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JPS6133972B2 - - Google Patents
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JPS6133972B2 - - Google Patents

Info

Publication number
JPS6133972B2
JPS6133972B2 JP52096553A JP9655377A JPS6133972B2 JP S6133972 B2 JPS6133972 B2 JP S6133972B2 JP 52096553 A JP52096553 A JP 52096553A JP 9655377 A JP9655377 A JP 9655377A JP S6133972 B2 JPS6133972 B2 JP S6133972B2
Authority
JP
Japan
Prior art keywords
fluid
heat exchanger
outlet
dish
inlet
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
JP52096553A
Other languages
Japanese (ja)
Other versions
JPS5325717A (en
Inventor
Suchuwaato Aagiru Chaarusu
Jii Bamujii Robaato
Suchiibun Torasukotsuto Miraado Guregorii
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.)
Dana Canada Corp
Original Assignee
Long Manufacturing 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 Long Manufacturing Ltd filed Critical Long Manufacturing Ltd
Publication of JPS5325717A publication Critical patent/JPS5325717A/en
Publication of JPS6133972B2 publication Critical patent/JPS6133972B2/ja
Granted 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
    • F28F3/00Plate-like or laminated elements; Assemblies of plate-like or laminated elements
    • F28F3/12Elements constructed in the shape of a hollow panel, e.g. with channels
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01NGAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL-COMBUSTION ENGINES
    • F01N3/00Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
    • F01N3/02Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust
    • F01N3/04Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust using liquids
    • F01N3/043Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust using liquids without contact between liquid and exhaust gases
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02MSUPPLYING COMBUSTION ENGINES IN GENERAL WITH COMBUSTIBLE MIXTURES OR CONSTITUENTS THEREOF
    • F02M26/00Engine-pertinent apparatus for adding exhaust gases to combustion-air, main fuel or fuel-air mixture, e.g. by exhaust gas recirculation [EGR] systems
    • F02M26/13Arrangement or layout of EGR passages, e.g. in relation to specific engine parts or for incorporation of accessories
    • F02M26/22Arrangement or layout of EGR passages, e.g. in relation to specific engine parts or for incorporation of accessories with coolers in the recirculation passage
    • F02M26/29Constructional details of the coolers, e.g. pipes, plates, ribs, insulation or materials
    • F02M26/32Liquid-cooled heat exchangers
    • 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
    • F28D7/00Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/10Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged one within the other, e.g. concentrically
    • F28D7/106Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged one within the other, e.g. concentrically consisting of two coaxial conduits or modules of two coaxial conduits
    • 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
    • F28D9/00Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D9/0031Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other
    • F28D9/0037Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other the conduits for the other heat-exchange medium also being formed by paired plates touching each other
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F13/00Arrangements for modifying heat-transfer, e.g. increasing, decreasing
    • F28F13/06Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F3/00Plate-like or laminated elements; Assemblies of plate-like or laminated elements
    • F28F3/08Elements constructed for building-up into stacks, e.g. capable of being taken apart for cleaning
    • F28F3/086Elements constructed for building-up into stacks, e.g. capable of being taken apart for cleaning having one or more openings therein forming tubular heat-exchange passages
    • 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
    • F28D21/00Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
    • F28D21/0001Recuperative heat exchangers
    • F28D21/0003Recuperative heat exchangers the heat being recuperated from exhaust gases
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02TCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
    • Y02T10/00Road transport of goods or passengers
    • Y02T10/10Internal combustion engine [ICE] based vehicles
    • Y02T10/12Improving ICE efficiencies

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
  • Exhaust Gas After Treatment (AREA)
  • Exhaust-Gas Circulating Devices (AREA)

Description

【発明の詳細な説明】 本発明は自動車内燃機関における排気ガス再循
環に関し、更に詳細には燃焼サイクルに戻される
排気ガスを冷却するための装置に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to exhaust gas recirculation in motor vehicle internal combustion engines, and more particularly to a device for cooling exhaust gas returned to the combustion cycle.

ほぼ1971年から、自動車産業は、自動車の安全
を増加し或は内燃機関からの排気ガスに固有の排
気物を減少するために、自動車に或は自動車の内
燃機関に、常に増加する数の要素すなわち装置を
加えることを要求されて来た。このような要素は
確実なクランクケースの換気、排気ガスの再循
環、蒸発制御装置および排気系における触媒コン
バータを含んでいる。
Since approximately 1971, the automobile industry has been adding an ever-increasing number of elements to automobiles or to automobile internal combustion engines in order to increase automobile safety or reduce the emissions inherent in exhaust gases from internal combustion engines. In other words, it has been requested that additional equipment be added. Such elements include positive crankcase ventilation, exhaust gas recirculation, evaporative control devices, and catalytic converters in the exhaust system.

