12-15 | 1995-06-27 | Tlv Co Ltd | Heating cooling apparatus |
JPH07167543A (en) * | 1993-12-15 | 1995-07-04 | Tlv Co Ltd | Pressure reduction-vaporization cooling device |
JP2000070796A (en) * | 1998-08-31 | 2000-03-07 | Nkk Corp | Method and device for controlling thickness of coating film |
-
2009
- 2009-05-15 JP JP2009118597A patent/JP5432588B2/en not_active Expired - Fee Related
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0361275U (en) * | 1989-10-13 | 1991-06-17 | ||
JPH0487737U (en) * | 1990-12-14 | 1992-07-30 | ||
JPH0526553A (en) * | 1991-07-15 | 1993-02-02 | Tlv Co Ltd | Vacuum gasification cooling device |
JPH0596229A (en) * | 1991-10-09 | 1993-04-20 | Fujitsu Ltd | Spin coating type resin liquid coating method |
JPH07163892A (en) * | 1993-12-15 | 1995-06-27 | Tlv Co Ltd | Heating cooling apparatus |
JPH07167543A (en) * | 1993-12-15 | 1995-07-04 | Tlv Co Ltd | Pressure reduction-vaporization cooling device |
JP2000070796A (en) * | 1998-08-31 | 2000-03-07 | Nkk Corp | Method and device for controlling thickness of coating film |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103528261A (en) * | 2013-10-15 | 2014-01-22 | 上海交通大学 | Passive type organics jet refrigeration device |
CN103528261B (en) * | 2013-10-15 | 2015-09-09 | 上海交通大学 | A kind of non-energy dynamic formula organic matter injection cooling device |
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