JP2000266495A - Plate type heat exchanger - Google Patents

Plate type heat exchanger

Info

Publication number
JP2000266495A
JP2000266495A JP11066472A JP6647299A JP2000266495A JP 2000266495 A JP2000266495 A JP 2000266495A JP 11066472 A JP11066472 A JP 11066472A JP 6647299 A JP6647299 A JP 6647299A JP 2000266495 A JP2000266495 A JP 2000266495A
Authority
JP
Japan
Prior art keywords
plate
fluid
heat exchange
heat
heat exchanger
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP11066472A
Other languages
Japanese (ja)
Inventor
Osayuki Inoue
修行 井上
Toshio Matsubara
利男 松原
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.)
Ebara Corp
Original Assignee
Ebara Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Ebara Corp filed Critical Ebara Corp
Priority to JP11066472A priority Critical patent/JP2000266495A/en
Priority to EP00906712A priority patent/EP1160530A4/en
Priority to CNB008045615A priority patent/CN1158499C/en
Priority to PCT/JP2000/001329 priority patent/WO2000052411A1/en
Priority to US09/926,103 priority patent/US6817406B1/en
Publication of JP2000266495A publication Critical patent/JP2000266495A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • 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
    • F28D9/0093Multi-circuit heat-exchangers, e.g. integrating different heat exchange sections in the same unit or heat-exchangers for more than two fluids
    • 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
    • F28D3/00Heat-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 flows in a continuous film, or trickles freely, over the 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
    • F28D3/00Heat-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 flows in a continuous film, or trickles freely, over the conduits
    • F28D3/04Distributing arrangements
    • 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

Abstract

PROBLEM TO BE SOLVED: To provide a plate type heat exchanger the manufacturing and assembling costs of which can be reduced and which does not allow liquid drops to be scattered between heat-exchanging elements and fulfills a high heat- exchanging function. SOLUTION: A plate type heat exchanger which simultaneously performs heat exchange on two sets of fluids is constituted by alternately arranging pluralities of heat-exchanging elements (A) 2, each of which is constituted by putting two facing plates 1 together and uses the internal space formed between the plates 1 as the flow passage of a first fluid and the external surfaces of the plates 1 as the flow passage of a second fluid, and heat-exchanging elements (B) 2' each of which is constituted by putting two facing plates 1 together and uses the internal space formed between the plates 1 as the flow passage of a third fluid and the external surfaces of the plates 1 as the flow passage of a fourth fluid at prescribed intervals and, at the same time, installing scattering preventing means 3 which prevents the scattering of liquid drops in the spaces among the elements 2 and 2'. Each scattering preventing means 3 can be constituted of two boards so as to return scattered liquid drops to the heat transferring surfaces from which the drops are scattered.

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は、プレートを積層さ
せてプレート間に交互に2流体を流して熱交換させるプ
レート式熱交換器に係り、特に、低圧冷媒を用いる冷凍
機の蒸発器、低温再生器、凝縮器のように、少なくとも
一方の流体が低圧蒸気である場合(あるいは相変化して
蒸気化、又は蒸気から液化させる場合)に好適なプレー
式熱交換器に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a plate heat exchanger in which plates are stacked and two fluids are alternately flowed between the plates to exchange heat. The present invention relates to a play heat exchanger suitable for a case where at least one fluid is low-pressure steam (or a case where a phase changes to vaporize or liquefy from vapor) such as a regenerator and a condenser.

