JP2823295B2 - Absorption refrigerator - Google Patents

Absorption refrigerator

Info

Publication number
JP2823295B2
JP2823295B2 JP2035215A JP3521590A JP2823295B2 JP 2823295 B2 JP2823295 B2 JP 2823295B2 JP 2035215 A JP2035215 A JP 2035215A JP 3521590 A JP3521590 A JP 3521590A JP 2823295 B2 JP2823295 B2 JP 2823295B2
Authority
JP
Japan
Prior art keywords
refrigerant
refrigerant liquid
pipe
condenser
evaporator
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.)
Expired - Fee Related
Application number
JP2035215A
Other languages
Japanese (ja)
Other versions
JPH03241270A (en
Inventor
数恭 伊良皆
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.)
Sanyo Electric Co Ltd
Original Assignee
Sanyo Electric Co Ltd
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 Sanyo Electric Co Ltd filed Critical Sanyo Electric Co Ltd
Priority to JP2035215A priority Critical patent/JP2823295B2/en
Publication of JPH03241270A publication Critical patent/JPH03241270A/en
Application granted granted Critical
Publication of JP2823295B2 publication Critical patent/JP2823295B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A30/00Adapting or protecting infrastructure or their operation
    • Y02A30/27Relating to heating, ventilation or air conditioning [HVAC] technologies
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02BCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y02B30/62Absorption based systems

Description

【発明の詳細な説明】 (イ)産業上の利用分野 本発明は冷媒、及び吸収液の循環サイクルを形成した
吸収冷凍機に関し、特に吸収液にオクチルアルコールな
どの界面活性剤を添加した吸収冷凍機に関する。
The present invention relates to an absorption refrigerator having a circulation cycle of a refrigerant and an absorption liquid, and particularly to an absorption refrigeration wherein a surfactant such as octyl alcohol is added to the absorption liquid. About the machine.

(ロ)従来の技術 例えば特開平1−114677号公報には、冷媒液流下管と
蒸発器との間に、冷媒液流下管内の冷媒液を蒸発器へオ
ーバーフローさせるオーバーフロー用管路を接続した吸
収冷凍機が開示されている。又、特公平1−21433号公
報には吸収器の伝熱性能を良くするために、吸収液にオ
クチルアルコールなどの界面活性剤を添加した吸収冷温
水機が開示されている。
(B) Conventional technology For example, Japanese Patent Application Laid-Open No. 1-114677 discloses an absorption device in which an overflow pipe connecting the refrigerant liquid in the refrigerant liquid downflow pipe to the evaporator is connected between the refrigerant liquid downflow pipe and the evaporator. A refrigerator is disclosed. Japanese Patent Publication No. 1-21433 discloses an absorption chiller / heater in which a surfactant such as octyl alcohol is added to an absorbing liquid in order to improve the heat transfer performance of the absorber.

(ハ)発明が解決しようとする課題 上記特公平1−21433号公報において、吸収液に添加
されているオクチルアルコールは吸収液とともに循環す
る。そして、吸収液中のオクチルアルコールは発生器に
て冷媒とともに吸収液から分離して凝縮器へ流れる。そ
して、凝縮器の例えば冷媒液溜め、或いは冷媒液流下管
では、オクチルアルコールの比重が冷媒液より小さいた
め、オクチルアルコールの一部が冷媒液の上に溜り、溜
っているオクチルアルコールの量が多くなった場合には
吸収液のオクチルアルコールの濃度が低下した場合に
は、吸収器での伝熱性能が低下するという問題が発生し
ていた。又、上記特開平1−114677号公報に示したよう
に、オーバーフロー用管路を設けた場合にも、凝縮器の
冷媒液溜め、或いはオーバーフロー管内の吸収液の上に
オクチルアルコールが溜り、吸収液のオクチルアルコー
ルの濃度が低下して上記特公平1−21433号公報に示さ
れた吸収冷温水機と同様に吸収器の伝熱性能が低下する
おそれがあった。
(C) Problems to be Solved by the Invention In the above Japanese Patent Publication No. 1-2433, the octyl alcohol added to the absorbing solution circulates together with the absorbing solution. Then, the octyl alcohol in the absorbing liquid is separated from the absorbing liquid together with the refrigerant in the generator and flows to the condenser. In the condenser, for example, in the refrigerant sump or the refrigerant downflow pipe, since the specific gravity of octyl alcohol is smaller than the refrigerant liquid, a part of octyl alcohol accumulates on the refrigerant liquid, and the amount of octyl alcohol accumulated is large. In such a case, when the concentration of octyl alcohol in the absorbent decreases, the heat transfer performance in the absorber decreases. Also, as described in the above-mentioned Japanese Patent Application Laid-Open No. 1-114677, when an overflow pipe is provided, octyl alcohol accumulates on the refrigerant liquid reservoir of the condenser or on the absorbing liquid in the overflow pipe and the absorbing liquid. Octyl alcohol, the heat transfer performance of the absorber may be reduced as in the absorption chiller / heater disclosed in Japanese Patent Publication No. 1-24333.

本発明は、オクチルアルコールなどの界面活性剤が凝
縮器などに大量に滞溜することを回避し、吸収器の伝熱
性能の低下を防止することを目的とする。
An object of the present invention is to prevent a large amount of a surfactant such as octyl alcohol from remaining in a condenser or the like, and to prevent a decrease in heat transfer performance of an absorber.

