JP2000266478A - Plate heat exchanger - Google Patents

Plate heat exchanger

Info

Publication number
JP2000266478A
JP2000266478A JP11067805A JP6780599A JP2000266478A JP 2000266478 A JP2000266478 A JP 2000266478A JP 11067805 A JP11067805 A JP 11067805A JP 6780599 A JP6780599 A JP 6780599A JP 2000266478 A JP2000266478 A JP 2000266478A
Authority
JP
Japan
Prior art keywords
plate
fluid
heat exchange
plates
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.)
Granted
Application number
JP11067805A
Other languages
Japanese (ja)
Other versions
JP3969556B2 (en
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 JP06780599A priority Critical patent/JP3969556B2/en
Priority to EP00906712A priority patent/EP1160530A4/en
Priority to US09/926,103 priority patent/US6817406B1/en
Priority to PCT/JP2000/001329 priority patent/WO2000052411A1/en
Priority to CNB008045615A priority patent/CN1158499C/en
Publication of JP2000266478A publication Critical patent/JP2000266478A/en
Application granted granted Critical
Publication of JP3969556B2 publication Critical patent/JP3969556B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related 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
    • 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
    • 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

Abstract

PROBLEM TO BE SOLVED: To provide a plate heat exchanger having high heat exchange efficiency by liquid flowing down evenly on plates without dispersion of liquid droplets in liquid supply. SOLUTION: The plate heat exchanger for exchanging heat between two sets of liquids at the same time comprises a heat exchange element (A) 2 wherein two plates facing each other is integrated, a space inside the two plates is to be a route of a first fluid and a fluid flowing along the outside surfaces of the plates is to be a second fluid and a heat exchange element (B) 2' wherein two plates 1 facing each other is integrated, a space inside the two plates is to be a route of a third fluid and a fluid flowing along the outside surfaces of the plates is to be a fourth fluid. The heat exchange elements (A), (B) are provided in line plurally alternately, and liquid distributors 4 for flowing the liquids respectively are provided on upper parts of surfaces of the heat exchange elements (A) and (B). The liquid distributors comprise troughs provided with orifice holes 5 on side surfaces, or plate surfaces can be utilized as the side surfaces of the troughs.

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
ト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 plate heat exchanger suitable for a case where at least one of the fluids is low-pressure steam (or a phase-change vaporization or liquefaction from a vapor) such as a regenerator or a condenser.

【0002】[0002]

【従来の技術】一般に、蒸発器出口の蒸気速度、あるい
は吸収器入口の蒸気速度は、50m/s以内程度に抑え
ないと、流動抵抗が増え、冷凍機能が低下する。従来、
プレート式熱交換器として、図5のように、吸収器要素
2と蒸発器要素2’とをプレート面同上を向かい合わせ
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。図5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個づつ製作し、冷水ヘッダ
ー、冷却水ヘッダーに1個づつ順次取り付けていく必要
があり、製作工数がおおきなものになり、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。
2. Description of the Related Art Generally, unless the vapor 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 refrigeration function deteriorates. Conventionally,
As a plate-type heat exchanger, as shown in FIG. 5, an absorber element 2 and an evaporator element 2 'are alternately arranged with their plate surfaces facing each other. 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. In the heat exchanger of the type as shown in FIG. 5, it is necessary to manufacture one heat exchange element by combining two plates, and sequentially attach them one by one to the cold water header and the cooling water header. However, the shapes of the absorber and the evaporator are different, and the types of parts are increased.

【0003】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、両要素間の隙間のプレート表面
の頂部に吸収溶液11と冷媒液12とを同時に供給する
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、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、冷凍機としての性能が劣化する。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。
Further, for example, when an absorber element and an evaporator element are alternately arranged, since the absorbing solution 11 and the refrigerant liquid 12 are simultaneously supplied to the top of the plate surface in the gap between the two elements, the droplets scatter. When the absorbing solution enters the refrigerant, the refrigerant is contaminated, raises the boiling point, raises the evaporation temperature, degrades the performance as a refrigerator, and also reduces the amount of the solution on the heat transfer surface, and becomes wet. There is a problem that becomes difficult. On the other hand, when the refrigerant liquid scatters as droplets and enters the absorber side, the solution concentration decreases,
The absorption capacity is reduced, and the performance as a 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、熱交換要素間への液体の供給に際して、液滴
の飛散がなく、プレート上を液体が平均して流下し、高
い熱交換効率を有する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 The present invention has been made in view of the above-mentioned prior art, and when liquid is supplied between heat exchange elements, the liquid does not scatter and the liquid flows down on the plate on average, resulting in high heat. It is an object to provide a plate heat exchanger having an exchange efficiency.