【0002】[0002]

【従来の技術】一般に、蒸発器出口の蒸気流速、あるい
は吸収器入口の蒸気流速は、50m/s以内程度に抑え
ないと、流動抵抗が増え、冷凍機性能が低下する。従
来、プレート式熱交換器として、図6のように、吸収器
要素2と蒸発器要素2’とをプレート面同士を向かい合
わせにして、交互に配置したものが提案されている。こ
の場合のプレート1面に対する蒸気通路の大きさは、プ
レート高さ×プレート幅となり、プレート間隙間は蒸気
流速からの制限を受けずコンパクト化が可能となる。
2. Description of the Related Art Generally, unless the vapor flow velocity at the outlet of an evaporator or the vapor velocity at the entrance of an absorber is controlled within about 50 m / s, the flow resistance increases and the performance of a refrigerator decreases. Conventionally, as a plate heat exchanger, as shown in FIG. 6, an absorber element 2 and an evaporator element 2 'have been proposed in which the plate faces face each other and are alternately arranged. In this case, the size of the steam passage with respect to the surface of the plate 1 is equal to the plate height × the plate width, and the gap between the plates is not limited by the steam flow rate, and can be made compact.

【0003】図6のような形式の熱交換器においては、
2枚のプレートを組み合わせた熱交換要素を1個ずつ製
作し、冷水ヘッダー、冷却水ヘッダーに、1個ずつ順次
取り付けていく必要があり、製作工数が大きなものにな
り、また、吸収器と蒸発器の形状が異なり部品の種類も
多くなる。さらに、例えば、吸収器要素と蒸発器要素と
を交互に配置した場合、両要素間の隙間に吸収溶液11
と冷媒液12とが同時に流下するため、液滴が飛散し、
吸収溶液が冷媒中に入ると冷媒が汚れて、沸点上昇をお
こし、蒸発温度が上昇し、冷凍機としての性能が劣化す
るし、また、伝熱面上の溶液量も減少し、濡れ難くなる
問題がある。一方、蒸発器伝熱面から、冷媒液が液滴と
して飛散し、吸収器側に入ると溶液濃度が低下して、吸
収能力が落ち、冷凍機の性能が劣化する。また、冷媒液
が蒸発せず、液のまま飛び出すことで、本来の冷凍効果
を発揮せず、効率が低下するし、また、伝熱面上の冷媒
液量も減少し、濡れ難くなる問題もある。
In a heat exchanger of the type shown in FIG.
It is necessary to manufacture one heat exchange element by combining two plates, and attach them one by one to the cold water header and the cooling water header one by one. The shapes of the vessels are different and the types of parts are also increased. Further, for example, when the absorber element and the evaporator element are alternately arranged, the absorbing solution 11
And the refrigerant liquid 12 flow down at the same time, so that the droplets scatter,
When the absorbing solution enters the refrigerant, the refrigerant is contaminated, raises the boiling point, raises the evaporation temperature, deteriorates the performance as a refrigerator, and reduces the amount of the solution on the heat transfer surface, making it hard to wet. There's a problem. On the other hand, the refrigerant liquid is scattered as droplets from the heat transfer surface of the evaporator, and when the refrigerant liquid enters the absorber side, the solution concentration is reduced, the absorption capacity is reduced, and the performance of the refrigerator is deteriorated. In addition, since the refrigerant liquid does not evaporate and jumps out as it is, the original refrigeration effect is not exhibited, the efficiency is reduced, and the amount of the refrigerant liquid on the heat transfer surface is reduced, and there is also a problem that it is difficult to get wet. is there.

【0004】[0004]

【発明が解決しようとする課題】本発明は、上記従来技
術に鑑み、部品点数が少なくて製造や組立てのコストが
軽減でき、しかも、熱交換要素間での液滴飛散もなく、
高い熱交換機能を有するようなプレート式熱交換器を提
供することを課題とする。
SUMMARY OF THE INVENTION In view of the above-mentioned prior art, the present invention reduces the number of parts, reduces the cost of manufacturing and assembling, and does not cause droplets to scatter between heat exchange elements.
An object is to provide a plate heat exchanger having a high heat exchange function.

