JP2007046869A - Evaporator - Google Patents

Evaporator Download PDF

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JP2007046869A
JP2007046869A JP2005234018A JP2005234018A JP2007046869A JP 2007046869 A JP2007046869 A JP 2007046869A JP 2005234018 A JP2005234018 A JP 2005234018A JP 2005234018 A JP2005234018 A JP 2005234018A JP 2007046869 A JP2007046869 A JP 2007046869A
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heat exchange
fin
pipe
plate
straight pipe
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JP4796800B2 (en
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Shigeo Marukasa
茂男 丸笠
Akio Kurihara
明男 栗原
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Resonac Holdings Corp
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Showa Denko KK
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Priority to JP2005234018A priority Critical patent/JP4796800B2/en
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F1/00Tubular elements; Assemblies of tubular elements
    • F28F1/10Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
    • F28F1/12Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element
    • F28F1/24Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending transversely
    • F28F1/32Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending transversely the means having portions engaging further tubular elements
    • 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
    • F28D1/00Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators
    • F28D1/02Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid
    • F28D1/04Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits
    • F28D1/047Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits the conduits being bent, e.g. in a serpentine or zig-zag
    • F28D1/0477Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits the conduits being bent, e.g. in a serpentine or zig-zag the conduits being bent in a serpentine or zig-zag

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

Abstract

<P>PROBLEM TO BE SOLVED: To provide an evaporator capable of preventing degradation of cooling performance over a long time. <P>SOLUTION: This evaporator 1 is provided with: a plurality of fin groups 3 each comprising a plurality of plate fins 2 made of aluminum and arranged at intervals in the ventilation direction; a first heat exchange tube 4 comprising a plurality of straight tube parts 5 fixed to the plate fins 2 of the respective fin groups 3 in a piercing form and bent tube parts 6 and 7 each connecting two of the straight tube parts 5 adjacent to each other; and a second heat exchange tube 8 comprising a plurality of straight tube parts 9 and bent tube parts 11 and 12 each connecting two of the straight tube parts 9 adjacent to each other and connected to one end of the first heat exchange tube 4. Cutouts 17 are formed at corner parts of the plate fins 2 of two of the fin groups 3 adjacent to each other. Fitting-in parts 19 are formed by the cutouts 17 of the plate fins 2 of both the fin groups 3 adjacent to each other in the airflow direction. The straight tube parts 9 of the second heat exchange tube 8 are brought into contact with the plate fins 2 of both the fin groups 3 in a state fitted in the fitting-in parts 19. <P>COPYRIGHT: (C)2007,JPO&INPIT

Description

この発明は蒸発器に関し、さらに詳しくは、たとえば冷蔵庫、冷蔵ショーケースなどの冷蔵装置に用いられる冷凍サイクルにおいて、蒸発器として好適に使用される蒸発器に関する。   The present invention relates to an evaporator, and more particularly to an evaporator suitably used as an evaporator in a refrigeration cycle used in a refrigeration apparatus such as a refrigerator or a refrigerated showcase.

この明細書および特許請求の範囲において、「アルミニウム」という用語には、純アルミニウムの他にアルミニウム合金を含むものとする。   In this specification and claims, the term “aluminum” includes aluminum alloys in addition to pure aluminum.

たとえば冷蔵庫の断熱箱体内には、圧縮機、凝縮器および蒸発器を備えた冷凍サイクルが設置されている。このような冷凍サイクルの蒸発器として、並列状に配置された複数のプレートフィンからなり、かつ空気流れ方向に間隔をおいて複数設けられたフィン群と、各フィン群のすべてのプレートフィンに貫通状に固定された複数の直管部および隣り合う2つの直管部を接続しかつ直管部より1つ少ない数の屈曲管部よりなる蛇行状の熱交換管とを備えたものが広く用いられている。   For example, a refrigeration cycle including a compressor, a condenser, and an evaporator is installed in a heat insulating box of a refrigerator. As an evaporator of such a refrigeration cycle, a plurality of fins arranged in parallel and spaced apart in the air flow direction, and all the plate fins of each fin group are penetrated. Widely used are a plurality of straight pipe parts fixed in a shape and two meandering pipe parts connected to each other and a meandering heat exchange pipe made up of one less number of bent pipe parts than the straight pipe parts. It has been.

ところで、このような蒸発器においては、空気中の水分により熱交換管の直管部における各プレートフィンを貫通している部分の外周面に着霜が発生するとともに、各プレートフィンに、直管部が貫通した部分を中心として着霜が発生する。各プレートフィンにおける着霜は、直管部の近傍でかなり厚肉となり、直管部から遠ざかるにつれて徐々に薄肉となる。このような着霜が発生すると、霜が抵抗となって各フィン群のプレートフィン間を流れる空気量が急激に減少したり、あるいは空気と熱交換管内を流れる冷媒との間での伝熱量が急激に減少したりすることによって、比較的短時間で冷却性能が低下するという問題がある。このような冷却性能の低下は、特に着霜量が多くなる空気流れ上流側で顕著である。   By the way, in such an evaporator, the moisture in the air causes frost formation on the outer peripheral surface of the portion passing through each plate fin in the straight tube portion of the heat exchange tube, and each plate fin has a straight tube. Frosting occurs around the part through which the part penetrates. The frost on each plate fin becomes considerably thick near the straight pipe portion and gradually becomes thin as the distance from the straight pipe portion increases. When such frost formation occurs, the amount of air flowing between the plate fins of each fin group becomes abruptly reduced due to frost, or the amount of heat transfer between the air and the refrigerant flowing in the heat exchange pipe is reduced. There is a problem that the cooling performance is lowered in a relatively short time due to a rapid decrease. Such a decrease in cooling performance is particularly remarkable on the upstream side of the air flow where the amount of frost formation increases.

そこで、従来から種々の除霜装置が用いられており、その具体例が特許文献1に記載されている。特許文献1に記載された第1の除霜装置は、断熱箱体内における蒸発器の下方に、輻射熱により蒸発器を加熱する除霜ヒータが設けられたものである(特許文献1、段落0035、図1参照)。また、第2の除霜装置は、蛇行状のパイプヒータが、蒸発器のプレートフィンに形成された切り欠き内に嵌め入れられたものである(特許文献1、段落0062〜0066、図7参照)。 しかしながら、特許文献1記載の2つの除霜装置を用いたとしても、上述したような着霜が発生する限り、頻繁に除霜を行わなければならない。
特開2002−130918号公報
Therefore, various defrosting devices have been used conventionally, and specific examples thereof are described in Patent Document 1. The first defrosting device described in Patent Document 1 is provided with a defrosting heater for heating the evaporator by radiant heat below the evaporator in the heat insulating box (Patent Document 1, paragraph 0035, (See FIG. 1). In the second defrosting device, a meandering pipe heater is fitted into a notch formed in a plate fin of an evaporator (see Patent Document 1, paragraphs 0062 to 0066, FIG. 7). ). However, even if the two defrosting devices described in Patent Document 1 are used, defrosting must be frequently performed as long as frost formation as described above occurs.
JP 2002-130918 A

この発明の目的は、上記問題を解決し、比較的長時間にわたって冷却性能の低下を防止しうる蒸発器を提供することにある。   An object of the present invention is to provide an evaporator that solves the above-described problems and can prevent a decrease in cooling performance for a relatively long time.

本発明は、上記目的を達成するために以下の態様からなる。   In order to achieve the above object, the present invention comprises the following aspects.

1)並列状に配置された複数のプレートフィンと、プレートフィンに貫通状に固定された複数の直管部および隣り合う2つの直管部を接続しかつ直管部より1つ少ない数の屈曲管部よりなる第1熱交換管と、複数の直管部および隣り合う2つの直管部を接続しかつ直管部より1つ少ない数の屈曲管部よりなるとともに、第1熱交換管の一端に接続された第2熱交換管とを備えており、第2熱交換管の直管部がプレートフィンに接触させられている冷凍冷蔵庫用蒸発器。   1) A plurality of plate fins arranged in parallel, a plurality of straight pipe portions fixed in a penetrating manner to the plate fins, and two adjacent straight pipe portions connected to each other and bent by one less than the straight pipe portions A first heat exchange pipe composed of a pipe section, a plurality of straight pipe sections and two adjacent straight pipe sections connected to each other, and one less bent pipe section than the straight pipe section; The evaporator for refrigerators which is provided with the 2nd heat exchange pipe connected to one end, and the straight pipe part of the 2nd heat exchange pipe is made to contact the plate fin.

2)第2熱交換管の直管部が、プレートフィンにおける空気流れ方向および第1熱交換管の直管部と直交する方向の側縁部に接触している上記1)記載の蒸発器。   2) The evaporator according to 1) above, wherein the straight pipe portion of the second heat exchange tube is in contact with the air flow direction in the plate fin and the side edge portion in the direction orthogonal to the straight pipe portion of the first heat exchange pipe.

3)第2熱交換管の直管部が、空気流れ方向の全体にわたってプレートフィンに接触させられている上記2)記載の蒸発器。   3) The evaporator according to 2) above, wherein the straight pipe portion of the second heat exchange pipe is in contact with the plate fin in the entire air flow direction.

4)第2熱交換管の空気流れ方向に隣り合う直管部間のピッチが、すべて均一になっている上記3)記載の蒸発器。   4) The evaporator according to 3) above, wherein the pitch between the straight pipe portions adjacent to each other in the air flow direction of the second heat exchange pipe is uniform.

5)第2熱交換管の空気流れ方向に隣り合う直管部間のピッチが、空気流れ方向下流側において同上流側よりも小さくなっている上記3)記載の蒸発器。   5) The evaporator according to 3) above, wherein the pitch between the straight pipe portions adjacent to each other in the air flow direction of the second heat exchange pipe is smaller on the downstream side in the air flow direction than on the upstream side.