【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、それぞれ異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、熱交換要素(A)及び(B)の表面上部に
それぞれ第2流体及び第4流体を流す液分配器を設ける
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 two sets of fluids having different temperatures.
A set of two plates facing each other is used, a sealed space inside the two plates is used as a first fluid passage, a plate surface is used as a heat transfer surface, and a fluid flowing along the outer surface of the plate is used as a second fluid. A heat exchange element (A) and a pair of plates facing each other form a set, a sealed space inside the two plates serves as a third fluid passage, and a plate surface serves as a heat transfer surface. A heat exchange element (B) having a flowing fluid as a fourth fluid, wherein the heat exchange elements (A) and (B) are separated by a predetermined gap so that the respective plate faces face each other, A plurality of liquid distributors are arranged alternately, and a liquid distributor through which the second fluid and the fourth fluid flow respectively is provided above the surfaces of the heat exchange elements (A) and (B) in the gap.

【0006】前記プレート式熱交換器において、液分配
器としては、側面にオリフィス穴を設けた樋を用いるこ
とができ、また、樋状で、樋の側面としてプレート面を
利用することもできる。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のがよい。
In the plate type heat exchanger, a gutter having an orifice hole on a side surface can be used as a liquid distributor, and a plate surface can be used as a gutter-like side surface of the gutter. The heat exchange elements (A) and (B)
It is preferable that a communication pipe is provided on the plate surface for communicating the inner space of the heat exchange element (A) and the inner space of the heat exchange element (B) separately.

【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、全周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, two plates having uneven portions are overlapped so as to form a space inside, and when the communication pipes (fluid inlets and outlets) of the peripheral portion and the openings at both ends are simply overlapped, the entire periphery is covered. When light contact (line contact) is applied and a force is applied in the overlapping direction, the shape of the contact portion changes to form surface contact. A shape suitable for sealing the periphery by tangling (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器が構成される。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
的に屈曲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、熱交換器の製造に関して
は、該要素間にスペーサを挿入して、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 exchanger. 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 two-dimensionally bent channel can be formed with a relatively simple configuration. Further, in the opening communicating pipes at both ends of the plate, since the heat exchange element and the scattering prevention means of another flow path are inserted between the heat exchange elements of the same flow path, the element and the prevention means can be inserted. A communication pipe of a length having an interval and an interval at which a flow path can be formed on the outer surface of the plate is provided, and the communication pipe can be provided on one side of both ends of the plate.For the manufacture of a heat exchanger, a spacer is provided between the elements. It can be inserted and brazed all at once while 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の表面上部に設
ける液分配器は、プレート表面と平行して樋状に設けら
れ、プレート表面に向けて液を流下するオリフィス穴が
側面に設けられており、また、該液分配器は、樋の一側
面として、プレート面を利用してもよい。これにより、
プレート表面に流体を供給する際の液の飛散を防止し
て、プレート表面上に流体を満遍なく平均に流すことが
できる。また、本発明の熱交換要素(A)と(B)との
間の液分配器の下部には、飛散防止手段を挿入すること
ができ、それにより、プレート面上に供給される流体の
飛散をより防止することができる。該飛散防止手段とし
ては、それぞれの飛散液を飛散元の伝熱面に戻すように
2枚の板材で構成される邪魔板とすることができる。
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. The liquid distributor provided on the upper surface of the heat exchange element of the present invention is provided in a gutter shape in parallel with the plate surface, and an orifice hole for flowing liquid toward the plate surface is provided on a side surface. The liquid distributor may use a plate surface as one side surface of the gutter. This allows
The liquid can be prevented from being scattered when the fluid is supplied to the plate surface, and the fluid can be evenly distributed over the plate surface. Further, a scattering prevention means can be inserted in the lower part of the liquid distributor between the heat exchange elements (A) and (B) of the present invention, whereby the scattering of the fluid supplied on the plate surface can be achieved. Can be further prevented. The scatter prevention means may be a baffle plate composed of two plates so as to return each scattered liquid to the heat transfer surface of the scatter source.

