JP2927006B2 - Heat exchanger - Google Patents

Heat exchanger

Info

Publication number
JP2927006B2
JP2927006B2 JP3023737A JP2373791A JP2927006B2 JP 2927006 B2 JP2927006 B2 JP 2927006B2 JP 3023737 A JP3023737 A JP 3023737A JP 2373791 A JP2373791 A JP 2373791A JP 2927006 B2 JP2927006 B2 JP 2927006B2
Authority
JP
Japan
Prior art keywords
header pipe
receiver tank
tube
compartment
pipe
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 - Fee Related
Application number
JP3023737A
Other languages
Japanese (ja)
Other versions
JPH04350498A (en
Inventor
佳史 安芸
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.)
Denso Corp
Original Assignee
Denso Corp
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 Denso Corp filed Critical Denso Corp
Priority to JP3023737A priority Critical patent/JP2927006B2/en
Publication of JPH04350498A publication Critical patent/JPH04350498A/en
Application granted granted Critical
Publication of JP2927006B2 publication Critical patent/JP2927006B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B39/00Evaporators; Condensers
    • F25B39/04Condensers
    • 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
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2339/00Details of evaporators; Details of condensers
    • F25B2339/04Details of condensers
    • F25B2339/044Condensers with an integrated receiver
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2339/00Details of evaporators; Details of condensers
    • F25B2339/04Details of condensers
    • F25B2339/044Condensers with an integrated receiver
    • F25B2339/0443Condensers with an integrated receiver the receiver being positioned horizontally

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Details Of Heat-Exchange And Heat-Transfer (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、熱交換器、特にクーラ
用コンデンサのように気体状の熱媒体を熱交換により凝
縮せしめて液化せしめる熱交換器に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a heat exchanger, and more particularly to a heat exchanger in which a gaseous heat medium is condensed by heat exchange and liquefied like a condenser for a cooler.

【従来の技術】カークーラ用コンデンサ等に用いられる
熱交換器として、該熱交換器の両側端に長さ方向を平行
せしめて配置した一対のヘツダパイプを、該ヘツダパイ
プの長さ方向に垂直に配設した複数個のチユーブを介し
て連通させ、該チユーブ間に熱交換用のフインを連結し
たものが広く知られている。これら従来の熱交換器は、
これに隣接してヘツダパイプに形成した熱媒体出口に連
通するレシーバタンクを設け、前記熱交換器により、凝
縮された熱媒体を貯溜するとともに、液体状の熱媒体よ
り気体状の熱媒体を除去して、熱サイクル回路に循環せ
しめるのを通例とする。
2. Description of the Related Art As a heat exchanger used for a condenser for a car cooler or the like, a pair of header pipes which are arranged at both ends of the heat exchanger with their length directions parallel to each other are arranged perpendicular to the length direction of the header pipe. It is widely known that the plurality of tubes communicate with each other and fins for heat exchange are connected between the tubes. These conventional heat exchangers
A receiver tank communicating with a heat medium outlet formed in the header pipe is provided adjacent to the heat tank, and the heat exchanger stores the condensed heat medium and removes the gaseous heat medium from the liquid heat medium. Then, it is customary to circulate through the heat cycle circuit.

【0002】[0002]

【発明が解決しようとする課題】上記熱交換器において
は、レシーバタンクを別体に設けており、熱交換器とレ
シーバタンクとの接続に手間を要する。そこでヘツダパ
イプとレシーバタンクとを一体成形することにより両者
の接続を行うことも提案されている(実開平2−139
54号公報参照)が、ヘツダタンクにおいては、内腔部
において気体状の熱媒体と凝縮して液化した熱媒体とが
流動するのに対し、レシーバタンクは凝縮して液化した
熱媒体を貯溜するものであつて、両者の機能が別個であ
るから、従来の熱交換器はレシーバタンクを熱交換器と
は独立せしめた構成とするため、全体の寸法の増大を招
来する結果となる。そこで本発明は従来の熱交換器の正
面寸法の範囲内において、レシーバタンクを一体的に付
設した熱交換器を提供することを目的とする。
In the above heat exchanger, the receiver tank is provided separately, and it takes time to connect the heat exchanger and the receiver tank. Therefore, it has been proposed to connect the head pipe and the receiver tank by integrally molding the head pipe and the receiver tank (Japanese Utility Model Laid-Open No. 2-139).
In the header tank, the gaseous heat medium and the condensed and liquefied heat medium flow in the inner cavity, whereas the receiver tank stores the condensed and liquefied heat medium. Since the two functions are separate, the conventional heat exchanger has a configuration in which the receiver tank is made independent of the heat exchanger, resulting in an increase in the overall size. Therefore, an object of the present invention is to provide a heat exchanger in which a receiver tank is integrally provided within a range of front dimensions of a conventional heat exchanger.

