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JPS5875689A - Heat exchanger for cooling mist - Google Patents

Heat exchanger for cooling mist

Info

Publication number
JPS5875689A
JPS5875689A JP17214481A JP17214481A JPS5875689A JP S5875689 A JPS5875689 A JP S5875689A JP 17214481 A JP17214481 A JP 17214481A JP 17214481 A JP17214481 A JP 17214481A JP S5875689 A JPS5875689 A JP S5875689A
Authority
JP
Japan
Prior art keywords
mist
heat
pipes
transmitting
group
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
JP17214481A
Other languages
Japanese (ja)
Other versions
JPS5925149B2 (en
Inventor
Heikichi Kuwabara
桑原 平吉
Shigeki Hirasawa
茂樹 平沢
Hisashi Nakayama
中山 恒
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 JP17214481A priority Critical patent/JPS5925149B2/en
Publication of JPS5875689A publication Critical patent/JPS5875689A/en
Publication of JPS5925149B2 publication Critical patent/JPS5925149B2/en
Expired legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D5/00Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, using the cooling effect of natural or forced evaporation
    • F28D5/02Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, using the cooling effect of natural or forced evaporation in which the evaporating medium flows in a continuous film or trickles freely over the conduits

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

PURPOSE:To secure a high heat-transmitting efficiency and contrive to reduce pump power required, by a method wherein grooved finned pipes suitable for a large mist amount are provided on the upstream side of a group of heat-transmitting pipe through which a heat-transmitting medium exchanging heat with a flow of a mist is passed, and grooved pipes suitable for a small mist amount are provided on the downstream side of the group of the heat-transmitting pipes. CONSTITUTION:The heat-transmitting medium such as the vapor of a refrigerant flows through each of the pipes in heat-transmitting pipe groups 5, 6, while gas flow is passed in the exterior of the pipes from inlets 1 toward an outlet 2 as indicated by arrows. The gas flow is generated by a blower 12, water is sprayed from nozzles 9 to be mixed into the gas flows as a mist, and the mist-containing gas flow is directed to the pipe group 5. A large amount of the mist collides with the grooved finned pipes 7 in the pipe group 5 located on the upstream side with respect to the gas flow, and wets the fin surfaces of the finned pipes 7 to enhance cooling efficiency. On the other hand, a small amount of the mist reaches the grooved pipes 8 in the pipe group 6 located on the downstream side with respect the gas flow, and wets the surfaces of the heat-transmitting pipes to enhance the cooling efficiency through evaporation of water films. Most of the mist in the gas flow is condensed by the time the heat-transmitting medium flow out from the pipe groups 5, 6.

Description

【発明の詳細な説明】 本発明は管外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冷却熱交換器、特に・U内熱媒体
が凝縮する各種凝縮器、地熱発電プラント用#縮器とし
て好適なミスト冷却熱交換器に関する。従来のこの種ミ
スト冷却熱交換器は、ミスト気流通路中に平滑管あるい
はフィン管などの伝熱管を格子状あるいは千鳥状に配置
し、上流部にミストを生成する噴霧ノズルを、上流ある
いは下流部に送風機を配置した構造のものである。
Detailed Description of the Invention The present invention relates to a mist cooling heat exchanger that exchanges heat between a mist airflow flowing outside the tube and a heat medium flowing inside the tube, particularly various condensers in which the heat medium inside the U is condensed, and for use in geothermal power generation plants. #Relating to a mist cooling heat exchanger suitable as a condenser. Conventional mist cooling heat exchangers of this type have heat transfer tubes such as smooth tubes or finned tubes arranged in a grid or staggered pattern in the mist air flow passage, and spray nozzles that generate mist are placed in the upstream or downstream portion. It has a structure in which a blower is installed.

ミスト冷却方式は、噴精したミスト水を伝熱管の表面に
衝突させ、水膜の蒸発を促進させることにより、冷却性
能の向上を図るものである。したがって、平滑管、フィ
ン管の濡れ性を促がすために、−up面やフィン側面に
微細な溝を付けることにより、溝内の水の毛細・u力を
利用して、伝熱管に摘果された水膜を伝熱面上に広げて
、濡れ性を良くシ、冷却性能を向上させている。
The mist cooling method aims to improve cooling performance by colliding ejected mist water with the surface of the heat transfer tube to promote evaporation of the water film. Therefore, in order to promote the wettability of smooth tubes and finned tubes, by forming fine grooves on the -up surface and the fin side surfaces, the capillary and u-force of water in the grooves can be used to thin the heat exchanger tubes. The resulting water film is spread over the heat transfer surface to improve wettability and improve cooling performance.