【0005】[0005]

【課題を解決するための手段】上記課題を解決するため
に、本発明では、それぞれなった温度を有する2組の流
体を同時に熱交換するプレート式熱交換器において、互
いに向かい合うプレート2枚を一組とし、この2枚の内
側の密閉された空間を第1流体の通路とし、プレート面
を伝熱面として、プレートの外面に沿って流れる流体を
第2流体とする熱交換要素(A)と、互いに向かい合う
プレート2枚を一組とし、この2枚の内側の密閉された
空間を第3流体の通路とし、プレート面を伝熱面とし
て、プレートの外面に沿って流れる流体を第4流体とす
る熱交換要素(B)とを有し、該熱交換要素(A)と
(B)とを、各プレート面が互いに向かい合うようにし
て、所定の隙間を隔てて、複数交互に並べると共に、前
記隙間には液滴の飛散を防止するための飛散防止手段を
設けることとしたものである。
According to the present invention, there is provided a plate heat exchanger for simultaneously exchanging heat between two sets of fluids having different temperatures. A heat exchange element (A) having a pair of inner sealed spaces as a first fluid passage, a plate surface as a heat transfer surface, and a fluid flowing along the outer surface of the plate as a second fluid; A pair of plates facing each other, a sealed space inside the two plates as a third fluid passage, a plate surface as a heat transfer surface, and a fluid flowing along the outer surface of the plate as a fourth fluid. And a plurality of heat exchange elements (A) and (B) are alternately arranged at predetermined intervals with the respective plate faces facing each other. Droplets scatter in gaps It is obtained by a providing a scattering prevention means for preventing.

【0006】前記プレート式熱交換器において、熱交換
要素(A)と(B)とのプレート面上には、該熱交換要
素(A)の内側空間同士と熱交換要素(B)の内側空間
同士とを別々に連通する連通管を設けるのがよく、ま
た、前記飛散防止手段は、それぞれの飛散液を飛散元の
伝熱面に戻すように、2枚の板材で構成することができ
る。また、本発明のプレート式熱交換器において、各熱
交換要素間を連通する連通管が、各熱交換要素のプレー
トの一部分として一体に構成することができ、また、前
記交互に配置する2つの熱交換要素(A)と(B)と
が、同一形状であり、向きを逆にした対象形とすること
ができ、さらに各熱交換要素(A)及び/又は(B)の
プレート外面には第2流体及び/又は第4流体の液分配
器を配備することができる。
[0006] In the plate heat exchanger, the inner space of the heat exchange element (A) and the inner space of the heat exchange element (B) are provided on the plate surfaces of the heat exchange elements (A) and (B). It is preferable to provide a communication pipe which communicates with each other separately, and the scatter prevention means can be constituted by two plate members so as to return each scattered liquid to the heat transfer surface of the scatter source. In the plate heat exchanger of the present invention, a communication pipe communicating between the heat exchange elements can be integrally formed as a part of a plate of each heat exchange element, and the two alternately arranged two The heat exchange elements (A) and (B) have the same shape and can be symmetrical in opposite directions, and the outer surface of the plate of each heat exchange element (A) and / or (B) A liquid distributor for the second fluid and / or the fourth fluid can be provided.

【0007】[0007]

【発明の実施の形態】次に、本発明を詳細に説明する。
本発明で用いるプレートは、凹凸部を有する2枚のプレ
ートを内部に空間を形成するように重ね、その周縁部及
び両端の開口部の連通管(流体出入口)を単に重ねた時
には、全局にわたって軽く接触し(線接触し)、重ね方
向に力を加えていくと、その接触部の形状が変化して面
接触となり、前記凹凸が接触するまで、力を加えると共
に接触面が大きくなり、ろう接(フレージング)で周縁
を密封するのに好適な形状のものを用いることができ
る。すなわち、前記のプレートは、ろう接の場合、プレ
ート同士を密着させるため、力を加えながらろう接を実
施するが、この力を加えたときに、周縁部が平行とな
り、さらにプレートの凹凸が接触するので好ましい。
Next, the present invention will be described in detail.
In the plate used in the present invention, when two plates having uneven portions are overlapped so as to form a space inside, and the communication pipes (fluid ports) of the peripheral portion and the openings at both ends are simply overlapped, the plate is light over the entire station. When a contact is made (line contact) and a force is applied in the overlapping direction, the shape of the contact portion changes to form a surface contact. A shape suitable for sealing the periphery by (phrasing) can be used. That is, in the case of the above-mentioned plate, in the case of brazing, in order to make the plates adhere to each other, brazing is performed while applying a force. Is preferred.