【0003】[0003]

【課題を解決するための手段】本発明は、上部と下部と
に配置したヘツダパイプの間に複数個のチユーブを、そ
の長手方向を鉛直方向として互いに平行せしめて配設す
る形式の熱交換器であつて、上部ヘツダパイプの内腔部
を隔壁によつて区画して、前記上部ヘツダパイプの内腔
部をその長手方向に互いに隣接する第1および第2の少
くとも2個の独立した区画室に区画するとともに、前記
複数個のチユーブを少くとも3個の群に編成し、その第
1のチユーブ群を上部ヘツダパイプにおける第1の区画
室と前記下部ヘツダパイプの内腔部とを連通せしめ、そ
の第2のチユーブ群を前記上部ヘツダパイプの第2の区
画室と前記第1のチユーブ群が連通している下部ヘツダ
パイプの内腔部とを連通せしめ、さらにその第3のチユ
ーブ群は、前記上部ヘツダパイプの第2の区画室と前記
下部ヘツダパイプの長手方向端部に隣接せしめて、かつ
前記下部ヘツダパイプの内腔部とは独立しているレシー
バタンクとを連通せしめ、該レシーバタンク内には、前
記第3のチユーブ群の下端開口部の直下に該チユーブ群
から流下する熱媒体に撹拌と混合作用を与える撹拌体を
配設したことを特徴とするものである。
SUMMARY OF THE INVENTION The present invention relates to a heat exchanger of the type in which a plurality of tubes are arranged between header pipes arranged at an upper portion and a lower portion, with a plurality of tubes being parallel to each other with the longitudinal direction thereof being vertical. Then, the lumen of the upper header pipe is partitioned by a partition wall, and the lumen of the upper header pipe is partitioned into first and second at least two independent compartments adjacent to each other in the longitudinal direction. And knitting the plurality of tubes into at least three groups, and connecting the first group of tubes to the first compartment of the upper header pipe and the inner cavity of the lower header pipe; The second group of tubes communicates with the second compartment of the upper header pipe and the lumen of the lower header pipe communicating with the first group of tubes, and the third group of tubes further communicates with the upper group of tubes. A second compartment of the header pipe and a receiver tank which is adjacent to a longitudinal end of the lower header pipe and communicates with a receiver tank which is independent of a lumen of the lower header pipe are communicated with each other. A stirrer is provided immediately below the lower end opening of the third tube group to provide stirring and mixing to the heat medium flowing down from the tube group.

【0004】[0004]

【作用】本発明によれば、上部ヘツダパイプの第1の区
画室に導入された熱媒体は、第1のチユーブ群を介して
下部ヘツダパイプに流入し、次いで第2のチユーブ群を
介して下部ヘツダパイプより上部ヘツダパイプの第2の
区画室に流入し、さらに該第2の区画室から第3のチユ
ーブ群を介してレシーバタンクに流入する。この間のク
ロスフロー型の流動により熱媒体は前記チユーブおよび
該チユーブ間に接続されているフインの間を流れる空気
と熱交換し、凝縮せしめられて、気体状の熱媒体の大部
分が凝縮して液化し、熱媒体の熱交換器における最後の
通路である第3のチユーブ群の下端からレシーバタンク
に流下し、液化した熱媒体はレシーバタンクに貯溜さ
れ、熱媒体出口から熱サイクル回路に再循環せしめられ
る。
According to the present invention, the heat medium introduced into the first compartment of the upper header pipe flows into the lower header pipe through the first tube group, and then flows through the lower header pipe through the second tube group. It flows into the second compartment of the upper header pipe and from the second compartment through the third group of tubes into the receiver tank. During this time, the heat medium exchanges heat with the air flowing between the tubes and the fins connected between the tubes by the cross-flow type flow, and is condensed, so that most of the gaseous heat medium is condensed. It liquefies and flows down to the receiver tank from the lower end of the third tube group, which is the last passage in the heat medium heat exchanger, and the liquefied heat medium is stored in the receiver tank and recirculated from the heat medium outlet to the heat cycle circuit. I'm sullen.

