JPS59191894A - Heat exchanger - Google Patents

Heat exchanger

Info

Publication number
JPS59191894A
JPS59191894A JP6531483A JP6531483A JPS59191894A JP S59191894 A JPS59191894 A JP S59191894A JP 6531483 A JP6531483 A JP 6531483A JP 6531483 A JP6531483 A JP 6531483A JP S59191894 A JPS59191894 A JP S59191894A
Authority
JP
Japan
Prior art keywords
heat transfer
headers
header
liquid
transfer tubes
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
Application number
JP6531483A
Other languages
Japanese (ja)
Inventor
Shigeki Hirasawa
茂樹 平沢
Heikichi Kuwabara
桑原 平吉
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.)
Hitachi Ltd
Original Assignee
Hitachi Ltd
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 Hitachi Ltd filed Critical Hitachi Ltd
Priority to JP6531483A priority Critical patent/JPS59191894A/en
Publication of JPS59191894A publication Critical patent/JPS59191894A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F9/00Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
    • F28F9/02Header boxes; End plates
    • F28F9/026Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits
    • F28F9/0265Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits by using guiding means or impingement means inside the header box
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28BSTEAM OR VAPOUR CONDENSERS
    • F28B9/00Auxiliary systems, arrangements, or devices
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F9/00Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
    • F28F9/02Header boxes; End plates
    • F28F9/0202Header boxes having their inner space divided by partitions
    • F28F9/0204Header boxes having their inner space divided by partitions for elongated header box, e.g. with transversal and longitudinal partitions
    • F28F9/0209Header boxes having their inner space divided by partitions for elongated header box, e.g. with transversal and longitudinal partitions having only transversal partitions
    • F28F9/0212Header boxes having their inner space divided by partitions for elongated header box, e.g. with transversal and longitudinal partitions having only transversal partitions the partitions being separate elements attached to header boxes

Landscapes

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

Abstract

PURPOSE:To improve the heat transferring ability of a condenser by promoting separation of liquid from vapor in a header, by providing a gas/liquid separating device in the neighborhood of the outlet of heat transfer tubes for heating medium, in a heat exchanger having many heat transfer tubes and a pair of headers which connect both ends of the heat transfer tubes, installed in an equipment such as an air-conditioner. CONSTITUTION:Headers 2 and 3 are connected to both ends of heat transfer tubes, and a partition pannel 4 is provided in each header 2 and 3. The horizontal sections of the headers 2 and 3 are semicircular and the heat transfer tubes 1 are protruded into the headers slipping off the center positions of them. The mixed flow of vapor and liquid being fed into the headers 2 and 3 from heat transfer tubes 1 rotates along the curved inner walls 2a and 3a of the headers 2 and 3, respectively, so that the vapor and the liquid adhering to the inner walls 2a and 3a are completely separated from each other by the centrifugal force. The liquid drips along the inner walls 2a and 3a, while the vapor flows through the inside of the headers 2 and 3, accordingly the vapor only is fed into the heat transfer tubes 1 on the lower stage. The liquid gathered in the lower part of a header 2 is fed into the headers 2 and 3 on the lower stage, passing through a gap 4a which is provided between the partition pannel 4 and the inner wall of a header 2.

Description

【発明の詳細な説明】 本発明は空調機やバイナリ−サイクル地、@発電プラン
ト用咲紬器など多数の伝熱管と、こ1しら伝熱dの両#
li側金各々接続するヘッダからなり、伝熱省内にて熱
媒体蒸気か凝縮する熱交換器特にそのヘッダ構造に関す
るものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention is applicable to a large number of heat transfer tubes such as air conditioners, binary cycle machines, and power generation plants.
This invention relates to a heat exchanger, in particular, to a header structure of a heat exchanger in which heat medium vapor is condensed in a heat transfer chamber, which consists of headers connected to each side of the li side.