【0008】上記のような2枚のプレートを、接触予定
部にろう材を置きながら(塗りながら)重ねると、上記
プレートの両端部に形成された開口部から上記空間の間
に流体流路を有する熱交換要素が構成される。本発明で
は、ろう接(フレージング)以外に、間にガスケットを
入れて外部から力を加える場合あるいは溶接で密閉する
場合等も含む。本発明のプレートの凹凸は、所定方向に
延びる波状パターンとして形成することができ、2次元
的に屈折する複雑な流路が比較的簡単な構成で形成でき
る。また、プレート両端の開口部連通管は、同一流路の
熱交換要素と要素の間には、他の流路の熱交換要素及び
飛散防止手段が挿入されるので、その要素及び防止手段
が挿入できる間隔と、プレート外面に流路が形成できる
間隔を設けた長さの連通管とし、該連通管をプレートの
両端の片側に設けることができ、該熱交換器の製造に際
しては、該要素間にスぺーサを挿入して、炉内で力を加
えながら、一挙にろう接することができる。
[0008] When the two plates as described above are overlapped with the brazing material placed (painted) on the portions to be contacted, a fluid flow path is formed between the spaces from the openings formed at both ends of the plates. Having a heat exchange element. In the present invention, in addition to brazing (phrasing), a case in which a gasket is inserted therebetween to apply a force from the outside or a case in which the gasket is sealed by welding is also included. The unevenness of the plate of the present invention can be formed as a wavy pattern extending in a predetermined direction, and a complicated flow path that refracts two-dimensionally can be formed with a relatively simple configuration. In addition, in the opening communicating pipes at both ends of the plate, since the heat exchange element of another flow path and the scattering prevention means are inserted between the heat exchange elements of the same flow path, the elements and the prevention means are inserted. The communication pipe can be provided on one side of both ends of the plate, and the communication pipe can be provided on one side of both ends of the plate. Can be soldered all at once by inserting a spacer into the furnace and applying force in the furnace.

【0009】このプレート両端の開口部連通管の一方
に、たちあがりを設けることにより、重ね合わせのとき
に、開口部の嵌め合いで位置決めを簡易にすることがで
きる。これにより、プレートを重ねるだけでプレート同
士の2次元的な位置決めが自然に行われるので、製造工
程が簡略化される。本発明の熱交換要素(A)と(B)
との間に挿入する飛散防止手段としては、両要素のプレ
ート表面の伝熱面を第2流体と第4流体が別々に流下し
て、両者の液滴が防止できる構造のものであればよく、
例えば、それぞれの飛散液を飛散元の伝熱面に戻すよう
に、2枚の板材で構成される邪魔板とすることができ
る。また、この挿入した邪魔板をプレート表面の凸部と
接触させ、さらに邪魔板同一を接触させることで、邪魔
板をスペーサとしてろう接部に荷重を伝えることで、熱
交換器を一挙にろう接することもできる。
Providing a swivel at one end of the communicating pipes at both ends of the plate makes it easy to position the fitting by fitting the openings when overlapping. Thus, the two-dimensional positioning of the plates is naturally performed only by overlapping the plates, thereby simplifying the manufacturing process. Heat exchange elements (A) and (B) of the present invention
The scattering prevention means to be inserted between the first and second fluids may have any structure in which the second fluid and the fourth fluid can separately flow down the heat transfer surfaces on the plate surfaces of both elements to prevent the droplets of both fluids. ,
For example, a baffle plate composed of two plate members can be used to return each scattered liquid to the heat transfer surface of the scatter source. In addition, the inserted baffle plate is brought into contact with the convex portion on the plate surface, and furthermore, the same baffle plate is brought into contact with the baffle plate to transmit a load to the brazing portion as a spacer, thereby brazing the heat exchanger at once. You can also.