(ニ)課題を解決するための手段 本発明は上記課題を解決するために、蒸発器、吸収
器、発生器、及び凝縮器などをそれぞれ配管接続して冷
媒とオクチルアルコールなどの界面活性剤が添加された
吸収液の循環経路を形成するとともに、蒸発器の上部に
設けられた冷媒散布器とこの蒸発器の下部に設けられた
冷媒液溜めとの間を冷媒液循環管で接続し、蒸発器或い
はこの冷媒液循環管に設けられた冷媒液ポンプの吐出側
と凝縮器の下部に設けられた冷媒液溜めとの間を冷媒液
流下管で接続した吸収冷凍機において、凝縮器の冷媒液
溜めの冷媒流下管が接続される位置より上方の位置と冷
媒液循環管に設けられた冷媒液ポンプの吸込側との間を
界面活性剤の戻し管で接続し、かつ、この戻し管と冷媒
液ポンプの吐出側の冷媒液循環管との間に冷媒液の補給
管を接続した吸収冷凍機を提供するものである。
(D) Means for Solving the Problems In order to solve the above problems, the present invention connects a refrigerant to a surfactant such as octyl alcohol by connecting pipes to an evaporator, an absorber, a generator, and a condenser. A circulation path for the added absorbent is formed, and a refrigerant liquid circulating pipe is connected between a refrigerant sprayer provided at an upper part of the evaporator and a refrigerant liquid reservoir provided at a lower part of the evaporator to evaporate. In a refrigerator or an absorption refrigerator in which a discharge side of a refrigerant liquid pump provided in the refrigerant liquid circulation pipe and a refrigerant liquid reservoir provided in a lower part of the condenser are connected by a refrigerant liquid flow down pipe, the refrigerant liquid of the condenser A return pipe of a surfactant is connected between a position above a position where the refrigerant downflow pipe of the reservoir is connected and a suction side of the refrigerant liquid pump provided in the refrigerant liquid circulation pipe, and the return pipe and the refrigerant are connected. Cool between the refrigerant liquid circulation pipe on the discharge side of the liquid pump It is an object of the present invention to provide an absorption refrigerator to which a supply pipe for a medium is connected.

又、蒸発器、吸収器、発生器、及び凝縮器などをそれ
ぞれ配管接続して冷媒とオクチルアルコールなどの界面
活性剤が添加された吸収液との循環経路を形成するとと
もに、蒸発器に冷媒液循環管を接続し、この冷媒液循環
管に冷媒液ポンプを設け、かつ、凝縮器に設けられた冷
媒液溜めと蒸発器或いは冷媒液ポンブの吐出側との間に
冷媒液流下管を接続した吸収冷凍機において、凝縮器の
冷媒液溜めの前記冷媒流下管が接続される位置より上方
の位置と冷媒液ポンプの吸込側の冷媒液循環管との間に
界面活性剤の戻し管を接続した吸収冷凍機を提供するも
のである。
In addition, the evaporator, the absorber, the generator, and the condenser are connected to each other by pipes to form a circulation path between the refrigerant and the absorbent to which a surfactant such as octyl alcohol is added. A circulation pipe was connected, a refrigerant liquid pump was provided in the refrigerant liquid circulation pipe, and a refrigerant liquid flow down pipe was connected between the refrigerant liquid reservoir provided in the condenser and the discharge side of the evaporator or the refrigerant liquid pump. In the absorption refrigerator, a return pipe of a surfactant was connected between a position above a position where the refrigerant downflow pipe of the refrigerant reservoir of the condenser was connected and the refrigerant liquid circulation pipe on the suction side of the refrigerant liquid pump. An absorption refrigerator is provided.

さらに、蒸発器、吸収器、発生器、及び凝縮器などを
それぞれ配管接続して冷媒とオクチルアルコールなどの
界面活性剤が添加された吸収液との循環経路を形成する
とともに、蒸発器に冷媒液循環管を接続し、この冷媒液
循環管に冷媒液ポンプを設け、かつ、凝縮器に設けられ
た冷媒液溜めと冷媒液循環管或いは蒸発器との間に冷媒
液流下管が接続された吸収冷凍機において、凝縮器の冷
媒液溜めの前記冷媒流下管が接続される位置より上方の
位置と冷媒液ポンブの吸込側の冷媒液循環管との間に界
面活性剤の戻し管を接続し、この戻し管の途中にUシー
ル部を形成し、このUシール部より上流の戻し管と冷媒
液ボンプの吐出側の冷媒液循環管との間に冷媒液の補給
管を接続した吸収冷凍機を提供するものである。
Further, an evaporator, an absorber, a generator, a condenser, and the like are connected to each other by pipes to form a circulation path between the refrigerant and an absorbent to which a surfactant such as octyl alcohol is added. A circulation pipe is connected, a refrigerant liquid pump is provided in the refrigerant liquid circulation pipe, and a refrigerant liquid flow down pipe is connected between the refrigerant liquid reservoir provided in the condenser and the refrigerant liquid circulation pipe or the evaporator. In the refrigerator, a return pipe of a surfactant is connected between a position above a position where the refrigerant downflow pipe of the refrigerant reservoir of the condenser is connected and a refrigerant liquid circulation pipe on a suction side of the refrigerant liquid pump, An absorption refrigerator in which a U seal portion is formed in the middle of the return pipe and a refrigerant liquid supply pipe is connected between the return pipe upstream of the U seal section and the refrigerant liquid circulation pipe on the discharge side of the refrigerant liquid pump. To provide.

(ホ)作用 吸収冷凍機の運転時、凝縮器(10)の冷媒液溜め(10
A)の冷媒液の上に溜った界面活性剤は、液位が上昇し
たときに戻し管(26)を経て冷媒液循環管(22)へ流
れ、蒸発器(2)から流れて来た冷媒液と一緒になって
冷媒液ポンプ(24)から吐出される。そして、界面活性
剤は冷媒液とともに蒸発器(2)で散布され、気化して
吸収器(3),(4)へ流れ濃吸収液に吸収されるの
で、冷媒液溜め(10A)に大量の界面活性剤が溜ること
を防止し、吸収液中の界面活性剤の濃度の低下を回避し
て吸収器(3),(4)の伝熱性能を維持することが可
能になる。
(E) Operation During operation of the absorption refrigerator, the refrigerant liquid in the condenser (10)
The surfactant accumulated on the refrigerant liquid of A) flows through the return pipe (26) to the refrigerant liquid circulation pipe (22) when the liquid level rises, and the refrigerant flowing from the evaporator (2) The refrigerant is discharged from the refrigerant liquid pump (24) together with the liquid. Then, the surfactant is sprayed together with the refrigerant liquid in the evaporator (2), vaporizes and flows into the absorbers (3) and (4), and is absorbed by the concentrated absorption liquid, so that a large amount of the surfactant is stored in the refrigerant reservoir (10A). It is possible to prevent the surfactant from accumulating, avoid the decrease in the concentration of the surfactant in the absorbing solution, and maintain the heat transfer performance of the absorbers (3) and (4).