主に重要なことは、内燃機関の排気ガスからの
排気物であり、その排気は、毎日多くの自動車が
走る大都市で発生するスモツグのような状態に対
し非難されて来た。窒素酸化物はこのような排気
物の一つであり、排気ガス再循環サイクルは機関
の排気ガス中にあるこれらの酸化物を減少するの
に使用される。窒素酸化物の生成は非常に高い温
度において行われかつその結果燃焼過程のピーク
温度時に発生する。窒素酸化物の生成を減少しか
つ制御するためにピーク温度をわずかに下げるこ
とが要求される。
Of primary interest are the emissions from the exhaust gases of internal combustion engines, which have been blamed for the smog-like conditions that occur in large cities with large numbers of automobiles traveling every day. Nitrogen oxides are one such exhaust gas, and exhaust gas recirculation cycles are used to reduce these oxides in engine exhaust gases. The formation of nitrogen oxides takes place at very high temperatures and therefore occurs at the peak temperatures of the combustion process. A slight reduction in peak temperature is required to reduce and control nitrogen oxide formation.

この温度の低下は、燃焼の最終生成物が比較的
不活性なガスを連続して供給するように、燃焼過
程に少量の不活性ガスを導入することによつて行
われ、それは、これらのガスを正しい比率で使用
することになる。このように再循環通路は排気マ
ニホルドに、かつ排気ガスの流れを制御するため
に取入れマニホルドに取付けられた真空被変調締
切および調節弁に接続されている。再循環通路す
なわち追加の排気ガス通路は機関に接近して置か
れ或は取入れマニホルドの複合ランナ装置内に一
体成形され得る。
This reduction in temperature is achieved by introducing a small amount of inert gas into the combustion process so that the end products of combustion are continuously supplied with relatively inert gases; will be used in the correct proportions. The recirculation passageway is thus connected to the exhaust manifold and to a vacuum modulated shutoff and control valve mounted on the intake manifold for controlling the flow of exhaust gases. Recirculation or additional exhaust gas passages may be located close to the engine or integrally formed within the composite runner arrangement of the intake manifold.

しかしながら、内燃機関サイクルからの排気ガ
スはなお非常に温度が高く、かつその温度を、ガ
スが、燃焼サイクルに再導入される前に、かなり
下げることが望ましい。
However, the exhaust gas from the internal combustion engine cycle is still very hot, and it is desirable to reduce its temperature considerably before the gas is reintroduced into the combustion cycle.

内燃機関の排気ガスを浄化する従来の装置とし
ては、例えば、実公昭37−17408号公報或は特開
昭48−59214号公報に示されるものがある。しか
しながら前者に示される装置は排気ガスの浄化を
行う室の回りに冷却液の包囲帯を形成するように
しているがその室内に浄化液を入れて浄化を行う
ようにしているため自動車などの排ガス浄化装置
としては軽量化、小型化の面で適用困難である。
Conventional devices for purifying exhaust gas from internal combustion engines include those shown in, for example, Japanese Utility Model Publication No. 37-17408 or Japanese Unexamined Patent Publication No. 48-59214. However, the device shown in the former type is designed to form an envelope of coolant around a chamber that purifies exhaust gas, but purification is performed by putting purification liquid into the chamber, so exhaust gas from automobiles, etc. It is difficult to apply it as a purification device in terms of weight reduction and miniaturization.

また後者に示される装置は、大型になつて熱効
率が悪くしかも排気ガスの熱が熱交換器の外部に
放散されるという問題がある。
Furthermore, the latter type of device has problems in that it is large in size and has poor thermal efficiency, and the heat of the exhaust gas is dissipated to the outside of the heat exchanger.

本発明が解決しようとする問題点は排ガス用の
熱交換器の小型化を図るとともに排ガスの流れ抵
抗又は圧力低下を小さくして熱効率の向上を図る
ことである。
The problem to be solved by the present invention is to reduce the size of a heat exchanger for exhaust gas, reduce the flow resistance or pressure drop of exhaust gas, and improve thermal efficiency.

上記問題を解決するため、本発明による二流体
熱交換器は、二対の金属板でつくられたほぼ平担
な熱交換器を備え、内側の対の金属板が室を形成
しかつ周辺フランジによつて接合されて向い合わ
せて配置された皿状部分を有し、その室が第1の
流体を受けるための入口および出口を有し、熱伝
達面が前記室内に受けられた少なくとも一つの金
属板で形成され、外側の対の金属板が向い合わせ
て配置された皿状部分および前記内側の金属板の
フランジにほぼ完全に接合された周辺フランジを
有し、前記外側皿状部分が室をほぼ囲みかつ中に
第2の流体を受けるための入口および出口を有す
る流体包囲帯を前記内側皿状部分と協同して形成
し、前記外側皿状部分の少なくとも一対の向い合
わせて配置された側壁が前記内側皿状部分の側壁
から隔てられ、内側の金属板の前記フランジが前
記内側の側壁と外側の側壁との間で伸びて前記包
囲帯を上部分と下部分とに分割しかつ前記上包囲
帯部分と下包囲帯部分との間を連通するための開
口を有し、前記第2の流体の入口および出口が一
方の外側皿状部分に配置され、中央のくぼみが皿
状部分を横切りかつ上包囲帯部分を入口と出口と
の間でほぼ等しい半分に分割するように外側皿状
部分に形成されて構成されている。
In order to solve the above problems, a two-fluid heat exchanger according to the present invention comprises a substantially flat heat exchanger made of two pairs of metal plates, the inner pair of metal plates forming a chamber and a peripheral flange. at least one chamber having an inlet and an outlet for receiving a first fluid, the heat transfer surface being received within the chamber; formed of metal plates, the outer pair of metal plates having oppositely disposed dish-shaped portions and a peripheral flange substantially completely joined to the flange of said inner metal plate, said outer plate-shaped portion being in a chamber; cooperating with said inner dish to form a fluid enclosure substantially surrounding said inner dish and having an inlet and an outlet for receiving a second fluid therein; a side wall is separated from the side wall of the inner dish, the flange of the inner metal plate extends between the inner and outer side walls to divide the envelope into an upper portion and a lower portion; an opening for communicating between the upper envelope portion and the lower envelope portion, the inlet and outlet for said second fluid being disposed in one of the outer dish-like portions, and a central recess extending through the dish-like portion; The outer dish is configured to cut across and divide the upper envelope portion into approximately equal halves between the inlet and the outlet.

