JPS58213167A - Heat recovery absorption heat pump - Google Patents

Heat recovery absorption heat pump

Info

Publication number
JPS58213167A
JPS58213167A JP9578682A JP9578682A JPS58213167A JP S58213167 A JPS58213167 A JP S58213167A JP 9578682 A JP9578682 A JP 9578682A JP 9578682 A JP9578682 A JP 9578682A JP S58213167 A JPS58213167 A JP S58213167A
Authority
JP
Japan
Prior art keywords
heat
absorber
evaporator
pump
refrigerant
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
JP9578682A
Other languages
Japanese (ja)
Inventor
佐藤 信和
越智 喜美雄
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 JP9578682A priority Critical patent/JPS58213167A/en
Publication of JPS58213167A publication Critical patent/JPS58213167A/en
Pending legal-status Critical Current

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  • Sorption Type Refrigeration Machines (AREA)

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) [Abstract] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 本発明は熱回収吸収ヒートポンプに関する。[Detailed description of the invention] The present invention relates to heat recovery and absorption heat pumps.

従来、廃熱の回収にあたって、吸収式のヒートポンプが
使用されており、この系統を示すと第1図のようになる
。即ち、脱熱流体(a)は蒸発器(1)内金通過させら
れるが、ここで冷媒の蒸発によって熱が奪われると共に
、この気化した?!6媒は吸収器(2)に移動して、吸
収器(2)内を通過する被加熱流体(例えばボイラー給
水)(b)を加熱する。また、上記発熱流体(a)の一
部は、蒸発器(1)を通過せずに再生器(3)に導かれ
て、吸収器(2)からポンプ(4)を介して送られてき
た重唱収液(clを加熱して、重唱収液内の冷媒を蒸発
させる。そして、この気化した冷媒は更に凝縮器(5)
内に入り冷却流体(例えば冷却水)(d)により凝縮さ
れてポンプ(6) 、 (7) fc介して蒸発器(1
)に送られる。なお、再生器(3)内で再生された濃吸
収液(e)はポンプ(8)により吸収器(2)に送られ
るが、この途中で熱交換器(9)を介して重唱収液(c
)から熱が回収されるつところで、従来、このようなも
のによると、吸収器(2)内には一種類の被加熱流体用
の被加熱管が配置されているだけで、例えば異なる種類
の流体を同時に加熱する必要がある場合には、被加熱流
体ごとに吸収ヒートポンプを設置しなければならず、不
経済−であった。
Conventionally, absorption type heat pumps have been used to recover waste heat, and this system is shown in Figure 1. That is, the heat removal fluid (a) is passed through the inner metal of the evaporator (1), where heat is removed by evaporation of the refrigerant, and the fluid is vaporized. ! The 6 medium moves to the absorber (2) and heats the fluid to be heated (eg boiler feed water) (b) passing through the absorber (2). Further, a part of the exothermic fluid (a) is guided to the regenerator (3) without passing through the evaporator (1), and is sent from the absorber (2) via the pump (4). The refrigerant in the collected liquid (Cl) is heated to evaporate the refrigerant in the collected liquid.Then, this vaporized refrigerant is further transferred to the condenser (5).
cooling fluid (e.g. cooling water) (d) and is condensed by the pump (6), (7) fc to the evaporator (1).
) will be sent to. Note that the concentrated absorption liquid (e) regenerated in the regenerator (3) is sent to the absorber (2) by the pump (8), but on the way, it is transferred to the concentrated absorption liquid (e) via the heat exchanger (9). c.
), conventionally, according to such devices, only a heated tube for one type of heated fluid is arranged in the absorber (2), and for example, a heated tube for a different type of heated fluid is disposed in the absorber (2). When it is necessary to heat fluids at the same time, an absorption heat pump must be installed for each fluid to be heated, which is uneconomical.

そこで、本発明は上記欠点を解消し得る熱回収吸収ヒー
トポンプを提供することを目的とする。
SUMMARY OF THE INVENTION Therefore, an object of the present invention is to provide a heat recovery and absorption heat pump that can eliminate the above-mentioned drawbacks.

即ち、本発明は蒸発器、吸収器、再生器及び凝縮器を有
する吸収式のヒートポンプにおいて、上記吸収器内を複
数の空間室に区画すると共に、これら各空間室内にそれ
ぞれ別個の被加熱管を配置したものである。
That is, the present invention provides an absorption heat pump having an evaporator, an absorber, a regenerator, and a condenser, in which the interior of the absorber is divided into a plurality of chambers, and a separate tube to be heated is provided in each of these chambers. This is what was placed.