又、冷媒液ポンプ(24)から吐出された冷媒液の一部
は補給管(35)を経て戻し管(26)へ流れ、冷媒液溜め
(10A)から界面活性剤、或いは冷媒液が戻し管(26)
へ流入しないときに、戻し管(26)の液シールが保た
れ、凝縮器(10)と蒸発器(2)との気相部が連通する
ことを防止することが可能になる。
A part of the refrigerant liquid discharged from the refrigerant liquid pump (24) flows through the supply pipe (35) to the return pipe (26), and the surfactant or the refrigerant liquid is returned from the refrigerant liquid reservoir (10A) to the return pipe. (26)
When the gas does not flow into the tub, the liquid seal of the return pipe (26) is maintained, and it is possible to prevent the gas phase portion between the condenser (10) and the evaporator (2) from communicating with each other.

さらに、戻し管(26)の途中にUシール部(36)を設
けた場合には、吸収冷凍機の停止に伴い吸収液ポンプ
(24)の運転が停止したとき、或いは吸収冷凍機の異常
停止に伴い吸収液ポンプ(24)の運転が停止したとき
に、Uシール部(36)に界面活性剤、或いは冷媒液が溜
っているため、戻し管(26)の液シールが保たれ、吸収
液ポンプ(24)の停止時においても凝縮器(10)と蒸発
器(2)との気相部が連通することを確実に防止するこ
とが可能になる。
Further, when the U-seal portion (36) is provided in the middle of the return pipe (26), the operation of the absorption pump (24) is stopped due to the stop of the absorption refrigerator, or the absorption refrigerator is stopped abnormally. When the operation of the absorbent pump (24) stops due to the above, since the surfactant or the refrigerant liquid is accumulated in the U seal portion (36), the liquid seal of the return pipe (26) is maintained, and the absorbent liquid is retained. Even when the pump (24) is stopped, it is possible to reliably prevent the gas phase portion between the condenser (10) and the evaporator (2) from communicating with each other.

(ヘ)実施例 以下、本発明の一実施例を図面に基づいて詳細に説明
する。
(F) Example Hereinafter, an example of the present invention will be described in detail with reference to the drawings.

図面に示したものは二重効用吸収冷凍機であり、冷媒
に水(H2O)、吸収液に臭化リチウム(LiBr)水溶液を
使用したものである。又、吸収液には後述する吸収器で
の伝熱性能を良くするためにオクチルアルコールなどの
界面活性剤が例えば0.1〜0.2wt%添加されている。
The drawing shows a double effect absorption refrigerator in which water (H 2 O) is used as a refrigerant and a lithium bromide (LiBr) aqueous solution is used as an absorption liquid. Further, a surfactant such as octyl alcohol is added to the absorbing solution in an amount of, for example, 0.1 to 0.2 wt% in order to improve the heat transfer performance in an absorber described later.

図面において(1)は蒸発吸収器胴、(1A)は吸収液
溜め、(2)は蒸発吸収器胴(1)内の中央に配置され
た蒸発器、(3)及び(4)はそれぞれ蒸発器(2)の
両側に配置された吸収器、(5)は吸収液ポンプ、(6
A)は低温熱交換器、(6B)は高温熱交換器、(7)は
蒸気を加熱源とする高温発生器、(8)は発生凝縮器
胴、(9)は低温発生器、(10)は凝縮器、(11)ない
し(14)は稀吸収液管(以下稀液管という)、(15)及
び(16)は中間吸収液管(以下中間液管という)、(1
7)及び(18)は濃吸収液管(以下濃液管という)、(1
7P)は濃液ポンプ、(20),(21)は冷媒管、(22)及
び(23)は蒸発器(2)の上部の冷媒散布器(2A)と下
部の冷媒液溜め(2B)との間に接続された冷媒液循環
管、(24)は冷媒液ポンプ、(25)は凝縮器(10)の冷
媒液溜め(10A)と冷媒液ポンプ(24)の吐出側の冷媒
液循環管(23)との間に接続された冷媒液流下管であ
り、それぞれは図面に示したように配置接続されてい
る。
In the drawing, (1) is an evaporator / absorber body, (1A) is an absorption liquid reservoir, (2) is an evaporator arranged in the center of the evaporator / absorber body (1), (3) and (4) are evaporators, respectively. Absorbers arranged on both sides of the vessel (2), (5) an absorbent pump, (6)
(A) is a low-temperature heat exchanger, (6B) is a high-temperature heat exchanger, (7) is a high-temperature generator using steam as a heating source, (8) is a generating condenser body, (9) is a low-temperature generator, (10) ) Is a condenser, (11) to (14) are dilute absorption liquid tubes (hereinafter referred to as dilute liquid tubes), (15) and (16) are intermediate absorption liquid tubes (hereinafter referred to as intermediate liquid tubes), (1)
7) and (18) are concentrated absorption liquid tubes (hereinafter referred to as concentrated liquid tubes), (1)
7P) is a concentrate pump, (20) and (21) are refrigerant pipes, (22) and (23) are a refrigerant sprayer (2A) at the upper part of the evaporator (2) and a refrigerant reservoir (2B) at the lower part. A refrigerant liquid circulation pipe connected between the refrigerant liquid pump, (24) a refrigerant liquid pump, and (25) a refrigerant liquid circulation pipe on the discharge side of the refrigerant liquid reservoir (10A) of the condenser (10) and the refrigerant liquid pump (24). And (23) are connected to each other as shown in the drawing.