上記構成において、第1の流体が入口から室内
に流入するとともに第2の流体が入口から内側の
金属板と外側の金属板との間に入つて前記室を囲
む第2の流体包囲帯を形成して第1の流体と第2
の流体との間で熱交換を行うとともに第1の流体
の熱が熱交換器の外部に放散するのを防止する。
熱交換の終つた第1の流体は第1の流体用の出口
からまた第2の流体は第2の流体用の出口からそ
れぞれ外部に出される。
In the above configuration, the first fluid flows into the chamber from the inlet, and the second fluid enters between the inner metal plate and the outer metal plate from the inlet to form a second fluid surrounding zone surrounding the chamber. and the first fluid and the second
The heat exchanger performs heat exchange with the first fluid and prevents the heat of the first fluid from dissipating to the outside of the heat exchanger.
The first fluid that has undergone heat exchange is discharged to the outside from the first fluid outlet, and the second fluid is discharged from the second fluid outlet.

以下図面を参照して本発明の実施例について説
明する。
Embodiments of the present invention will be described below with reference to the drawings.

第1図から第3図は、機関室の制限されたスペ
ース内に機関に沿つて容易にかつコンパクトに嵌
り得るほぼ平らな形状の本発明の一実施例の熱交
換器31を示している。この熱交換器は、一対の
対称の内側板32,32aおよび一対のほぼ同じ
外側板47,47aを含む4個の打ち抜かれた金
属板で成形されていて、内側部品すなわち内側板
はユニツトすなわち熱交換器の3側部に平らなフ
ランジ33,33aを有しかつ第4の側部に二対
の反対側に配置された浮出し部(エンボスメン
ト)35,35aが設けられたほぼ平らなフラン
ジ34,34aを有し、その浮出し部35はフラ
ンジ34,34aの平面上で伸び他の浮出し部3
5aはフランジの平面の下で伸びている。
Figures 1-3 show an embodiment of the heat exchanger 31 of the present invention having a generally flat shape that allows it to fit easily and compactly along the engine within the restricted space of the engine room. The heat exchanger is formed of four stamped metal plates including a pair of symmetrical inner plates 32, 32a and a pair of substantially identical outer plates 47, 47a, the inner parts or plates being a unit or heat exchanger. The exchanger is generally flat with flat flanges 33, 33a on three sides and provided with two pairs of oppositely disposed embossments 35, 35a on the fourth side. It has flanges 34, 34a, the raised part 35 of which extends on the plane of the flanges 34, 34a and the other raised part 3.
5a extends below the plane of the flange.

内側板32,32aは、フランジ33で終るほ
ぼ垂直の側壁37,37aおよびフランジ34で
終る壁38,38aを有する反対方向に凹んでい
る中央部分36,36aを有している。壁37,
37aは、壁38に平行でかつその壁と対向する
壁39,39aに、続いている。ほぼ円錐形の浮
出し部40,40aが中央部分36,36aに形
成されかつ浮出し部35,35aで終つていて入
口導管41および出口導管42用の開口を形成し
ている。円錐形浮出し部40,40aは第2図に
示されるように内側板32,32aに形成されて
いる。凹んだ中央部分すなわち皿状部分36,3
6aによつて形成された中央室43内には、その
室を複数の平行な流路に分割するように室内で長
手方向に伸びている複数の折曲げターブライザ4
4が置かれ、その乱流装置すなわちターブライザ
は排気ガス用の入口タンク(図示されていない)
および出口タンク46を形成するように室の端部
から少し離れて終つている。
The inner plates 32, 32a have oppositely concave central portions 36, 36a having generally vertical side walls 37, 37a terminating in a flange 33 and walls 38, 38a terminating in a flange 34. wall 37,
37a continues to walls 39, 39a parallel to and opposite wall 38. A generally conical embossment 40, 40a is formed in the central portion 36, 36a and terminates in an embossment 35, 35a forming an opening for an inlet conduit 41 and an outlet conduit 42. Conical embossments 40, 40a are formed on the inner plates 32, 32a as shown in FIG. Recessed central portion or dish-shaped portion 36,3
Within the central chamber 43 formed by 6a are a plurality of folded turbulators 4 extending longitudinally within the chamber so as to divide the chamber into a plurality of parallel flow paths.
4 is placed and its turbulence device or turbulator is connected to the inlet tank (not shown) for the exhaust gas.
and terminates a short distance from the end of the chamber to form an outlet tank 46.

