JPH03260593A - Heat feed apparatus - Google Patents
Heat feed apparatusInfo
- Publication number
- JPH03260593A JPH03260593A JP5827490A JP5827490A JPH03260593A JP H03260593 A JPH03260593 A JP H03260593A JP 5827490 A JP5827490 A JP 5827490A JP 5827490 A JP5827490 A JP 5827490A JP H03260593 A JPH03260593 A JP H03260593A
- Authority
- JP
- Japan
- Prior art keywords
- gas
- liquid
- heater
- pipe
- radiator
- 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
Links
- 239000007788 liquid Substances 0.000 claims abstract description 48
- 238000010438 heat treatment Methods 0.000 claims abstract description 14
- 239000007789 gas Substances 0.000 claims description 13
- 238000009834 vaporization Methods 0.000 claims description 12
- 230000008016 vaporization Effects 0.000 claims description 12
- 239000002918 waste heat Substances 0.000 claims description 2
- 238000001704 evaporation Methods 0.000 abstract description 4
- 230000008020 evaporation Effects 0.000 abstract description 4
- 230000002159 abnormal effect Effects 0.000 abstract description 3
- 230000005484 gravity Effects 0.000 abstract description 3
- 239000002826 coolant Substances 0.000 abstract 1
- 238000013021 overheating Methods 0.000 description 3
- 239000000470 constituent Substances 0.000 description 2
- 239000003507 refrigerant Substances 0.000 description 2
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- NBVXSUQYWXRMNV-UHFFFAOYSA-N fluoromethane Chemical compound FC NBVXSUQYWXRMNV-UHFFFAOYSA-N 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 230000005514 two-phase flow Effects 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Fuel Cell (AREA)
Abstract
Description
【発明の詳細な説明】
産業上の利用分野
本発明は暖冷房の空調機および排熱回収装置に用いられ
る熱搬送装置に関するものである。DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to a heat transfer device used in a heating/cooling air conditioner and an exhaust heat recovery device.
従来の技術
従来、この種の熱搬送装置は第2図のような構造となっ
ていた。すなわち上部ヘッダー1と下部ヘッダー2とを
接続する熱交換器3を有する加熱器4と、上部ヘッダー
1に接続されるガス管5と、下部ヘッダー2に接続され
る液戻り管6とによって接続される気液分離器7と、加
熱器4の上方に設けられた放熱器8と、気液分離器7と
放熱器8を接続する往管9と、放熱器8と下部ヘッダー
2を接続する復管10によって構成される密閉回路に水
または、フロンのような蒸発性潜熱媒体11を封入し、
熱源12で加熱器4を熱し廃熱はそのまま外部に放出す
る構造になっていた。BACKGROUND OF THE INVENTION Conventionally, this type of heat transfer device has had a structure as shown in FIG. That is, the upper header 1 and the lower header 2 are connected by a heater 4 having a heat exchanger 3, a gas pipe 5 connected to the upper header 1, and a liquid return pipe 6 connected to the lower header 2. a gas-liquid separator 7, a radiator 8 provided above the heater 4, an outgoing pipe 9 connecting the gas-liquid separator 7 and the radiator 8, and a return pipe connecting the radiator 8 and the lower header 2. Water or an evaporative latent heat medium 11 such as fluorocarbon is sealed in a closed circuit constituted by a tube 10,
The heater 4 was heated by the heat source 12 and the waste heat was directly released to the outside.
したがって、加熱器4が加熱されると内部の蒸発性潜熱
媒体11は蒸発し、気液二相状態となってガス管5を通
り、気液分離器7でガスと液がほぼ分離されるものの若
干湿った気液二相状態で往管9を採って放熱器8に導か
れる。一方、気液分離器7内の液は液戻り管6を通って
加熱器4の下部ヘッダー2に落とし込まれる。この時、
放熱器8内の気液二相流は、ガスの凝縮および液体の顕
熱放出によって放熱する。放熱器8内の液は重力作用に
よって復管10を通り、加熱器4の下部ヘッダー2に戻
り、再び熱源12で加熱され蒸発、凝縮をくり返す事に
より密閉回路内を循環することとなる。Therefore, when the heater 4 is heated, the internal evaporative latent heat medium 11 evaporates, becomes a gas-liquid two-phase state, passes through the gas pipe 5, and is almost separated into gas and liquid by the gas-liquid separator 7. The outgoing pipe 9 is taken in a slightly moist gas-liquid two-phase state and guided to the radiator 8. On the other hand, the liquid in the gas-liquid separator 7 passes through the liquid return pipe 6 and is dropped into the lower header 2 of the heater 4. At this time,
The gas-liquid two-phase flow within the heat radiator 8 radiates heat by condensing the gas and releasing sensible heat from the liquid. The liquid in the radiator 8 passes through the return pipe 10 under the action of gravity, returns to the lower header 2 of the heater 4, is heated again by the heat source 12, and is circulated in the closed circuit by repeating evaporation and condensation.