【0010】本発明の熱交換要素は、外表面を流体が流
れ、内部流体との間でプレートの伝熱面を介して熱交換
を行うため、外表面を流れる流体は、該伝熱面に広が
り、乾いた面がないように濡れ性を良くする必要があ
る。そのため、熱交換要素の伝熱面を構成するプレート
はステンレス鋼製とし、その外表面に、電解的に溶解し
た多孔質層、クロムの溶融塩浴で処理した酸化クロムの
拡散層又は小さな多数の凹みを設けるか、あるいは、梨
地状にするのがよい。前記の外表面に多数の小さな凹み
を設けるには、プレートの成形時に、金型表面の多数の
小さな突起を転写するように凹みを設けることにより、
また、梨地状にするには、素材表面が既に梨地状になっ
ているもの、例えばステンレス鋼素材の表面を薄板製造
時にローラーで梨地状に形成したものを用いるか、ある
いは、表面を放電加工により形成することができ、放電
加工は、水中で行うことが好ましく、また、放電加工
は、プレート薄板(素材)のとき行っても、プレート成
形後で、プレート熱交換器を製作する際に行ってもよ
い。素材時であれば、電極形状を平面としておき、電極
を動かしながら、あるいは、薄板を動かしながら、パル
ス電流を与えればよく、電極形状が簡易化できる。
In the heat exchange element of the present invention, the fluid flows on the outer surface and exchanges heat with the internal fluid via the heat transfer surface of the plate. It is necessary to improve the wettability so that there is no spread and no dry surface. Therefore, the plate constituting the heat transfer surface of the heat exchange element is made of stainless steel, and on its outer surface, a porous layer electrolytically dissolved, a diffusion layer of chromium oxide treated with a molten salt bath of chromium, or a large number of small It is good to provide a dent or make it satin-like. In order to provide a large number of small depressions on the outer surface, by providing a depression so as to transfer a large number of small protrusions on the mold surface during molding of the plate,
In addition, in order to form a matte surface, a material whose surface is already matte, for example, a stainless steel material whose surface is formed in a matte shape with a roller at the time of manufacturing a thin plate, or the surface is formed by electric discharge machining It is preferable that the electric discharge machining is performed in water, and the electric discharge machining is performed when manufacturing the plate heat exchanger after forming the plate, even when performing the thin plate (material). Is also good. In the case of a raw material, the electrode shape may be made flat, and a pulse current may be applied while moving the electrode or while moving the thin plate, so that the electrode shape can be simplified.

【0011】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つずつの熱交換要素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、凹凸パターンの接触部と周
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、2’の上部には、液分配器4
が設置されており、液分配器のオリフィス穴5から流体
がプレート表面の伝熱面に沿って流れる。
Hereinafter, the present invention will be described in detail with reference to the drawings. FIG. 1 is a sectional view showing an example of a plate heat exchanger according to 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 of the uneven pattern and the peripheral portion 6. A baffle plate 3 is provided 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, 2'.
The fluid flows from the orifice hole 5 of the liquid distributor along the heat transfer surface of the plate surface.

【0012】このように、プレート表面の伝熱面に接す
るように、液分配器を設置し、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1
2、例えば、吸収溶液11又は冷媒液12の飛散を防止
することができ、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、さらに邪魔板を設置することで、
溶液を吸収器側に戻すことができ、また冷媒液を蒸発器
側に戻すことができ、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。熱交換要素2の下には冷媒受
皿7が設けられており、蒸発しない冷媒液12を回収す
る。回収した冷媒液12は循環して供給できる。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。
As described above, if the liquid distributor is installed so as to be in contact with the heat transfer surface of the plate surface and the baffle plate is placed,
Second fluid 11 or fourth fluid 1 flowing down from liquid distributor 4
2. For example, it is possible to prevent the absorption solution 11 or the refrigerant liquid 12 from scattering, to prevent the absorption solution 11 or the refrigerant liquid 12 from entering the evaporator side or the absorber side, respectively, and to install a baffle plate.
The solution can be returned to the absorber side, the refrigerant liquid can be returned to the evaporator side, and the absorption solution amount and the refrigerant liquid amount can be secured. A refrigerant tray 7 is provided below the heat exchange element 2, and collects a refrigerant liquid 12 that does not evaporate. The collected refrigerant liquid 12 can be circulated and supplied. In FIG. 1, although not shown, the first 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.