外側部分47,47aは熱交換器の3側部を囲
んでフランジ33,33aを挾んでいる平らなフ
ランジ48,48aおよび第4の側部のフランジ
34,34aを挾んでいるほぼ平らなフランジ4
9,49aを有している。円錐形浮出し部50,
50aが、浮出し部35,35aと係合しかつそ
の浮出し部に固定されている外縁51,51aの
あるフランジ48,48a,49,49aによつ
て限定された中央の凹んだ部分すなわち皿状部分
52,52aに、形成されている。皿状部分5
2,52aは中に浮出し部を有する後壁45,4
5aからかつ後壁54,54aに平行な前壁5
5,55aに向つて収束している側壁53,53
aを有していて、壁は内側皿状部分36,36a
の壁の外側に隔てられいる。皿状部分52の刻み
目56は各々の内側皿状部分36と係合して皿状
部分36,36a,52,52aの間で形成され
た流体包囲帯57の上部を分割し、冷却流体の流
れを下包囲帯部分に向ける。
The outer portions 47, 47a surround three sides of the heat exchanger and include flat flanges 48, 48a sandwiching the flanges 33, 33a and a generally flat flange 4 sandwiching the fourth side flanges 34, 34a.
9,49a. conical embossment 50,
50a is a central recessed portion defined by a flange 48, 48a, 49, 49a with an outer edge 51, 51a which engages and is fixed to the embossment 35, 35a; That is, they are formed in the dish-shaped portions 52, 52a. Dish-shaped part 5
2, 52a is a rear wall 45, 4 having a raised part therein;
5a and parallel to the rear walls 54, 54a.
Side walls 53, 53 converging toward 5, 55a
a, the wall has an inner dish-shaped portion 36, 36a
separated by a wall outside. A notch 56 in the dish 52 engages each inner dish 36 to divide the upper portion of the fluid envelope 57 formed between the dish 36, 36a, 52, 52a, and to permit the flow of cooling fluid. towards the lower enveloping zone.

内側板32,32aのフランジ33は、第2図
および第3図に示されるように、流体包囲帯57
を上部分と下部分とに分割する作用をするが、流
体ポートすなわち開口58が内側部分の両端にお
いて反対に配置されたフランジ33に形成されて
包囲帯の上部分と下部分との間で流体を連通させ
る。冷却流体入口導管59および流体出口導管6
0が刻み目56に近接して上皿状部分52に固定
され、それらの導管は流体包囲帯57の上部分と
連通している。第1図において矢印によつて示さ
れるように、熱い排気ガスは導管41を通つて
(矢印A)入口タンク46内に入り、平行通路4
4を通して出口タンクを通り、かつ冷却されたガ
スは導管42(矢印B)を通して去る。冷却水
は、導管59を通して包囲帯57の上部分の半分
内に入つて開口58を通して下包囲帯部分に下降
し、下包囲帯部分を横切つて流れかつ反対側の組
の開口58を通して上包囲帯部分の他の半分内に
流れ、かつ導管60(矢印D)を通して出て排気
ガスを冷却する。
The flanges 33 of the inner plates 32, 32a form a fluid surround 57, as shown in FIGS. 2 and 3.
fluid ports or apertures 58 are formed in oppositely disposed flanges 33 at each end of the inner portion to permit fluid flow between the upper and lower portions of the envelope. communicate. Cooling fluid inlet conduit 59 and fluid outlet conduit 6
0 are fixed to the upper dished portion 52 adjacent to the notch 56 and their conduits communicate with the upper portion of the fluid surround 57 . As indicated by the arrow in FIG.
4 through the outlet tank and the cooled gas leaves through conduit 42 (arrow B). Cooling water enters the upper half of the envelope 57 through conduits 59 and descends through openings 58 into the lower envelope section, flows across the lower envelope section and through the opposite set of openings 58 into the upper envelope section. It flows into the other half of the band and exits through conduit 60 (arrow D) to cool the exhaust gas.

第4図、第5図および第6図はほぼ長方形の対
象形状を有する第2の実施例の熱交換器を示して
いる。この装置は平行な側フランジ63および曲
つた端フランジ64を有する一対の内側金属板6
2,62aを備え、その金属板は皿状端部延長部
66,66aがある対向する凹んだ部分すなわち
皿状部分65,65aを有している。皿状部分6
5,65aは、延長部66,66aが入口室およ
び出口室を形成して排気ガス用の中央室67を形
成している。延長部66の長い開口68は入口ポ
ートを形成し、長い開口69は反対側の延長部6
6で出口ポートを形成している。
4, 5 and 6 show a second embodiment of the heat exchanger having a substantially rectangular symmetrical shape. The device consists of a pair of inner metal plates 6 having parallel side flanges 63 and curved end flanges 64.
2, 62a, the metal plate having opposing recessed or dished portions 65, 65a with dished end extensions 66, 66a. Dish-shaped part 6
5, 65a, extensions 66, 66a form an inlet chamber and an outlet chamber to form a central chamber 67 for exhaust gas. An elongated opening 68 in the extension 66 forms an inlet port and an elongated opening 69 in the opposite extension 6
6 forms an outlet port.