又、(26)は界面活性剤(以下アルコールという)の
戻し管であり、この戻し管(26)は凝縮器(10)の冷媒
液溜め(10A)と冷媒液ポンプ(24)の吸込側の冷媒液
循環管(22)との間に接続されており、この戻り管(2
6)の冷媒液溜め(10A)側先端は冷媒液流下管(25)の
冷媒液溜め(10A)への接続部より上方の冷媒液溜め側
壁に接続されている。(27)及び(28)は冷媒液の補給
管である。これらの補給管(27)及び(28)は冷媒液循
環管(22)などより内径が小さい管であり、冷媒液循環
管(23)と戻し管(26)との間に接続されている。(3
0)は補給管(27)(28)が接続され、蒸発吸収器胴
(1)より高い位置に設けられた冷媒液タンクであり、
(31)は堰である。又、(32)及び(33)は蒸発器
(2)と吸収器(3)(4)との間のエリミネータ、
(34)及び(35)は低温発生器(9)と凝縮器(10)と
の間のエリミネータである。又、(36)は冷水管、(3
7),(38)、及び(40)は冷却水管であり、(36A)は
蒸発器熱交換器、(37A),(38A)、及び(40A)は吸
収器熱交換器、及び凝縮器熱交換器である。
Reference numeral (26) denotes a return pipe for a surfactant (hereinafter referred to as alcohol). The return pipe (26) is provided between the refrigerant reservoir (10A) of the condenser (10) and the suction side of the refrigerant liquid pump (24). It is connected between the refrigerant liquid circulation pipe (22) and this return pipe (2
The tip of the coolant reservoir (10A) side of 6) is connected to the coolant reservoir side wall above the connection of the coolant downflow pipe (25) to the coolant reservoir (10A). (27) and (28) are refrigerant liquid supply pipes. These supply pipes (27) and (28) are pipes having a smaller inner diameter than the refrigerant liquid circulation pipe (22) and the like, and are connected between the refrigerant liquid circulation pipe (23) and the return pipe (26). (3
Reference numeral 0) denotes a refrigerant liquid tank to which the supply pipes (27) and (28) are connected and which is provided at a position higher than the evaporator / absorber body (1).
(31) is a weir. (32) and (33) are eliminators between the evaporator (2) and the absorbers (3) (4);
(34) and (35) are eliminators between the low temperature generator (9) and the condenser (10). (36) is a cold water pipe, (3
7), (38) and (40) are cooling water pipes, (36A) is an evaporator heat exchanger, (37A), (38A) and (40A) are an absorber heat exchanger and a condenser heat exchanger It is an exchanger.

上記のように構成された吸収冷凍機の運転時、従来の
吸収冷凍機と同様に高温発生器(7)で吸収液から分離
した冷媒は低温発生器(9)を経て凝縮して凝縮器(1
0)へ流れる。又、低温発生器(9)から凝縮器(10)
へ流入した冷媒蒸気は凝縮器熱交換器(40A)を流れる
水と熱交換して凝縮液化する。そして、凝縮器(10)の
冷媒液は冷媒液溜め(10A)に溜る。冷媒液溜め(10A)
の冷媒液は冷媒液流下管(25)を経て冷媒液循環管(2
3)へ流れ、冷媒液ポンプ(24)から吐出された冷媒液
とともに冷媒散布器(2A)から散布される。そして、冷
媒液が蒸発器熱交換器(36A)にて冷水と熱交換して蒸
発し、気化熱によって冷水が冷却される。蒸発器(2)
にて蒸発した冷媒は吸収器(3),(4)へ流れ、吸収
器熱交換器(37A),(38A)に散布されている濃吸収液
に吸収される。
During operation of the absorption refrigerator configured as described above, the refrigerant separated from the absorption liquid by the high-temperature generator (7) is condensed through the low-temperature generator (9) and condensed into the condenser ( 1
Flow to 0). In addition, low temperature generator (9) to condenser (10)
The refrigerant vapor flowing into the heat exchanger exchanges heat with water flowing through the condenser heat exchanger (40A) and condenses and liquefies. Then, the refrigerant liquid of the condenser (10) accumulates in the refrigerant liquid reservoir (10A). Refrigerant liquid reservoir (10A)
The refrigerant liquid from the refrigerant liquid circulation pipe (2) passes through the refrigerant liquid down pipe (25).
It flows to 3) and is sprayed from the refrigerant sprayer (2A) together with the refrigerant liquid discharged from the refrigerant liquid pump (24). The refrigerant liquid exchanges heat with the cold water in the evaporator heat exchanger (36A) to evaporate, and the cold water is cooled by the heat of vaporization. Evaporator (2)
The refrigerant evaporated in the above flows into the absorbers (3) and (4), and is absorbed by the concentrated absorption liquid sprayed on the absorber heat exchangers (37A) and (38A).

冷媒を吸収して濃度が薄くなった稀吸収液は蒸発吸収
器胴(1)下部の吸収液溜め(1A)に溜る。そして、稀
吸収液は吸収液ポンプ(5)から吐出されて高温発生器
(7)へ流れ加熱され、稀吸収液から冷媒蒸気が分離す
る。そして、中濃度になった吸収液(以下中間吸収液と
いう)が高温発生器(7)から高温熱交換器(6B)を経
て低温発生器(8)へ流れる。又、高温発生器(7)に
て冷媒とともに吸収液からアルコールが分離して冷媒管
(20)を経て低温発生器(9)へ流れる。そして、低温
発生器(9)で中間吸収液が冷媒蒸気及びアルコールと
熱交換して加熱され、中間吸収液からさらに冷媒及び残
っていたアルコールが分離する。そして、さらに濃度が
高くなった濃吸収液が低温発生器(9)から吸収器
(3),(4)へ流れる散布される。又、低温発生器
(9)で中間吸収液と熱交換して凝縮した冷媒液及びア
ルコールが冷媒管(21)を経て凝縮器(10)へ流れ、冷
媒液溜め(10A)に溜る。又、低温発生器(9)にて中
間吸収液から分離した冷媒蒸気及びアルコールは凝縮器
(10)へ流れ、凝縮器熱交換器(40A)で冷却され、凝
縮した冷媒液、及びアルコールが冷媒液溜め(10A)に
溜る。
The diluted absorbing liquid having a reduced concentration by absorbing the refrigerant is stored in the absorbing liquid reservoir (1A) below the evaporative absorber body (1). Then, the rare absorbing liquid is discharged from the absorbing liquid pump (5), flows to the high-temperature generator (7), is heated, and refrigerant vapor is separated from the rare absorbing liquid. Then, the absorbent having a medium concentration (hereinafter referred to as an intermediate absorbent) flows from the high-temperature generator (7) to the low-temperature generator (8) via the high-temperature heat exchanger (6B). Further, alcohol is separated from the absorbing liquid together with the refrigerant in the high-temperature generator (7) and flows to the low-temperature generator (9) through the refrigerant pipe (20). Then, in the low-temperature generator (9), the intermediate absorbent is heated by exchanging heat with the refrigerant vapor and the alcohol, and the refrigerant and the remaining alcohol are further separated from the intermediate absorbent. Then, the concentrated absorbent having a higher concentration is sprayed from the low-temperature generator (9) to the absorbers (3) and (4). The refrigerant liquid and alcohol condensed by heat exchange with the intermediate absorbing liquid in the low-temperature generator (9) flow through the refrigerant pipe (21) to the condenser (10), and accumulate in the refrigerant liquid reservoir (10A). The refrigerant vapor and alcohol separated from the intermediate absorption liquid by the low-temperature generator (9) flow to the condenser (10), and are cooled by the condenser heat exchanger (40A). Collect in the reservoir (10A).