6)第2熱交換管の直管部が、空気流れ方向上流側においてプレートフィンに接触している上記2)記載の蒸発器。   6) The evaporator according to 2) above, wherein the straight pipe portion of the second heat exchange pipe is in contact with the plate fin on the upstream side in the air flow direction.

7)並列状に配置された複数のプレートフィンからなるフィン群が、空気流れ方向に間隔をおいて複数設けられている上記1)〜6)のうちのいずれかに記載の蒸発器。   7) The evaporator according to any one of 1) to 6) above, wherein a plurality of fin groups including a plurality of plate fins arranged in parallel are provided at intervals in the air flow direction.

8)すべてのフィン群のプレートフィンが平板状である上記7)記載の蒸発器。   8) The evaporator according to 7) above, wherein the plate fins of all fin groups are flat.

9)空気流れ方向下流側のフィン群のプレートフィンの伝熱面積が、空気流れ方向上流側のフィン群のプレートフィンの伝熱面積よりも大きくなっている上記7)記載の蒸発器。   9) The evaporator according to 7) above, wherein the heat transfer area of the plate fins in the fin group on the downstream side in the air flow direction is larger than the heat transfer area of the plate fins in the fin group on the upstream side in the air flow direction.

10)空気流れ方向上流側のフィン群のプレートフィンが平板状であり、空気流れ方向下流側のフィン群のプレートフィンが波板状である上記9)記載の蒸発器。   10) The evaporator according to 9) above, wherein the plate fins of the fin group on the upstream side in the air flow direction are flat and the plate fins of the fin group on the downstream side in the air flow direction are corrugated.

11)空気流れ方向下流側のフィン群のフィンピッチが、空気流れ方向上流側のフィン群のフィンピッチよりも小さくなっている上記7)〜10)のうちのいずれかに記載の蒸発器。   11) The evaporator according to any one of the above items 7) to 10), wherein the fin pitch of the fin group on the downstream side in the air flow direction is smaller than the fin pitch of the fin group on the upstream side in the air flow direction.

12)各フィン群のすべてのプレートフィンに、第1熱交換管の2つの直管部が貫通状に固定されている上記7)〜11)のうちのいずれかに記載の蒸発器。   12) The evaporator according to any one of 7) to 11) above, wherein two straight pipe portions of the first heat exchange pipe are fixed in a penetrating manner to all the plate fins of each fin group.

13)第2熱交換管の直管部が、プレートフィンに形成された切り欠きからなる嵌入部内に嵌め入れられた状態でプレートフィンに接触させられている上記7)〜12)のうちのいずれかに記載の蒸発器。   13) Any one of the above 7) to 12), wherein the straight pipe portion of the second heat exchange pipe is brought into contact with the plate fin in a state of being fitted into a fitting portion made of a notch formed in the plate fin. The evaporator according to crab.

14)空気流れ方向に隣り合う2つのフィン群のプレートフィンの角部に切り欠きが形成され、空気流れ方向に隣り合う両フィン群のプレートフィンの切り欠きにより嵌入部が設けられ、第2熱交換管の直管部が、嵌入部内に嵌め入れられた状態で両フィン群のプレートフィンに接触させられている上記13)記載の蒸発器。   14) Notches are formed in the corners of the plate fins of the two fin groups adjacent to each other in the air flow direction, and fitting portions are provided by the notches of the plate fins of both fin groups adjacent in the air flow direction. The evaporator according to 13) above, wherein the straight pipe portion of the exchange pipe is brought into contact with the plate fins of both fin groups in a state of being fitted into the fitting portion.

15)プレートフィンにおける切り欠きの周縁部に、直管部の外周面に面接触するカラーが一体に形成されている上記13)または14)記載の蒸発器。   15) The evaporator according to 13) or 14) above, wherein a collar that is in surface contact with the outer peripheral surface of the straight pipe portion is integrally formed at a peripheral portion of the notch in the plate fin.

16)すべてのフィン群におけるプレートフィンの並び方向の外側にそれぞれ側板が配置され、両側板に、それぞれ第1熱交換管の屈曲管部および屈曲管部により接続された2つの直管部の端部が通される貫通穴と、第2熱交換管の直管部の端部が嵌る切り欠きとが形成され、側板における切り欠きの両側にそれぞれ固定片が形成され、第2熱交換管の直管部の端部が、側板の切り欠き内に嵌め入れられるとともに両固定片により挟着固定されている上記7)〜15)のうちのいずれかに記載の蒸発器。   16) Ends of two straight pipe portions, in which side plates are arranged on the outer sides of the plate fins in all fin groups, and are connected to both side plates by the bent pipe portion and the bent pipe portion of the first heat exchange pipe, respectively. A through hole through which the portion passes and a notch into which an end of the straight pipe portion of the second heat exchange pipe fits, and fixing pieces are formed on both sides of the notch in the side plate, The evaporator according to any one of 7) to 15), wherein an end portion of the straight pipe portion is fitted into a notch of the side plate and is sandwiched and fixed by both fixing pieces.

17)プレートフィンと、第1および第2熱交換管がアルミニウムからなる上記1)〜16)のうちのいずれかに記載の蒸発器。   17) The evaporator according to any one of 1) to 16) above, wherein the plate fins and the first and second heat exchange tubes are made of aluminum.

18)ヘアピン状管と、複数の直管部および隣り合う2つの直管部を接続しかつ直管部より1つ少ない数の屈曲管部よりなる第2熱交換管と、2つの貫通穴を有する複数のプレートフィンとを用意すること、各プレートフィンの各角部に切り欠きを形成しておくこと、ヘアピン状管の両直管部をそれぞれすべてのプレートフィンの貫通穴に通すとともにプレートフィンに固定することにより、複数の並列状プレートフィンからなるフィン群を直管部の長さ方向に間隔をおいて複数設けること、フィン付きヘアピン状管を、直管部の長さ方向に関して同一位置にあるフィン無し部において曲げるとともに、隣り合う2つのフィン無し部での曲げ方向を逆向きにすることにより両直管部を蛇行状とし、フィン付き第1熱交換管を形成すること、第2熱交換管の直管部を、フィン付き第1熱交換管の隣り合う2つのフィン群のプレートフィンの角部に形成された切り欠きからなる嵌入部内に嵌め入れること、ならびに第1熱交換管の一端部と第2熱交換管の一端部とを接合することを含む蒸発器の製造方法。   18) A hairpin tube, a plurality of straight pipe portions and two adjacent straight pipe portions, a second heat exchange pipe comprising a number of bent pipe portions, one less than the straight pipe portion, and two through holes Preparing a plurality of plate fins, forming notches at each corner of each plate fin, passing both straight pipe portions of the hairpin tube through the through holes of all plate fins, and plate fins A plurality of fin groups composed of a plurality of parallel plate fins spaced apart in the length direction of the straight tube portion, and the hairpin tube with fins at the same position with respect to the length direction of the straight tube portion. Forming a first heat exchange tube with fins by bending both straight pipe portions in a meandering manner by bending the two fin-less portions adjacent to each other and reversing the bending direction of two adjacent fin-less portions. heat The straight pipe portion of the exchange tube is fitted into the fitting portion formed of a notch formed in the corner portion of the plate fin of the two adjacent fin groups of the first heat exchange tube with fins, and the first heat exchange tube The manufacturing method of the evaporator including joining one end part and the one end part of a 2nd heat exchange pipe.

19)フィン付き第1熱交換管の屈曲管部および屈曲管部により接続された2つの直管部の端部が通される貫通穴と、第2熱交換管の直管部の端部が嵌る切り欠きと、各切り欠きの両側にそれぞれ形成された固定片とを有する1対の側板を用意すること、第2熱交換管の直管部を、フィン付き第1熱交換管の隣り合う2つのフィン群のプレートフィンの角部に形成された切り欠きからなる嵌入部内に嵌め入れた後、両側板を、フィン付き第1熱交換管におけるすべてのフィン群のプレートフィンの並び方向の外側に配置すること、フィン付き第1熱交換管の屈曲管部および屈曲管部により接続された2つの直管部の両端部をそれぞれ両側板の貫通穴に通すこと、第2熱交換管の直管部の両端部をそれぞれ両側板の切り欠き内に嵌め入れること、ならびに両側板の固定片を変形させ、固定片により第2熱交換管の直管部を挟着固定することを含む上記18)記載の蒸発器の製造方法。   19) A bent pipe part of the first heat exchange pipe with fins and a through hole through which the ends of the two straight pipe parts connected by the bent pipe part pass, and an end part of the straight pipe part of the second heat exchange pipe Preparing a pair of side plates each having a notch to be fitted and fixing pieces respectively formed on both sides of each notch; a straight pipe portion of the second heat exchange pipe is adjacent to the first heat exchange pipe with fins; After fitting into the fitting part which consists of a notch formed in the corner | angular part of the plate fin of two fin groups, both sides are outside the arrangement direction of the plate fins of all the fin groups in the finned first heat exchange pipe , The bent pipe part of the first heat exchange pipe with fins and both ends of the two straight pipe parts connected by the bent pipe part are respectively passed through the through holes of both side plates, and the straight line of the second heat exchange pipe Insert both ends of the pipe part into the cutouts on both side plates, Deforming the fixing pieces of the side plates each time, the 18) A method of manufacturing an evaporator according to comprising clamping fixing the straight tube portions of the second heat exchange tubes by a fixing piece.