【0013】また、図2に、液分配器4を邪魔板3と一
体に形成した場合を示し、このように構成することもで
きる。図3に、吸収冷凍機の再生器/凝縮器の組合わせ
に適用する場合を示し、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’
のプレート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12を凝縮さ
せる。凝縮した冷媒液12は冷媒受皿7で回収される。
従って、熱交換要素2には液分配器を設置する必要はな
いが、付いていても液を導入しなければよい。図4に、
本発明の他の液分配器を設置したプレート式熱交換器の
概略構成図を示し、(a)は正面図、(b)は部分平面
図である。このように、液分配器4の樋状の一側面をプ
レート表面で兼用することができ、この場合、オリフィ
ス穴は、プレート表面との接触部に設けた切り欠き8と
することができる。
FIG. 2 shows a case where the liquid distributor 4 is formed integrally with the baffle plate 3, and such a configuration can be adopted. FIG. 3 shows a case where the present invention is applied to a combination of a regenerator / condenser of an absorption refrigerator, and cooling water,
A heat source fluid is supplied into the heat exchange element 2 ′ through the communication pipe, and the absorbing solution 11 is supplied through the liquid distributor 4 to the heat exchange element 2 ′.
The refrigerant liquid is allowed to flow on the heat transfer surface on the plate surface to evaporate the refrigerant liquid, and the refrigerant 12 is condensed on the heat transfer surface on the plate surface of the heat exchange element 2. The condensed refrigerant liquid 12 is collected in the refrigerant tray 7.
Therefore, it is not necessary to install a liquid distributor in the heat exchange element 2, but it is sufficient if no liquid is introduced even if it is attached. In FIG.
FIG. 3 is a schematic configuration diagram of a plate heat exchanger provided with another liquid distributor of the present invention, where (a) is a front view and (b) is a partial plan view. As described above, one side of the gutter-like side of the liquid distributor 4 can also be used as the plate surface, and in this case, the orifice hole can be a notch 8 provided in a contact portion with the plate surface.

【0014】[0014]

【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種類の部分から構成される熱交換要素の内
外に凹凸により屈折した流路が形成されると共に、異な
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。さらに、本発明によれば、プ
レート面上に流下する流体を満遍なく平均して流すこと
ができるので、熱交換効率の良いプレート式熱交換器が
得られた。
As described above, according to the present invention,
A complicated plate-type heat exchanger, in which a flow path bent by unevenness is formed inside and outside of a heat exchange element composed of one or two types of parts and exchanges heat from two fluids having different temperatures, With a small number of parts and a simple manufacturing process,
A heat exchanger having a low-cost and efficient heat exchange function can be provided. Further, according to the present invention, since the scattering of the liquid 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, it can be used as a refrigerator. Thus, an absorption refrigerator having a high heat exchange function can be obtained without deteriorating the performance of the device and without causing a problem that it becomes difficult to get wet. Further, according to the present invention, since the fluid flowing down on the plate surface can be evenly distributed on the plate surface, a plate heat exchanger having good heat exchange efficiency can be obtained.

【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他の例を示す断
面構成図。
FIG. 2 is a sectional configuration view showing another example of the plate heat exchanger of the present invention.

【図3】本発明のプレート式熱交換器の他の例を示す断
面構成図。
FIG. 3 is a sectional view showing another example of the plate heat exchanger of the present invention.

【図4】本発明のプレート式熱交換器の別の例を示す概
略構成図で、(a)正面図、(b)部分平面図。
FIG. 4 is a schematic configuration diagram showing another example of the plate heat exchanger of the present invention, in which (a) is a front view and (b) is a partial plan view.