冷媒液溜め(10A)に溜った冷媒液及びアルコールは
冷媒液流下管(25)を経て冷媒液循環管(23)へ流れ、
蒸発器(2)で散布される。又、冷媒液溜め(10A)に
冷媒液とともに溜ったアルコールの一部は冷媒液から分
離し、冷媒液の上に層になって溜る。又、冷媒液ポンプ
(24)から吐出された冷媒液の一部は補給管(27)を経
て冷媒液タンク(30)へ流れ、冷媒液タンク(30)に溜
った冷媒液が堰(31)を越えて補給管(28)へ流れる。
そして、冷媒液が戻し管(26)へ補給されて戻し管(2
6)の液シールは保たれる。
The refrigerant liquid and alcohol stored in the refrigerant liquid reservoir (10A) flow through the refrigerant liquid downflow pipe (25) to the refrigerant liquid circulation pipe (23),
Sprayed in the evaporator (2). In addition, a part of the alcohol that has accumulated together with the refrigerant liquid in the refrigerant liquid reservoir (10A) is separated from the refrigerant liquid, and accumulates as a layer on the refrigerant liquid. A part of the refrigerant liquid discharged from the refrigerant liquid pump (24) flows through the supply pipe (27) to the refrigerant liquid tank (30), and the refrigerant liquid stored in the refrigerant liquid tank (30) is discharged from the weir (31). Over the supply pipe (28).
Then, the refrigerant liquid is supplied to the return pipe (26) and the return pipe (2
6) The liquid seal is kept.

上記のように吸収冷凍機が運転されているとき、凝縮
器(10)の冷媒液溜め(10A)の冷媒液及びアルコール
の量が増加し、アルコール層が戻し管(26)の接続部に
達した時には、アルコールが戻し管(26)を流れる。そ
して、戻し管(26)に溜っているアルコールの液面が上
昇すると、補給管(28)を流れて来た冷媒液と一緒にア
ルコールが冷媒液ポンプ(24)に引かれる。冷媒液ポン
プ(24)に引かれて冷媒液と一緒に冷媒液ポンプ(24)
から吐出されたアルコールは冷媒散布器(2A)から蒸発
器熱交換器(36A)に散布される。そして、蒸発器
(2)で気化したアルコールは各吸収器(3),(4)
へ流れて冷媒蒸気とともに濃吸収液に吸収されて吸収器
熱交換器(37A),(38A)を流下し、各熱交換器(37
A),(38A)の表面のマランゴニ対流が促進される。以
後、同様に、冷媒液溜め(10)の液面が上昇して戻し管
(26)の接続部に達した時には、冷媒溜め(10)の冷媒
液の上に溜っているアルコールが戻し管(26)を経て冷
媒液循環管(23)へ流れ、冷媒液とともに蒸発器(2)
で散布される。
When the absorption refrigerator is operated as described above, the amounts of the refrigerant liquid and the alcohol in the refrigerant liquid reservoir (10A) of the condenser (10) increase, and the alcohol layer reaches the connection portion of the return pipe (26). When it does, the alcohol flows through the return pipe (26). Then, when the liquid level of the alcohol stored in the return pipe (26) rises, the alcohol is drawn by the refrigerant liquid pump (24) together with the refrigerant liquid flowing through the supply pipe (28). Refrigerant liquid pump (24) drawn with refrigerant liquid pump (24) together with refrigerant liquid
Is discharged from the refrigerant sprayer (2A) to the evaporator heat exchanger (36A). The alcohol vaporized in the evaporator (2) is supplied to each of the absorbers (3) and (4).
And flows into the absorber heat exchangers (37A) and (38A).
A), Marangoni convection on the surface of (38A) is promoted. Thereafter, similarly, when the liquid level of the refrigerant liquid reservoir (10) rises and reaches the connection portion of the return pipe (26), the alcohol accumulated on the refrigerant liquid of the refrigerant liquid reservoir (10) returns to the return pipe ( After passing through 26) to the refrigerant liquid circulation pipe (23), the evaporator (2) together with the refrigerant liquid
Sprayed on.

上記実施例によれば、凝縮器(10)の冷媒液溜め(10
A)に溜ったアルコールは、液面が上昇したときに戻し
管(26)へ流れ、補給管(28)を流れて来た冷媒液とと
もに冷媒循環管(23)へ流れる。そして、アルコールは
冷媒液ポンプ(24)から吐出され、冷媒液とともに蒸発
器(2)で散布され、気化して吸収器(3),(4)へ
流れ濃吸収液に吸収される。このため、冷媒液溜め(10
A)に大量のアルコールが溜ることを防止でき、吸収液
中のアルコール濃度の低下を防止し、各吸収器(3),
(4)での伝熱性能が低下することを回避でき、吸収冷
凍機の運転を安定させることができる。又、冷媒液ポン
プ(24)から吐出した冷媒液の一部が、補給管(27)、
冷媒液タンク(30)、及び補給管(28)を経て戻し管
(26)へ流れるので、冷媒液溜め(10A)から戻し管(2
6)へアルコールが流入しないときにも、戻し管(26)
の液シールを保つことができ、この結果、凝縮器(10)
と蒸発器(2)との気相部が連通することを防止でき
る。
According to the above embodiment, the refrigerant reservoir (10) of the condenser (10) is
The alcohol accumulated in A) flows to the return pipe (26) when the liquid level rises, and flows to the refrigerant circulation pipe (23) together with the refrigerant liquid flowing through the supply pipe (28). Then, the alcohol is discharged from the refrigerant liquid pump (24), dispersed in the evaporator (2) together with the refrigerant liquid, vaporized, flows into the absorbers (3) and (4), and is absorbed by the concentrated absorbent. For this reason, the coolant reservoir (10
It is possible to prevent a large amount of alcohol from accumulating in A), to prevent a decrease in the alcohol concentration in the absorbing solution, and to make each absorber (3),
The heat transfer performance in (4) can be prevented from lowering, and the operation of the absorption refrigerator can be stabilized. A part of the refrigerant liquid discharged from the refrigerant liquid pump (24) is supplied to the supply pipe (27),
The refrigerant flows into the return pipe (26) via the refrigerant liquid tank (30) and the supply pipe (28).
When no alcohol flows into 6), return pipe (26)
The liquid seal of the condenser (10)
It is possible to prevent the communication between the gaseous phase part and the evaporator (2).

