JPS5920957B2 - Heat exchanger - Google Patents

Heat exchanger

Info

Publication number
JPS5920957B2
JPS5920957B2 JP13241380A JP13241380A JPS5920957B2 JP S5920957 B2 JPS5920957 B2 JP S5920957B2 JP 13241380 A JP13241380 A JP 13241380A JP 13241380 A JP13241380 A JP 13241380A JP S5920957 B2 JPS5920957 B2 JP S5920957B2
Authority
JP
Japan
Prior art keywords
heat exchanger
mist
heat exchange
heat
tube
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.)
Expired
Application number
JP13241380A
Other languages
Japanese (ja)
Other versions
JPS5758083A (en
Inventor
平吉 桑原
茂樹 平沢
恒 中山
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
National Institute of Advanced Industrial Science and Technology AIST
Original Assignee
Agency of Industrial Science and Technology
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 Agency of Industrial Science and Technology filed Critical Agency of Industrial Science and Technology
Priority to JP13241380A priority Critical patent/JPS5920957B2/en
Publication of JPS5758083A publication Critical patent/JPS5758083A/en
Publication of JPS5920957B2 publication Critical patent/JPS5920957B2/en
Expired legal-status Critical Current

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

Description

【発明の詳細な説明】 本発明は、ミストを含んだ気流と、この気流と温度差を
もった熱媒体とを熱交換するものとくに管内熱媒体が凝
縮する各種凝縮器、地熱発電プラント用凝縮器として好
適な熱交換器に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to various types of condensers that exchange heat between an air flow containing mist and a heat medium having a temperature difference with this air flow, particularly various condensers in which a heat medium in a pipe is condensed, and a condenser for geothermal power generation plants. The present invention relates to a heat exchanger suitable as a heat exchanger.

従来のミスト気流冷却式熱交換器は、ミスト気流通路中
に伝熱管(平滑管・・イフイン管)を千鳥状に配置し、
伝熱管の上流部にノズルを、上流あるいは下流部に送風
機に配置した構造のものである。
Conventional mist airflow cooling type heat exchangers have heat transfer tubes (smooth tubes, even tubes) arranged in a staggered manner in the mist airflow path.
It has a structure in which a nozzle is placed upstream of the heat transfer tube and a blower is placed upstream or downstream.

送風機によってミスト気流通路内に空気の流れを生じさ
せる一方ノズルから水を空気の流れ中に噴射してやりミ
スト気流とし、このミスト気流と伝熱管内を通る冷媒蒸
気を凝縮させる。
While the blower generates a flow of air in the mist airflow passage, water is injected into the airflow from a nozzle to form a mist airflow, and this mist airflow and the refrigerant vapor passing through the heat transfer tube are condensed.

このような熱交換器においては、ノズルからのミストが
衝突するのは最上流側(第1夕1泪)の伝熱管、第2列
目の伝熱管程度までであって第3列目から下流の管列に
はミストがほとんど衝突しない。
In such a heat exchanger, the mist from the nozzle collides with the most upstream heat exchanger tube (1st column), up to the second row of heat exchanger tubes, and from the third row downstream. The mist hardly collides with the tube rows.

従って下流側の伝熱管は、下流になるにともなって乾き
面が広くなり、伝熱性能が低下する。
Therefore, the dry surface of the downstream heat transfer tube becomes wider as it moves downstream, and the heat transfer performance deteriorates.

本発明の目的は、伝熱性能が高くかつミストが熱交換器
の外部に排出されない熱交換器を提供することにある。
An object of the present invention is to provide a heat exchanger that has high heat transfer performance and prevents mist from being discharged to the outside of the heat exchanger.

本発明の特徴は、ミスト気流通路の上流側にミスト伸長
手段を有するミスト熱交換方式の伝熱管を配置し、下流
側に、バイフィン管からなる強制対流熱交換方式の伝熱
管を配置したことにある。
The feature of the present invention is that a mist heat exchange type heat exchanger tube having a mist extension means is arranged on the upstream side of the mist airflow passage, and a forced convection heat exchange type heat exchanger tube consisting of a bifin tube is arranged on the downstream side. be.

以下本発明の実施例を第1図〜第3図により説明する。Embodiments of the present invention will be described below with reference to FIGS. 1 to 3.

第1図および第2図は第1の実施例を示すものである。1 and 2 show a first embodiment.

゛入口1.出口2および水受は部3を有するケー
ス4内には、伝熱管群5,6が配置されている。
゛Entrance 1. In a case 4 having an outlet 2 and a water receiver 3, heat transfer tube groups 5 and 6 are arranged.