20)圧縮機、凝縮器および蒸発器を備えており、蒸発器が上記1)〜17)のうちのいずれかに記載された蒸発器からなる冷凍サイクル。   20) A refrigeration cycle comprising a compressor, a condenser and an evaporator, wherein the evaporator comprises the evaporator described in any one of 1) to 17) above.

21)断熱箱体内に上記20)記載の冷凍サイクルが設置されている冷蔵装置。   21) A refrigeration apparatus in which the refrigeration cycle according to 20) is installed in a heat insulating box.

22)断熱箱体内において、冷凍サイクルの蒸発器の下方に、輻射熱により蒸発器を加熱する除霜装置が配置されている上記21)記載の冷蔵装置。   22) The refrigeration apparatus according to 21) above, wherein a defrosting device that heats the evaporator by radiant heat is disposed below the evaporator of the refrigeration cycle in the heat insulating box.

上記1)の蒸発器を冷蔵装置の冷凍サイクルに適用した場合、第2熱交換管の直管部がプレートフィンに接触しているので、第1熱交換管の直管部における各プレートフィンを貫通している部分の外周面および各プレートフィンにおける直管部が貫通した部分の周囲の他に、第2熱交換管の直管部におけるプレートフィンに接触している部分の外周面およびプレートフィンにおける直管部に接触している部分の近傍にも着霜が発生する。ところで、空気中の水分量は限られているので、着霜量の合計はほぼ一定となる。したがって、各部の霜の厚みは全体的に均一となって、特許文献1記載の蒸発器の場合よりも薄くなり、各フィン群のプレートフィン間を流れる空気量の減少、および空気と両熱交換管内を流れる冷媒との間での伝熱量の減少が緩やかになる。その結果、比較的長時間にわたって冷却性能の低下を防止することができる。   When the evaporator of 1) above is applied to the refrigeration cycle of the refrigeration apparatus, the straight pipe part of the second heat exchange pipe is in contact with the plate fin, so that each plate fin in the straight pipe part of the first heat exchange pipe is In addition to the outer peripheral surface of the penetrating portion and the periphery of the portion through which the straight pipe portion of each plate fin penetrates, the outer peripheral surface of the portion in contact with the plate fin and the plate fin in the straight pipe portion of the second heat exchange pipe Frost is also generated in the vicinity of the portion in contact with the straight pipe portion. By the way, since the amount of moisture in the air is limited, the total amount of frost formation is almost constant. Therefore, the thickness of the frost in each part becomes uniform as a whole, which is thinner than in the case of the evaporator described in Patent Document 1, the amount of air flowing between the plate fins of each fin group, and the heat exchange with air. The decrease in the amount of heat transfer with the refrigerant flowing in the pipe becomes moderate. As a result, it is possible to prevent the cooling performance from being lowered for a relatively long time.

上記2)の蒸発器によれば、第2熱交換管を、直管部がプレートフィンに接触するように配置する作業を比較的簡単に行うことができる。   According to the evaporator of 2), the operation of arranging the second heat exchange pipe so that the straight pipe portion contacts the plate fin can be performed relatively easily.

上記3)および4)の蒸発器によれば、着霜量の多い空気流れ方向上流側において、上記1)と同様の効果を奏する。また、空気流れ方向上流側において、特許文献1記載の蒸発器に比較して着霜量が多くなるので、空気流れ方向下流側においては、空気中の水分量が減少して着霜量が比較的少なくなるが、この場合には、空気流れ方向下流側でのプレートフィンのフィンピッチを小さくすることが可能になり、空気流れ方向下流側のプレートフィンに第2熱交換管の直管部が接触していることと相俟って、空気流れ方向下流側での冷却性能が向上する。したがって、蒸発器全体の小型化を図ることができる。   According to the evaporators 3) and 4), the same effect as 1) is obtained on the upstream side in the air flow direction with a large amount of frost formation. In addition, since the amount of frost increases on the upstream side in the air flow direction as compared with the evaporator described in Patent Document 1, the amount of moisture in the air decreases on the downstream side in the air flow direction and the frost amount is compared. In this case, it is possible to reduce the fin pitch of the plate fins on the downstream side in the air flow direction, and the straight pipe portion of the second heat exchange pipe is provided on the plate fins on the downstream side in the air flow direction. Combined with the contact, the cooling performance on the downstream side in the air flow direction is improved. Therefore, the entire evaporator can be reduced in size.

上記3)および5)の蒸発器によれば、着霜量の多い空気流れ方向上流側において、上記1)の効果が一層優れたものになる。また、空気流れ方向上流側において、特許文献1記載の蒸発器に比較して着霜量が多くなるので、空気流れ方向下流側においては、空気中の水分量が減少して着霜量が比較的少なくなるが、この場合には、空気流れ方向下流側でのプレートフィンのフィンピッチを小さくすることが可能になり、空気流れ方向下流側のプレートフィンに第2熱交換管の直管部が接触していること、および第2熱交換管の隣り合う直管部間のピッチが空気流れ方向下流側で同上流側よりも小さくなっていることと相俟って、空気流れ方向下流側での冷却性能が一層向上する。したがって、蒸発器全体の小型化を図ることができる。   According to the evaporators 3) and 5), the effect 1) is further improved on the upstream side in the air flow direction with a large amount of frost formation. In addition, since the amount of frost increases on the upstream side in the air flow direction as compared with the evaporator described in Patent Document 1, the amount of moisture in the air decreases on the downstream side in the air flow direction and the frost amount is compared. In this case, it is possible to reduce the fin pitch of the plate fins on the downstream side in the air flow direction, and the straight pipe portion of the second heat exchange pipe is provided on the plate fins on the downstream side in the air flow direction. Combined with the contact and the fact that the pitch between the adjacent straight pipe portions of the second heat exchange pipe is smaller on the downstream side in the air flow direction than on the upstream side, The cooling performance is further improved. Therefore, the entire evaporator can be reduced in size.

上記6)の蒸発器によれば、着霜量の多い空気流れ方向上流側において、上記1)と同様の効果を奏する。また、空気流れ方向上流側において、特許文献1記載の蒸発器に比較して着霜量が多くなるので、空気流れ方向下流側においては、空気中の水分量が減少して着霜量が比較的少なくなるが、この場合には、空気流れ方向下流側でのプレートフィンのフィンピッチを小さくすることが可能になり、空気流れ方向下流側での冷却性能が一層向上する。したがって、蒸発器全体の小型化を図ることができる。   According to the evaporator of 6), the same effect as in 1) is obtained on the upstream side in the air flow direction where the amount of frost formation is large. In addition, since the amount of frost increases on the upstream side in the air flow direction as compared with the evaporator described in Patent Document 1, the amount of moisture in the air decreases on the downstream side in the air flow direction and the frost amount is compared. In this case, however, the fin pitch of the plate fins on the downstream side in the air flow direction can be reduced, and the cooling performance on the downstream side in the air flow direction is further improved. Therefore, the entire evaporator can be reduced in size.

上記9)および10)の蒸発器によれば、空気流れ方向下流側での冷却性能が一層向上する。すなわち、空気流れ方向上流側において、特許文献1記載の蒸発器に比較して着霜量が多くなるので、空気流れ方向下流側においては、空気中の水分量が減少して着霜量が比較的少なくなり、その結果空気流れ方向下流側のプレートフィンの形状を霜を落とすのに適した平板状とする必要がなくなる。したがって、空気流れ方向下流側のプレートフィンの形状を、たとえば波板状とすることにより、伝熱面積を空気流れ方向上流側のプレートフィンよりも大きくして冷却性能を向上させることができ、蒸発器全体の小型化を図ることができる。   According to the evaporators 9) and 10), the cooling performance on the downstream side in the air flow direction is further improved. That is, the amount of frost increases on the upstream side in the air flow direction as compared with the evaporator described in Patent Document 1, so the amount of moisture in the air decreases on the downstream side in the air flow direction and the frost amount is compared. As a result, it is not necessary to make the shape of the plate fin downstream in the air flow direction into a flat plate suitable for removing frost. Therefore, the shape of the plate fin on the downstream side in the air flow direction is, for example, a corrugated plate, so that the heat transfer area can be made larger than that on the plate fin on the upstream side in the air flow direction to improve the cooling performance. The overall size of the vessel can be reduced.

上記11)の蒸発器によれば、空気流れ方向下流側のフィン群のフィンピッチが、空気流れ方向上流側のフィン群のフィンピッチよりも小さくなっているので、冷却性能が向上する。したがって、蒸発器全体の小型化を図ることができる。また、空気流れ方向上流側において、特許文献1記載の蒸発器に比較して着霜量が多くなるので、空気流れ方向下流側においては、空気中の水分量が減少して着霜量が比較的少なくなり、空気流れ方向下流側でのプレートフィンのフィンピッチを小さくしても、霜が抵抗となることに起因する各フィン群のプレートフィン間を流れる空気量の減少を防止することができる。   According to the evaporator 11), the fin pitch of the fin group on the downstream side in the air flow direction is smaller than the fin pitch of the fin group on the upstream side in the air flow direction, so that the cooling performance is improved. Therefore, the entire evaporator can be reduced in size. In addition, since the amount of frost increases on the upstream side in the air flow direction as compared with the evaporator described in Patent Document 1, the amount of moisture in the air decreases on the downstream side in the air flow direction and the frost amount is compared. Even if the fin pitch of the plate fins on the downstream side in the air flow direction is reduced, it is possible to prevent a decrease in the amount of air flowing between the plate fins of each fin group due to frost becoming resistance. .

上記13)および14)の蒸発器によれば、第2熱交換管の直管部を確実にプレートフィンに接触させることができる。   According to the evaporators 13) and 14), the straight pipe portion of the second heat exchange pipe can be reliably brought into contact with the plate fin.