【0010】以下、図面を参照して本発明を詳細に説明
する。図1は、本発明のプレート式熱交換器の一例を示
す断面構成図であり、3つの熱交換要素2、2’を交互
に結合して構成されている。熱交換要素2は、2つのプ
レート1を重ね合わせ、凸凹パターン7の接触部8と周
縁部6の間を溶接又はろう接することにより、固着して
作成されている。熱交換要素2と2’の間には、プレー
ト表面を流れる流体の飛散を防止するための邪魔板3が
配備され、熱交換要素2と2’の上部には、液分配器4
が設置されており、液分配器オリフィスの穴5から流体
がプレート表面の伝熱面に沿って流れる。このように、
プレート表面の伝熱面に接するように、あるいは少し離
して邪魔板を置いておけば、液分配器4から流下する第
2流体11又は第4流体12、例えば、吸収溶液11又
は冷媒液12が飛散しても、それらがそれぞれ蒸発器側
又は吸収器側に入り込むことが防止でき、溶液を吸収器
側に戻すことで、吸収溶液量及び冷媒液量をそれぞれ確
保することができる。回収した冷媒液12は循環して供
給できる。
Hereinafter, the present invention will be described in detail with reference to the drawings. FIG. 1 is a sectional view showing an example of the plate heat exchanger of the present invention, which is configured by alternately connecting three heat exchange elements 2, 2 ′. The heat exchange element 2 is formed by laminating the two plates 1 and fixing them by welding or brazing between the contact portion 8 of the uneven pattern 7 and the peripheral portion 6. A baffle plate 3 is disposed between the heat exchange elements 2 and 2 'to prevent the fluid flowing on the plate surface from scattering. A liquid distributor 4 is provided above the heat exchange elements 2 and 2'.
The fluid flows from the hole 5 of the liquid distributor orifice along the heat transfer surface of the plate surface. in this way,
If the baffle is placed in contact with or slightly away from the heat transfer surface of the plate surface, the second fluid 11 or the fourth fluid 12 flowing down from the liquid distributor 4, for example, the absorbing solution 11 or the refrigerant liquid 12, Even if they scatter, they can be prevented from entering the evaporator side or the absorber side, respectively, and by returning the solution to the absorber side, the amount of the absorbing solution and the amount of the refrigerant liquid can be secured, respectively. The collected refrigerant liquid 12 can be circulated and supplied.

【0011】図1において、図示されていないが、第1
流体は熱交換要素2’を連通する連通管によって供給さ
れており、また第3流体は熱交換要素2を連通する連通
管によって供給されている。そして、第1流体を冷却
水、第3流体を冷水として、吸収冷凍機のプレート式吸
収・蒸発器とすることができる。なお、吸収冷凍機の再
生器/凝縮器の組合わせに適用する場合は、熱交換要素
2の内部に冷却水、熱交換要素2’の内部に熱源流体を
連通管を通して供給し、吸収溶液11を液分配器4を介
して熱交換要素2’表面の伝熱面に流して冷媒液を蒸発
させ、熱交換要素2のプレート表面の伝熱面に冷媒を凝
縮させる。従って、熱交換要素2には液分配器4から液
を流す必要はない。
In FIG. 1, although not shown, the first
The fluid is supplied by a communication pipe communicating with the heat exchange element 2 ′, and the third fluid is supplied by a communication pipe communicating with the heat exchange element 2. Then, the plate-type absorption / evaporator of the absorption refrigerator can be obtained by using the first fluid as the cooling water and the third fluid as the cold water. When applied to a regenerator / condenser combination of an absorption refrigerator, cooling water is supplied to the inside of the heat exchange element 2 and a heat source fluid is supplied to the inside of the heat exchange element 2 ′ through the communication pipe. Flows through the liquid distributor 4 to the heat transfer surface on the surface of the heat exchange element 2 ′ to evaporate the refrigerant liquid and condense the refrigerant on the heat transfer surface on the plate surface of the heat exchange element 2. Therefore, it is not necessary to flow the liquid from the liquid distributor 4 to the heat exchange element 2.