【0005】前記レシーバタンクの内部において、前記
第3のチユーブ群を構成するチユーブの下端開口部の直
下に、流下する熱媒体に撹拌混合作用を付与する撹拌体
を配設したことにより、前記レシーバタンク内に流下し
た熱媒体中の液化した熱媒体から気体状の熱媒体が分離
され前記レシーバタンク内に貯溜される液化した熱媒体
から未凝縮の熱媒体が分離される。
In the receiver tank, a stirrer for imparting a stirring and mixing action to the heat medium flowing down is provided immediately below a lower end opening of a tube constituting the third tube group, thereby providing the receiver with a stirrer. The gaseous heat medium is separated from the liquefied heat medium in the heat medium that has flowed down into the tank, and the uncondensed heat medium is separated from the liquefied heat medium stored in the receiver tank.

【0006】[0006]

【実施例】図1は本発明をカークーラ用コンデンサに施
した一実施例の断面正面図、図2はその要部の分解斜面
図を示す。図において、上部ヘツダパイプ1は、コンデ
ンサの正面からみて全幅にわたる長さの中空円筒状の金
属製のパイプ本体2と、該パイプ本体2の両端を閉じる
端板3,3、前記パイプ本体2の内腔部を第1の区画室
5および第2の区画室6に区画する隔壁4および前記第
1の区画室5に連通する冷媒導入口7よりなる。下部ヘ
ツダパイプ8は前記パイプ本体2の長さより短く、その
ほぼ2/3の長さの中空円筒状の金属製のパイプ本体9
と、その一端を閉じる端板10とからなり、該下部ヘツ
ダパイプ8のパイプ本体9の他端には、レシーバタンク
11が連設される。前記レシーバタンク11は、下部ヘ
ツダパイプ8のパイプ本体9より直径が大なる中空円筒
状の金属製のパイプ本体12と、該パイプ本体12の一
端と前記下部ヘツダパイプ8のパイプ本体9の他端とを
閉じて該パイプ本体9内に流動室13を形成する連結板
14と、レシーバタンク11のパイプ本体12の他端を
閉じて該パイプ本体12内に貯溜室15を形成する端板
16とからなり、冷媒排出口17が前記端板16に設け
られる。
1 is a sectional front view of an embodiment in which the present invention is applied to a condenser for a car cooler, and FIG. 2 is an exploded perspective view of a main part thereof. In the figure, an upper header pipe 1 has a hollow cylindrical metal pipe body 2 having a length extending over the entire width as viewed from the front of the condenser, end plates 3 and 3 for closing both ends of the pipe body 2, and the inside of the pipe body 2. It comprises a partition wall 4 for partitioning the cavity into a first compartment 5 and a second compartment 6, and a refrigerant inlet 7 communicating with the first compartment 5. The lower header pipe 8 is shorter than the length of the pipe body 2, and is a hollow cylindrical metal pipe body 9 having a length of about / thereof.
, And an end plate 10 closing one end thereof. A receiver tank 11 is connected to the other end of the pipe main body 9 of the lower header pipe 8. The receiver tank 11 includes a hollow cylindrical metal pipe body 12 having a diameter larger than the pipe body 9 of the lower header pipe 8, and one end of the pipe body 12 and the other end of the pipe body 9 of the lower header pipe 8. It comprises a connecting plate 14 which is closed to form a flow chamber 13 in the pipe body 9 and an end plate 16 which closes the other end of the pipe body 12 of the receiver tank 11 and forms a storage chamber 15 in the pipe body 12. A refrigerant outlet 17 is provided in the end plate 16.

【0007】下部ヘツダパイプ8のパイプ本体9および
レシーバタンク11のパイプ本体12は、連結板14を
介して、それぞれの最下端が一線上にあるように直列に
固定され、パイプ本体9の端板10からパイプ本体12
の端板16までの距離は、上部ヘツダパイプ1のパイプ
本体2の両端の端板3,3間の距離に等しい。即ち連結
された下部ヘツダパイプ8とレシーバタンク11の全長
は、上部ヘツダパイプ1の長さに等しくされる。
The pipe main body 9 of the lower header pipe 8 and the pipe main body 12 of the receiver tank 11 are fixed in series via a connecting plate 14 so that the lowermost ends thereof are aligned with each other. From the pipe body 12
Is equal to the distance between the end plates 3 at both ends of the pipe body 2 of the upper header pipe 1. That is, the total length of the connected lower header pipe 8 and the receiver tank 11 is made equal to the length of the upper header pipe 1.