このような従来技術の熱交換器においては、ノズルで生
成されたミストが衝突するのは、最上流側(第1列目)
の伝熱管、第2列目の伝熱管程度までであって、第3列
目から下流側の後方列の伝熱管へはミストの到達量は減
する。従って、後方列の伝熱管は、下流になるにともな
って伝熱表面上に水膜が存在しない乾き面が広がシ、冷
却性能が低下する。
In such a conventional heat exchanger, the mist generated by the nozzle collides with the most upstream side (first row).
The amount of mist reaching the heat exchanger tubes in the rear row downstream from the third row is reduced. Therefore, as the heat transfer tubes in the rear row move downstream, the dry surface on which no water film exists spreads on the heat transfer surface, and the cooling performance deteriorates.

本発明の目的は、上記の従来技術の問題点に鑑み、伝熱
性能の高いミスト冷却熱交換器を提供するごとにある。
SUMMARY OF THE INVENTION An object of the present invention is to provide a mist cooling heat exchanger with high heat transfer performance in view of the problems of the prior art described above.

本発明は伝熱前群のうちミスト上流側に多量のミスト水
が存在す。れば伝熱表面の濡れ性が良くなり、かつ濡れ
面積が広い伝熱管を配列し、下流側に微量なミスト水の
存在でもあるいはミストが殆んど到達しなくても伝熱表
面の鏑れ性が良い伝熱前を配列させ高性能熱交換器を得
るものでおる。
In the present invention, a large amount of mist water exists on the upstream side of the mist in the pre-heat transfer group. This will improve the wettability of the heat transfer surface, and by arranging heat transfer tubes with a wide wetted area, the heat transfer surface will not be chipped even if there is a small amount of mist water on the downstream side or even if the mist hardly reaches the downstream side. A high-performance heat exchanger can be obtained by arranging the heat transfer front with good heat transfer properties.

本発明において円管に溝を付けた溝付官は、比較的深い
溝を付けることが1丁能であるから、微量なミストiで
伝熱表面全域を濡らすことができる。
In the present invention, the groover for forming grooves on the circular tube is capable of forming relatively deep grooves, so that the entire heat transfer surface can be wetted with a small amount of mist i.

そしてフィンがないため、電ピッチを狭くして、多くの
伝熱管を配列できる。また、フィン側面に溝を付は丸溝
付レイン管はフィンに溝を設けるため深い溝は付けられ
ないが、多量のミスitが傭j突する場合は、フィン側
面が良く濡れ、伝熱面積が内宮に比べて膨大に大きくな
るため、高い冷却性能が保たれる。
Since there are no fins, the electric pitch can be narrowed and many heat transfer tubes can be arranged. In addition, with round grooved rain pipes, deep grooves cannot be made because the fins have grooves, but if there is a large amount of misalignment, the fin sides will be well wetted and the heat transfer area will be reduced. Because it is vastly larger than the inner shrine, high cooling performance is maintained.

このような高性能伝熱管を組み合せた管吐、博造として
、本発明の実施例を第1図〜第6図に示す。
Embodiments of the present invention are shown in FIGS. 1 to 6 as tubes and pipes that combine such high-performance heat exchanger tubes.

第1図および第2図は第1の実@列を示すものである。1 and 2 show the first real @ column.

入口1、出口2および水受は部3を有するダクト4内に
は、上流側伝熱・U群5と下流側伝熱管群6が配置され
ている。伝熱管群5は比較的多電のミスト電の場合によ
く藺れる溝付フィン管7である。伝熱前群6は少量のミ
スitでもよく藺れる溝付管8である。
In a duct 4 having an inlet 1, an outlet 2, and a water receiver 3, an upstream heat transfer/U group 5 and a downstream heat transfer tube group 6 are arranged. The heat exchanger tube group 5 is a grooved fin tube 7 which is often used in the case of a mist electric current with a relatively large number of electric currents. The heat transfer front group 6 is a grooved tube 8 that can be easily detected even by a small amount of mistake.

ノズル9はダクト4の入口1の部分に配置され、伝熱管
′Insに向って水を噴射する。
The nozzle 9 is arranged at the inlet 1 of the duct 4 and injects water toward the heat exchanger tube 'Ins.

ノズル9には、配−gloとポンプ11が連結され、水
受は部3の水を圧送する。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。
A glo and a pump 11 are connected to the nozzle 9, and the water receiver pumps water from the section 3. The water receiver is separately replenished when the amount of water in section 3 becomes low.

送風機12はダクト4の出口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
流れ金生じさせる。
The blower 12 is installed at the outlet 2 of the duct 4 (or on the upstream side of the heat exchanger tube group 5), and causes air to flow from the inlet 1 to the outlet 2.