従来のこの種熱交換器はそのヘッダの水平断面が円形や
半円形をしておシ、伝熱管がその水平断面のはy中央部
に配設されている。しかしこのような構造では、伝熱管
からヘッダに流入する熱媒、体の凝輸液と未凝紬蒸気と
がヘッダにおいて十分に分離せず、一部の液が蒸気に混
じって下段の伝熱管に流入し、伝、熱性能が低下する欠
点があった。
In conventional heat exchangers of this type, the horizontal cross section of the header is circular or semicircular, and the heat transfer tubes are disposed at the center of the horizontal cross section. However, in this structure, the heat medium, condensed liquid, and uncondensed steam flowing into the header from the heat transfer tubes are not sufficiently separated in the header, and some of the liquid mixes with the steam and flows into the heat transfer tubes in the lower stage. There was a drawback that the inflow, heat transfer, and thermal performance deteriorated.

本発明の目的はヘッダ内にて液と蒸気の分離を促進し、
蒸気のみが下段の伝熱管に流入するようなヘッダ構造を
有する熱交換器を提供することにある。
The purpose of the present invention is to promote separation of liquid and vapor in the header,
It is an object of the present invention to provide a heat exchanger having a header structure such that only steam flows into the lower stage heat exchanger tubes.

上記の目的を達成するため、本発明はヘッダを、気液混
合流の熱媒体流に遠心力を与える構造としこの熱媒体流
の遠心力を利用してヘッダ内において気液分離全促進し
たことを特徴とする。
In order to achieve the above object, the present invention provides a header with a structure that applies centrifugal force to the heating medium flow of the gas-liquid mixed flow, and utilizes the centrifugal force of the heating medium flow to fully promote gas-liquid separation within the header. It is characterized by

以下1本発明の一実施例を第1図および第2図によシ説
明する。多数並設された伝熱管1にはその両端側にヘッ
ダ2.3が接続されている。ヘッダ2.3内には仕切板
4が設けられている。第2図はこれらヘッダ2,3の水
平断面図を示す。ヘッダ2,3の水平断面形状は半円形
状であシ、伝熱管1は中央位置よシずらして突出しであ
る。本実施例によれば、伝熱管1からヘッダ2,3に流
入した蒸気と液の混合流は、ヘッダ2.3の曲面内壁2
a 、3aに沿って回転するため、遠心力によって液が
ヘッダ2.3の内壁2a、3aに付着し蒸気と液とが完
全に分離する。液はヘッダ2.3の内%2a+3a′f
:伝わって流下し、蒸気はヘッダ2.3内部を流れるだ
め、下段の伝熱管には蒸気のみが流入することになる。
An embodiment of the present invention will be described below with reference to FIGS. 1 and 2. Headers 2.3 are connected to both ends of a large number of heat exchanger tubes 1 arranged in parallel. A partition plate 4 is provided within the header 2.3. FIG. 2 shows a horizontal sectional view of these headers 2, 3. The horizontal cross-sectional shape of the headers 2 and 3 is semicircular, and the heat exchanger tube 1 protrudes from the center position. According to this embodiment, the mixed flow of steam and liquid flowing from the heat exchanger tube 1 into the headers 2 and 3 flows through the curved inner wall of the header 2.3.
Since the header 2.3 rotates along the a and 3a, the liquid adheres to the inner walls 2a and 3a of the header 2.3 due to centrifugal force, and the vapor and liquid are completely separated. The liquid is %2a+3a'f in header 2.3
: The steam is transmitted and flows down, and since it does not flow inside the header 2.3, only the steam flows into the lower heat transfer tube.

ヘッダ2の下部に果まった液ば、ヘッダ2内の仕切板4
にある穴4af通って下段のヘッダ内に流れる。
Liquid reservoir at the bottom of header 2, partition plate 4 inside header 2
It flows through the hole 4af in the lower header.

本実施91によnばヘッダ内の液と蒸気の分離が十分に
行わ肛るため、液が伝熱管に流入して伝熱性能が低下す
る問題点が解決される。
According to the present embodiment 91, the liquid and steam in the header are sufficiently separated, so that the problem of liquid flowing into the heat transfer tubes and deteriorating heat transfer performance is solved.