発明が解決しようとする課題
このような従来の熱搬送装置では、気液分離器7におい
て、気液の完全な分離が不可能であるため、熱媒体11
が気液二相状態で往管を循環し、熱媒が液体状態で放熱
器8に偏在してしまう傾向があった。このため、加熱器
4内の熱媒が不足し、加熱器4が異常に過熱し、更に放
熱器8の熱交換器において、潜熱域での熱交換器面積が
減少して熱交換器3の効率が低下し、熱媒の搬送系の圧
力が上昇するので、熱交換器の面積を大きくしなければ
ならなかった。Problems to be Solved by the Invention In such a conventional heat transfer device, complete separation of gas and liquid is impossible in the gas-liquid separator 7.
There was a tendency for the heating medium to circulate in the outgoing pipe in a gas-liquid two-phase state, and the heat medium to be unevenly distributed in the radiator 8 in a liquid state. As a result, the heat medium in the heater 4 becomes insufficient, causing the heater 4 to overheat abnormally, and furthermore, in the heat exchanger of the radiator 8, the heat exchanger area in the latent heat region decreases, causing the heat exchanger 3 to become overheated. The area of the heat exchanger had to be increased because the efficiency decreased and the pressure in the heat transfer system increased.
本発明は上記課題を解消するもので、気液分離器の性能
を向上させることにより、熱媒の搬送系の圧力上昇を防
ぎ、小さな放熱器での運転を可能とするとともに、排熱
の有効利用によって、システム効率を向上させることの
できる熱搬送装置を提供することを目的としている。The present invention solves the above problems, and by improving the performance of the gas-liquid separator, it prevents the pressure increase in the heat medium conveyance system, enables operation with a small radiator, and effectively dissipates heat. It is an object of the present invention to provide a heat transfer device that can improve system efficiency when utilized.
課題を解決するための手段
本発明は上記目的を達成するために、上部ヘッダーと下
部ヘッダーとを接続する熱交換器により構成される加熱
器と、上部へフグ−にガス管によって接続されるととも
に、底部から液戻り管によって下部ヘッダーに接続され
、冷媒を加熱することによって熱媒の気化を促進させる
。Means for Solving the Problems In order to achieve the above object, the present invention provides a heater constituted by a heat exchanger connecting an upper header and a lower header, and a heater connected to an upper header by a gas pipe. , connected to the lower header by a liquid return pipe from the bottom, which accelerates the vaporization of the heating medium by heating the refrigerant.
気化促進器を有する気液分離器と、加熱器の上方に設け
られる放熱器と、気液分離器と放熱器とを接続する往管
と、下部ヘッダーと放熱器を接続する復管からなる密閉
回路に蒸発性の熱媒を封入した構成を備えたものである
。A sealed system consisting of a gas-liquid separator with a vaporization accelerator, a radiator installed above the heater, an outgoing pipe that connects the gas-liquid separator and the radiator, and a return pipe that connects the lower header and the radiator. It has a configuration in which an evaporative heating medium is enclosed in the circuit.
作用
本発明は上記した構成によって、往管内を流れる熱媒の
状態を完全に気体としたものである。このため放熱器へ
の熱媒の偏在が防止され、加熱器の液切れによる異常過
熱を防止し、更に放熱器熱交換器の潜熱域での熱交換面
積を増加させ熱交換効率を向上させることができるもの
である。Operation The present invention has the above-described configuration, so that the state of the heating medium flowing in the outgoing pipe is completely gaseous. This prevents uneven distribution of the heat medium in the radiator, prevents abnormal overheating due to liquid shortage in the heater, and further increases the heat exchange area in the latent heat area of the radiator heat exchanger to improve heat exchange efficiency. It is something that can be done.
実施例
以下、本発明の一実施例について第1図を参照しながら
説明する。なお、従来と同一部分については同一符号を
付けて詳細な説明は省略する。EXAMPLE Hereinafter, an example of the present invention will be described with reference to FIG. It should be noted that the same parts as in the prior art are given the same reference numerals and detailed explanations will be omitted.