特に、上記14)の蒸発器によれば、次の効果を奏する。すなわち、特許文献1に記載されたパイプヒータは、通常、空気流れ方向に隣り合う両フィン群のプレートフィンの角部に形成された切り欠きにより設けられた嵌入部内に嵌め入れられて用いられるので、上記14)の蒸発器によれば、従来のプレートフィンと同じプレートフィンを使用することが可能になる。したがって、プレートフィンの製造コストが安くなる。   In particular, according to the evaporator 14), the following effects can be obtained. That is, since the pipe heater described in Patent Document 1 is normally used by being fitted into a fitting portion provided by a notch formed at the corners of the plate fins of both fin groups adjacent to each other in the air flow direction. According to the evaporator of 14), it is possible to use the same plate fin as the conventional plate fin. Therefore, the manufacturing cost of the plate fin is reduced.

上記15)の蒸発器によれば、第2熱交換管の直管部とプレートフィンとの接触が強固に行われるとともに、両者間での伝熱面積が増大する。   According to the evaporator 15), the straight pipe portion of the second heat exchange pipe and the plate fin are firmly contacted, and the heat transfer area between the two is increased.

上記16)の蒸発器によれば、第2熱交換管を簡単に固定することができる。しかも、側板は、この種の蒸発器が通常備えているものであるから、第2熱交換管の固定に専用の部材を必要としない。   According to the evaporator 16), the second heat exchange tube can be easily fixed. Moreover, since the side plate is normally provided in this type of evaporator, no special member is required for fixing the second heat exchange tube.

上記17)の蒸発器によれば、冷却性能が向上するとともに、全体の軽量化を図ることができる。   According to the evaporator 17), the cooling performance can be improved and the overall weight can be reduced.

上記18)の製造方法によれば、上記14)の蒸発器を比較的簡単に製造することができる。   According to the production method of 18), the evaporator of 14) can be produced relatively easily.

上記19)製造方法によれば、上記16)の蒸発器を比較的簡単に製造することができる。   According to the manufacturing method 19), the evaporator 16) can be manufactured relatively easily.

以下、この発明の実施形態を、図面を参照して説明する。なお、全図面を通じて同一部分および同一物には同一符号を付して重複する説明を省略する。   Embodiments of the present invention will be described below with reference to the drawings. In addition, the same code | symbol is attached | subjected to the same part and the same thing through all drawings, and the overlapping description is abbreviate | omitted.

以下の説明において、図1、図2、図10および図11の上下、左右を上下、左右といい、図2の紙面表側(図3の右側、図4の左側)を前、これと反対側を後というものとする。   In the following description, the top, bottom, left and right in FIGS. 1, 2, 10, and 11 are referred to as top and bottom, and left and right. The front side of FIG. 2 (the right side in FIG. 3 and the left side in FIG. 4) is the front and the opposite side. Let's call it after.

実施形態1
この実施形態は図1〜図9に示すものである。
Embodiment 1
This embodiment is shown in FIGS.

図1〜図4は実施形態1の蒸発器の全体構成を示し、図5および図6はその要部の構成を示す。また、図7〜図9は実施形態1の蒸発器の製造方法を示す。   1 to 4 show the overall configuration of the evaporator according to Embodiment 1, and FIGS. 5 and 6 show the configuration of the main part thereof. 7 to 9 show a method for manufacturing the evaporator according to the first embodiment.

図1〜図4において、蒸発器(1)は、左右方向に並列状に配置された複数のアルミニウム製プレートフィン(2)からなりかつ上下方向(通風方向)に間隔をおいて複数設けられたフィン群(3)と、各フィン群(3)のプレートフィン(2)に貫通状に固定された左右方向に伸びる複数の直管部(5)および隣り合う2つの直管部(5)を接続しかつ直管部(5)より1つ少ない数の屈曲管部(6)(7)よりなるアルミニウム製第1熱交換管(4)と、左右方向に伸びる複数の直管部(9)および隣り合う2つの直管部(9)を接続しかつ直管部(9)より1つ少ない数の屈曲管部(11)(12)よりなるとともに、第1熱交換管(4)の一端に接続されたアルミニウム製第2熱交換管(8)と、すべてのフィン群(3)の左右方向外側に配置されたアルミニウム製側板(13)(14)とを備えている。   1 to 4, the evaporator (1) is composed of a plurality of aluminum plate fins (2) arranged in parallel in the left-right direction, and a plurality of evaporators (1) are provided at intervals in the vertical direction (ventilation direction). A fin group (3), a plurality of straight pipe parts (5) extending in the left-right direction fixed to the plate fins (2) of each fin group (3) and two adjacent straight pipe parts (5) A first aluminum heat exchange pipe (4) consisting of a bent pipe section (6) and (7), one less than the straight pipe section (5), and a plurality of straight pipe sections (9) extending in the left-right direction And two adjacent straight pipe portions (9) are connected to each other, and the number of bent pipe portions (11) and (12) is one less than the straight pipe portion (9), and one end of the first heat exchange pipe (4). And a second aluminum heat exchange pipe (8) connected to each other, and aluminum side plates (13) and (14) arranged on the outer side in the left-right direction of all the fin groups (3).

プレートフィン(2)は、図5に示すように、前後方向に長い方形の平板状であり、その高さ方向の中央部に2つの貫通穴(15)が前後方向に間隔をおいて形成されている。プレートフィン(2)における各貫通穴(15)の周縁部に、カラー(16)が全周にわたって一体に形成されている。また、プレートフィン(2)の各角部に切り欠き(17)が形成されており、プレートフィン(2)における各切り欠き(17)の周縁部に、カラー(18)が一体に形成されている。そして、上下に隣接するフィン群(3)の近接した2つのプレートフィン(2)の切り欠き(18)により、第2熱交換管(8)の直管部(9)が嵌め入れられる嵌入部(19)が形成されている。   As shown in FIG. 5, the plate fin (2) has a rectangular flat plate shape that is long in the front-rear direction, and two through holes (15) are formed at intervals in the front-rear direction at the center in the height direction. ing. A collar (16) is integrally formed over the entire periphery at the peripheral edge of each through hole (15) in the plate fin (2). In addition, a notch (17) is formed at each corner of the plate fin (2), and a collar (18) is integrally formed at the peripheral edge of each notch (17) in the plate fin (2). Yes. And the fitting part by which the straight pipe part (9) of a 2nd heat exchange pipe (8) is inserted by the notch (18) of the two plate fins (2) which the fin group (3) adjacent up and down adjoined. (19) is formed.

空気流れ方向下流側(上側)のフィン群(3)の隣り合うプレートフィン(2)間のフィンピッチは、空気流れ方向上流側(下側)のフィン群(3)のフィンピッチよりも小さくなっている。図示の例では、フィン群(3)の隣り合うプレートフィン(2)間のフィンピッチは、下端のフィン群(3)が最も大きく、上方のフィン群(3)に向かうにつれて小さくなっている。なお、上端のフィン群(3)のフィンピッチが、下端のフィン群(3)のフィンピッチよりも小さくなっているのであれば、上下に隣り合う複数のフィン群(3)のフィンピッチは、等しい場合があってもよく、フィン群(3)のフィンピッチの組み合わせは任意である。   The fin pitch between adjacent plate fins (2) of the fin group (3) on the downstream side (upper side) in the air flow direction is smaller than the fin pitch of the fin group (3) on the upstream side (lower side) in the air flow direction. ing. In the illustrated example, the fin pitch between adjacent plate fins (2) of the fin group (3) is the largest at the lower end fin group (3) and decreases toward the upper fin group (3). If the fin pitch of the upper fin group (3) is smaller than the fin pitch of the lower fin group (3), the fin pitch of the plurality of fin groups (3) adjacent vertically is The fin pitches of the fin group (3) may be arbitrary.

第1熱交換管(4)は、同一垂直面内において上下方向に間隔をおいて設けられかつ左右方向に伸びる複数の直管部(5)、および上下に隣り合う直管部(5)どうしを左右交互に接続する第1の屈曲管部(6)よりなる2つの蛇行状管部(4A)(4B)が、前後に間隔をおいて配置され、両蛇行状管部(4A)(4B)の下端の直管部(5)の右端部どうしが第2の屈曲管部(7)により接続されることによって構成されている。各蛇行状管部(4A)(4B)の直管部(5)は、各フィン群(3)のプレートフィン(2)の各貫通穴(15)に通され、直管部(5)外周面がカラー(16)に密着するようにプレートフィン(2)に固定されている。   The first heat exchange pipe (4) includes a plurality of straight pipe sections (5) provided at intervals in the vertical direction within the same vertical plane and extending in the left-right direction, and straight pipe sections (5) adjacent to each other in the vertical direction. The two meandering pipe parts (4A) and (4B) consisting of the first bent pipe parts (6) that connect the left and right alternately are arranged at intervals in the front and rear, and both meandering pipe parts (4A) (4B ) Are connected by connecting the right end portions of the straight pipe portion (5) at the lower end with a second bent pipe portion (7). The straight pipe part (5) of each serpentine pipe part (4A) (4B) is passed through each through hole (15) of the plate fin (2) of each fin group (3), and the outer circumference of the straight pipe part (5) It is fixed to the plate fin (2) so that the surface is in close contact with the collar (16).