一対の外側板71,71aはフランジ63(第
5図参照)と係合しているフランジ72および皿
状延長部66,66a(第6図)と係合している
フランジ73を有していて、その外側板は室67
の回りで冷却流体の包囲帯を形成するように皿状
部分65,65aと協働する反対側に凹んだ部分
すなわち皿状部分74,74aを有している。第
5図に示されるように、皿状部分65,65aの
壁75は、側フランジ63が流体の包囲帯を上部
分77と下部分78とにそれぞれ分割するように
して皿状部分74,74aの壁76の内側で隔て
られ、かつこれらの二つの部分を連通するために
開口79が設けられている。浮出し部80は、冷
却流体の包囲帯内に伸びるように、好ましくは外
側板71,71aに形成される。
The pair of outer plates 71, 71a have a flange 72 that engages a flange 63 (see FIG. 5) and a flange 73 that engages a dished extension 66, 66a (see FIG. 6). , its outer plate is chamber 67
It has oppositely recessed portions or dished portions 74, 74a which cooperate with the dished portions 65, 65a to form a cooling fluid envelope therearound. As shown in FIG. 5, the walls 75 of the dished portions 65, 65a are arranged in the dished portions 74, 74a such that the side flanges 63 divide the fluid envelope into an upper portion 77 and a lower portion 78, respectively. an opening 79 is provided to communicate these two parts. A raised portion 80 is preferably formed on the outer plates 71, 71a so as to extend into the cooling fluid envelope.

外側板71は中央のくぼみ82の一側部の皿状
部分74に形成された流体入口導管81およびく
ぼみの反対側に近接した流体出口導管83を有し
ている。中央の横方向に長いくぼみ82は皿状部
分74を横切つて伸びかつ内側に伸長して内側板
62の皿状部分65に接してそこに接合されてい
る。くぼみ82は上包囲帯部分77を二つに分け
て流体の所望の流れパターンを与えている。
The outer plate 71 has a fluid inlet conduit 81 formed in the dished portion 74 on one side of the central recess 82 and a fluid outlet conduit 83 adjacent the opposite side of the recess. A central laterally elongated recess 82 extends across the dish 74 and extends inwardly to abut and join the dish 65 of the inner plate 62. Recess 82 bisects upper envelope portion 77 to provide the desired flow pattern of fluid.

使用時、熱い排気ガスは入口室の入口ポート6
8に入りかつ複数の折曲げ金属板84が複数の流
路を形成している中央室内を通過する。冷却され
たガスは出口室内に流れかつポート69を介して
出る。水のような冷却流体は導管81を介して上
包囲帯部分77に入るが、くぼみ82によつて出
口導管83に直接流れるのが阻止される。このよ
うに、流体は端部86における開口79を通して
上部分から下包囲帯部分に流れ、端部87におけ
る開口87まで部分78を横切り、かつ上包囲帯
部分77に入つて出口導管を介して出る。皿状部
分74,74a(第5図を参照せよ)に形成され
たリブすなわちくぼみ80は包囲帯内での流体の
直線的流れを阻止しかつ流体を乱して熱伝達を強
めかつ冷却流体の流れが溝流(channelling)と
なるのを阻止する。
In use, the hot exhaust gas is transferred to the inlet port 6 of the inlet chamber.
8 and passes through a central chamber in which a plurality of bent metal plates 84 form a plurality of channels. The cooled gas flows into the outlet chamber and exits through port 69. Cooling fluid, such as water, enters upper envelope portion 77 via conduit 81 but is prevented from flowing directly to outlet conduit 83 by recess 82 . Fluid thus flows from the top to the lower envelope section through opening 79 at end 86, across section 78 to opening 87 at end 87, and enters upper envelope section 77 and exits via the outlet conduit. . Ribs or depressions 80 formed in the dished portions 74, 74a (see FIG. 5) prevent straight flow of fluid within the enclosure and disrupt the fluid to enhance heat transfer and increase cooling fluid flow. Prevents flow from channelling.

第7図から第9図は、排気ガス入口および出口
の位置決めを除いては第4図から第6図に示され
た熱交換器と同じである他の熱交換器91を示し
ている。この熱交換器91は周囲にフランジ93
を有しかつ中央室95を形成している両側に配置
された凹んだ部分すなわち皿状部分94,94a
を限定している一対の内側板92,92aを使用
している。外側金属板96,96aは外周フラン
ジ97および両側の凹んだ部分すなわち皿状部分
98,98aを有している。第8図に示されるよ
うに、排気ガス入口99および排気ガス出口10
1は、板が導管を形成するように寄せられて両板
92,96を通して形成される。部分的に折り曲
げられた金属板102が室95内に置かれて熱ガ
スの流れを分割しかつ包囲帯内の冷却流体への熱
伝達を強める。
FIGS. 7-9 show another heat exchanger 91 that is the same as the heat exchanger shown in FIGS. 4-6 except for the positioning of the exhaust gas inlet and outlet. This heat exchanger 91 has a flange 93 around it.
recessed or dish-shaped portions 94, 94a located on both sides and forming a central chamber 95;
A pair of inner plates 92, 92a are used to limit the area. The outer metal plates 96, 96a have an outer peripheral flange 97 and recessed or dished portions 98, 98a on both sides. As shown in FIG. 8, an exhaust gas inlet 99 and an exhaust gas outlet 10
1 is formed through both plates 92, 96 brought together so that the plates form a conduit. A partially bent metal plate 102 is placed within chamber 95 to divide the flow of hot gas and enhance heat transfer to the cooling fluid within the envelope.