【0012】図2は、本発明のプレート式熱交換器の別
の要部断面構成図を示す。図2においては、プレート周
縁部6、プレート凸凹交差部8で、プレート同士の接触
をさせ、また邪魔板3もプレート1及び他の邪魔板3と
も接触9させ、邪魔板3を伝熱要素2、2’間のスペー
サ代わりとすることで、プレート式熱交換器を製作加熱
時にプレート1全体のろう接部に荷重を伝えることがで
き、熱交換器全体を一挙にろう接することができるよう
になる。図3、図4、図5にプレート表面の伝熱面形状
7を示し、図3(a)は正面図、(b)は平面図であ
り、10は開口部である。図5の破線は裏側のプレート
の凸凹を表わす。図3〜5のように、凸凹を設け、プレ
ート1同士の接触部をろう接することで、強度が増す
し、またその形状を直線状波形で垂直あるいは垂直に近
い形状とすると、流れる液の偏りがなく、プレート上を
満遍なく流れる。また、プレートの表面の伝熱面は、サ
ンドブラストをかけたりして、液の濡れ性を良くし、ま
た広がりをよくすることが好ましい。このように、プレ
ート表面は親水性を高める処理を施すこと、あるいは施
しておくことが望ましい。
FIG. 2 is a sectional view showing another essential part of the plate heat exchanger of the present invention. In FIG. 2, the plates are brought into contact with each other at the plate peripheral edge 6 and the plate convex / concave intersection 8, the baffle plate 3 is also brought into contact with the plate 1 and the other baffle plate 9, and the baffle plate 3 is connected to the heat transfer element 2. By using the spacer as a spacer between the 2 ′ and the plate type heat exchanger, the load can be transmitted to the brazing portion of the entire plate 1 at the time of manufacturing and heating, so that the entire heat exchanger can be brazed at once. Become. 3, 4 and 5 show the shape 7 of the heat transfer surface on the plate surface. FIG. 3 (a) is a front view, FIG. 3 (b) is a plan view, and 10 is an opening. The dashed line in FIG. 5 represents the unevenness of the back plate. As shown in FIGS. 3 to 5, the strength is increased by providing irregularities and brazing the contact portions of the plates 1, and when the shape is made to be vertical or nearly vertical with a linear waveform, the unevenness of the flowing liquid is increased. And flows evenly over the plate. Further, it is preferable that the heat transfer surface on the surface of the plate is improved in wettability and spread of the liquid by sandblasting or the like. As described above, it is desirable that the plate surface is subjected to a treatment for increasing hydrophilicity or is subjected to the treatment.

【0013】[0013]

【発明の効果】以上説明したように、本発明によれば、
1種類又は2種類の部品から構成される熱交換要素の内
外に凸凹により屈折した流路が形成されると共に、異っ
た温度の2個の流体から熱交換する複雑なプレート式熱
交換器を、少ない部品点数と簡単な製造工程により、低
コストで効率の良い熱交換機能を持つ熱交換器を提供す
ることができる。また、本発明によれば、液滴の飛散を
防止できるので、2つの流下する流体が混合することが
なく、吸収冷凍機の吸収・蒸発器、及び再生・凝縮器と
して用いた場合、冷凍機としての性能が劣化することが
なく、濡れ難くなる問題もなく、高い熱交換機能を有す
る吸収冷凍機が得られる。
As described above, according to the present invention,
A complicated plate-type heat exchanger is provided in which a flow path bent by unevenness is formed inside and outside of a heat exchange element composed of one or two kinds of parts and heat exchanges from two fluids having different temperatures. With a small number of parts and a simple manufacturing process, a heat exchanger having an efficient heat exchange function at low cost can be provided. Further, according to the present invention, since the scattering of droplets can be prevented, the two flowing fluids do not mix, and when used as an absorption / evaporator and a regeneration / condenser of an absorption refrigerator, the refrigerator As a result, an absorption refrigerator having a high heat exchange function can be obtained without deteriorating the performance of the device and without the problem of becoming less wet.