【0008】上部ヘツダパイプ1および下部ヘツダパイ
プ8とレシーバタンク11とは、互いにその長手方向
(中心軸方向)を水平とし、互いに平行に配置され、上
部ヘツダパイプ1と下部ヘツダパイプ8との間および上
部ヘツダパイプ1とレシーバタンク11との間に複数個
の金属製のチユーブ18が、鉛直方向にかつ相互に平行
に配設され、これらのチユーブ18により上部ヘツダパ
イプ1のパイプ本体2の内腔と下部ヘツダパイプ8およ
びレシーバタンク11のパイプ本体9,12の内腔が連
通せしめられる。またこれらチユーブ18の両外側に、
該チユーブ18に平行せしめて、サイドプレート19,
19を配設し、上部ヘツダパイプ1と下部ヘツダパイプ
8のパイプ本体2,9の間および上部ヘツダパイプ1と
レシーバタンク11のパイプ本体2,12の間を連結す
る。上記チユーブ18の相互間およびチユーブ18とサ
イドプレート19,19間には放熱フイン20を取付け
る。前記チユーブ18の各パイプ本体2,9,12への
固着および放熱フイン20の固着は、従来技術と同じで
ある。
The upper header pipe 1, the lower header pipe 8, and the receiver tank 11 are arranged parallel to each other with their longitudinal directions (central axis directions) being horizontal, and between the upper header pipe 1 and the lower header pipe 8, and between the upper header pipe 1 and the upper header pipe 1. A plurality of metal tubes 18 are arranged vertically and in parallel with each other between the receiver tank 11 and the inner space of the pipe body 2 of the upper header pipe 1 and the lower header pipe 8 and The lumens of the pipe bodies 9 and 12 of the receiver tank 11 are communicated. Also, on both sides of these tubes 18,
The side plate 19,
The upper header pipe 1 is connected to the pipe bodies 2 and 9 of the lower header pipe 8 and the upper header pipe 1 is connected to the pipe bodies 2 and 12 of the receiver tank 11. Heat radiation fins 20 are mounted between the tubes 18 and between the tubes 18 and the side plates 19, 19. The fixing of the tube 18 to each of the pipe bodies 2, 9, 12 and the fixing of the radiation fin 20 are the same as in the prior art.

【0009】上記複数個のチユーブ18は、上部ヘツダ
パイプ1の第1の区画室5と下部ヘツダパイプ8の流動
室13とを連通する第1のチユーブ群21と、上部ヘツ
ダパイプ1の第2の区画室6と下部ヘツダパイプ8の流
動室13とを連通する第2のチユーブ群22と、上部ヘ
ツダパイプ1の第2の区画室6とレシーバタンク11の
貯溜室15とを連通する第3のチユーブ群23の3個の
群に区分される。第3のチユーブ群23を構成する各チ
ユーブ18の下端はレシーバタンク11の最高部におい
て貯溜室15内に開口する。図1に示す実施例において
は、各チユーブ群はそれぞれ4本のチユーブ18により
構成されている。圧縮機から冷媒導入口7を経てコンデ
ンサの上部ヘツダパイプ1の第1の区画室5に導入され
る高温高圧の気体状冷媒は、第1のチユーブ群21を介
して下部ヘツダパイプ8の流動室13に流入し、さらに
該流動室13から第2のチユーブ群22を介して上部ヘ
ツダパイプ1の第2の区画室6に流入し、該第2の区画
室6から第3のチユーブ群23を介してレシーバタンク
11の貯溜室15に流下する。気体状冷媒が各チユーブ
群を流れる間に放熱フイン20およびチユーブ18間を
流れる空気との間に熱交換が行われ、凝縮し、バーチカ
ルタイプのクロスフロー方式の熱交換が行われる。
The plurality of tubes 18 include a first group of tubes 21 communicating the first compartment 5 of the upper header pipe 1 and the flow chamber 13 of the lower header pipe 8, and a second compartment of the upper header pipe 1. 6 and a third tube group 23 which communicates the flow chamber 13 of the lower header pipe 8 with the second compartment 6 of the upper header pipe 1 and the storage chamber 15 of the receiver tank 11. It is divided into three groups. The lower end of each tube 18 constituting the third tube group 23 opens into the storage chamber 15 at the highest part of the receiver tank 11. In the embodiment shown in FIG. 1, each tube group is constituted by four tubes 18. The high-temperature and high-pressure gaseous refrigerant introduced from the compressor through the refrigerant inlet 7 into the first compartment 5 of the upper header pipe 1 of the condenser passes through the first tube group 21 to the flow chamber 13 of the lower header pipe 8. And flows into the second compartment 6 of the upper header pipe 1 from the flow chamber 13 via the second tube group 22, and from the second compartment 6 to the receiver via the third tube group 23. It flows down into the storage chamber 15 of the tank 11. While the gaseous refrigerant flows through each tube group, heat is exchanged with the air flowing between the radiation fins 20 and the tubes 18, condensed, and vertical type cross-flow heat exchange is performed.