皿状部分間の間隙は上部分103および下部分
104を有する流体の包囲帯を形成する。長い中
央のくぼみすなわちリブ105が板に形成されか
つ上包帯部分103を二つの室に分割するように
内側板92と係合していて、外側板96の流体取
入れ導管106はリブ105の一側部の室と連通
しかつ流体出口導管107が反対の室と連通して
いる。複数の開口108が導管106に近接して
皿状部分94,94aおよび98,98aの隔て
られた壁の間でフランジ93に形成されかつ第2
組の開口が出口導管に隣接してフランジ93に形
成されている。排気ガスおよび冷却水の流れは熱
交換器61と実質的に同じ通路になる。
The gap between the dished portions forms a fluid envelope having an upper portion 103 and a lower portion 104. A long central recess or rib 105 is formed in the plate and engages the inner plate 92 to divide the upper bandage portion 103 into two chambers, with a fluid intake conduit 106 in the outer plate 96 on one side of the rib 105. one chamber and a fluid outlet conduit 107 communicates with the opposite chamber. A plurality of apertures 108 are formed in the flange 93 adjacent the conduit 106 and between the spaced walls of the dished portions 94, 94a and 98, 98a and
A set of openings are formed in flange 93 adjacent the outlet conduit. The flow of exhaust gas and cooling water is substantially in the same path as the heat exchanger 61.

明らかに第1図から第3図、第4図から第6図
および第7図から第9図の実施例において水の接
続は、冷却流体の最も効果的な分配および循環を
行うために外側包囲帯内に位置決めされ得て内側
室内の折りたたまれた金属板は排気ガスから包囲
内の冷却流体への熱伝達を効果的に行うために熱
ガス流を小さな流れに分ける作用をする。冷却流
体の流れは、冷却流体ジヤケツトが一部に集中さ
れた高温区域を被つて、ガス流と同方向の流れで
も逆方向の流れでもよい。いくつかの実施例およ
び流れパターンが説明のために示されたが本発明
は図示のものに限定されるものではない。
Obviously in the embodiments of FIGS. 1-3, 4-6 and 7-9 the water connections are connected to the outer enclosure to provide the most effective distribution and circulation of the cooling fluid. Folded metal plates within the inner chamber, which may be positioned within the band, serve to divide the hot gas flow into smaller streams for effective heat transfer from the exhaust gases to the cooling fluid within the enclosure. The flow of cooling fluid may be co-flowing or counter-flowing with the flow of gas, with the cooling fluid jacket overlying the concentrated hot area. Although several embodiments and flow patterns are shown for illustrative purposes, the invention is not limited to what is shown.

熱交換器のために選ばれた材料は腐食性排気ガ
スの環境から腐食に対して高い抵抗を有し好まし
い材料はタイプ304ステンレススチールのよう
なステンレススチールである。
The material selected for the heat exchanger has a high resistance to corrosion from corrosive exhaust gas environments and the preferred material is stainless steel, such as type 304 stainless steel.

以上の説明から明らかなように本発明による熱
交換器は、極めてコンパクトで、構造が簡単であ
り、流れ抵抗或は圧力降下が小さくて熱効率が良
く、しかも安価に製造できるという効果を有す
る。
As is clear from the above description, the heat exchanger according to the present invention is extremely compact, has a simple structure, has low flow resistance or pressure drop, has good thermal efficiency, and has the advantage of being inexpensive to manufacture.

【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第1の実施例の斜
視図、第2図は第1図の線5−5に沿つて切断し
た断面図、第3図は第1図の線6−6に沿つて切
つた部分断面図、第4図は熱交換器の第2の実施
例の上平面図、第5図は第4図の線8−8に沿つ
て切つた断面図、第6図は第4図の線9―9に沿
つて切つた部分断面図、第7図は熱交換器の第3
の実施例の上平面図、第8図は第7図の線11―
11に沿つて切つた断面図、第9図は第7図の線
12―12に沿つて切つた部分断面図である。 32,32a:金属板、33,33a:周辺フ
ランジ、34,34a:周辺フランジ、36,3
6a:皿状部分、43:室、47,47a:金属
板、48,48a:周辺フランジ、49,49
a:周辺フランジ、52,52a:皿状部分、5
7:包囲帯、65,65a:皿状部分、66,6
6a:延長部、68:入口、69:出口、80:
リブ、74,74a:皿状部分、77,78:包
囲、94,94a:皿状部分、98,98a:皿
状部分、99:入口、101:出口。
1 is a perspective view of a first embodiment of the heat exchanger of the present invention, FIG. 2 is a sectional view taken along line 5--5 in FIG. 1, and FIG. 3 is a cross-sectional view taken along line 6 in FIG. 1. 4 is a top plan view of the second embodiment of the heat exchanger; FIG. 5 is a sectional view taken along line 8--8 of FIG. 4; Figure 6 is a partial cross-sectional view taken along line 9--9 in Figure 4, and Figure 7 is the third section of the heat exchanger.
FIG. 8 is a top plan view of the embodiment of FIG.
9 is a partial cross-sectional view taken along line 12--12 of FIG. 7. 32, 32a: Metal plate, 33, 33a: Peripheral flange, 34, 34a: Peripheral flange, 36, 3
6a: Dish-shaped portion, 43: Chamber, 47, 47a: Metal plate, 48, 48a: Peripheral flange, 49, 49
a: Peripheral flange, 52, 52a: Dish-shaped portion, 5
7: Surrounding zone, 65, 65a: Dish-shaped portion, 66, 6
6a: extension, 68: entrance, 69: exit, 80:
Ribs, 74, 74a: dish-shaped part, 77, 78: surrounding, 94, 94a: dish-shaped part, 98, 98a: dish-shaped part, 99: inlet, 101: outlet.

