JPS61225559A - Heat exchanger - Google Patents

Heat exchanger

Info

Publication number
JPS61225559A
JPS61225559A JP60068252A JP6825285A JPS61225559A JP S61225559 A JPS61225559 A JP S61225559A JP 60068252 A JP60068252 A JP 60068252A JP 6825285 A JP6825285 A JP 6825285A JP S61225559 A JPS61225559 A JP S61225559A
Authority
JP
Japan
Prior art keywords
section
flow path
heat
plate
refrigerant vapor
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
JP60068252A
Other languages
Japanese (ja)
Inventor
哲郎 古川
井上 司郎
雅晴 古寺
馬場 弘
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.)
Hitachi Zosen Corp
Original Assignee
Hitachi Zosen 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 Hitachi Zosen Corp filed Critical Hitachi Zosen Corp
Priority to JP60068252A priority Critical patent/JPS61225559A/en
Publication of JPS61225559A publication Critical patent/JPS61225559A/en
Pending legal-status Critical Current

Links

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は、吸収ヒートポンプや吸収冷凍機などに採用さ
れる熱交換装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to a heat exchange device employed in absorption heat pumps, absorption refrigerators, and the like.

従来の技術 従来の例えば吸収冷凍機は第7図に示すように、蒸発器
(60)、吸収器(61)、熱回収器(62)、再生器
(68)、凝縮器(64)など少なくとも5つの熱交換
器により構成されており、そして、これら熱交換器に亘
って内部流体を流す内部流体用配管(65)や、冷水配
管(66)、熱源水配管(67)、冷却水配管(68)
などを設けている。
2. Description of the Related Art A conventional absorption refrigerator, for example, as shown in FIG. It is composed of five heat exchangers, and includes internal fluid piping (65) for flowing internal fluid across these heat exchangers, cold water piping (66), heat source water piping (67), and cooling water piping ( 68)
etc. are established.

発明が解決しようとする問題点 上記のような従来構成によると、これらのアセンブル、
すなわち相対的据付け、配管、保温などの作業が多くあ
ってコストアップの原因となり、またリークなどのトラ
ブルの原因ともなる。
Problems to be Solved by the Invention According to the conventional configuration as described above, these assemblers,
That is, there is a lot of work involved in relative installation, piping, heat insulation, etc., which increases costs and also causes troubles such as leaks.

問題点を解決するための手段 上記問題点を解決すべく本発明における熱交換装置は、
蒸発器用区画部と吸収器用区画部と再生器用区画部と凝
縮器用区画部とを区割り形成した内部流体区割板を設け
ると共に、前記各区画部に対応する外部流体路を形成し
た外部流体区割板と伝熱板とを設け、前記伝熱板を中に
して内部流体区割板と外部流体区割板とを交互に重ね合
わせたのち、両側に外板を配設して一体化している。
Means for Solving the Problems In order to solve the above problems, the heat exchange device according to the present invention includes:
An external fluid partition is provided with an internal fluid partition plate that divides an evaporator partition, an absorber partition, a regenerator partition, and a condenser partition, and forms an external fluid path corresponding to each partition. A plate and a heat transfer plate are provided, and after the internal fluid partition plate and the external fluid partition plate are stacked alternately with the heat transfer plate inside, outer plates are placed on both sides to integrate them. .

作用 かかる本発明構成によると、複数の熱交換器部分を板積
み重ねにより集積し得る。
According to the configuration of the present invention, a plurality of heat exchanger parts can be integrated by stacking plates.

実施例 以下に本発明の一実施例を第1図〜第6図に基づいて説
明する。
EXAMPLE An example of the present invention will be described below with reference to FIGS. 1 to 6.

(1)は外板、(2)は内部流体区割板、(3)は外部
流体区割板、(4)は伝熱板で、これらは厚さは異なる
が外形状は同一にしである。
(1) is the outer plate, (2) is the internal fluid partition plate, (3) is the external fluid partition plate, and (4) is the heat transfer plate, which have different thicknesses but the same external shape. .

前記外板(1)は矩形平板で、穿孔など何んら加工は施
こしてない。
The outer plate (1) is a rectangular flat plate without any processing such as perforations.