第2熱交換管(8)は、同一垂直面内において上下方向に間隔をおいて設けられかつ左右方向に伸びる複数の直管部(9)、および上下に隣り合う直管部(9)どうしを左右交互に接続する第1の屈曲管部(11)よりなる2つの蛇行状管部(8A)(8B)が、前後に間隔をおいて配置され、両蛇行状管部(8A)(8B)の下端の直管部(9)の右端部どうしが第2の屈曲管部(12)により接続されることによって構成されている。各蛇行状管部(8A)(8B)の上下に隣り合う直管部(9)間のピッチは、下側において大きく、上方に向かうにつれて小さくなっている。各蛇行状管部(8A)(8B)の下端の直管部(9)を除いた他の直管部(9)は、上下に隣接するフィン群(3)の近接した2つのプレートフィン(2)の切り欠き(17)からなる嵌入部(19)内に、直管部(9)外周面がカラー(18)と密着するように嵌め入れられており、これにより直管部(9)がプレートフィン(2)の前後両側縁部に接触している。また、各蛇行状管部(8A)(8B)の下端の直管部(9)は、下端のフィン群(3)の下側の切り欠き(17)内に、外周面の一部がカラー(18)と密着するように嵌め入れられており、これにより直管部(9)がプレートフィン(2)の前後両側縁部に接触している。なお、各蛇行状管部(8A)(8B)の上下に隣り合う直管部(9)間のピッチが、下側において大きく、上方に向かうにつれて小さくなっているので、嵌入部(19)の中には蛇行状管部(8A)(8B)の直管部(9)が嵌め入れられていないものも存在する。また、第2熱交換管(8)の後側の蛇行状管部(8B)における上端の直管部(9)の左端部は前方にU字状に屈曲され、この屈曲部(21)の先端部が、第1熱交換管(4)の前側の蛇行状管部(4A)における上端の直管部(5)の左端部に接合されている。   The second heat exchange pipe (8) includes a plurality of straight pipe portions (9) provided in the same vertical plane at intervals in the vertical direction and extending in the left-right direction, and straight pipe portions (9) adjacent to each other in the vertical direction. Two meandering pipe parts (8A) and (8B) consisting of first bent pipe parts (11) that connect the left and right alternately are arranged at intervals in the front and rear, and both meandering pipe parts (8A) (8B) ) Are connected by connecting the right end portions of the straight pipe portion (9) at the lower end with the second bent pipe portion (12). The pitch between the straight pipe portions (9) adjacent to the upper and lower sides of the meandering pipe portions (8A) and (8B) is large on the lower side and decreases as it goes upward. The other straight pipe portions (9) except for the straight pipe portion (9) at the lower end of each meandering pipe portion (8A) (8B) are two plate fins ( 2) The straight pipe part (9) is fitted into the fitting part (19) consisting of the notch (17) so that the outer peripheral surface is in close contact with the collar (18). Are in contact with both front and rear edges of the plate fin (2). In addition, the straight pipe part (9) at the lower end of each meandering pipe part (8A) (8B) is partly colored in the notch (17) on the lower side of the fin group (3) at the lower end. The straight pipe portion (9) is in contact with the front and rear side edges of the plate fin (2). In addition, since the pitch between the straight pipe parts (9) adjacent to the upper and lower sides of each meandering pipe part (8A) (8B) is large on the lower side and becomes smaller toward the upper side, the fitting part (19) Some of them do not have the straight pipe portions (9) of the meandering pipe portions (8A) (8B). Further, the left end portion of the straight pipe portion (9) at the upper end of the meandering pipe portion (8B) on the rear side of the second heat exchange pipe (8) is bent forward in a U shape, and the bent portion (21) The distal end portion is joined to the left end portion of the straight pipe portion (5) at the upper end of the meandering tube portion (4A) on the front side of the first heat exchange tube (4).

左側板(13)には、第1熱交換管(4)の両蛇行状管部(4A)(4B)における上端の直管部(5)の左端部を通す貫通穴(22)、第1熱交換管(4)の第1屈曲管部(6)および各第1屈曲管部(6)により接続された上下に隣り合う直管部(5)の左端部を通す縦長貫通穴(23)、ならびに第2熱交換管(8)の両蛇行状管部(8A)(8B)における各直管部(9)の左端部を嵌め入れる切り欠き(24)が形成されている。右側板(14)には、第1熱交換管(4)の第1屈曲管部(6)および各第1屈曲管部(6)により接続された上下に隣り合う直管部(5)の右端部を通す縦長貫通穴(23)、第1熱交換管(4)の第2屈曲管部(7)および第2屈曲管部(7)により接続された前後に隣り合う直管部(5)の右端部を通す横長貫通穴(26)、ならびに第2熱交換管(8)の両蛇行状管部(8A)(8B)における各直管部(9)の右端部を嵌め入れる切り欠き(24)が形成されている。各側板(13)(14)における切り欠き(24)の上下両縁部にはそれぞれ固定片(28)が一体に形成されており、第2熱交換管(8)の各直管部(9)は、切り欠き(24)内に嵌め入れられるとともに、両固定片(28)により挟着固定されている(図6参照)。両固定片(28)は、図6の鎖線で示す状態から変形させられたものである。なお、切り欠き(24)は、上下に隣り合うフィン群(3)間と対応するすべての部分に形成されており、各蛇行状管部(8A)(8B)の上下に隣り合う直管部(9)間のピッチが、下側において大きく、上方に向かうにつれて小さくなっていることから、切り欠き(24)の中には、第2熱交換管(8)の直管部が嵌め入れられていないものもある。   The left side plate (13) has a through hole (22) through which the left end portion of the straight pipe portion (5) at the upper end of both meandering tube portions (4A) and (4B) of the first heat exchange tube (4) passes, A vertically long through-hole (23) that passes through the left end of the first straight pipe part (5) that is connected by the first bent pipe part (6) and each first bent pipe part (6) of the heat exchange pipe (4). In addition, a notch (24) for fitting the left end portion of each straight pipe portion (9) in both meandering pipe portions (8A) and (8B) of the second heat exchange pipe (8) is formed. The right side plate (14) has a first bent pipe portion (6) of the first heat exchange pipe (4) and a straight pipe portion (5) vertically adjacent to each other connected by the first bent pipe portions (6). A straight pipe portion adjacent to the front and rear connected by the vertically long through hole (23) passing through the right end portion, the second bent pipe portion (7) and the second bent pipe portion (7) of the first heat exchange pipe (4) (5 ) Through the right end of the straight through hole (26) and the notch into which the right end of each straight pipe part (9) in the two meandering pipe parts (8A) (8B) of the second heat exchange pipe (8) (24) is formed. Fixing pieces (28) are integrally formed on the upper and lower edges of the notch (24) in each side plate (13) (14), and each straight pipe portion (9) of the second heat exchange pipe (8) is formed. ) Is fitted in the notch (24) and is clamped and fixed by both fixing pieces (28) (see FIG. 6). Both fixed pieces (28) are deformed from the state indicated by the chain line in FIG. The notches (24) are formed in all the portions corresponding to the space between the fin groups (3) that are vertically adjacent to each other, and the straight pipe portions that are adjacent to the upper and lower sides of each meandering pipe portion (8A) (8B). Since the pitch between (9) is large on the lower side and becomes smaller toward the upper side, the straight pipe part of the second heat exchange pipe (8) is fitted into the notch (24). Some are not.

上記蒸発器(1)において、冷媒は、第2熱交換管(8)の前側蛇行状管部(8A)における上端の直管部(9)の左端から第2熱交換管(8)内に流入し、第2および第1熱交換管(8)(4)内を流れ、図1に矢印Xで示すように、下方から上方に流れる空気と熱交換をし、第1熱交換管(4)の後側蛇行状管部(4B)における上端の直管部の左端部から流出する。   In the evaporator (1), the refrigerant enters the second heat exchange pipe (8) from the left end of the straight pipe section (9) at the upper end of the front meandering pipe section (8A) of the second heat exchange pipe (8). Flows in the second and first heat exchange pipes (8) and (4), exchanges heat with the air flowing upward from below as shown by arrow X in FIG. ) Flows out from the left end of the straight pipe at the upper end of the rear meandering pipe (4B).

そして、第1熱交換管(4)の直管部(5)における各プレートフィン(2)を貫通している部分の外周面、各プレートフィン(2)における直管部(5)が貫通した貫通穴(15)の周囲の部分、第2熱交換管(8)の直管部(9)におけるプレートフィン(2)に接触している部の外周面、ならびにプレートフィン(2)における直管部(9)が接触している部分の近傍に着霜が発生する。ところで、空気中の水分量は限られているので、着霜量の合計はほぼ一定となる。したがって、各部の霜の厚みは全体的に均一でかつ薄肉となり、各フィン群(3)のプレートフィン(2)間を流れる空気量の減少、および空気と両熱交換管(4)(8)内を流れる冷媒との間での伝熱量の減少が緩やかになる。その結果、比較的長時間にわたって冷却性能の低下を防止することができる。特に、着霜量の多い空気流れ方向上流側である下側において、上述した効果が一層優れたものになる。   And the outer peripheral surface of the part which has penetrated each plate fin (2) in the straight pipe part (5) of the 1st heat exchange pipe (4), the straight pipe part (5) in each plate fin (2) penetrated The peripheral portion of the through hole (15), the outer peripheral surface of the portion in contact with the plate fin (2) in the straight pipe portion (9) of the second heat exchange pipe (8), and the straight pipe in the plate fin (2) Frosting occurs in the vicinity of the part in contact with the part (9). By the way, since the amount of moisture in the air is limited, the total amount of frost formation is almost constant. Therefore, the frost thickness of each part is uniform and thin as a whole, the amount of air flowing between the plate fins (2) of each fin group (3) is reduced, and the air and both heat exchange tubes (4) (8) The decrease in the amount of heat transfer with the refrigerant flowing inside becomes moderate. As a result, it is possible to prevent the cooling performance from being lowered for a relatively long time. In particular, the effect described above is further improved on the lower side which is the upstream side in the air flow direction with a large amount of frost formation.