又、図面に破線にて示したように、吸収冷凍機の冷媒
液循環管(23)と戻し管(26)との間に冷媒液の補給管
(35)を配管接続する。このように、冷媒液の補給管
(35)を接続した場合には、吸収冷凍機の運転時、冷媒
液ポンプ(24)から吐出された冷媒液の一部が補給管
(35)を経て戻し管(26)へ流れ、凝縮器(10)の冷媒
液溜め(10A)からアルコール或いは冷媒液が戻し管(2
6)へ流入しないときにも、戻し管(26)の液シールを
保つことができ、この結果、凝縮器(10)と蒸発器
(2)との気相部が連通することを回避することができ
る。又、補給管(35)を流れる冷媒液の量を調整するた
めに、補給管(35)に例えばオリフィス等を設けても良
い。
Further, as shown by a broken line in the drawing, a refrigerant liquid supply pipe (35) is connected between the refrigerant liquid circulation pipe (23) and the return pipe (26) of the absorption refrigerator. As described above, when the refrigerant liquid supply pipe (35) is connected, a part of the refrigerant liquid discharged from the refrigerant liquid pump (24) returns through the supply pipe (35) during the operation of the absorption refrigerator. Flows into the pipe (26), and the alcohol or refrigerant liquid from the refrigerant reservoir (10A) of the condenser (10) returns to the return pipe (2).
Even when the gas does not flow into 6), the liquid seal of the return pipe (26) can be maintained, and as a result, communication between the gas phase portion of the condenser (10) and the evaporator (2) is avoided. Can be. Further, for example, an orifice or the like may be provided in the supply pipe (35) in order to adjust the amount of the refrigerant liquid flowing through the supply pipe (35).

さらに、図面に一点鎖線にて示したように、戻し管
(26)の下部の途中に、戻し管(26)を上方へ曲げ所定
の高さで下方へ曲げたUシール部(36)を形成した場合
には、戻し管(26)を流れたアルコール、或いは冷媒液
がUシール部(36)に溜る。このため、蒸発器(2)の
冷媒液溜め(2B)の冷媒液が大幅に減少して、冷媒液ポ
ンプ(24)の冷媒液吐出量も大幅に減少し、補給管(3
5)から戻し管(26)への冷媒液の補給量が低下したと
き、或いは冷媒液溜め(2B)の冷媒液がなくなり、冷媒
液ポンプ(24)が冷媒液を吐出しなくなったときに、U
シール部(36)にて液シールを保つことができ、凝縮器
(10)と蒸発器(2)との気相部が連通することを確実
に回避することができる。
Further, as shown by a dashed line in the drawing, a U-seal portion (36) is formed in the lower part of the return pipe (26) by bending the return pipe (26) upward and bending downward at a predetermined height. In this case, the alcohol or the refrigerant liquid flowing through the return pipe (26) accumulates in the U seal portion (36). For this reason, the refrigerant liquid in the refrigerant reservoir (2B) of the evaporator (2) is greatly reduced, the refrigerant liquid discharge amount of the refrigerant liquid pump (24) is also largely reduced, and the supply pipe (3
When the supply amount of the refrigerant liquid from 5) to the return pipe (26) decreases, or when the refrigerant liquid in the refrigerant reservoir (2B) runs out and the refrigerant liquid pump (24) stops discharging the refrigerant liquid, U
The liquid seal can be maintained by the seal portion (36), and the communication between the gas phase portion of the condenser (10) and the gas phase portion of the evaporator (2) can be reliably avoided.

尚、本発明は上記実施例に限定されるものではなく、
例えば吸収器の稀吸収液を高温発生器と低温発生器とへ
並列に流す吸収冷凍機、又は、ガスバーナなどの燃焼装
置を備えた高温発生器を配管接続した吸収冷凍機などに
おいて、上記実施例に示したように、アルコールの戻し
管、又は冷媒液の補給管を配管接続することによって同
様に作用効果を得ることができる。又、図面に二点鎖線
にて示したように冷媒液流下管(25)を冷媒液溜め(2
B)に接続しても良い。
The present invention is not limited to the above embodiment,
For example, in the absorption refrigerator in which the rare absorption liquid of the absorber flows in parallel to the high-temperature generator and the low-temperature generator, or in an absorption refrigerator in which a high-temperature generator equipped with a combustion device such as a gas burner is connected by piping, As shown in the above, the same effect can be obtained by connecting the return pipe of the alcohol or the supply pipe of the refrigerant liquid with the pipe. Also, as shown by the two-dot chain line in the drawing, the refrigerant liquid downflow pipe (25) is connected to the refrigerant liquid reservoir (2).
B) may be connected.