図に示すように、上部ヘッダー1に接続されるガス管5
と、下部ヘッダー2に接続される液戻り管6に接続され
る気液分離器13の内部に加熱器4の排気を行う排気管
14の一部を導きいれて熱媒を加熱する気化促進器15
を構成したものである。Gas pipe 5 connected to the upper header 1 as shown in the figure
and a vaporization promoter that heats the heat medium by introducing a part of the exhaust pipe 14 that exhausts the heater 4 into the gas-liquid separator 13 that is connected to the liquid return pipe 6 that is connected to the lower header 2. 15
It is composed of
上記構成において、加熱器4内で加熱された蒸発性潜熱
媒体11は熱交換器3内で蒸発し、気液二相状態になっ
て上部ヘッダー管1および、ガス管5を通って気液分離
器13へ導入され、液分は液戻り管6を通って下部ヘッ
ダー2へ戻され、気化促進器15により加熱されて完全
にガス化された熱媒は往管9を通って放熱器8へ導かれ
凝縮し、復管lOを通って下部ヘッダー4へ重力作用に
より戻されるものである。In the above configuration, the evaporative latent heat medium 11 heated in the heater 4 evaporates in the heat exchanger 3, becomes a gas-liquid two-phase state, passes through the upper header pipe 1 and the gas pipe 5, and is separated into gas and liquid. The liquid is introduced into the vessel 13 and returned to the lower header 2 through the liquid return pipe 6, and the heat medium that has been completely gasified by being heated by the vaporization accelerator 15 passes through the outgoing pipe 9 to the radiator 8. It is guided, condensed and returned by gravity to the lower header 4 through the return pipe IO.
従って、気液分離器13から放熱器8へ流れる熱媒はガ
ス状態であり、放熱器8へ液状態の余分な熱媒が送られ
放熱器8への熱媒の偏在が防止させる。この結果、加熱
器4の液切れによる過熱が起こり難くなり、更に放熱器
8の熱交換効率も向上する。また気化促進器15で排熱
回収を行うことにより、システム効率も向上する。Therefore, the heat medium flowing from the gas-liquid separator 13 to the radiator 8 is in a gas state, and excess heat medium in a liquid state is sent to the radiator 8, thereby preventing uneven distribution of the heat medium in the radiator 8. As a result, overheating due to liquid shortage in the heater 4 is less likely to occur, and the heat exchange efficiency of the radiator 8 is also improved. Furthermore, by recovering exhaust heat using the vaporization accelerator 15, system efficiency is also improved.
なお、他の実施例として、気化促進器の熱源に電気ヒー
タ等を利用した構成も考えられる。In addition, as another embodiment, a configuration in which an electric heater or the like is used as the heat source of the vaporization accelerator can also be considered.
発明の効果
以上の実施例から明らかなように、本発明の熱搬送装置
によれば気液分離器に気化促進器を設けているので、気
液分離器の性能が向上し、冷媒の分布が放熱器に偏らず
、加熱器の異常過熱や系の圧力上昇が防止されることの
できる熱搬送装置を提供できる。Effects of the Invention As is clear from the above embodiments, according to the heat transfer device of the present invention, the gas-liquid separator is provided with a vaporization accelerator, so the performance of the gas-liquid separator is improved and the refrigerant distribution is improved. It is possible to provide a heat transfer device that can prevent abnormal overheating of the heater and pressure increase in the system without relying on the radiator.
また、気液分離器の気化促進器の熱源に、排気からの排
熱を利用した構成においては、システム効率が向上する
ものである。Further, in a configuration in which exhaust heat from exhaust gas is used as a heat source for a vaporization accelerator of a gas-liquid separator, system efficiency is improved.
第1図は本発明の一実施例における熱搬送装置の構成国
、第2図は従来の熱搬送装置の構成国である。
1・・・・・・上部ヘッダー、2・・・・・・下部ヘッ
ダー、3・・・・・・熱交換器、4・・・・・・加熱器
、5・・・・・・ガス管、6・・・・・・液戻り管、1
1・・・・・・熱媒、13・・・・・・気液分離器、1
4・・・・・・排気管、15・・・・・・気化促進器。FIG. 1 shows the constituent countries of a heat transfer device according to an embodiment of the present invention, and FIG. 2 shows the constituent countries of a conventional heat transfer device. 1... Upper header, 2... Lower header, 3... Heat exchanger, 4... Heater, 5... Gas pipe , 6...Liquid return pipe, 1
1... Heat medium, 13... Gas-liquid separator, 1
4... Exhaust pipe, 15... Vaporization accelerator.