かかる構成によると、−基の吸収ヒートポンプで、同時
に多種類の被加熱流体を加熱することができ、非常に経
済的である。
According to this configuration, it is possible to simultaneously heat many kinds of fluids to be heated using the -based absorption heat pump, which is very economical.

以下、本発明の一実施例を第2図及び第3図に基づき説
明する。(ロ)は冷媒を蒸発させる蒸発器、吠は蒸発器
(ロ)で気化した冷媒全吸収液に吸収する吸収器、口は
吸収器@で冷媒を吸収した重唱収液を加熱して冷媒を蒸
発させ、濃吸収液を得る再生器、0勺は再生器−で気化
された冷媒を凝縮する凝縮器、四は重唱収液(D)を再
生器(2)に送るポンプ、qQは濃吸収液の)を吸収器
@に送るポンプ、叩は重唱収液(D)の熱を濃吸収液間
に与えて熱回収を行なう熱交換器、艶α呻は冷媒IF)
を蒸発器Oυ内に送るポンプである。ところで、上記蒸
発器(ロ)と吸収器側は、第3図に示すように、−個の
円筒@17]K且つ上下方向の主仕切板のD全弁して隣
設して設けらn、また吸収器り内部は、上下方向の側仕
切板@により複数(不実施例では2個〕の空間室(23
A)(23B)に区画され、更にこれら空間室(23A
) (23B )と蒸発器I内とは、それぞれ別個に、
整流板(ハ)及びエリミネータ−(4)を介して連通さ
れている。上記各空間室(23AX23B)内には、キ
れぞれ別個の被加勢管(伝熱管群) (26A)(26
B)が配置されている。なお、(支)は蒸発器I内に配
置された加熱管(伝熱管群)である。また、詳細には図
示していないが、再生器@と凝縮器q4は、1個の国筒
内に仕切板を介して隣接して設けられている。
An embodiment of the present invention will be described below with reference to FIGS. 2 and 3. (B) is an evaporator that evaporates the refrigerant, an absorber that absorbs all of the refrigerant vaporized by the evaporator (B), and an absorber @ that heats the liquid that has absorbed the refrigerant to release the refrigerant. 0 is a regenerator that evaporates and obtains a concentrated absorption liquid, 0 is a condenser that condenses the refrigerant vaporized in the regenerator, 4 is a pump that sends the collected liquid (D) to the regenerator (2), and qQ is a concentrated absorption A pump that sends the liquid (D) to the absorber, a heat exchanger that transfers the heat of the collected liquid (D) between the concentrated absorbing liquid and recovers it, and a refrigerant IF)
This is a pump that sends the water into the evaporator Oυ. By the way, as shown in FIG. 3, the evaporator (b) and the absorber side are provided with - cylinders @17]K and D valves of the main partition plate in the vertical direction and are disposed adjacent to each other. Also, inside the absorber, a plurality of (two in the non-example) space chambers (23
A) (23B), and further these space chambers (23A
) (23B) and the inside of the evaporator I are each separately,
They are communicated via a current plate (c) and an eliminator (4). In each of the space chambers (23AX23B), separate energized tubes (heat exchanger tube group) (26A) (26
B) is placed. In addition, (branch) is a heating tube (heat exchanger tube group) arranged in the evaporator I. Further, although not shown in detail, the regenerator @ and the condenser q4 are provided adjacent to each other in one cylinder with a partition plate interposed therebetween.

次に、熱回収作用について説明するっ廃蕨流体囚の一部
は、蒸発器(ロ)内の加熱管勿を通るが、ここで冷媒の
蒸発によって熱が奪われ、この気化した冷媒(F)はそ
れぞれエリミネータ−四及び整流板(至)を通って、吸
収器0の各空間室(23AX23B)内に移動して、各
被加熱管(26A)(26B)内を流れる被加熱流体の
)(0を加熱する。−万、残りの発熱流体囚は再生器側
内の加熱管を通されるが、ここで重唱収液■)内の冷媒
を蒸発させる。この気化した冷媒劇は凝縮器CI4内に
移動して、その冷却管内を流れる冷却流体(G)によっ
て凝縮させられる。
Next, we will explain the heat recovery effect. A part of the waste fluid particles passes through the heating tube in the evaporator (b), where heat is taken away by the evaporation of the refrigerant, and this vaporized refrigerant (F ) of the heated fluid that passes through the eliminator 4 and the rectifying plate (to), moves into each space chamber (23AX23B) of the absorber 0, and flows in each heated tube (26A) (26B). (Heating 0. - 10,000, the remaining exothermic fluid is passed through the heating tube in the regenerator side, where the refrigerant in the liquid collected ①) is evaporated. The vaporized refrigerant moves into the condenser CI4 and is condensed by the cooling fluid (G) flowing through the cooling pipe.