【0010】上部ヘツダパイプ1の第2の区画室6から
第3のチユーブ群23を介してレシーバタンク11の貯
溜室15に流下する冷却の最終段階では、第3のチユー
ブ群23を構成する各チユーブ18内において、チユー
ブ内壁に沿つて流下する液体状の冷媒とチユーブの中心
部を流下する未凝縮の気体状の冷媒の二相流が存在す
る。そこでレシーバタンク11の貯溜室15の最高部に
おいて開口する第3のチユーブ群23の各チユーブ18
の開口端の直下位置に、前記連結板14と端板16とに
両端を固定して撹拌体24を固定する。撹拌体24は、
多数の孔を穿設したパンチメタルを筒状またはスパイラ
ル状に巻いたものを図示している。第3のチユーブ群2
3を構成する各チユーブ18の下端開口から貯溜室15
内に流下する液体状の冷媒は、撹拌体24に衝突、撹拌
され、過冷却冷媒によつて未凝縮の気体状冷媒の凝縮が
さらに進行し、貯溜室15内に滴下する。これにより液
相の冷媒中に閉じ込められている気泡状の冷媒は分離さ
れ、液相の冷媒中での気泡の発生も抑制され、液体状の
冷媒が貯溜室15の下層に、未凝縮の気体状の冷媒はそ
の上層に貯溜され、貯溜室15の下部に連通する冷媒排
出口17から、気液分離されて気体状冷媒が気泡状に閉
じ込められていない液体状冷媒が、次段の膨張弁へ送り
出される。
In the final stage of cooling down from the second compartment 6 of the upper header pipe 1 to the storage chamber 15 of the receiver tank 11 via the third tube group 23, each of the tubes constituting the third tube group 23 is formed. Within 18, there is a two-phase flow of liquid refrigerant flowing down the tube inner wall and uncondensed gaseous refrigerant flowing down the center of the tube. Therefore, each tube 18 of the third tube group 23 opening at the highest part of the storage chamber 15 of the receiver tank 11 is provided.
The stirrer 24 is fixed to the connecting plate 14 and the end plate 16 at both ends at a position directly below the opening end of the stirrer 24. The stirring body 24 is
The figure shows a punched metal having a large number of holes wound in a cylindrical or spiral shape. Third Tube Group 2
3 to the storage chamber 15 from the lower end opening of each tube 18.
The liquid refrigerant flowing down into the inside collides with and is stirred by the stirring body 24, and the uncondensed gaseous refrigerant is further condensed by the supercooled refrigerant, and drops into the storage chamber 15. As a result, the gaseous refrigerant confined in the liquid-phase refrigerant is separated, the generation of air bubbles in the liquid-phase refrigerant is also suppressed, and the liquid refrigerant is placed in the lower layer of the storage chamber 15 as uncondensed gas. The liquid refrigerant is stored in the upper layer, and the liquid refrigerant, which is gas-liquid separated and the gaseous refrigerant is not confined in the form of bubbles, is supplied from a refrigerant outlet 17 communicating with the lower part of the storage chamber 15 to the next-stage expansion valve. Sent out to

【0011】前記撹拌体24は気液二相冷媒を撹拌・混
合する機能をもたせたもので、前記パンチメタルを筒状
またはスパイラル状に巻いたもののほか、パンチメタル
を数回折り曲げて数層に折りたたんだもの、あるいは金
属線を螺旋状に巻き成形したもの等を用いることができ
る。また撹拌体24は、図示したように連結板14と端
板16との間に橋架して、第3のチユーブ群23のすべ
てのチユーブ18に1個の撹拌体24を対応させるほ
か、レシーバタンク11のパイプ本体12の円筒状壁間
に橋架して、第3のチユーブ群23の各チユーブ18に
それぞれ1本の撹拌体24を対応せしめてもよい。
The agitator 24 has a function of agitating and mixing a gas-liquid two-phase refrigerant. In addition to the punch metal wound in a cylindrical or spiral shape, the punch metal is bent several times to form several layers. A folded one, a spirally wound metal wire, or the like can be used. The stirrer 24 is bridged between the connecting plate 14 and the end plate 16 as shown in the drawing, so that one stirrer 24 corresponds to all the tubes 18 of the third tube group 23 and a receiver tank. One stirrer 24 may correspond to each tube 18 of the third tube group 23 by bridging between the cylindrical walls of the 11 pipe bodies 12.