前記内部流体区割板(2)には、下方から順次上方に、
蒸発器用区画部(5)と、吸収器用区画部(6)と、熱
回収器用区画部(7)と、再生器用区画部(8)と、凝
縮器用区画部(9)とが区割り形成されている。−側端
には縦仕切りQOが設けられ、冷媒水である内部流体(
ロ)を凝縮器用区画部(9)から蒸発器用区画部〈5)
に自然流動させる流路(2)を形成している。前記蒸発
器用区画部(5)と吸収器用区画部(6)との間に位置
する第1横仕切り(至)には冷媒蒸気流路α→が形成さ
れ、また吸収器用区画部(6)の下端と熱回収器用区画
部(7)の下端とは、循環ポンプ(至)を有する循環通
路Q時で連通しである。前記吸収器用区画部(6)と熱
回収用区画部(7)との間に位置する第2横仕切りQカ
の下方には第8横仕切り(至)が配設され、両横仕切り
(ロ)(財)間に通路Q’Jを形成すると共に、第3横
仕切抄(ト)に多数形成した通孔曽により通路Qeを吸
収器用区画部(6)に連通している。熱回収器用区画部
(7)と再生器用区画部(8)との間に位置する第4横
仕切り(2)と、その下方に位置する第5横仕切ゆ■と
により熱回収器用区画部(7)は蛇行状に形成され、ま
た再生器用区画部(8)の側部には濃液を落下させる循
環通路に)が形成されている。そして再生器用区画部(
8)と凝縮器用区画部(9)との間に位置する第6横仕
切り弼には冷媒蒸気流路四が形成される。
The internal fluid partition plate (2) includes, sequentially from the bottom to the top,
An evaporator section (5), an absorber section (6), a heat recovery device section (7), a regenerator section (8), and a condenser section (9) are divided and formed. There is. - A vertical partition QO is provided at the side end, and the internal fluid, which is refrigerant water (
b) from the condenser compartment (9) to the evaporator compartment (5)
A flow path (2) is formed to allow natural flow. A refrigerant vapor flow path α→ is formed in the first horizontal partition located between the evaporator compartment (5) and the absorber compartment (6), and the absorber compartment (6) has a refrigerant vapor flow path α→. The lower end and the lower end of the heat recovery section (7) communicate with each other through a circulation passage Q having a circulation pump. An eighth horizontal partition (to) is disposed below the second horizontal partition Q located between the absorber compartment (6) and the heat recovery compartment (7), and both horizontal partitions (RO) are arranged below the second horizontal partition Q. ) (Incorporated) A passage Q'J is formed between them, and the passage Qe is communicated with the absorber compartment (6) through a large number of through holes formed in the third horizontal partition (G). The heat recovery device section ( 7) is formed in a serpentine shape, and a circulation passage for dropping the concentrated liquid is formed on the side of the regenerator compartment (8). And the regenerator compartment (
A refrigerant vapor flow path 4 is formed in the sixth horizontal partition located between the condenser section 8) and the condenser compartment (9).

前記外部流体区割板(3)は、各区画部(5) (6)
 (7) (8) (9)に対応する外部流体路を形成
している。すなわち蒸発器用区画部(5)に対応して冷
水流路部(至)が形成され、この冷水流路部(7)に連
通ずる給水ノズル(ロ)と排水ノズル(至)とを設けて
、冷水(至)を流すべ(構成しである。そして吸収器用
区画部(6)に対応して下位冷却水流路部(2)が形成
され、この下位冷却水流路部−に給水ノズル(2)を通
して冷却水−を供給すべく構成しである。前記熱回収器
用区画部(7)に対応して濃液留め部(ロ)が形成され
る。さらに再生器用区画部(8)に対応して熱源水流路
部■が形成され、この熱源水流路部(2)に連通ずる給
水ノズル(至)と排水ノズル(イ)とを設けて、熱源水
(ロ)を流すべく構成しである。前記凝縮器用区画部(
9)に対応して上位冷却水流路部−が形成され、この上
位冷却水流路部(6)に排水ノズル彎を連通ずると共に
、前記下位冷却水流路(至)に通路(ロ)を介して連通
している。
The external fluid partition plate (3) has respective partition parts (5) (6).
(7) (8) An external fluid path corresponding to (9) is formed. That is, a cold water passage part (to) is formed corresponding to the evaporator partition part (5), and a water supply nozzle (b) and a drainage nozzle (to) that communicate with this cold water passage part (7) are provided. A lower cooling water passage part (2) is formed corresponding to the absorber partition part (6), and a water supply nozzle (2) is formed in this lower cooling water passage part. A concentrated liquid holding part (b) is formed corresponding to the heat recovery device partition part (7). Furthermore, a concentrated liquid holding part (b) is formed corresponding to the regenerator partition part (8). A heat source water flow path section (2) is formed, and a water supply nozzle (to) and a drainage nozzle (a) communicating with this heat source water flow path section (2) are provided to flow the heat source water (b). Condenser compartment (
An upper cooling water passage section is formed corresponding to (9), and a drain nozzle curve is communicated with this upper cooling water passage section (6), and a passage (b) is connected to the lower cooling water passage (to). It's communicating.