次に本実施列の動作を説明する。伝熱・9群5゜6内は
、冷媒蒸気などの熱媒体が流れ、営外を気流が矢印に示
すように入口lから出口2に向って流れる。気流は送風
機12によって起こされる。
Next, the operation of this embodiment will be explained. Heat transfer: Inside the 9th group 5°6, a heat medium such as refrigerant vapor flows, and airflow outside the building flows from the inlet 1 to the outlet 2 as shown by the arrow. The airflow is generated by a blower 12.

ノズル9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・9群5に流入する。
Water is injected from the nozzle 9, becomes mist in the airflow, mixes, and flows into the heat transfer/9 group 5.

ミストは気流の上流側に位置する伝熱管群5の溝付フィ
ン管7の菅フィン表面を濡らし、冷却性へ 能を高める。また気流の下流側に位置する伝熱前群6の
溝付f8にはミストが少菫到達し、伝pA官六面が濡れ
て、水膜の蒸発によシ冷却性能を旨める。気流中に混合
しているミストは熱媒体が伝熱−rit群5.6から出
るころには、そのほとんどが凝縮している。
The mist wets the surface of the tube fins of the grooved fin tubes 7 of the heat transfer tube group 5 located on the upstream side of the airflow, thereby improving cooling performance. In addition, a small amount of mist reaches the grooved f8 of the heat transfer front group 6 located on the downstream side of the airflow, wets the transfer pA 6 surface, and improves the cooling performance by evaporation of the water film. Most of the mist mixed in the airflow has been condensed by the time the heat medium leaves the heat transfer rit group 5.6.

第3図は本−A明の第2の実、頬列全示すものである。Figure 3 shows the second fruit of Hon-A Ming, which shows the whole row of cheeks.

上流側の伝熱f群5に捕捉されたミストは、ミスト気流
が速い速度になると上流側の下段の伝熱・U上に落下す
るのではなく、下流側の伝熱・ぎ群6の下段の伝熱前へ
落下する。したがってこの部分の伝熱aへもミス)it
が多くなる。このときは下流側の伝熱管群6の下方の伝
熱管にも上fi 114!Iの伝熱ぽ群5と同泳な溝付
フィン管7を配置する。
When the mist air flow reaches a high speed, the mist captured by the upstream heat transfer group 5 does not fall onto the lower stage of the heat transfer group 6 on the downstream side, but instead falls onto the lower stage of the heat transfer group 6 on the downstream side. falls before the heat transfer. Therefore, there is also a mistake in heat transfer a in this part)
will increase. At this time, upper fi 114 is also applied to the lower heat exchanger tubes of the downstream heat exchanger tube group 6! A grooved fin tube 7 that swims with the heat transfer port group 5 of I is arranged.

第4図は本発明の第3の実1列を示すもので必る。この
実施列は伝FA営群5.6の後方に強制空冷に有効な伝
熱管で構成した伝熱前群13を配列するものである。こ
の部分にはミストがほとんどとんでとないので平滑ハイ
フィン管14などを配置して、冷却性能を尚め、スペー
スの有効利用を図るとともに、ミストの噴霧をやめて、
この熱交換器を章なる空気冷却のみに利用する時に、こ
の伝熱管群13は冷却性能を高めるのに有利となる。
FIG. 4 shows the third real row of the present invention. In this implementation row, a heat transfer front group 13 made up of heat transfer tubes effective for forced air cooling is arranged behind the FA group 5.6. Since there is almost no mist in this area, we installed a smooth high-fin pipe 14 to improve the cooling performance and make effective use of the space, as well as stop spraying the mist.
When this heat exchanger is used only for cooling air, this heat transfer tube group 13 is advantageous in improving cooling performance.

第5図は本発明の第4の実施例を示すものである。この
例は第3図に示す第2の実施例と第4図に示す第3の実
施例を併用したものであり、このようにすると、第4図
に示すクリにおいて、さらに冷却性能を同上することが
できる。
FIG. 5 shows a fourth embodiment of the invention. This example is a combination of the second embodiment shown in FIG. 3 and the third embodiment shown in FIG. be able to.

第6図は本発明のJ5の実施例を示すものである。この
列は第4図に示す第3の実施列において、最俊方側に配
置した平滑ハイフィン1t14からなる強制空冷用の伝
熱管群13をダクト4の入口1のノズル9前方に設置し
たものである。送風機によって入口1に導びかれた気流
は各列の伝熱管と熱交換して順次温度が^まる。そのと
き、単なる空気流によってのみ冷却する場合には、伝熱
管の表面温度と′3A流の温度との諷度差が大きいほど
よいので、第6図のようにすると冷却性能が向上する。
FIG. 6 shows an embodiment of J5 of the present invention. This row is the third implementation row shown in FIG. 4, in which a heat transfer tube group 13 for forced air cooling consisting of smooth high fins 1t14 placed on the most agile side is installed in front of the nozzle 9 at the entrance 1 of the duct 4. be. The airflow guided to the inlet 1 by the blower exchanges heat with the heat exchanger tubes in each row, and its temperature is sequentially lowered. At that time, when cooling is performed only by a simple air flow, the larger the difference in the difference between the surface temperature of the heat exchanger tube and the temperature of the '3A flow, the better, so the cooling performance is improved by doing as shown in FIG. 6.

