JPS5959680U - Separate type heat exchange equipment - Google Patents

Separate type heat exchange equipment

Info

Publication number
JPS5959680U
JPS5959680U JP15224182U JP15224182U JPS5959680U JP S5959680 U JPS5959680 U JP S5959680U JP 15224182 U JP15224182 U JP 15224182U JP 15224182 U JP15224182 U JP 15224182U JP S5959680 U JPS5959680 U JP S5959680U
Authority
JP
Japan
Prior art keywords
liquid
pipe
pump
tank
section
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.)
Granted
Application number
JP15224182U
Other languages
Japanese (ja)
Other versions
JPS6215660Y2 (en
Inventor
池野 健
郡山 日出夫
西山 哲司
二上 伸宏
Original Assignee
川崎製鉄株式会社
古河電気工業株式会社
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 川崎製鉄株式会社, 古河電気工業株式会社 filed Critical 川崎製鉄株式会社
Priority to JP15224182U priority Critical patent/JPS5959680U/en
Publication of JPS5959680U publication Critical patent/JPS5959680U/en
Application granted granted Critical
Publication of JPS6215660Y2 publication Critical patent/JPS6215660Y2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

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

第1図は従来のセパレート型熱交換装置の系統図、第2
図は本考案め実施例に係るセパレート型熱交換装置の系
統図である。 10・・・・・・受熱部、12・・・・・・蒸発管、1
4・・・・・・放熱部、16・・・・・・凝縮管、18
・・・・・・蒸気管、20・・・・・・液管、22・・
・・・・ポンプ、24・・・・・・液面レベル管、26
・・・・・・断熱材、36・!・・・・管路、38・・
・・・・弁、42・・・・・・制御器、44・・・・・
・タンク、46・・・・・・液面センサ。
Figure 1 is a system diagram of a conventional separate heat exchanger;
The figure is a system diagram of a separate type heat exchange device according to an embodiment of the present invention. 10... Heat receiving part, 12... Evaporation tube, 1
4... Heat dissipation section, 16... Condensing pipe, 18
...Steam pipe, 20...Liquid pipe, 22...
... Pump, 24 ... Liquid level pipe, 26
...Insulation material, 36.! ...Pipe line, 38...
...Valve, 42...Controller, 44...
・Tank, 46...Liquid level sensor.

Claims (1)

【実用新案登録請求の範囲】 放熱部と、液分配部と蒸気集合部との間に蒸発管が上下
方向に配列されてなる受熱部と、該受熱部の蒸気集合部
と前記放熱部の蒸気導入口とを一通する蒸気管と、前記
放熱部の凝縮液排出口と前記受熱部の液分配部とを連通
ずる液管と、この液、管の途中に設けられた液移送用の
ポンプと、該ポンプよりも上流側の液管の途中に該ポン
プと接近して配設されたタンクと、該タンクに設けられ
た液面センサと、前記ポンプを迂回して該ポンプ下流側
の液管と該タンクとを連通する管路と、該管路の途中に
設けられた流量調節用の弁と、前記液面センサからの信
号を受けて前記タンク内の液面レベルの変動幅h1が前
記蒸発管内の液面レベルの許容変動幅h2に対して下記
(1)式を満たすように前記弁の開度を調節する制御器
と、を備えてなるセパレート型熱交換装置。 h□≦−$−1×h2・・・・・・・・・(1)Sま ただしく1)式中S1は前記タンクの水平断面積であり
、S2は前記蒸発管の水平断面積の総和である。
[Claims for Utility Model Registration] A heat radiating section, a heat receiving section in which evaporation tubes are vertically arranged between a liquid distribution section and a vapor collecting section, a vapor collecting section of the heat receiving section, and steam of the heat radiating section. A steam pipe that communicates with the inlet, a liquid pipe that communicates the condensate discharge port of the heat radiating part with the liquid distribution part of the heat receiving part, and a pump for transferring the liquid provided in the middle of the pipe. , a tank disposed close to the pump in the middle of a liquid pipe on the upstream side of the pump, a liquid level sensor provided in the tank, and a liquid pipe bypassing the pump and downstream of the pump. A pipe line that communicates with the tank, a valve for adjusting the flow rate provided in the middle of the pipe line, and a signal from the liquid level sensor are received so that the range of fluctuation h1 of the liquid level in the tank is determined as described above. A separate heat exchange device comprising: a controller that adjusts the opening degree of the valve so as to satisfy the following formula (1) with respect to an allowable fluctuation range h2 of the liquid level in the evaporation tube. h□≦-$-1×h2 (1) S and especially 1) In the formula, S1 is the horizontal cross-sectional area of the tank, and S2 is the sum of the horizontal cross-sectional areas of the evaporation tubes. It is.
JP15224182U 1982-10-07 1982-10-07 Separate type heat exchange equipment Granted JPS5959680U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15224182U JPS5959680U (en) 1982-10-07 1982-10-07 Separate type heat exchange equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15224182U JPS5959680U (en) 1982-10-07 1982-10-07 Separate type heat exchange equipment

Publications (2)

Publication Number Publication Date
JPS5959680U true JPS5959680U (en) 1984-04-18
JPS6215660Y2 JPS6215660Y2 (en) 1987-04-21

Family

ID=30337144

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15224182U Granted JPS5959680U (en) 1982-10-07 1982-10-07 Separate type heat exchange equipment

Country Status (1)

Country Link
JP (1) JPS5959680U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2019017297A1 (en) * 2017-07-18 2019-01-24 日本電気株式会社 Phase change refrigerating device and phase change refrigerating method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2019017297A1 (en) * 2017-07-18 2019-01-24 日本電気株式会社 Phase change refrigerating device and phase change refrigerating method

Also Published As

Publication number Publication date
JPS6215660Y2 (en) 1987-04-21

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