(ト)発明の効果 本発明は以上のように構成されて吸収冷凍機であり、
凝縮器に設けられた冷媒液溜めにオクチルアルコールな
どの界面活性剤の戻し管の一端を接続し、この戻し管の
他端を冷媒液ポンプの吸込側の冷媒液循環管に接続し、
かつ、戻し管と冷媒液ポンプの吐出側の冷媒液循環管と
の間に冷媒液の補給管を接続したので、吸収冷凍機の運
転中に凝縮器の冷媒液溜めに溜まり、冷媒液と分離して
冷媒液の上に層を形成した界面活性剤を冷媒液溜めの液
位が上昇したときに戻し管を経て冷媒液循環管へ流し、
冷媒液溜めに溜っていた冷媒を冷媒液ポンプから冷媒液
と一緒に吐出して蒸発器の冷媒散布器から散布して吸収
器の吸収液に吸収させることができ、吸収液の界面活性
剤濃度の低下を防止して吸収器での伝熱性能の低下を回
避することができる。又、冷媒液ポンプから吐出した冷
媒液の一部を補給管を介して戻し管へ流すことができ、
この結果、戻し管の液シールを保ち、凝縮器と蒸発器と
の気相部が戻し管を介して連通することを回避すること
ができる。
(G) Effect of the Invention The present invention is an absorption refrigerator configured as described above,
One end of a return pipe of a surfactant such as octyl alcohol is connected to the refrigerant reservoir provided in the condenser, and the other end of the return pipe is connected to the refrigerant liquid circulation pipe on the suction side of the refrigerant liquid pump,
In addition, since a supply line for the refrigerant liquid is connected between the return pipe and the refrigerant liquid circulation pipe on the discharge side of the refrigerant liquid pump, the refrigerant liquid is collected in the refrigerant liquid reservoir of the condenser during operation of the absorption refrigerator and separated from the refrigerant liquid. When the liquid level of the refrigerant reservoir rises, the surfactant having formed a layer on the refrigerant liquid flows through the return pipe to the refrigerant liquid circulation pipe,
The refrigerant stored in the refrigerant liquid reservoir can be discharged together with the refrigerant liquid from the refrigerant liquid pump and sprayed from the refrigerant sprayer of the evaporator to be absorbed by the absorbing liquid of the absorber, and the surfactant concentration of the absorbing liquid can be absorbed. Of the heat transfer performance of the absorber can be prevented. Also, a part of the refrigerant liquid discharged from the refrigerant liquid pump can flow to the return pipe via the supply pipe,
As a result, it is possible to maintain the liquid seal of the return pipe and to prevent the gas phase portion between the condenser and the evaporator from communicating with each other via the return pipe.

又、凝縮器の冷媒液溜めと冷媒液ポンプの吸込側の冷
媒液循環管との間に界面活性剤の戻し管を接続すること
により、凝縮器の冷媒液溜めに溜った界面活性剤を戻し
管、冷媒液ポンプ、及び冷媒液循環管を介して蒸発器へ
送り、蒸発器にて界面活性剤を気化させ吸収器の吸収液
に吸収させることができ、この結果、吸収液の界面活性
剤濃度の低下を防止して吸収器での伝熱性能の低下を回
避することができる。
Also, by connecting a return pipe of the surfactant between the refrigerant reservoir of the condenser and the refrigerant circulation pipe on the suction side of the refrigerant liquid pump, the surfactant accumulated in the refrigerant reservoir of the condenser is returned. It can be sent to an evaporator through a pipe, a refrigerant liquid pump, and a refrigerant liquid circulation pipe, and the surfactant can be vaporized by the evaporator and absorbed by the absorbent in the absorber. As a result, the surfactant in the absorbent can be absorbed. It is possible to prevent a decrease in the concentration and avoid a decrease in the heat transfer performance in the absorber.

さらに、凝縮器の冷媒液溜めと冷媒液ポンプの吸込側
の冷媒液循環管との間に界面活性剤の戻し管を接続し、
この戻し管の途中にUシール部を形成し、かつ、戻し管
と冷媒液ポンプの吐出側の冷媒液循環管との間に冷媒液
の補給管を接続することにより、凝縮器の冷媒液溜めに
溜った界面活性剤を戻し管、冷媒液ポンプ、及び冷媒液
循環管を介して蒸発器へ流し、蒸発器にて気化させて吸
収器の吸収液に吸収させることができ、この結果、吸収
液の界面活性剤濃度の低下を防止して吸収器の伝熱性能
の低下を回避することができる。又、冷媒液ポンプから
吐出した冷媒液の一部を戻し管へ流して戻し管の液シー
ルを保つことができるとともに、冷媒液ポンプの冷媒液
の吐出量が大幅に減少したとき、或いは冷媒液の吐出が
停止したときに、Uシール部にて戻し管の液シールを保
つことができ、この結果、凝縮器と蒸発器との気相部の
連通を確実に防止することができる。
Furthermore, a surfactant return pipe is connected between the refrigerant liquid reservoir of the condenser and the refrigerant liquid circulation pipe on the suction side of the refrigerant liquid pump,
By forming a U-seal portion in the middle of the return pipe and connecting a supply pipe for the refrigerant liquid between the return pipe and the refrigerant liquid circulation pipe on the discharge side of the refrigerant liquid pump, the refrigerant liquid in the condenser is stored. Surfactant accumulated in the evaporator can be flowed to the evaporator via the return pipe, the refrigerant liquid pump, and the refrigerant liquid circulation pipe, vaporized by the evaporator, and absorbed by the absorbent in the absorber. It is possible to prevent a decrease in the surfactant concentration of the liquid and avoid a decrease in the heat transfer performance of the absorber. Also, a part of the refrigerant liquid discharged from the refrigerant liquid pump can flow to the return pipe to maintain the liquid seal of the return pipe, and when the discharge amount of the refrigerant liquid from the refrigerant liquid pump is significantly reduced, or When the discharge of is stopped, the liquid seal of the return pipe can be maintained at the U seal portion, and as a result, communication of the gas phase portion between the condenser and the evaporator can be reliably prevented.

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

図面は本発明の一実施例を示す吸収冷凍機の回路構成図
である。 (2)……蒸発器、(2A)……冷媒散布器、(2B)……
冷媒液溜め、(3),(4)……吸収器、(5)……吸
収液ポンプ、(7)……高温発生器、(10)……凝縮
器、(10A)……冷媒液溜め、(22),(23)……冷媒
液循環管、(24)……冷媒液ポンプ、(25)……冷媒液
流下管、(26)……戻し管、(27),(28)……補給
管、(35)……補給管、(36)……Uシール部。
The drawing is a circuit configuration diagram of an absorption refrigerator showing one embodiment of the present invention. (2) evaporator (2A) refrigerant sprayer (2B)
Refrigerant reservoir, (3), (4) ... absorber, (5) ... absorbent pump, (7) ... high temperature generator, (10) ... condenser, (10A) ... refrigerant reservoir , (22), (23) ... refrigerant liquid circulation pipe, (24) ... refrigerant liquid pump, (25) ... refrigerant liquid down pipe, (26) ... return pipe, (27), (28) ... ... supply tube, (35) ... supply tube, (36) ... U seal part.