前記冷水流路部曽と下位冷却水流路部(財)の側部間に
亘って下位冷媒蒸気留め部−が形成され、また熱源水流
路部に)と上位冷却水流路部(至)との間に上位冷媒蒸
気留め部に)を形成している。そして(54)は内部流
体区画板(3)に形成された凝縮器用区画部(9)の真
空を維持するために設けられる真空ポンプ(図示せず)
に連通ずるための通路である。
A lower refrigerant vapor retaining portion is formed between the cold water flow path portion and the side portion of the lower cooling water flow path portion, and a lower refrigerant vapor retaining portion is formed between the heat source water flow path portion and the upper cooling water flow path portion. In between, an upper refrigerant vapor retaining section) is formed. And (54) is a vacuum pump (not shown) provided to maintain the vacuum of the condenser compartment (9) formed in the internal fluid compartment plate (3).
It is a passageway to connect to.

前記伝熱板(4)は、冷媒蒸気流路C14と下位冷媒蒸
気留、め部■とを連通ずる下位ホール曽と、冷媒蒸気流
路(ハ)と上位冷媒蒸気留め部−とを連通する上位ホー
ル(51)と、循環経路に)と濃液留め部(ロ)とを連
通ずる導入孔(52)と、濃液留め部(ロ)と通路α呻
とを連通する導出孔(53)と、真空ポンプに連通ずる
通路(55)とが形成されている。前記伝熱板(4)を
中にして内部流体区割板(2)と外部流体区割板(3)
とが交互に重ね合わされ、そして両側に外板(1)を配
設した状態で、隣接する板間をろう付けなどにより溶接
し一体化している。
The heat exchanger plate (4) communicates the lower hole which communicates the refrigerant vapor flow path C14 with the lower refrigerant vapor retainer and the upper refrigerant vapor retainer. An introduction hole (52) that communicates between the upper hole (51), the circulation path) and the concentrated liquid retaining part (b), and an outlet hole (53) that communicates the concentrated liquid retaining part (b) with the passage α. and a passageway (55) communicating with the vacuum pump. An internal fluid partition plate (2) and an external fluid partition plate (3) with the heat transfer plate (4) inside.
are alternately stacked on top of each other, and with outer plates (1) disposed on both sides, adjacent plates are welded together by brazing or the like to integrate them.

上記実施例によると、内部流体区画板(2)の凝縮器用
区画部(9)で凝縮された冷媒水である内部流体C11
)は、流路(2)を通って蒸発器用区画部(5)に流入
する。ここで冷水流路部(7)を流れる冷水(至)との
間で伝熱板(4)を介して熱交換され、それによって生
じた冷媒蒸気は冷媒蒸気流路α4を通って吸収器用区画
部(6)に流入する。前記冷水(至)は冷えて出て行く
According to the above embodiment, the internal fluid C11 is refrigerant water condensed in the condenser compartment (9) of the internal fluid compartment plate (2).
) enters the evaporator compartment (5) through the channel (2). Here, heat is exchanged with the cold water flowing through the cold water flow path section (7) via the heat transfer plate (4), and the resulting refrigerant vapor passes through the refrigerant vapor flow path α4 into the absorber section. It flows into part (6). The cold water cools down and leaves.