【0012】上述した実施例においては、上部ヘツダパ
イプ1と下部ヘツダパイプ8およびレシーバタンク11
とを連通せしめる複数個のチユーブ18を3個のチユー
ブ群に編成し、図3に示すバーチカルタイプのクロスフ
ロー方式の冷媒の熱交換通路を構成する熱交換器であ
る。本発明においては、上部ヘツダパイプ1、下部ヘツ
ダパイプ8およびチユーブ18で構成され最終的にはレ
シーバタンク11に達する熱媒体である冷媒の通路を、
その最終段階の通路を上部ヘツダパイプ1の第2の区画
室6から鉛直方向下方に延びる第3のチユーブ群23を
構成するチユーブ18によりレシーバタンク11に連通
せしめた構成により、レシーバタンクを熱交換器内に組
み込むことに成功したものである。従つて、例えば図4
に示すように下部ヘツダパイプ8の流動室13を隔壁3
0により第1および第2の流動室31,32に分割し、
下部ヘツダパイプ8の第1の流動室31に冷媒導入口7
を連通せしめるとともに、前記第1の流動室31を上部
ヘツダパイプ1の第1の区画室5と連通する第4のチユ
ーブ群24を形成すると、図4に示す冷媒通路が構成で
き、さらに上部ヘツダパイプ1の第1の区画室5を隔壁
44により2個の独立した区画室51,52に分割し、
下部ヘツダパイプ8の流動室13を前述したように2個
の独立した流動室31,32に分割するとともに、複数
個のチユーブ18を第1および第2のチユーブ群21,
22の間に前記第1の流動室31と区画室52とを連通
する第4のチユーブ群25および前記区画室52と第2
の流動室32とを連通する第5のチユーブ群26を形成
すると、図5に示す冷媒通路を形成することができる。
In the above-described embodiment, the upper header pipe 1, the lower header pipe 8, and the receiver tank 11
A plurality of tubes 18 that communicate with each other are formed into a group of three tubes to constitute a vertical-type cross-flow type refrigerant heat exchange passage shown in FIG. In the present invention, the passage of the refrigerant, which is constituted by the upper header pipe 1, the lower header pipe 8 and the tube 18, and finally reaches the receiver tank 11,
The final stage passage is connected to the receiver tank 11 by a tube 18 constituting a third tube group 23 extending vertically downward from the second compartment 6 of the upper header pipe 1 so that the receiver tank is connected to the heat exchanger. It has been successfully incorporated within. Thus, for example, FIG.
The flow chamber 13 of the lower header pipe 8 is
0 to divide into first and second flow chambers 31, 32,
The refrigerant inlet 7 is provided in the first flow chamber 31 of the lower header pipe 8.
And a fourth group of tubes 24 connecting the first flow chamber 31 with the first compartment 5 of the upper header pipe 1 to form a refrigerant passage shown in FIG. Is divided into two independent compartments 51 and 52 by a partition 44,
As described above, the flow chamber 13 of the lower header pipe 8 is divided into two independent flow chambers 31 and 32, and the plurality of tubes 18 are divided into the first and second tube groups 21, 32.
A fourth tube group 25 which connects the first flow chamber 31 and the compartment 52 between the second chamber 22 and the second tube group 25 and the second
When the fifth tube group 26 that communicates with the fluid chamber 32 is formed, the refrigerant passage shown in FIG. 5 can be formed.

【0013】[0013]