第3図〜第7図にヘッダ構造の他の実施例を示す。第3
図はヘッダ2,3の水平断面ノ杉状755円筒の一易合
である。第4図は、伝熱管1のヘッダ2内に望む出口端
1aを曲げて、ヘッダ2の曲面内壁と伝熱管出口端1a
によって液と蒸気を分離する場合である。
Other embodiments of the header structure are shown in FIGS. 3 to 7. Third
The figure shows a horizontal section of the headers 2 and 3 of a cedar-shaped 755 cylinder. FIG. 4 shows the curved inner wall of the header 2 and the outlet end 1a of the heat exchanger tube by bending the outlet end 1a of the heat exchanger tube 1 that is desired to be inside the header 2.
This is the case when liquid and vapor are separated by

第5図はヘッダ2内にわん曲状のガイド5を設けて液と
蒸気を分離する場合である。
FIG. 5 shows a case where a curved guide 5 is provided in the header 2 to separate liquid and steam.

第6図は伝熱管1金ペンダ2の曲面内壁2aの近くまで
突出させ、ヘッダ2の曲面内壁2aにて液と蒸気を分離
する場合である。
FIG. 6 shows a case where the heat exchanger tube 1 is made to protrude close to the curved inner wall 2a of the metal pender 2, and liquid and steam are separated at the curved inner wall 2a of the header 2.

第7図はヘッダ2内の伝熱管1出口付近に円筒6を設け
て、円筒60表面にて液と蒸気を分離する場合である。
FIG. 7 shows a case where a cylinder 6 is provided near the outlet of the heat exchanger tube 1 in the header 2, and liquid and steam are separated on the surface of the cylinder 60.

第3図〜第7図とも円筒形状の壁面に熱媒体流を衝突さ
せて熱媒体流の遠心力によシヘツダ内の液と蒸気の分離
が十分に行われ伝熱性能が促進される効果は同じである
In both Figures 3 to 7, the effect of colliding the heat medium flow against the cylindrical wall surface is that the centrifugal force of the heat medium flow sufficiently separates the liquid and steam inside the header, promoting heat transfer performance. It's the same.

本発明によればヘッダ内の液と蒸気の分離が促進され、
蒸気のみが下段の伝熱管に流入するため、凝縮器の伝熱
性能が向上し、凝縮器の小形化はかることができる。
According to the present invention, separation of liquid and steam in the header is promoted,
Since only steam flows into the lower heat transfer tube, the heat transfer performance of the condenser is improved and the condenser can be made smaller.

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

第1図は本発明の熱交換器の一実施例を説明する断面図
、第2図は第1図におけるヘッダの水平断面図、第3図
〜第7図は本発明におけるヘッダ構造の他の実施例を示
す水平断面図である。 1・・・伝熱管、2,3・・・ヘッダ、4・・・ヘッダ
内の仕切板、5・・・曲面ガイド、6・・・円筒。 畜 1 日 X z 巴 茅 3121 蓬 4 ■ イ t 圀 ? 茅 7 日
FIG. 1 is a sectional view illustrating an embodiment of the heat exchanger of the present invention, FIG. 2 is a horizontal sectional view of the header in FIG. 1, and FIGS. FIG. 2 is a horizontal cross-sectional view showing an example. DESCRIPTION OF SYMBOLS 1... Heat exchanger tube, 2, 3... Header, 4... Partition plate in header, 5... Curved surface guide, 6... Cylinder. Animal 1 day Kaya 7 days

Claims (1)

【特許請求の範囲】[Claims] 多数並設された伝熱管とこれら伝熱管の両端側を各々接
続するヘッダを有し、伝熱音内にて熱媒体蒸気を凝縮す
る熱交換器において、前記ヘッダ内の伝熱前熱媒体出口
近傍に、気液分離機構を構成したことを特徴とする熱交
換器。
In a heat exchanger that has a large number of heat transfer tubes arranged in parallel and a header that connects both ends of these heat transfer tubes, and condenses heat medium vapor within a heat transfer sound, a heat medium outlet in the header before heat transfer is provided. A heat exchanger characterized in that a gas-liquid separation mechanism is configured nearby.
JP6531483A 1983-04-15 1983-04-15 Heat exchanger Pending JPS59191894A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6531483A JPS59191894A (en) 1983-04-15 1983-04-15 Heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6531483A JPS59191894A (en) 1983-04-15 1983-04-15 Heat exchanger

Publications (1)

Publication Number Publication Date
JPS59191894A true JPS59191894A (en) 1984-10-31