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

【図1】本発明のプレート式熱交換器の一例を示す断面
構成図。
FIG. 1 is a sectional view showing an example of a plate heat exchanger according to the present invention.

【図2】本発明のプレート式熱交換器の一例を示す要部
断面構成図。
FIG. 2 is a cross-sectional configuration view illustrating a main part of an example of a plate heat exchanger according to the present invention.

【図3】本発明のプレート式熱交換器のプレートの表面
形状を示す構成図で、(a)正面図、(b)平面図。
FIGS. 3A and 3B are configuration diagrams showing a surface shape of a plate of the plate heat exchanger of the present invention, wherein FIG. 3A is a front view and FIG.

【図4】本発明のプレート式熱交換器の他のプレート表
面形状を示す構成図。
FIG. 4 is a configuration diagram showing another plate surface shape of the plate heat exchanger of the present invention.

【図5】本発明のプレート式熱交換器の他のプレート表
面形状を示す構成図。
FIG. 5 is a configuration diagram showing another plate surface shape of the plate heat exchanger of the present invention.

【図6】従来のプレート式熱交換器を吸収器/蒸発器に
適用した部分構成図。
FIG. 6 is a partial configuration diagram in which a conventional plate heat exchanger is applied to an absorber / evaporator.

【符号の説明】[Explanation of symbols]

1:プレート、2、2’:熱交換要素、3:邪魔板、
4:液分配器、5:オリフィス穴、6:周縁部、7:プ
レートの凸凹パターン、8:凸凹交差部、9:邪魔板接
触部、10:開口部、11:第2流体、12:第4流体
1: plate, 2 ': heat exchange element, 3: baffle plate
4: liquid distributor, 5: orifice hole, 6: peripheral portion, 7: uneven pattern of plate, 8: uneven intersection, 9: baffle plate contact portion, 10: opening, 11: second fluid, 12: second 4 fluids