伝熱管群5は、ミスト熱交換方式の伝熱管で、細かい溝
を有するフィンを設けた伝熱管である。
The heat exchanger tube group 5 is a mist heat exchange type heat exchanger tube, and is a heat exchanger tube provided with fins having fine grooves.

細かい溝をもったフィン付伝熱管のほか、伝熱管の表面
に濡れ性を高めるためのミスト伸長手段たとえば細かい
溝、おうとつを設けたものでよい。
In addition to a finned heat exchanger tube with fine grooves, a heat exchanger tube with mist extending means such as fine grooves or holes provided on the surface of the heat exchanger tube to improve wettability may be used.

伝熱管群6は、強制対流熱交換方式の伝熱管で伝熱管群
5の下流側に配置され、この管群6としては、パイフィ
ン管が用いられている。
The heat exchanger tube group 6 is a forced convection heat exchange type heat exchanger tube and is arranged on the downstream side of the heat exchanger tube group 5, and a pie fin tube is used as the tube group 6.

ノズル7は入口10部分に配置され伝熱管群5に向って
水を噴射する。
The nozzle 7 is arranged at the inlet 10 and injects water toward the heat exchanger tube group 5.

ノズル7には、配管7aとポンプ9が連結され、水受は
部3の水を圧送する。
A pipe 7a and a pump 9 are connected to the nozzle 7, and the water receiver pumps water from the section 3.

水受は部3の水量が少なくなったときは別途補給される
The water receiver is separately replenished when the amount of water in section 3 becomes low.

送風機8は出口2(あるいは伝熱管群5の上流側)に設
置され、入口1から出口2へ向かう空気の流れを生じさ
せる。
The blower 8 is installed at the outlet 2 (or on the upstream side of the heat exchanger tube group 5) and generates a flow of air from the inlet 1 toward the outlet 2.

次に本実施例の動作を説明する。Next, the operation of this embodiment will be explained.

伝熱管群5,6内は、冷媒蒸気などの熱媒体が流れ、管
外を気流が入口1から出口2に向って流れる。
A heat medium such as refrigerant vapor flows inside the heat transfer tube groups 5 and 6, and an air current flows outside the tubes from the inlet 1 toward the outlet 2.

気流は送風機8によって起こされる。ノズル7からは水
が噴射され、気流中にミストとなって混合して伝熱管群
5に流入する。
The airflow is generated by a blower 8. Water is injected from the nozzle 7, becomes mist in the airflow, mixes, and flows into the heat exchanger tube group 5.

ミストは伝熱管群5(伝熱管とフィン)の表面を漏らし
、冷却性能を高める。
The mist leaks from the surface of the heat exchanger tube group 5 (heat exchanger tubes and fins) to improve cooling performance.

伝熱管群6にはミストが達しない場合が多いけれど、気
流によって強制冷却される。
Although the mist often does not reach the heat exchanger tube group 6, it is forcibly cooled by the airflow.

そして熱媒体は、管群5,6から出るころにはそのほと
んどが凝縮している。
By the time the heat medium leaves the tube groups 5 and 6, most of it has been condensed.

第3図は本発明の第2の実施例を示すものである。FIG. 3 shows a second embodiment of the invention.

ミスト熱交換方式の伝熱管5が上流側、強制熱交換方式
の伝熱管群6が下流側にそれぞれ配置されていることは
第1の実施例と同じである。
As in the first embodiment, the mist heat exchange type heat exchanger tubes 5 are arranged on the upstream side, and the forced heat exchange type heat exchanger tube group 6 is arranged on the downstream side.

この実施例は、上方側の伝熱管は乾きやすいのでミスト
熱交換方式の伝熱管群5の上方側の部分を強制対流熱交
換方式の伝熱管9に置き換えたものである。
In this embodiment, the upper part of the heat exchanger tube group 5 of the mist heat exchange type is replaced with a heat exchanger tube 9 of the forced convection heat exchange type, since the upper heat exchanger tubes tend to dry out easily.

各伝熱管9は伝熱管群6と同じ構成である。Each heat exchanger tube 9 has the same configuration as the heat exchanger tube group 6.