また、空気流れ方向下流側のフィン群(3)のフィンピッチが、空気流れ方向上流側のフィン群(3)のフィンピッチよりも小さいので、空気流れ方向下流側のプレートフィン(2)に第2熱交換管(8)の直管部(9)が接触していること、および第2熱交換管(8)の各蛇行状管部(8A)(8B)の上下に隣り合う直管部(9)間のピッチが空気流れ方向下流側で小さくなっていることと相俟って、空気流れ方向下流側での冷却性能が一層向上する。したがって、蒸発器(1)全体の小型化を図ることができる。しかも、空気流れ方向上流側での着霜量が多くなるので、空気流れ方向下流側においては、空気中の水分量が減少して着霜量が比較的少なくなり、空気流れ方向下流側でのフィン群(3)のフィンピッチを小さくしても、霜が抵抗となることに起因する各フィン群(3)のプレートフィン(2)間を流れる空気量の減少を防止することができる。   In addition, the fin pitch of the fin group (3) on the downstream side in the air flow direction is smaller than the fin pitch of the fin group (3) on the upstream side in the air flow direction. 2 The straight pipe part (9) of the heat exchange pipe (8) is in contact, and the straight pipe part adjacent to the upper and lower sides of the meandering pipe parts (8A) (8B) of the second heat exchange pipe (8) Combined with the fact that the pitch between (9) is smaller on the downstream side in the air flow direction, the cooling performance on the downstream side in the air flow direction is further improved. Therefore, it is possible to reduce the size of the entire evaporator (1). Moreover, since the amount of frost on the upstream side in the air flow direction increases, the amount of moisture in the air decreases on the downstream side in the air flow direction, and the amount of frost formation becomes relatively small. Even if the fin pitch of the fin group (3) is reduced, it is possible to prevent a reduction in the amount of air flowing between the plate fins (2) of each fin group (3) due to resistance of frost.

蒸発器(1)は、次のようにして製造される。   The evaporator (1) is manufactured as follows.

まず、2つの直管部(31)および両直管部(31)の一端部どうしを接続する屈曲管部(32)からなるアルミニウム製ヘアピン状管(30)を用意し、ヘアピン状管(30)の両直管部(31)をそれぞれ複数のプレートフィン(2)の貫通穴(15)に通すとともにプレートフィン(2)に固定することにより、複数の並列状プレートフィン(2)からなるフィン群(3)が直管部(31)の長さ方向に間隔をおいて複数設けれたフィン付きヘアピン状管(30)を形成する(図7参照)。   First, an aluminum hairpin tube (30) comprising two straight tube portions (31) and a bent tube portion (32) for connecting one end portions of both straight tube portions (31) is prepared, and a hairpin tube (30 ) Through the through holes (15) of the plurality of plate fins (2) and fixed to the plate fins (2), thereby forming fins comprising a plurality of parallel plate fins (2). The group (3) forms a finned hairpin tube (30) provided with a plurality of intervals in the length direction of the straight tube portion (31) (see FIG. 7).

ついで、フィン付きヘアピン状管(30)を、直管部(31)の長さ方向に関して同一位置にあるフィン無し部において曲げるとともに、隣り合う2つのフィン無し部での曲げ方向を逆向きにすることにより両直管部(31)を蛇行状とし、2つの蛇行状管部(4A)(4B)およびヘアピン状管(30)の屈曲管部(32)からなる第2屈曲管部(7)を有するフィン付き第1熱交換管(4)を形成する(図8参照)。   Next, the finned hairpin tube (30) is bent at the finless portion at the same position with respect to the length direction of the straight tube portion (31), and the bending direction at the two adjacent finless portions is reversed. As a result, both straight pipe parts (31) are meandered, and the second bent pipe part (7) comprising the two meandering pipe parts (4A) (4B) and the bent pipe part (32) of the hairpin-like pipe (30) The finned first heat exchange pipe (4) having the shape is formed (see FIG. 8).

ついで、フィン付き第1熱交換管(4)の両蛇行状管部(4A)(4B)における上端の直管部(5)の左端部を貫通穴(22)に通すとともに、フィン付き第1熱交換管(4)の第1屈曲管部(6)および各第1屈曲管部(6)により接続された上下に隣り合う直管部(5)の左端部を縦長貫通穴(23)に通すことにより、フィン付き第1熱交換管(4)の左側に左側板(13)を配置する。また、フィン付き第1熱交換管(4)の第1屈曲管部(6)および各第1屈曲管部(6)により接続された上下に隣り合う直管部(5)の右端部を縦長貫通穴(23)に通すとともに、フィン付き第1熱交換管(4)の第2屈曲管部(7)および第2屈曲管部(7)により接続された前後に隣り合う直管部(5)の右端部を横長貫通穴(26)に通すことにより、フィン付き第1熱交換管(4)の右側に右側板(14)を配置する。このとき、両側板(13)(14)の固定片(28)は、図6に鎖線で示すように、外側方に真っ直ぐに伸びている。   Next, the left end portion of the straight pipe portion (5) at the upper end of the two meandering tube portions (4A) and (4B) of the first heat exchange tube (4) with fins is passed through the through hole (22), and the first The left end of the first bent pipe portion (6) of the heat exchange pipe (4) and the straight pipe portion (5) adjacent to each other connected by the first bent pipe portion (6) is formed into a vertically long through hole (23). By passing, the left side plate (13) is arranged on the left side of the finned first heat exchange tube (4). Also, the first bent pipe part (6) of the finned first heat exchange pipe (4) and the right end part of the straight pipe part (5) vertically adjacent to each other connected by the first bent pipe parts (6) are vertically long. The straight pipe part (5) which is passed through the through hole (23) and adjacent to the front and rear connected by the second bent pipe part (7) and the second bent pipe part (7) of the finned first heat exchange pipe (4) The right side plate (14) is disposed on the right side of the finned first heat exchange pipe (4) by passing the right end of the first through the through hole (26). At this time, the fixing pieces (28) of the side plates (13) and (14) extend straight outward as indicated by chain lines in FIG.

ついで、第2熱交換管(8)の両蛇行状管部(8A)(8B)を、第2屈曲管部(12)において若干開き(図9参照)、両蛇行状管部(8A)(8B)の下端の直管部(9)を除いた他の直管部(9)を、フィン付き第1熱交換管(4)の隣り合う2つのフィン群(3)のプレートフィン(2)の角部に形成された切り欠き(17)からなる嵌入部(19)内に嵌め入れるとともに、下端の直管部(9)を、下端のフィン群(3)の下側の切り欠き(17)内に嵌め入れ、さらに第2熱交換管(8)の両蛇行状管部(8A)(8B)の直管部(9)の両端部をそれぞれ両側板(13)(14)の切り欠き(24)内に嵌め入れる。   Next, the two meandering tube portions (8A) and (8B) of the second heat exchange tube (8) are slightly opened at the second bent tube portion (12) (see FIG. 9), and the two meandering tube portions (8A) ( 8B), except for the straight pipe portion (9) at the lower end, plate fins (2) of two adjacent fin groups (3) of the first heat exchange pipe (4) with fins Is fitted into a fitting part (19) consisting of a notch (17) formed at the corner of the lower end of the straight pipe part (9) at the lower end and a lower notch (17 at the lower end fin group (3)). ), And the both ends of the straight pipe part (9) of the two meandering pipe parts (8A) and (8B) of the second heat exchange pipe (8) are notched on both side plates (13) and (14), respectively. (24) Fit in.

最後に、両側板(13)(14)の固定片(28)を変形させ(図6参照)、固定片(28)により第2熱交換管(8)の直管部(9)を挟着固定する。こうして、蒸発器(1)が製造される。   Finally, the fixing pieces (28) of the side plates (13) and (14) are deformed (see FIG. 6), and the straight pipe portion (9) of the second heat exchange pipe (8) is clamped by the fixing pieces (28). Fix it. Thus, the evaporator (1) is manufactured.

実施形態2
この実施形態は図10に示すものである。
Embodiment 2
This embodiment is shown in FIG.

実施形態2の蒸発器(40)の場合、第2熱交換管(8)の両蛇行状管部(8A)(8B)における直管部(9)の数はフィン群(3)の数と等しく、かつ上下に隣り合う直管部(9)間のピッチはすべて等しくなっている。そして、下端の直管部(9)を除いた他のすべての直管部(9)は、上下に隣接するフィン群(3)の近接した2つのプレートフィン(2)の切り欠き(18)からなる嵌入部(19)内に、直管部(9)外周面がカラー(18)と密着するように嵌め入れられており、これにより直管部(9)がプレートフィン(2)の前後両側縁部に接触している。また、下端の直管部(9)は、下端のフィン群(3)の下側の切り欠き(17)内に配され、直管部(9)の外周面はカラー(18)と密着するようにプレートフィン(2)の前後両側縁部に接触している。   In the case of the evaporator (40) of Embodiment 2, the number of straight pipe portions (9) in both meandering pipe portions (8A) and (8B) of the second heat exchange pipe (8) is the number of fin groups (3). The pitches between the straight pipe portions (9) that are equal and adjacent in the vertical direction are all equal. All the other straight pipe portions (9) except for the straight pipe portion (9) at the lower end are notched (18) in the two plate fins (2) adjacent to each other in the upper and lower adjacent fin groups (3). The straight pipe part (9) is fitted into the fitting part (19) so that the outer peripheral surface of the straight pipe part (9) is in close contact with the collar (18), so that the straight pipe part (9) is placed before and after the plate fin (2). It touches both side edges. The straight pipe portion (9) at the lower end is arranged in the notch (17) on the lower side of the fin group (3) at the lower end, and the outer peripheral surface of the straight pipe portion (9) is in close contact with the collar (18). In this manner, the plate fins (2) are in contact with the front and rear side edges.