Claims (1)

【特許請求の範囲】 1 二対の金属板でつくられたほぼ平担な熱交換
器を備え、内側の対の金属板が室を形成しかつ周
辺フランジによつて接合されて向い合わせて配置
された皿状部分を有し、その室が第1の流体を受
けるための入口および出口を有し、熱伝達面が前
記室内に受けられた少なくとも一つの金属板で形
成され、外側の対の金属板が向い合わせて配置さ
れた皿状部分および前記内側の金属板のフランジ
にほぼ完全に接合された周辺フランジを有し、前
記外側皿状部分が室をほぼ囲みかつ中に第2の流
体を受けるための入口および出口を有する流体包
囲帯を前記内側皿状部分と協同して形成し、前記
外側皿状部分の少なくとも一対の向い合わせて配
置された側壁が前記内側皿状部分の側壁から隔て
られ、内側の金属板の前記フランジが前記内側の
側壁と外側の側壁との間で伸びて前記包囲帯を上
部分と下部分に分割しかつ前記上包囲帯部分と下
包囲帯部分との間を連通するための開口を有し、
前記第2の流体の入口および出口が一方の外側皿
状部分に配置され、中央のくぼみが皿状部分を横
切りかつ上包囲帯部分を入口と出口との間でほぼ
等しい半分に分割するように外側皿状部分に形成
されている二流体熱交換器。 2 第2の流体の流れが入口および対応する上包
囲帯部分の半分に入り、入口に隣接する内側フラ
ンジ内の開口を通過し、熱交換器の反対側におけ
る内側フランジの開口まで下包囲帯部分を通過
し、反対側の上包囲帯部分の半分に入りかつ出口
から出る特許請求の範囲第1項に記載の二流体熱
交換器。 3 前記第1の流体の入口および出口が熱交換器
の両端に隣接して内側および外側皿状部分の一対
の整合された側壁に配置され、前記第1の流体の
入口および出口を受けている熱交換器の側部の前
記内側および外側フランジが入口および出口の回
りで浮出し成形され、前記室が前記第1の流体の
入口および出口と整合された入口部分および出口
部分を有し、前記部分的に折り曲げられた金属シ
ートが前記入口室部分と出口室部分との間で縦方
向に伸びている特許請求の範囲第1項に記載の二
流体熱交換器。 4 前記内側および外側フランジの前記浮出し部
がそれぞれ前記内側皿状部分および外側皿状部分
に合体している特許請求の範囲第3項に記載の二
流体熱交換器。 5 前記内側皿状状部分は外側フランジを越えて
突出している両側に配置された皿状延長部が設け
られかつ前記第1の流体入口および出口は前記延
長部に配置されている特許請求の範囲第1項に記
載の二流体熱交換器。 6 前記内側皿状延長部が二つの平行な側部に配
置され、二つの外側皿状部分が二つの平行な側部
上で内側皿状部分を越えて伸びている特許請求の
範囲第5項に記載の二流体熱交換器。 7 前記中央の室内の前記第1の流体の流れが前
記外側包囲帯の前記第2の流体の流れをほぼ横切
る特許請求の範囲第6項に記載の二流体熱交換
器。 8 前記外側皿状部分に形成されかつ前記流体の
包囲帯部分内に伸びている複数の流れをそらせリ
ブを備えている特許請求の範囲第7項に記載の二
流体熱交換器。 9 前記第2の流体の入口および出口が中央のく
ぼみに隣接して一方の外側皿状部分の中央に配置
され、前記第1の流体の入口および出口が一方の
外側皿状部分の中央に配置されかつ中央のくぼみ
の両側で前記内側の皿状部分を通して伸び、前記
第1の流体の入口および出口が互いにひだ付けさ
れている前記隣接する内側皿状部分と外側皿状部
分のフレア部分により限定されている特許請求の
範囲第1項に記載の二流体熱交換器。 10 前記熱交換面が前記室内にありかつ一対の
向い合わさつた端部の近くで終つている部分的に
折りたたまれた金属板を有する特許請求の範囲第
1項に記載の二流体熱交換器。
[Claims] 1. A substantially flat heat exchanger made of two pairs of metal plates, the inner pair of metal plates forming a chamber and being joined by a peripheral flange and arranged facing each other. a chamber having an inlet and an outlet for receiving a first fluid, a heat transfer surface formed by at least one metal plate received within the chamber, and an outer pair of a metal plate having oppositely disposed dish-like portions and a peripheral flange substantially completely joined to the flange of said inner metal plate, said outer dish-like portion generally surrounding a chamber and having a second fluid therein; a fluid surround having an inlet and an outlet for receiving fluidic fluid in cooperation with said inner dish, wherein at least one pair of oppositely disposed side walls of said outer dish extends from a side wall of said inner dish. separated, the flange of the inner metal plate extending between the inner sidewall and the outer sidewall to divide the envelope into an upper portion and a lower portion and between the upper and lower envelope portions. has an opening for communication between the
said second fluid inlet and outlet are disposed in one outer dish, such that a central recess crosses the dish and divides the upper envelope portion into approximately equal halves between the inlet and the outlet; A two-fluid heat exchanger formed in the outer dish-shaped part. 2 A second fluid flow enters the inlet and corresponding half of the upper envelope section, passes through an opening in the inner flange adjacent the inlet, and passes through the lower envelope section to the opening in the inner flange on the opposite side of the heat exchanger. 2. A two-fluid heat exchanger as claimed in claim 1, in which the heat exchanger passes through the opposite half of the upper envelope section and exits from the outlet. 3 said first fluid inlet and outlet are disposed adjacent opposite ends of the heat exchanger in a pair of aligned side walls of the inner and outer dished portions and receiving said first fluid inlet and outlet; the inner and outer flanges of the sides of the heat exchanger are embossed around the inlet and outlet, the chamber having inlet and outlet portions aligned with the first fluid inlet and outlet; A two-fluid heat exchanger according to claim 1, wherein said partially folded metal sheet extends longitudinally between said inlet chamber portion and outlet chamber portion. 4. A two-fluid heat exchanger according to claim 3, wherein the raised portions of the inner and outer flanges are integrated into the inner and outer dish portions, respectively. 5. The inner dished portion is provided with a bilaterally disposed dished extension projecting beyond the outer flange, and the first fluid inlet and outlet are located in the extension. The two-fluid heat exchanger according to item 1. 6. Claim 5, wherein the inner dished extension is arranged on two parallel sides, and the two outer dished parts extend beyond the inner dished part on the two parallel sides. The two-fluid heat exchanger described in . 7. The two-fluid heat exchanger of claim 6, wherein the first fluid flow in the central chamber substantially crosses the second fluid flow in the outer envelope. 8. A two-fluid heat exchanger as claimed in claim 7, including a plurality of flow diverting ribs formed in said outer dish and extending into said fluid envelope portion. 9 said second fluid inlet and outlet are centrally located on one outer dish adjacent to a central recess, and said first fluid inlet and outlet are centrally located on one outer dish. and extending through the inner dish on either side of a central recess, defined by flared portions of the adjacent inner dish and outer dish, with the first fluid inlet and outlet being pleated to each other. A two-fluid heat exchanger according to claim 1. 10. The two-fluid heat exchanger of claim 1, wherein said heat exchange surface comprises a partially folded metal plate within said chamber and terminating near a pair of opposing ends.
JP9655377A 1976-08-23 1977-08-11 Exhaust gas heat exchanger Granted JPS5325717A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US71662876A 1976-08-23 1976-08-23