なお蒸発器用区画部(5)での気液分離を行なわせるた
めに広い空間が必要であり、これは下位ホール曽を介し
て連通ずる下位冷媒蒸気留め部−が利用される。吸収器
用区画部(6)の冷媒蒸気は、通孔■から吸収器用区画
部(6)に排出される濃吸収液である内部流体に吸収さ
れ、この吸収のきいに発生する熱は下位冷却水流路部(
至)を流れる冷却水(至)と伝熱板(4)を介して熱交
換される。一方、冷媒気を吸収して希釈された希吸収液
である内部流体(ロ)は、循環ポンプ(至)の作動によ
り循環通路QQを介して熱回収器用区画部(7〕に送ら
れ、そして再生器用区画部(8)へと移る。再生器用区
画部(8)の内部流体(ロ)は、熱源水流路部(至)を
流れる熱源水ゆと伝熱板(4)を介して熱交換され、そ
れによって生じた冷媒蒸気が冷媒蒸気流路四を通って凝
縮器用区画部(9)に流入する。その際の気液分離のた
めの空間は、上位ホール(51)を介して連通ずる上位
冷媒蒸気留め部−が利用される。凝縮器用区画部(9)
内の冷媒蒸気は、下位冷却水流路部(ロ)から通路−を
通って上位冷却水流踏部的を流れる冷却水(至)と伝熱
板(4)を介して熱交換され、再び液化されて前述した
ように流路(財)内を流れて行く。再生器用区画部(8
)の濃縮された吸収液である内部流体(ロ)の一部は、
循環経路(ホ)と導入孔(52)とを介して濃液留め部
(2)に流入し、熱回収器用区画部内の希吸収液である
内部流体(ロ)と伝熱板(4)を介して熱交換される。
Note that a wide space is required to perform gas-liquid separation in the evaporator compartment (5), and a lower refrigerant vapor retaining section communicating through the lower hole is utilized for this purpose. The refrigerant vapor in the absorber compartment (6) is absorbed by the internal fluid, which is a concentrated absorption liquid, which is discharged from the through hole (■) into the absorber compartment (6), and the heat generated during this absorption is transferred to the lower cooling water stream. Road section (
Heat is exchanged with the cooling water (4) flowing through the heat exchanger plate (4). On the other hand, the internal fluid (b), which is a diluted absorption liquid that absorbs refrigerant air, is sent to the heat recovery device compartment (7) through the circulation passage QQ by the operation of the circulation pump (to), and Moving on to the regenerator compartment (8), the internal fluid (b) of the regenerator compartment (8) exchanges heat with the heat source water flowing through the heat source water flow path (to) via the heat transfer plate (4). The resulting refrigerant vapor flows through the refrigerant vapor flow path 4 into the condenser compartment (9).The space for gas-liquid separation at this time is communicated via the upper hole (51). The upper refrigerant vapor retention section is used. Condenser section (9)
The refrigerant vapor inside is heat exchanged with the cooling water flowing from the lower cooling water flow path section (B) through the passageway through the upper cooling water flow section through the heat transfer plate (4), and is liquefied again. As mentioned above, it flows through the channel (goods). Regenerator compartment (8
) A part of the internal fluid (b), which is the concentrated absorption liquid, is
It flows into the concentrated liquid retention part (2) through the circulation path (E) and the introduction hole (52), and the internal fluid (B), which is the dilute absorption liquid in the heat recovery section, and the heat exchanger plate (4). heat is exchanged through the

そして導出孔(58)から通路Qlへと流れ、通孔(1
)を介して吸収器用区画部(6)に排出される。
Then, it flows from the outlet hole (58) to the passage Ql, and the through hole (1
) to the absorber compartment (6).

なお両流路α4(2)や通路(2)などは、伝熱板(4
)をプレスにより凹凸成形して区割すしてもよい。
Note that both channels α4 (2) and passages (2) are connected to the heat exchanger plate (4).
) may be partitioned by pressing into concavo-convex shapes.

発明の効果 上記構成の本発明によると、複数の熱交換器部分を板積
み重ねにより集積することができ、したがって相対的据
付け、配管、保温などの作業を製作上不要にできて安価
に提供できるとともに、トラブルが少なく信頼性の高い
装置を提供できる。
Effects of the Invention According to the present invention having the above configuration, a plurality of heat exchanger parts can be integrated by stacking plates, and therefore operations such as relative installation, piping, and heat insulation are not required in production, and the product can be provided at low cost. , it is possible to provide a highly reliable device with fewer troubles.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図〜第6図は本発明の一実施例を示し、第1図は一
体化状態での正面図、第2図は内部流体区割板の縦断側
面図、第8図は外部流体区割板の縦断側面図、第4図は
伝熱板の側面図、第5図は一体化状態での第2図〜第4
図におけるA−A断面図、第6図は同B−B断面図、第
7図は従来例を示すフローである。
Figures 1 to 6 show one embodiment of the present invention, with Figure 1 being a front view in an integrated state, Figure 2 being a longitudinal side view of the internal fluid partition plate, and Figure 8 being the external fluid partition plate. Fig. 4 is a side view of the heat exchanger plate, and Fig. 5 is a longitudinal side view of the split plate, and Fig. 5 is a side view of the heat transfer plate in the integrated state.
6 is a sectional view taken along line AA in the figure, FIG. 6 is a sectional view taken along line BB, and FIG. 7 is a flowchart showing a conventional example.