【図5】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. 5 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:冷
媒受皿、8:切り欠き、11:第2流体(吸収溶液)、
12:第4流体(冷媒液)
1: plate, 2 ': heat exchange element, 3: baffle plate
4: liquid distributor, 5: orifice hole, 6: peripheral part, 7: refrigerant tray, 8: notch, 11: second fluid (absorbing solution),
12: Fourth fluid (refrigerant liquid)

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】それぞれ異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、
熱交換要素(A)及び(B)の表面上部にそれぞれ第2
流体及び第4流体を流す液分配器を設けたことを特徴と
するプレート式熱交換器。
1. A plate heat exchanger for simultaneously exchanging heat of two sets of fluids having different temperatures, wherein two plates facing each other form a set, and a sealed space inside the two plates is defined as a first space. A heat exchange element (A) in which a fluid flows along the plate surface as a heat transfer surface, and a fluid flowing along the outer surface of the plate as a second fluid, and a pair of two plates facing each other are formed as a set. A closed space of the third fluid passage, the plate surface 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)
And, in such a manner that the respective plate surfaces face each other, with a predetermined gap therebetween, and a plurality of them are alternately arranged, and in the gap,
Each of the heat exchange elements (A) and (B) has a second
A plate type heat exchanger comprising a liquid distributor for flowing a fluid and a fourth fluid.
【請求項2】前記液分配器が、側面にオリフィス穴を設
けた樋であることを特徴とする請求項1に記載のプレー
ト式熱交換器。
2. The plate heat exchanger according to claim 1, wherein the liquid distributor is a gutter having an orifice hole on a side surface.
【請求項3】前記液分配器が、樋状であり、樋の側面と
してプレート面を利用していることを特徴とする請求項
1又は2に記載のプレート式熱交換器。
3. The plate heat exchanger according to claim 1, wherein the liquid distributor has a gutter shape, and a plate surface is used as a side surface of the gutter.
【請求項4】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、2又は3
に記載のプレート式熱交換器。
4. The space inside the heat exchange element (A) and the space inside the heat exchange element (B) are separately provided on the plate surfaces of the heat exchange elements (A) and (B). 4. A communication pipe for communication is formed.
4. The plate heat exchanger according to 1.
JP06780599A 1999-03-04 1999-03-15 Plate heat exchanger Expired - Fee Related JP3969556B2 (en)

Priority Applications (5)

Application Number Priority Date Filing Date Title
JP06780599A JP3969556B2 (en) 1999-03-15 1999-03-15 Plate heat exchanger
EP00906712A EP1160530A4 (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
PCT/JP2000/001329 WO2000052411A1 (en) 1999-03-04 2000-03-06 Plate type heat exchanger
CNB008045615A CN1158499C (en) 1999-03-04 2000-03-06 Plate type heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP06780599A JP3969556B2 (en) 1999-03-15 1999-03-15 Plate heat exchanger

Publications (2)

Publication Number Publication Date
JP2000266478A true JP2000266478A (en) 2000-09-29
JP3969556B2 JP3969556B2 (en) 2007-09-05

Family

ID=13355546

Family Applications (1)

Application Number Title Priority Date Filing Date
JP06780599A Expired - Fee Related JP3969556B2 (en) 1999-03-04 1999-03-15 Plate heat exchanger

Country Status (1)

Country Link
JP (1) JP3969556B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008501925A (en) * 2004-06-02 2008-01-24 プジョー シトロエン オトモビル エスアー Heat exchange heat transfer device for automobile
KR101556199B1 (en) * 2013-07-19 2015-09-30 삼성중공업 주식회사 Apparatus for liquefied gas vaporization

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008501925A (en) * 2004-06-02 2008-01-24 プジョー シトロエン オトモビル エスアー Heat exchange heat transfer device for automobile
JP4721192B2 (en) * 2004-06-02 2011-07-13 プジョー シトロエン オトモビル エスアー Heat exchange heat transfer device for automobile
KR101556199B1 (en) * 2013-07-19 2015-09-30 삼성중공업 주식회사 Apparatus for liquefied gas vaporization

Also Published As

Publication number Publication date
JP3969556B2 (en) 2007-09-05

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