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 それぞれ異った温度を有する2組の流体
を同時に熱交換するプレート式熱交換器において、互い
に向かい合うプレート2枚を1組とし、この2枚の内側
の密閉された空間を第1流体の通路とし、プレート面を
伝熱面として、プレートの外面に沿って流れる流体を第
2流体とする熱交換要素(A)と、互いに向かい合うプ
レート2枚を1組とし、この2枚の内側の密閉された空
間を第3流体の通路とし、プレート面を伝熱面として、
プレートの外面に沿って流れる流体を第4流体とする熱
交換要素(B)とを有し、該熱交換要素(A)と(B)
とを、各プレート面が互いに向かい合うようにして、所
定の隙間を隔てて、複数交互に並べると共に、前記隙間
には液滴の飛散を防止するための飛散防止手段を設けた
ことを特徴とするプレート式熱交換器。
1. A plate type heat exchanger for simultaneously exchanging heat of two sets of fluids having different temperatures, wherein two sets of plates facing each other are formed as one set, and a sealed space inside the two sets is defined as a first set. One set of a heat exchange element (A) using a fluid flowing along the outer surface of the plate as a second fluid, and a pair of two plates facing each other as a single fluid passage and a plate surface as a heat transfer surface. The inner sealed space is used as a third fluid passage, and the plate surface is used as a heat transfer surface.
A heat exchange element (B) having a fluid flowing along the outer surface of the plate as a fourth fluid, wherein the heat exchange elements (A) and (B)
A plurality of plates are arranged alternately at predetermined gaps so that the respective plate surfaces face each other, and scatter prevention means for preventing scatter of droplets is provided in the gaps. Plate heat exchanger.
【請求項2】 前記熱交換要素(A)と(B)とのプレ
ート面上には、該熱交換要素(A)の内側空間同士と熱
交換要素(B)の内側空間同士とを別々に連通する連通
管が形成されていることを特徴とする請求項1記載のプ
レート式熱交換器。
2. On the plate surfaces of the heat exchange elements (A) and (B), separate the inner spaces of the heat exchange element (A) and the inner spaces of the heat exchange element (B) separately. 2. The plate heat exchanger according to claim 1, wherein a communicating pipe is formed to communicate with the plate.
【請求項3】 前記各熱交換要素間を連通する連通管
が、各熱交換要素のプレートの一部分として構成されて
いることを特徴とする請求項2記載のプレート式熱交換
器。
3. The plate heat exchanger according to claim 2, wherein the communication pipe communicating between the heat exchange elements is configured as a part of a plate of each heat exchange element.
【請求項4】 前記飛散防止手段が、それぞれの飛散液
を飛散元の伝熱面に戻すように、2枚の板材で構成され
ることを特徴とする請求項1、2又は3に記載のプレー
ト式熱交換器。
4. The apparatus according to claim 1, wherein the scatter prevention means is constituted by two plates so as to return each scattered liquid to the heat transfer surface of the scattered source. Plate heat exchanger.
【請求項5】 前記各熱交換要素(A)及び/又は
(B)のプレート外面には、第2流体及び/又は第4流
体の液分配器が配備されることを特徴とする請求項1〜
4のいずれか1項記載のプレート式熱交換器。
5. A liquid distributor for a second fluid and / or a fourth fluid is provided on an outer surface of the plate of each of the heat exchange elements (A) and / or (B). ~
5. The plate heat exchanger according to any one of 4.
JP11066472A 1999-03-04 1999-03-12 Plate type heat exchanger Pending JP2000266495A (en)

Priority Applications (5)

Application Number Priority Date Filing Date Title
JP11066472A JP2000266495A (en) 1999-03-12 1999-03-12 Plate type heat exchanger
EP00906712A EP1160530A4 (en) 1999-03-04 2000-03-06 Plate type heat exchanger
CNB008045615A CN1158499C (en) 1999-03-04 2000-03-06 Plate type heat exchanger
PCT/JP2000/001329 WO2000052411A1 (en) 1999-03-04 2000-03-06 Plate type heat exchanger
US09/926,103 US6817406B1 (en) 1999-03-04 2000-03-06 Plate type heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11066472A JP2000266495A (en) 1999-03-12 1999-03-12 Plate type heat exchanger

Publications (1)

Publication Number Publication Date
JP2000266495A true JP2000266495A (en) 2000-09-29

Family

ID=13316773

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11066472A Pending JP2000266495A (en) 1999-03-04 1999-03-12 Plate type heat exchanger

Country Status (1)

Country Link
JP (1) JP2000266495A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101497560B1 (en) * 2013-06-05 2015-03-02 삼성중공업 주식회사 Open rack vaporizer having guide
KR101531264B1 (en) * 2013-10-10 2015-06-24 삼성중공업 주식회사 Open rack vaporizer
CN114583205A (en) * 2020-11-30 2022-06-03 丹佛斯有限公司 Heat exchanger
JP7379911B2 (en) 2019-08-02 2023-11-15 株式会社アイシン Absorption heat pump device

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101497560B1 (en) * 2013-06-05 2015-03-02 삼성중공업 주식회사 Open rack vaporizer having guide
KR101531264B1 (en) * 2013-10-10 2015-06-24 삼성중공업 주식회사 Open rack vaporizer
JP7379911B2 (en) 2019-08-02 2023-11-15 株式会社アイシン Absorption heat pump device
CN114583205A (en) * 2020-11-30 2022-06-03 丹佛斯有限公司 Heat exchanger

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