以上のように、本発明は、ミスト気流が流れる上流側に
、ミスト伸長手段を有する伝熱管を配置したのでこの領
域の熱交換部では、ミストによる冷却効果を充分に発揮
させることができるとともに、この領域には強制対流熱
交換方式の伝熱管よりも伝熱面積の小さいものを配置可
能となる。
As described above, in the present invention, since the heat exchanger tube having the mist extension means is arranged on the upstream side through which the mist airflow flows, the cooling effect of the mist can be sufficiently exerted in the heat exchange section in this area, and In this region, it is possible to arrange a tube with a smaller heat transfer area than a forced convection heat exchange type heat transfer tube.

このことによって、ミスト熱交換方式の熱交換部では、
強制対流方式の熱交換部よりも伝熱管を密に配置でき単
位面積当りの熱交換熱量は増大する。
As a result, in the heat exchange section of the mist heat exchange method,
The heat exchanger tubes can be arranged more densely than in a forced convection type heat exchange section, and the amount of heat exchanged per unit area increases.

また、気流中のミスト量が少ない下流側に大きな伝熱面
積をもった・・イフイン管を配置しているので所望の冷
却効果を確保できるとともに、・・イフイン管は、気流
との接触面積が大きいので、気流中のミストを捕集もよ
くなり、ミストが熱交換器の外部に放出されることがな
くなる。
In addition, by placing the IF-IN tube with a large heat transfer area on the downstream side where the amount of mist in the airflow is small, it is possible to secure the desired cooling effect. Since it is large, the mist in the airflow can be captured well, and the mist will not be released to the outside of the heat exchanger.

このように全体として効率的な熱交換を可能にし、高い
性能をもった熱交換器を提供できる。
In this way, efficient heat exchange is possible as a whole, and a heat exchanger with high performance can be provided.

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

第1図は本発明の第1の実施例の正面断面図、第2図は
第1図の要部詳細図、第3図は第2の実施例を示す要部
詳細図である。 1・・・入口、2・・・出口、3・・・水受は部、4・
・・ケース、5・・・ミスト熱交換方式の伝熱管、6,
9・・・強制対流方式の伝熱管、1・・・ノズル、8・
・・送風機。
FIG. 1 is a front sectional view of a first embodiment of the present invention, FIG. 2 is a detailed view of the main part of FIG. 1, and FIG. 3 is a detailed view of the main part of the second embodiment. 1...Inlet, 2...Outlet, 3...Water tray, 4...
...Case, 5...Mist heat exchange type heat exchanger tube, 6,
9... Forced convection heat transfer tube, 1... Nozzle, 8...
··Blower.

Claims (1)

【特許請求の範囲】[Claims] 1 管内を流れるミスト気流と管内を流れる熱媒体とを
熱交換するミスト熱交換方式の熱交換部と、管外を流れ
る気流と管内を流れる熱媒体とを熱交換する強制対流方
式の熱交換部とを備え、気流通路の上流側にミスト熱交
換方式の熱交換部を、下流側に強制対流方式の熱交換部
を配置したものにおいて、ミスト熱交換方式の熱交換部
には、ミスト伸長手段を備えた伝熱管を配置し、強制対
流方式の熱交換部には、・・イフインを有する・・イフ
イン管を配置したことを特徴とする熱交換器。
1 A heat exchange section using a mist heat exchange method that exchanges heat between the mist airflow flowing inside the tube and a heat medium flowing inside the tube, and a heat exchange section using a forced convection method that exchanges heat between the air flow flowing outside the tube and the heat medium flowing inside the tube. A mist heat exchange type heat exchange part is arranged on the upstream side of the airflow passage, and a forced convection type heat exchange part is arranged on the downstream side of the airflow passage, wherein the mist heat exchange type heat exchange part has a mist extension means. 1. A heat exchanger characterized in that a heat exchanger tube having a heat exchanger is disposed, and a forced convection type heat exchange section is disposed with an equalizer tube having an equalizer.
JP13241380A 1980-09-25 1980-09-25 Heat exchanger Expired JPS5920957B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13241380A JPS5920957B2 (en) 1980-09-25 1980-09-25 Heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13241380A JPS5920957B2 (en) 1980-09-25 1980-09-25 Heat exchanger

Publications (2)

Publication Number Publication Date
JPS5758083A JPS5758083A (en) 1982-04-07
JPS5920957B2 true JPS5920957B2 (en) 1984-05-16

Family

ID=15080799

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13241380A Expired JPS5920957B2 (en) 1980-09-25 1980-09-25 Heat exchanger

Country Status (1)

Country Link
JP (1) JPS5920957B2 (en)

Also Published As

Publication number Publication date
JPS5758083A (en) 1982-04-07

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