その他の構成は、実施形態1の蒸発器(1)と同様である。   Other configurations are the same as those of the evaporator (1) of the first embodiment.

実施形態3
この実施形態は図11に示すものである。
Embodiment 3
This embodiment is shown in FIG.

実施形態3の蒸発器(50)の場合、上端から所定数、ここでは2つのフィン群(3)のプレートフィン(51)は波板状であり、その伝熱面積は、平板状である他のプレートフィン(2)よりも大きくなっている。また、波板状プレートフィン(51)の角部には切り欠きは形成されていない。   In the case of the evaporator (50) of Embodiment 3, a predetermined number from the upper end, here, the plate fins (51) of the two fin groups (3) are corrugated, and the heat transfer area is flat. It is larger than the plate fin (2). Moreover, the notch is not formed in the corner | angular part of a corrugated plate fin (51).

第2熱交換管(8)の前後両蛇行状管部(8A)の高さは蒸発器(1)全体の高さよりも低く、両蛇行状管部(8A)(8B)の直管部(9)は、平板状プレートフィン(2)を有する上下方向に隣り合ったフィン群(3)の間に配され、嵌入部(19)に嵌め入れられている。また、第2熱交換管(8)の後側蛇行状管部(8B)の上端の直管部(9)は上方に屈曲されるとともに前方に屈曲され、この屈曲部(52)の先端部が、第1熱交換管(4)の前側蛇行状管部(4A)の上端の直管部(5)の左端部に接合されている。   The height of the two meandering pipe sections (8A) before and after the second heat exchange pipe (8) is lower than the overall height of the evaporator (1), and the straight pipe section of the two meandering pipe sections (8A) (8B) ( 9) is arranged between the vertically adjacent fin groups (3) having the flat plate fins (2), and is fitted into the fitting portion (19). Further, the straight pipe portion (9) at the upper end of the rear meandering pipe portion (8B) of the second heat exchange pipe (8) is bent upward and bent forward, and the distal end portion of the bent portion (52). Is joined to the left end of the straight pipe part (5) at the upper end of the front meandering pipe part (4A) of the first heat exchange pipe (4).

その他の構成は、実施形態1の蒸発器(1)と同様である。   Other configurations are the same as those of the evaporator (1) of the first embodiment.

実施形態2および3の蒸発器(1)は、実施形態1の蒸発器(1)と同様にして製造される。   The evaporator (1) of the second and third embodiments is manufactured in the same manner as the evaporator (1) of the first embodiment.

実施形態1〜3の蒸発器(1)(40)(50)は、圧縮機および凝縮器とともに冷凍サイクルを構成する。このような冷凍サイクルは、冷蔵装置の断熱箱体内に配置される。この冷蔵装置において、断熱箱体内における冷凍サイクルの蒸発器(1)(40)(50)の下方部分に、輻射熱により蒸発器(1)を加熱する除霜装置が配置される。   The evaporators (1), (40), and (50) of Embodiments 1 to 3 constitute a refrigeration cycle together with the compressor and the condenser. Such a refrigerating cycle is arrange | positioned in the heat insulation box of a refrigerator. In this refrigeration apparatus, a defrosting device for heating the evaporator (1) by radiant heat is disposed below the evaporators (1), (40), and (50) of the refrigeration cycle in the heat insulation box.

上記実施形態1〜3においては、空気流れ方向下流側(上側)のフィン群の隣り合うプレートフィン間のフィンピッチは、空気流れ方向上流側(下側)のフィン群のフィンピッチよりも小さくなっているが、これに限定されるものではなく、すべてのフィン群のフィンピッチが等しくなっていてもよい。   In the first to third embodiments, the fin pitch between adjacent plate fins of the fin group on the downstream side (upper side) in the air flow direction is smaller than the fin pitch of the fin group on the upstream side (lower side) in the air flow direction. However, the present invention is not limited to this, and the fin pitches of all the fin groups may be equal.

この発明の実施形態1の蒸発器の全体構成を示す斜視図である。It is a perspective view which shows the whole structure of the evaporator of Embodiment 1 of this invention. 図1のII−II線断面図である。It is the II-II sectional view taken on the line of FIG. この発明の実施形態1の蒸発器の全体構成を示す左側面図である。It is a left view which shows the whole structure of the evaporator of Embodiment 1 of this invention. この発明の実施形態1の蒸発器の全体構成を示す右側面図である。It is a right view which shows the whole structure of the evaporator of Embodiment 1 of this invention. 図1の蒸発器のプレートフィンを示す部分拡大斜視図である。It is a partial expansion perspective view which shows the plate fin of the evaporator of FIG. 図1の蒸発器の側板の一部分を示す拡大図である。It is an enlarged view which shows a part of side plate of the evaporator of FIG. 図1の蒸発器の製造方法における一工程を示す図である。It is a figure which shows one process in the manufacturing method of the evaporator of FIG. 図1の蒸発器の製造方法における図7とは異なる工程を示す図である。It is a figure which shows the process different from FIG. 7 in the manufacturing method of the evaporator of FIG. 図1の蒸発器の製造方法における図7および図8とは異なる工程を示す図である。It is a figure which shows the process different from FIG.7 and FIG.8 in the manufacturing method of the evaporator of FIG. この発明の実施形態2の蒸発器の全体構成を示す斜視図である。It is a perspective view which shows the whole structure of the evaporator of Embodiment 2 of this invention. この発明の実施形態3の蒸発器の全体構成を示す斜視図である。It is a perspective view which shows the whole structure of the evaporator of Embodiment 3 of this invention.

符号の説明Explanation of symbols

(1)(40)(50):蒸発器
(2)(51):プレートフィン
(3):フィン群
(4):第1熱交換管
(5):直管部
(6)(7):屈曲管部
(8):第2熱交換管
(9):直管部
(11)(12):屈曲管部
(13)(14):側板
(17):切り欠き
(18):カラー
(19):嵌入部
(23):縦長貫通穴
(24):切り欠き
(26):横長貫通穴
(28):固定片
(30):ヘアピン状管
(31):直管部
(1) (40) (50): Evaporator
(2) (51): Plate fin
(3): Fin group
(4): 1st heat exchange tube
(5): Straight pipe
(6) (7): Bent tube
(8): Second heat exchange tube
(9): Straight pipe
(11) (12): Bent tube
(13) (14): Side plate
(17): Notch
(18): Color
(19): Insertion section
(23): Vertically long through hole
(24): Notch
(26): Horizontally long through hole
(28): Fixed piece
(30): Hairpin tube
(31): Straight pipe

Claims (22)