Claims (3)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】蒸発器、吸収器、発生器、及び凝縮器など
をそれぞれ配管接続して冷媒とオクチルアルコールなど
の界面活性剤が添加された吸収液の循環経路を形成する
とともに、蒸発器の上部に設けられた冷媒散布器とこの
蒸発器の下部に設けられた冷媒液溜めとの間を冷媒液循
環管で接続し、蒸発器或いはこの冷媒液循環管に設けら
れた冷媒液ポンプの吐出側と凝縮器の下部に設けられた
冷媒液溜めとの間を冷媒液流下管で接続した吸収冷凍機
において、凝縮器の冷媒液溜めの冷媒流下管が接続され
る位置より上方の位置と冷媒液循環管に設けられた冷媒
液ポンプの吸込側との間を界面活性剤の戻し管で接続
し、かつ、この戻し管と冷媒液ポンプの吐出側の冷媒液
循環管との間に冷媒液の補給管を接続したことを特徴と
する吸収冷凍機。
An evaporator, an absorber, a generator, a condenser and the like are connected to each other by pipes to form a circulation path for a refrigerant and an absorbent to which a surfactant such as octyl alcohol is added. The refrigerant disperser provided at the upper part and the refrigerant liquid reservoir provided at the lower part of the evaporator are connected by a refrigerant liquid circulation pipe, and the discharge of the refrigerant liquid pump provided at the evaporator or the refrigerant liquid circulation pipe is performed. In the absorption refrigerator in which the side and the refrigerant reservoir provided at the lower part of the condenser are connected by a refrigerant downflow pipe, the position of the refrigerant above the position at which the refrigerant downflow pipe of the refrigerant reservoir of the condenser is connected A refrigerant return pipe connected to the suction side of the refrigerant liquid pump provided in the liquid circulation pipe is connected with a surfactant return pipe, and the refrigerant liquid is connected between the return pipe and the refrigerant liquid circulation pipe on the discharge side of the refrigerant liquid pump. An absorption refrigerator characterized by connecting a supply pipe of (1).
【請求項2】蒸発器、吸収器、発生器、及び凝縮器など
をそれぞれ配管接続して冷媒とオクチルアルコールなど
の界面活性剤が添加された吸収液との循環経路を形成す
るとともに、蒸発器に冷媒液循環管を接続し、この冷媒
液循環管に冷媒液ポンプを設け、かつ、凝縮器に設けら
れた冷媒液溜めと蒸発器或いは冷媒液ポンブの吐出側と
の間に冷媒液流下管を接続した吸収冷凍機において、凝
縮器の冷媒液溜めの前記冷媒流下管が接続される位置よ
り上方の位置と冷媒液ポンプの吸込側の冷媒液循環管と
の間に界面活性剤の戻し管を接続したことを特徴とする
吸収冷凍機。
2. An evaporator, an absorber, a generator, a condenser, and the like are connected by pipes to form a circulation path between the refrigerant and an absorbent to which a surfactant such as octyl alcohol is added. The refrigerant liquid circulation pipe is connected to the refrigerant liquid circulation pipe, and a refrigerant liquid pump is provided in the refrigerant liquid circulation pipe, and the refrigerant liquid flow down pipe is provided between the refrigerant liquid reservoir provided in the condenser and the discharge side of the evaporator or the refrigerant liquid pump. The return pipe of the surfactant is connected between a position of the refrigerant reservoir of the condenser above the position where the refrigerant downflow pipe is connected and the refrigerant liquid circulation pipe on the suction side of the refrigerant liquid pump. Is connected to the absorption refrigerator.
【請求項3】蒸発器、吸収器、発生器、及び凝縮器など
をそれぞれ配管接続して冷媒とオクチルアルコールなど
の界面活性剤が添加された吸収液との循環経路を形成す
るとともに、蒸発器に冷媒液循環管を接続し、この冷媒
液循環管に冷媒液ポンプを設け、かつ、凝縮器に設けら
れた冷媒液溜めと冷媒液循環管或いは蒸発器との間に冷
媒液流下管が接続された吸収冷凍機において、凝縮器の
冷媒液溜めの前記冷媒流下管が接続される位置より上方
の位置と冷媒液ポンブの吸込側の冷媒液循環管との間に
界面活性剤の戻し管を接続し、この戻し管の途中にUシ
ール部を形成し、このUシール部より上流の戻し管と冷
媒液ボンプの吐出側の冷媒液循環管との間に冷媒液の補
給管を接続したことを特徴とする吸収冷凍機。
3. An evaporator, an absorber, a generator, a condenser and the like are connected to each other by piping to form a circulation path between the refrigerant and an absorbent to which a surfactant such as octyl alcohol is added. The refrigerant liquid circulation pipe is connected to the refrigerant liquid circulation pipe, a refrigerant liquid pump is provided in the refrigerant liquid circulation pipe, and a refrigerant liquid flow down pipe is connected between the refrigerant liquid reservoir provided in the condenser and the refrigerant liquid circulation pipe or the evaporator. In the absorption refrigerator, the return pipe of the surfactant is provided between a position above the position where the refrigerant downflow pipe of the refrigerant reservoir of the condenser is connected and the refrigerant liquid circulation pipe on the suction side of the refrigerant liquid pump. Connected, forming a U-seal part in the middle of the return pipe, and connecting a refrigerant liquid supply pipe between the return pipe upstream of the U-seal part and the refrigerant liquid circulation pipe on the discharge side of the refrigerant liquid pump. An absorption refrigerator.
JP2035215A 1990-02-15 1990-02-15 Absorption refrigerator Expired - Fee Related JP2823295B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2035215A JP2823295B2 (en) 1990-02-15 1990-02-15 Absorption refrigerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2035215A JP2823295B2 (en) 1990-02-15 1990-02-15 Absorption refrigerator

Publications (2)

Publication Number Publication Date
JPH03241270A JPH03241270A (en) 1991-10-28
JP2823295B2 true JP2823295B2 (en) 1998-11-11

Family

ID=12435623

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2035215A Expired - Fee Related JP2823295B2 (en) 1990-02-15 1990-02-15 Absorption refrigerator

Country Status (1)

Country Link
JP (1) JP2823295B2 (en)

Also Published As

Publication number Publication date
JPH03241270A (en) 1991-10-28

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