Family

ID=13283317

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6531483A Pending JPS59191894A (en) 1983-04-15 1983-04-15 Heat exchanger

Country Status (1)

Country Link
JP (1) JPS59191894A (en)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0195288A (en) * 1987-10-07 1989-04-13 Showa Alum Corp Heat exchanger
FR2665757A1 (en) * 1990-08-08 1992-02-14 Valeo Thermique Moteur Sa Coolant fluid condenser with vertical circulation, and method of manufacture
FR2747768A1 (en) * 1996-04-18 1997-10-24 Valeo Thermique Moteur Sa Condenser for refrigeration circuit in vehicle air conditioning
FR2749647A1 (en) * 1996-06-05 1997-12-12 Valeo Thermique Moteur Sa SEPARATE TANK CONDENSER FOR AIR CONDITIONING INSTALLATION, ESPECIALLY A MOTOR VEHICLE
EP0854327A1 (en) * 1997-01-16 1998-07-22 Ford Motor Company High capacity condenser
EP0886113A3 (en) * 1997-06-16 1999-10-27 Halla Climate Control Corp Multistage gas and liquid phase separation type condenser
WO2003100338A1 (en) * 2002-05-29 2003-12-04 Alfa Laval Corporate Ab A plate heat exchanger device and a heat exchanger plate
DE102011080673A1 (en) * 2011-08-09 2013-02-14 Behr Gmbh & Co. Kg Refrigerant condenser component for motor car air conditioning apparatus, has aperture mounted in collecting pipe portion or in return section, where flow cross-sectional area for coolant to aperture is smaller than outer side of aperture
WO2013162222A1 (en) * 2012-04-26 2013-10-31 Lg Electronics Inc. Heat exchanger

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS55105196A (en) * 1979-02-07 1980-08-12 Babcock Hitachi Kk Piping header for heat exchanger with steam separator

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS55105196A (en) * 1979-02-07 1980-08-12 Babcock Hitachi Kk Piping header for heat exchanger with steam separator

Cited By (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0195288A (en) * 1987-10-07 1989-04-13 Showa Alum Corp Heat exchanger
FR2665757A1 (en) * 1990-08-08 1992-02-14 Valeo Thermique Moteur Sa Coolant fluid condenser with vertical circulation, and method of manufacture
FR2747768A1 (en) * 1996-04-18 1997-10-24 Valeo Thermique Moteur Sa Condenser for refrigeration circuit in vehicle air conditioning
FR2749647A1 (en) * 1996-06-05 1997-12-12 Valeo Thermique Moteur Sa SEPARATE TANK CONDENSER FOR AIR CONDITIONING INSTALLATION, ESPECIALLY A MOTOR VEHICLE
US5946938A (en) * 1996-06-05 1999-09-07 Valeo Thermique Moteur Condenser with a separate reservoir for an air conditioning installation, especially for motor vehicles
EP0854327A1 (en) * 1997-01-16 1998-07-22 Ford Motor Company High capacity condenser
EP0886113A3 (en) * 1997-06-16 1999-10-27 Halla Climate Control Corp Multistage gas and liquid phase separation type condenser
WO2003100338A1 (en) * 2002-05-29 2003-12-04 Alfa Laval Corporate Ab A plate heat exchanger device and a heat exchanger plate
US7669643B2 (en) 2002-05-29 2010-03-02 Alfa Laval Corporate Ab Plate heat exchanger device and a heat exchanger plate
DE102011080673A1 (en) * 2011-08-09 2013-02-14 Behr Gmbh & Co. Kg Refrigerant condenser component for motor car air conditioning apparatus, has aperture mounted in collecting pipe portion or in return section, where flow cross-sectional area for coolant to aperture is smaller than outer side of aperture
WO2013162222A1 (en) * 2012-04-26 2013-10-31 Lg Electronics Inc. Heat exchanger
CN104246413A (en) * 2012-04-26 2014-12-24 Lg电子株式会社 Heat exchanger
CN104246413B (en) * 2012-04-26 2016-08-17 Lg电子株式会社 Heat exchanger
US10551127B2 (en) 2012-04-26 2020-02-04 Lg Electronics Inc. Heat exchanger

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