Publications (2)

Publication Number Publication Date
JPS5325717A JPS5325717A (en) 1978-03-09
JPS6133972B2 true JPS6133972B2 (en) 1986-08-05

Family

ID=24878784

Family Applications (2)

Application Number Title Priority Date Filing Date
JP9655377A Granted JPS5325717A (en) 1976-08-23 1977-08-11 Exhaust gas heat exchanger
JP60175638A Granted JPS6183881A (en) 1976-08-23 1985-08-09 Two fluid heat exchanger

Family Applications After (1)

Application Number Title Priority Date Filing Date
JP60175638A Granted JPS6183881A (en) 1976-08-23 1985-08-09 Two fluid heat exchanger

Country Status (7)

Country Link
JP (2) JPS5325717A (en)
AU (1) AU518454B2 (en)
CA (1) CA1090778A (en)
DE (2) DE2733215C3 (en)
FR (1) FR2363073A1 (en)
GB (2) GB1579276A (en)
SE (2) SE429675B (en)

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JPS5763123U (en) * 1980-09-30 1982-04-15
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Also Published As

Publication number Publication date
JPS6183881A (en) 1986-04-28
JPS6223236B2 (en) 1987-05-21
SE7708696L (en) 1978-02-24
DE2733215B2 (en) 1980-10-23
AU518454B2 (en) 1981-10-01
SE8303353L (en) 1983-06-13
AU2655677A (en) 1979-01-04
SE8303353D0 (en) 1983-06-13
DE2733215A1 (en) 1978-03-09
GB1579275A (en) 1980-11-19
DE2733215C3 (en) 1981-06-25
CA1090778A (en) 1980-12-02
GB1579276A (en) 1980-11-19
FR2363073A1 (en) 1978-03-24
SE429675B (en) 1983-09-19
JPS5325717A (en) 1978-03-09
DE2759785C2 (en) 1985-04-04
FR2363073B1 (en) 1982-06-11

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