なお、上記第1図〜第6図に示した実施例において、各
々独立の特徴を有する伝熱管の列数は図示したものに限
ることはなく、ノズルから噴霧するミスト童、伝熱管の
温度、熱交換器、および伝熱管の配列ピッチなどにより
適宜決足されるもの下ある。
In the embodiments shown in FIGS. 1 to 6 above, the number of rows of heat exchanger tubes, each having independent characteristics, is not limited to what is shown in the figures, and the number of rows of heat exchanger tubes that are sprayed from the nozzle, the temperature of the heat exchanger tubes, It is decided as appropriate depending on the arrangement pitch of the heat exchanger and heat transfer tubes, etc.

以上説明したように、本発明によれば高い伝熱性能を有
する熱交換器を得ることができ、また、ミスト水の蒸発
伝熱の促進により、ミスト・水の循環ポンプの動力の低
減を図ることができる。
As explained above, according to the present invention, a heat exchanger with high heat transfer performance can be obtained, and the power of the mist/water circulation pump can be reduced by promoting evaporative heat transfer of mist water. be able to.

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

第1図は本発明のミスト冷却熱交換器の第1の実施例を
示す正面断面図、第2図は第1図の安部拡大断1目図、
第3図〜第6図は本発明のミスト冷、即熱交換器の他の
実施列を示す要部拡大断面図である。 1・・・入口、2・・・出口、3・・・水受は部、4・
・・ダクト、5.6.13・・・伝熱管群、7・・・溝
付フィン管、8・・・溝付管、14・・・平滑ハイフィ
ン官、9・・・ノズル。 特許出願人 エ菓技術院長 石板誠− 第 1 図 、fl z 図 第 3 図
FIG. 1 is a front sectional view showing a first embodiment of the mist cooling heat exchanger of the present invention, FIG. 2 is an enlarged first section view of the lower part of FIG. 1,
FIGS. 3 to 6 are enlarged sectional views of main parts showing other embodiments of the mist cooling and instant heat exchanger of the present invention. 1...Inlet, 2...Outlet, 3...Water tray, 4...
...Duct, 5.6.13... Heat exchanger tube group, 7... Grooved fin tube, 8... Grooved tube, 14... Smooth high fin tube, 9... Nozzle. Patent applicant: Makoto Ishiita, director of Eka Institute of Technology - Fig. 1, fl z Fig. 3

Claims (1)

【特許請求の範囲】[Claims] 1、管外に冷却用気流に微細な水滴を含んだミスト気流
を流し、11内を九れる熱媒体と熱交換するミスト冷却
熱交換器において、前記ミスト気流の上流側にフィンの
少なくとも一万の面に微細な溝を付けた溝付フィン管か
らなる伝熱官群を配置し、下流側に管表面に微細なlI
Iを設けた溝付管からなる伝熱管群を配置したことを特
徴とするミスト冷却熱交換器。
1. In a mist cooling heat exchanger that flows a mist airflow containing fine water droplets in a cooling airflow outside the tube and exchanges heat with a heat medium flowing inside the tube, at least 10,000 fins are provided on the upstream side of the mist airflow. A group of heat transfer elements consisting of grooved fin tubes with fine grooves on the surface of the tube is arranged, and on the downstream side there is a
A mist cooling heat exchanger characterized in that a heat transfer tube group consisting of grooved tubes provided with I is arranged.
JP17214481A 1981-10-29 1981-10-29 mist cooling heat exchanger Expired JPS5925149B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17214481A JPS5925149B2 (en) 1981-10-29 1981-10-29 mist cooling heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17214481A JPS5925149B2 (en) 1981-10-29 1981-10-29 mist cooling heat exchanger

Publications (2)

Publication Number Publication Date
JPS5875689A true JPS5875689A (en) 1983-05-07
JPS5925149B2 JPS5925149B2 (en) 1984-06-14

Family

ID=15936371

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17214481A Expired JPS5925149B2 (en) 1981-10-29 1981-10-29 mist cooling heat exchanger

Country Status (1)

Country Link
JP (1) JPS5925149B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006105541A (en) * 2004-10-07 2006-04-20 Mitsubishi Heavy Ind Ltd Air conditioner and outdoor unit therefor

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006105541A (en) * 2004-10-07 2006-04-20 Mitsubishi Heavy Ind Ltd Air conditioner and outdoor unit therefor

Also Published As

Publication number Publication date
JPS5925149B2 (en) 1984-06-14

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