Claims (1)

【特許請求の範囲】 1、蒸発器用区画部と吸収器用区画部と再生器用区画部
と凝縮器用区画部とを区割り形成した内部流体区割板を
設けると共に、前記各区画部に対応する外部流体路を形
成した外部流体区割板と伝熱板とを設け、前記伝熱板を
中にして内部流体区割板と外部流体区割板とを交互に重
ね合わせたのち、両側に外板を配設して一体化したこと
を特徴とする熱交換装置。 2、蒸発器用区画部と吸収器用区画部とを連通する冷媒
蒸気流路と、再生器用区画部と凝縮器用区画部とを連通
する冷媒蒸気流路と、凝縮器用区画部と蒸発器用区画部
とを連通する流路とを、内部流体区割板に区割形成した
ことを特徴とする特許請求の範囲第1項に記載の熱交換
装置。 8、蒸発器用区画部と吸収器用区画部とを連通する冷媒
蒸気流路と、再生器用区画部と凝縮器用区画部とを連通
する冷媒蒸気流路と、凝縮器用区画部と蒸発器用区画部
とを連通する流路とを、伝熱板に凹凸形成したことを特
徴とする特許請求の範囲第1項記載の熱交換装置。
[Claims] 1. An internal fluid partition plate is provided which divides an evaporator section, an absorber section, a regenerator section, and a condenser section, and an external fluid corresponding to each section. An external fluid partition plate and a heat transfer plate are provided, and the internal fluid partition plate and the external fluid partition plate are stacked alternately with the heat transfer plate inside, and then outer plates are placed on both sides. A heat exchange device characterized by being arranged and integrated. 2. A refrigerant vapor flow path that communicates the evaporator section and the absorber section, a refrigerant vapor flow path that communicates the regenerator section and the condenser section, and the condenser section and the evaporator section. 2. The heat exchange device according to claim 1, wherein the internal fluid partition plate is divided into a flow path that communicates with the flow path. 8. A refrigerant vapor flow path that communicates between the evaporator section and the absorber section, a refrigerant vapor flow path that communicates between the regenerator section and the condenser section, and the condenser section and the evaporator section. 2. The heat exchange device according to claim 1, wherein the heat exchanger plate has a concave and convex shape formed on the heat exchanger plate to form a flow path that communicates with the flow path.
JP60068252A 1985-03-29 1985-03-29 Heat exchanger Pending JPS61225559A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60068252A JPS61225559A (en) 1985-03-29 1985-03-29 Heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60068252A JPS61225559A (en) 1985-03-29 1985-03-29 Heat exchanger

Publications (1)

Publication Number Publication Date
JPS61225559A true JPS61225559A (en) 1986-10-07

Family

ID=13368378

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60068252A Pending JPS61225559A (en) 1985-03-29 1985-03-29 Heat exchanger

Country Status (1)

Country Link
JP (1) JPS61225559A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012202562A (en) * 2011-03-23 2012-10-22 Osaka Gas Co Ltd Absorption refrigerating machine and method of manufacturing absorption refrigerating machine
JP2014102054A (en) * 2012-11-21 2014-06-05 Yazaki Corp Panel for cooling and cooling system including the same
JP2017058119A (en) * 2015-09-18 2017-03-23 拓樹 中村 Heat exchanger device

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5710086A (en) * 1980-05-26 1982-01-19 Uni Shidonii Za Heat exchanger
JPS5775103A (en) * 1980-08-22 1982-05-11 Enerugiiagaarukoasu Petenii Thermo-engineering device for executing thermodynamic process consisting of two kind of mutually contradictory phase transition of working medium
JPS6093276A (en) * 1983-10-27 1985-05-25 株式会社日阪製作所 Heat exchanger

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5710086A (en) * 1980-05-26 1982-01-19 Uni Shidonii Za Heat exchanger
JPS5775103A (en) * 1980-08-22 1982-05-11 Enerugiiagaarukoasu Petenii Thermo-engineering device for executing thermodynamic process consisting of two kind of mutually contradictory phase transition of working medium
JPS6093276A (en) * 1983-10-27 1985-05-25 株式会社日阪製作所 Heat exchanger

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012202562A (en) * 2011-03-23 2012-10-22 Osaka Gas Co Ltd Absorption refrigerating machine and method of manufacturing absorption refrigerating machine
JP2014102054A (en) * 2012-11-21 2014-06-05 Yazaki Corp Panel for cooling and cooling system including the same
JP2017058119A (en) * 2015-09-18 2017-03-23 拓樹 中村 Heat exchanger device

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