Claims (2)
器により構成される加熱器と、前記上部ヘッダーにガス
管によって接続されるとともに底部から液戻り管によっ
て下部ヘッダーに接続された気液分離器と、前記加熱器
の上方に設けられる放熱器と、前記気液分離器と前記放
熱器とを接続する往管と、前記下部ヘッダーと前記放熱
器を接続する復管からなり、内部に蒸発性の熱媒を封入
した密閉回路を備え、前記気液分離器に熱媒を加熱する
気化促進器を設けた熱搬送装置。(1) A heater composed of a heat exchanger that connects the upper header and the lower header, and a gas-liquid separator that is connected to the upper header by a gas pipe and from the bottom to the lower header by a liquid return pipe. and a radiator provided above the heater, an outgoing pipe connecting the gas-liquid separator and the radiator, and a return pipe connecting the lower header and the radiator, and an evaporative pipe inside. 1. A heat transfer device comprising a sealed circuit in which a heating medium is enclosed, and a vaporization accelerator for heating the heating medium is provided in the gas-liquid separator.
源からの廃熱を用いて熱媒を加熱する気化促進器を有す
る気液分離器を備えた請求項(1)記載の熱搬送装置。(2) The heat transfer according to claim (1), further comprising a gas-liquid separator having a vaporization accelerator that heats a heat medium using waste heat from a heat source that heats the heater as a heat source of the vaporization accelerator. Device.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5827490A JPH03260593A (en) | 1990-03-09 | 1990-03-09 | Heat feed apparatus |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5827490A JPH03260593A (en) | 1990-03-09 | 1990-03-09 | Heat feed apparatus |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH03260593A true JPH03260593A (en) | 1991-11-20 |
Family
ID=13079611
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP5827490A Pending JPH03260593A (en) | 1990-03-09 | 1990-03-09 | Heat feed apparatus |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH03260593A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2016059799A1 (en) * | 2014-10-17 | 2016-04-21 | Necプラットフォームズ株式会社 | Cooling system and electronic device |
-
1990
- 1990-03-09 JP JP5827490A patent/JPH03260593A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2016059799A1 (en) * | 2014-10-17 | 2016-04-21 | Necプラットフォームズ株式会社 | Cooling system and electronic device |
JPWO2016059799A1 (en) * | 2014-10-17 | 2017-07-06 | Necプラットフォームズ株式会社 | Cooling system and electronic device |
US10203163B2 (en) | 2014-10-17 | 2019-02-12 | Nec Platforms, Ltd | Cooling system and electronic device |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
WO1999032841A2 (en) | Liquid desiccant dehumidifier and air conditioner | |
JP2006284144A (en) | Exhaust heat recovery device | |
US6820440B2 (en) | Absorption-type air conditioner core structure | |
JPH03260593A (en) | Heat feed apparatus | |
JP2004349551A (en) | Boiling cooling system | |
US5027616A (en) | Air-cooled absorption type cooling and heating apparatus | |
JP2548380B2 (en) | Heat exchanger | |
JPS5864486A (en) | Heat exchanger | |
JP2652416B2 (en) | Latent heat recovery unit | |
JPS6222779Y2 (en) | ||
JP2004116964A (en) | Solar heat collector tube and water heater using the same | |
KR0139349Y1 (en) | Circulation of condensed water of evaporator for absorption type refrigerator | |
JPH0726793B2 (en) | Cold plate | |
KR100286833B1 (en) | Heat exchanger for regenerator of cool/heating system | |
JP3021860B2 (en) | Heat exchanger | |
JPH0645171Y2 (en) | Heat pipe heat exchanger | |
JPS6115990B2 (en) | ||
JPH0718596B2 (en) | Heat exchanger | |
JP2861544B2 (en) | Heat exchanger | |
JPH0678860B2 (en) | Absorption heat pump type heat storage device | |
JPS5974493A (en) | Heat accumulator utilizing solar heat | |
JPH0697127B2 (en) | Air-cooled absorption heat pump | |
JP2000018760A (en) | Method for operating absorption heat pump | |
JPH05118778A (en) | Heat exchanger | |
JPH07208826A (en) | Air conditioner |