【発明の効果】本発明によれば、熱交換器の上部位置に
水平に配設した上部ヘツダパイプは、その内腔部を隔壁
により第1および第2の区画室の互いに独立した少くと
も2個の区画室に形成され、熱交換器の下部位置に前記
上部ヘツダパイプに平行せしめて配設した下部ヘツダパ
イプの内腔部とを、前記第1の区画室に連通する第1の
チユーブ群と、前記第2の区画室に連通する第2のチユ
ーブ群とにより連結し、また前記下部ヘツダパイプの長
手方向の一端部に隣接せしめて配設したレシーバタンク
の内腔部は、前記上部ヘツダパイプの第2の区画室と第
3のチユーブ群により連通せしめてあるので、上部ヘツ
ダパイプの第1の区画室から第1のチユーブ群を介して
下部ヘツダパイプに連通する熱媒体通路と、前記下部ヘ
ツダパイプから第2のチユーブ群を介して上部ヘツダパ
イプの第2の区画室に連通する熱媒体通路と、前記第2
の区画室から第3のチユーブ群を介してレシーバタンク
に連通する熱媒体通路とが直列に接続されて長い熱媒体
通路を形成する。そして上記熱媒体通路の最終段階を構
成する第3のチユーブ群は、上部ヘツダパイプの第2の
区画室から鉛直方向下方に延びてレシーバタンクに連通
し、レシーバタンク内においては前記第3のチユーブ群
の下端開口部の直下に、該開口部に対応せしめて前記チ
ユーブから流下する熱媒体に撹拌と混合作用を付与する
撹拌体を配設したことにより、第3のチユーブ群を構成
する各チユーブ内を流下してレシーバタンク内に流入す
る気液二相の熱媒体は撹拌体により撹拌および混合作用
を受け、未凝縮の気相熱媒体の凝縮を促進するととも
に、液相熱媒体中に気泡状に閉じ込められている気相熱
媒体を分離するので、気液分離が促進され、気液分離が
行われた液体状の熱媒体がレシーバタンクの下部に貯溜
され、気体状の未凝縮熱媒体がレシーバタンクの上部に
貯溜されるので、前記第3のチユーブ群を構成する各チ
ユーブの下端が液体状の熱媒体中に浸漬されることはな
く、これにより熱媒体の流通抵抗を高めたり圧損を生ず
ることがないので、レシーバタンクを熱交換器のチユー
ブとともに組付けて一体に構成することができる。
According to the present invention, the upper header pipe horizontally disposed at the upper position of the heat exchanger has at least two independent lumens of the first and second compartments separated by a partition wall. A first tube group that is formed in a compartment of the heat exchanger and communicates with the inner space of the lower header pipe arranged at a lower position of the heat exchanger in parallel with the upper header pipe to the first compartment; The inner cavity of the receiver tank, which is connected to a second group of tubes communicating with the second compartment and is disposed adjacent to one longitudinal end of the lower header pipe, is connected to the second header of the upper header pipe. Since the compartment and the third tube group communicate with each other, a heat medium passage communicating from the first compartment of the upper header pipe to the lower header pipe via the first tube group, and a heat medium passage extending from the lower header pipe to the third header group. A heat medium passage communicating with the second compartment of the upper Hetsudapaipu through the Chiyubu group, the second
And a heat medium passage communicating with the receiver tank through the third tube group from the compartment (3) is connected in series to form a long heat medium passage. The third tube group constituting the final stage of the heat medium passage extends vertically downward from the second compartment of the upper header pipe and communicates with the receiver tank. In the receiver tank, the third tube group is disposed. A stirrer that provides stirring and mixing to the heat medium flowing down from the tube corresponding to the opening is disposed directly below the lower end opening of the tube, so that the inside of each tube constituting the third tube group is provided. The gas-liquid two-phase heat medium that flows down into the receiver tank is stirred and mixed by the stirrer to promote the condensation of the uncondensed gas-phase heat medium and to form bubbles in the liquid-phase heat medium. Since the gas-phase heat medium confined in the gas tank is separated, the gas-liquid separation is promoted, the liquid heat medium subjected to the gas-liquid separation is stored in the lower part of the receiver tank, and the gaseous uncondensed heat medium is removed. Lesy Since it is stored in the upper part of the tank, the lower end of each tube constituting the third tube group is not immersed in the liquid heat medium, thereby increasing the flow resistance of the heat medium or causing pressure loss. Therefore, the receiver tank can be assembled integrally with the tube of the heat exchanger.

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

【図1】本発明の熱交換器をクーラ用コンデンサに適用
した一実施例の断面正面図である。
FIG. 1 is a cross-sectional front view of an embodiment in which a heat exchanger of the present invention is applied to a cooler condenser.

【図2】前記実施例の要部の分解斜面図である。FIG. 2 is an exploded perspective view of a main part of the embodiment.

【図3】上記実施例の冷媒の流れを示す説明図である。FIG. 3 is an explanatory diagram showing a flow of a refrigerant in the embodiment.

【図4】他の実施例の冷媒の流れを示す説明図である。FIG. 4 is an explanatory diagram showing a flow of a refrigerant according to another embodiment.

【図5】他の実施例の冷媒の流れを示す説明図である。FIG. 5 is an explanatory diagram showing a flow of a refrigerant according to another embodiment.