このように、上記実施例のものによると、−基の吸収ヒ
ートポンプで、同時に多種類の被加熱流体を加熱するこ
とができ、非常に経済的である。
As described above, according to the above-mentioned embodiments, it is possible to simultaneously heat many types of fluids to be heated using the -based absorption heat pump, which is very economical.

ところで、上記実施例においては、蒸発器回及び再生器
側を通るR熱流体(A)を一種類として説明したが、例
えばこれら蒸発器(6)及び再生器(13内を、吸収器
(転)と同様に複数の空間室に区画すると共に、廃熱流
体の通る加熱管上それぞれの空間室に設けるようにすれ
L;゛、−基の吸収と一トポンプで同時に多種類の廃応
流体から熱回収を行なうことができる。
Incidentally, in the above embodiment, the R thermal fluid (A) passing through the evaporator and regenerator side was explained as one type, but for example, the inside of these evaporator (6) and regenerator (13) is ), it is divided into a plurality of chambers, and each chamber is provided on the heating pipe through which the waste heat fluid passes. Heat recovery can be performed.

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

第1図は従来例の70−シート図、第2図は本発明の一
実施例を示すフローシート図、第3゛図は要部水平断面
図である。 (ロ)・・・蒸発器、@・・・吸収器、叫・・・再生器
、α弔・・・凝縮器、(4)・・・円筒、Qη・・・主
仕切板、■・・・側仕切板、(23A)(23B)・・
・空間室、例・・・整流板、125・・・工IJ ミネ
ーター、(26A)(26B)・・・被加熱管、代理人
   森  本  義  弘 第1図 第2図 第3図 329−
FIG. 1 is a 70-sheet diagram of a conventional example, FIG. 2 is a flow sheet diagram showing an embodiment of the present invention, and FIG. 3 is a horizontal sectional view of the main part. (b)...Evaporator, @...Absorber, Scream...Regenerator, α-Condenser, (4)...Cylinder, Qη...Main partition plate, ■...・Side partition plate, (23A) (23B)...
・Space chamber, e.g. rectifying plate, 125... Engineering IJ Minator, (26A) (26B)... heated tube, agent Yoshihiro Morimoto Figure 1 Figure 2 Figure 3 329-

Claims (1)

【特許請求の範囲】[Claims] 1、 蒸発器、吸収器、再生器及び凝縮器全有する吸収
式のヒートポンプにおいて、上記吸収器内を複数の空間
室に区画すると共に、これら各空間室内にそれぞれ別個
の被加熱管を配置したことを特徴とする熱回収吸収ヒー
トポンプ。
1. In an absorption heat pump that has an evaporator, an absorber, a regenerator, and a condenser, the interior of the absorber is divided into a plurality of chambers, and separate heated tubes are arranged in each of these chambers. A heat recovery and absorption heat pump featuring:
JP9578682A 1982-06-03 1982-06-03 Heat recovery absorption heat pump Pending JPS58213167A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9578682A JPS58213167A (en) 1982-06-03 1982-06-03 Heat recovery absorption heat pump

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9578682A JPS58213167A (en) 1982-06-03 1982-06-03 Heat recovery absorption heat pump

Publications (1)

Publication Number Publication Date
JPS58213167A true JPS58213167A (en) 1983-12-12

Family

ID=14147136

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9578682A Pending JPS58213167A (en) 1982-06-03 1982-06-03 Heat recovery absorption heat pump

Country Status (1)

Country Link
JP (1) JPS58213167A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62155482A (en) * 1985-12-27 1987-07-10 株式会社荏原製作所 Absorption refrigerator

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5251317U (en) * 1975-10-08 1977-04-13

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5251317U (en) * 1975-10-08 1977-04-13

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62155482A (en) * 1985-12-27 1987-07-10 株式会社荏原製作所 Absorption refrigerator
JPH0478904B2 (en) * 1985-12-27 1992-12-14 Ebara Mfg

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