並列状に配置された複数のプレートフィンと、プレートフィンに貫通状に固定された複数の直管部および隣り合う2つの直管部を接続しかつ直管部より1つ少ない数の屈曲管部よりなる第1熱交換管と、複数の直管部および隣り合う2つの直管部を接続しかつ直管部より1つ少ない数の屈曲管部よりなるとともに、第1熱交換管の一端に接続された第2熱交換管とを備えており、第2熱交換管の直管部がプレートフィンに接触させられている蒸発器。 A plurality of plate fins arranged in parallel, a plurality of straight pipe portions fixed in a penetrating manner to the plate fins, and two adjacent straight pipe portions, and one less bent pipe portion than the straight pipe portions A first heat exchange pipe, a plurality of straight pipe sections and two adjacent straight pipe sections connected to each other and one bent pipe section less than the straight pipe section, and at one end of the first heat exchange pipe The evaporator which is provided with the connected 2nd heat exchange pipe, and the straight pipe part of the 2nd heat exchange pipe is made to contact with a plate fin. 第2熱交換管の直管部が、プレートフィンにおける空気流れ方向および第1熱交換管の直管部と直交する方向の側縁部に接触している請求項1記載の蒸発器。 The evaporator according to claim 1, wherein the straight pipe portion of the second heat exchange pipe is in contact with the air flow direction in the plate fin and the side edge portion in a direction orthogonal to the straight pipe portion of the first heat exchange pipe. 第2熱交換管の直管部が、空気流れ方向の全体にわたってプレートフィンに接触させられている請求項2記載の蒸発器。 The evaporator according to claim 2, wherein the straight pipe portion of the second heat exchange pipe is brought into contact with the plate fin over the entire air flow direction. 第2熱交換管の空気流れ方向に隣り合う直管部間のピッチが、すべて均一になっている請求項3記載の蒸発器。 The evaporator according to claim 3, wherein the pitches between the straight pipe portions adjacent to each other in the air flow direction of the second heat exchange pipe are all uniform. 第2熱交換管の空気流れ方向に隣り合う直管部間のピッチが、空気流れ方向下流側において同上流側よりも小さくなっている請求項3記載の蒸発器。 The evaporator according to claim 3, wherein a pitch between straight pipe portions adjacent to each other in the air flow direction of the second heat exchange pipe is smaller on the downstream side in the air flow direction than on the upstream side. 第2熱交換管の直管部が、空気流れ方向上流側においてプレートフィンに接触している請求項2記載の蒸発器。 The evaporator according to claim 2, wherein the straight pipe portion of the second heat exchange pipe is in contact with the plate fin on the upstream side in the air flow direction. 並列状に配置された複数のプレートフィンからなるフィン群が、空気流れ方向に間隔をおいて複数設けられている請求項1〜6のうちのいずれかに記載の蒸発器。 The evaporator according to any one of claims 1 to 6, wherein a plurality of fin groups including a plurality of plate fins arranged in parallel are provided at intervals in the air flow direction. すべてのフィン群のプレートフィンが平板状である請求項7記載の蒸発器。 The evaporator according to claim 7, wherein the plate fins of all the fin groups are flat. 空気流れ方向下流側のフィン群のプレートフィンの伝熱面積が、空気流れ方向上流側のフィン群のプレートフィンの伝熱面積よりも大きくなっている請求項7記載の蒸発器。 The evaporator according to claim 7, wherein the heat transfer area of the plate fins in the fin group on the downstream side in the air flow direction is larger than the heat transfer area of the plate fins in the fin group on the upstream side in the air flow direction. 空気流れ方向上流側のフィン群のプレートフィンが平板状であり、空気流れ方向下流側のフィン群のプレートフィンが波板状である請求項9記載の蒸発器。 The evaporator according to claim 9, wherein the plate fin of the fin group on the upstream side in the air flow direction has a flat plate shape, and the plate fin of the fin group on the downstream side in the air flow direction has a corrugated plate shape. 空気流れ方向下流側のフィン群のフィンピッチが、空気流れ方向上流側のフィン群のフィンピッチよりも小さくなっている請求項7〜10のうちのいずれかに記載の蒸発器。 The evaporator according to any one of claims 7 to 10, wherein a fin pitch of the fin group on the downstream side in the air flow direction is smaller than a fin pitch of the fin group on the upstream side in the air flow direction. 各フィン群のすべてのプレートフィンに、第1熱交換管の2つの直管部が貫通状に固定されている請求項7〜11のうちのいずれかに記載の蒸発器。 The evaporator according to any one of claims 7 to 11, wherein two straight pipe portions of the first heat exchange pipe are fixed in a penetrating manner to all the plate fins of each fin group. 第2熱交換管の直管部が、プレートフィンに形成された切り欠きからなる嵌入部内に嵌め入れられた状態でプレートフィンに接触させられている請求項7〜12のうちのいずれかに記載の蒸発器。 The straight pipe part of a 2nd heat exchange pipe is made to contact with a plate fin in the state inserted by the insertion part which consists of a notch formed in the plate fin. Evaporator. 空気流れ方向に隣り合う2つのフィン群のプレートフィンの角部に切り欠きが形成され、空気流れ方向に隣り合う両フィン群のプレートフィンの切り欠きにより嵌入部が設けられ、第2熱交換管の直管部が、嵌入部内に嵌め入れられた状態で両フィン群のプレートフィンに接触させられている請求項13記載の蒸発器。 A notch is formed in the corner of the plate fin of two fin groups adjacent in the air flow direction, and a fitting portion is provided by the notch of the plate fin of both fin groups adjacent in the air flow direction. The evaporator according to claim 13, wherein the straight pipe portion is brought into contact with the plate fins of both fin groups in a state of being fitted into the fitting portion. プレートフィンにおける切り欠きの周縁部に、直管部の外周面に面接触するカラーが一体に形成されている請求項13または14記載の蒸発器。 The evaporator according to claim 13 or 14, wherein a collar in surface contact with the outer peripheral surface of the straight pipe portion is integrally formed at a peripheral portion of the notch in the plate fin. すべてのフィン群におけるプレートフィンの並び方向の外側にそれぞれ側板が配置され、両側板に、それぞれ第1熱交換管の屈曲管部および屈曲管部により接続された2つの直管部の端部が通される貫通穴と、第2熱交換管の直管部の端部が嵌る切り欠きとが形成され、側板における切り欠きの両側にそれぞれ固定片が形成され、第2熱交換管の直管部の端部が、側板の切り欠き内に嵌め入れられるとともに両固定片により挟着固定されている請求項7〜15のうちのいずれかに記載の蒸発器。 Side plates are arranged on the outer sides in the arrangement direction of the plate fins in all the fin groups, and the end portions of the two straight pipe portions connected to the both side plates by the bent pipe portion and the bent pipe portion of the first heat exchange pipe, respectively. A through hole to be passed through and a notch into which an end of the straight pipe portion of the second heat exchange pipe is fitted, and fixing pieces are formed on both sides of the cutout in the side plate, and the straight pipe of the second heat exchange pipe The evaporator according to any one of claims 7 to 15, wherein an end portion of the portion is fitted into a notch of the side plate and is fixed by being sandwiched by both fixing pieces. プレートフィンと、第1および第2熱交換管がアルミニウムからなる請求項1〜16のうちのいずれかに記載の蒸発器。 The evaporator according to any one of claims 1 to 16, wherein the plate fin and the first and second heat exchange tubes are made of aluminum. ヘアピン状管と、複数の直管部および隣り合う2つの直管部を接続しかつ直管部より1つ少ない数の屈曲管部よりなる第2熱交換管と、2つの貫通穴を有する複数のプレートフィンとを用意すること、各プレートフィンの各角部に切り欠きを形成しておくこと、ヘアピン状管の両直管部をそれぞれすべてのプレートフィンの貫通穴に通すとともにプレートフィンに固定することにより、複数の並列状プレートフィンからなるフィン群を直管部の長さ方向に間隔をおいて複数設けること、フィン付きヘアピン状管を、直管部の長さ方向に関して同一位置にあるフィン無し部において曲げるとともに、隣り合う2つのフィン無し部での曲げ方向を逆向きにすることにより両直管部を蛇行状とし、フィン付き第1熱交換管を形成すること、第2熱交換管の直管部を、フィン付き第1熱交換管の隣り合う2つのフィン群のプレートフィンの角部に形成された切り欠きからなる嵌入部内に嵌め入れること、ならびに第1熱交換管の一端部と第2熱交換管の一端部とを接合することを含む蒸発器の製造方法。 A plurality of hairpin tubes, a plurality of straight tube portions and a second heat exchange tube that connects two adjacent straight tube portions and includes a number of bent tube portions, one less than the straight tube portions, and a plurality of through holes. Plate fins, notches in each corner of each plate fin, and both straight tube sections of hairpin tubes are passed through the through holes of all plate fins and fixed to the plate fins. By providing a plurality of fin groups composed of a plurality of parallel plate fins at intervals in the length direction of the straight tube portion, the finned hairpin tube is in the same position with respect to the length direction of the straight tube portion. Bending at the finless portion and making the straight pipe portions meandering by reversing the bending direction at the two adjacent finless portions to form a finned first heat exchange tube, second heat exchange Fitting the straight pipe part of the pipe into a fitting part made of a notch formed in a corner part of a plate fin of two adjacent fin groups of the first heat exchange pipe with fins, and one end of the first heat exchange pipe The evaporator and the manufacturing method of the evaporator including joining the one end part of a 2nd heat exchange pipe | tube. フィン付き第1熱交換管の屈曲管部および屈曲管部により接続された2つの直管部の端部が通される貫通穴と、第2熱交換管の直管部の端部が嵌る切り欠きと、各切り欠きの両側にそれぞれ形成された固定片とを有する1対の側板を用意すること、第2熱交換管の直管部を、フィン付き第1熱交換管の隣り合う2つのフィン群のプレートフィンの角部に形成された切り欠きからなる嵌入部内に嵌め入れた後、両側板を、フィン付き第1熱交換管におけるすべてのフィン群のプレートフィンの並び方向の外側に配置すること、フィン付き第1熱交換管の屈曲管部および屈曲管部により接続された2つの直管部の両端部をそれぞれ両側板の貫通穴に通すこと、第2熱交換管の直管部の両端部をそれぞれ両側板の切り欠き内に嵌め入れること、ならびに両側板の固定片を変形させ、固定片により第2熱交換管の直管部を挟着固定することを含む請求項18記載の蒸発器の製造方法。 A through-hole through which the end of two straight pipe parts connected by the bent pipe part and the bent pipe part of the first heat exchange pipe with fins passes, and the end where the end part of the straight pipe part of the second heat exchange pipe fits Preparing a pair of side plates each having a notch and a fixing piece formed on each side of each notch; connecting the straight pipe portion of the second heat exchange pipe to two adjacent fin heat exchange pipes; After fitting into the fitting part which consists of a notch formed in the corner | angular part of the plate fin of a fin group, both side plates are arrange | positioned on the outer side of the arrangement direction of the plate fin of all the fin groups in the 1st heat exchange pipe | tube with a fin. Passing both ends of two straight pipe parts connected by the bent pipe part and the bent pipe part of the first heat exchange pipe with fins through the through holes of both side plates, and the straight pipe part of the second heat exchange pipe Fit both ends into the cutouts on both side plates, The process according to claim 18 evaporator according to deform the fixing pieces of the side plates comprises securing clamping the straight pipe portion of the second heat exchange tubes by a fixing piece. 圧縮機、凝縮器および蒸発器を備えており、蒸発器が請求項1〜17のうちのいずれかに記載された蒸発器からなる冷凍サイクル。 A refrigeration cycle comprising a compressor, a condenser, and an evaporator, wherein the evaporator comprises the evaporator according to any one of claims 1 to 17. 断熱箱体内に請求項20記載の冷凍サイクルが設置されている冷蔵装置。 A refrigeration apparatus in which the refrigeration cycle according to claim 20 is installed in an insulating box. 断熱箱体内において、冷凍サイクルの蒸発器の下方に、輻射熱により蒸発器を加熱する除霜装置が配置されている請求項21記載の冷蔵装置。 The refrigeration apparatus according to claim 21, wherein a defrosting device for heating the evaporator by radiant heat is disposed below the evaporator of the refrigeration cycle in the heat insulating box.
JP2005234018A 2005-08-12 2005-08-12 Evaporator Expired - Fee Related JP4796800B2 (en)

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