【符号の説明】[Explanation of symbols]

1 上部ヘツダパイプ 4 隔壁 5 第1の区画室 6 第2の区画室 8 下部ヘツダパイプ 11 レシーバタンク 13 流動室 15 貯溜室 18 チユーブ 21 第1のチユーブ群 22 第2のチユーブ群 23 第3のチユーブ群 24 撹拌体 DESCRIPTION OF SYMBOLS 1 Upper header pipe 4 Partition wall 5 1st compartment 6 2nd compartment 8 Lower header pipe 11 Receiver tank 13 Flow chamber 15 Storage chamber 18 Tube 21 1st tube group 22 2nd tube group 23 3rd tube group 24 Stirring body

───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.6,DB名) F25B 39/04,43/00 F28F 9/00 - 9/26 ──────────────────────────────────────────────────続 き Continued on front page (58) Field surveyed (Int.Cl. 6 , DB name) F25B 39 / 04,43 / 00 F28F 9/00-9/26

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 上部と下部とに水平方向に互いに平行せ
しめて配設した2個のヘツダパイプの間に、複数個のチ
ユーブを鉛直方向に互いに平行せしめて配置し、前記2
個のヘツダパイプの内腔部を前記チユーブにより連通せ
しめた熱交換器において、上部ヘツダパイプはその内腔
部を少くとも1個の隔壁により区画して互いに独立の第
1および第2の区画室を少くとも形成するとともに、下
部ヘツダパイプに隣接せしめて該下部ヘツダパイプの内
腔部とは独立せしめたレシーバタンクを連結し、前記複
数個のチユーブを、前記上部ヘツダパイプの第1の区画
室と下部ヘツダパイプの内腔部とを連通する第1のチユ
ーブ群と、前記上部ヘツダパイプの第2の区画室と下部
ヘツダパイプの内腔部とを連通する第2のチユーブ群
と、前記上部ヘツダパイプの第2の区画室とレシーバタ
ンクの内腔部とを連通する第3のチユーブ群との少くと
も3個の群に区分し、前記レシーバタンク内には該タン
クの内腔部に開口する前記第3のチユーブ群のチユーブ
の下端開口部の直下に該開口部に対応せしめて、該チユ
ーブから流下する熱媒体に撹拌と混合作用を付与する撹
拌体を配設したことを特徴とする熱交換器。
1. A plurality of tubes arranged vertically parallel to each other between two header pipes arranged parallel to each other in an upper part and a lower part in a horizontal direction.
In the heat exchanger in which the lumens of the header pipes are communicated with each other by the tube, the upper header pipe is divided by at least one partition so that the first and second compartments independent of each other are reduced. And a receiver tank that is adjacent to the lower header pipe and is independent of the lumen of the lower header pipe, and connects the plurality of tubes to the first compartment and the lower header pipe of the upper header pipe. A first tube group communicating with the cavity, a second tube group communicating the second compartment of the upper header pipe with the inner cavity of the lower header pipe, and a second compartment of the upper header pipe. The receiver tank is divided into at least three groups including a third tube group that communicates with the bore of the receiver tank, and the receiver tank has an opening in the bore of the tank. A stirrer is provided directly below the lower end opening of the tube of the third tube group so as to correspond to the opening and imparts a stirring and mixing action to the heat medium flowing down from the tube. Exchanger.
JP3023737A 1991-01-25 1991-01-25 Heat exchanger Expired - Fee Related JP2927006B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3023737A JP2927006B2 (en) 1991-01-25 1991-01-25 Heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3023737A JP2927006B2 (en) 1991-01-25 1991-01-25 Heat exchanger

Publications (2)

Publication Number Publication Date
JPH04350498A JPH04350498A (en) 1992-12-04
JP2927006B2 true JP2927006B2 (en) 1999-07-28

Family

ID=12118626

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3023737A Expired - Fee Related JP2927006B2 (en) 1991-01-25 1991-01-25 Heat exchanger

Country Status (1)

Country Link
JP (1) JP2927006B2 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4043577B2 (en) * 1998-01-22 2008-02-06 昭和電工株式会社 Subcool system capacitor
US6874569B2 (en) * 2000-12-29 2005-04-05 Visteon Global Technologies, Inc. Downflow condenser
JP2004309127A (en) * 2003-04-03 2004-11-04 Behr Gmbh & Co Kg Refrigerant condensing device
JP5538045B2 (en) * 2010-04-16 2014-07-02 株式会社ケーヒン・サーマル・テクノロジー Capacitor

Also Published As

Publication number Publication date
JPH04350498A (en) 1992-12-04

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