JPH04347464A - Absorption type heat pump device - Google Patents

Absorption type heat pump device

Info

Publication number
JPH04347464A
JPH04347464A JP11895791A JP11895791A JPH04347464A JP H04347464 A JPH04347464 A JP H04347464A JP 11895791 A JP11895791 A JP 11895791A JP 11895791 A JP11895791 A JP 11895791A JP H04347464 A JPH04347464 A JP H04347464A
Authority
JP
Japan
Prior art keywords
refrigerant
regenerator
transfer pipe
liquid
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.)
Granted
Application number
JP11895791A
Other languages
Japanese (ja)
Other versions
JP2554793B2 (en
Inventor
Masaharu Kodera
雅晴 古寺
Tetsuo Furukawa
哲郎 古川
Sanae Omori
大森 早苗
Tatsuhiko Umeda
梅田 辰彦
Takeshi Yano
猛 矢野
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 JP3118957A priority Critical patent/JP2554793B2/en
Publication of JPH04347464A publication Critical patent/JPH04347464A/en
Application granted granted Critical
Publication of JP2554793B2 publication Critical patent/JP2554793B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Sorption Type Refrigeration Machines (AREA)

Abstract

PURPOSE:To prevent a crystallization of absorption liquid by a method wherein a regenerator is disposed at a lower position than that of an evaporator, a diluting refrigerant transporting pipe for supplying refrigerant liquid within the evaporator is disposed and an opening or closing valve opened at an emergency stopping is disposed in the midway part of the diluting refrigerant liquid transporting pipe. CONSTITUTION:In the case that a device is stopped in emergency due to power interruption during an operation of an absorption cycle, an electromagnetic opening or closing valve 23 is closed and at the same time remaining electromagnetic opening or closing valves 24, 26 are opened, refrigerant liquid within the evaporator 1 and the condensor 4 is flowed into a regenerator 3 through the first and second diluting refrigerant liquid transporting pipes 17, 18. Accordingly, since a concentration of absorption liquid within the regenerator 3 is reduced, a crystallization of the absorption liquid is prevented. As the refrigerant liquid flows into the regenerator 3, phenomena such as a vapor explosion or a water hammering and the like may occur. However, the phenomena are restricted by arranging many injection holes formed in blowing pipes 17a, 18a for the refrigerant liquid disposed in the regenerator 3 and blowing the refrigerant liquid uniformly within the regenerator 3.

Description

【発明の詳細な説明】[Detailed description of the invention]

【0001】0001

【産業上の利用分野】本発明は、吸収式ヒートポンプ装
置、特に装置停止時において吸収液の結晶化を防止し得
るようにした吸収式ヒートポンプ装置に関するものであ
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an absorption heat pump device, and more particularly to an absorption heat pump device that can prevent crystallization of an absorption liquid when the device is stopped.

【0002】0002

【従来の技術】従来、吸収式ヒートポンプ装置には、ア
ルカリ金属と硝酸塩との混合物/水の組み合わせからな
る吸収液が使用されており、またこの吸収式ヒートポン
プ装置は、冷媒(水)を蒸発させる蒸発器と、この蒸発
器で蒸発された冷媒蒸気を吸収液に吸収する吸収器と、
この吸収器で冷媒を吸収して濃度が薄くなった稀吸収液
を加熱して冷媒蒸気を分離するための再生器と、この再
生器で分離された冷媒蒸気を凝縮させる凝縮器と、蒸発
器内の冷媒蒸気を吸収器に移送する冷媒蒸気移送管と、
吸収器内の稀吸収液を再生器に移送する稀吸収液移送管
と、再生器で分離された冷媒蒸気を凝縮器に移送する冷
媒蒸気移送管と、凝縮器で凝縮された冷媒液を蒸発器に
移送する冷媒液移送管と、再生器で再生されて濃度が濃
くなった濃吸収液を吸収器に移送する濃吸収液移送管と
から構成されていた。
[Prior Art] Conventionally, an absorption liquid consisting of a mixture of an alkali metal and a nitrate/water is used in an absorption heat pump device, and this absorption heat pump device also evaporates the refrigerant (water). an evaporator; an absorber that absorbs refrigerant vapor evaporated by the evaporator into an absorption liquid;
A regenerator for separating refrigerant vapor by heating the diluted absorption liquid that absorbs refrigerant in this absorber, a condenser for condensing the refrigerant vapor separated by this regenerator, and an evaporator. a refrigerant vapor transfer pipe for transferring refrigerant vapor in the absorber to the absorber;
A dilute absorption liquid transfer pipe that transfers the dilute absorption liquid in the absorber to the regenerator, a refrigerant vapor transfer pipe that transfers the refrigerant vapor separated in the regenerator to the condenser, and a refrigerant liquid condensed in the condenser that evaporates. It consisted of a refrigerant liquid transfer pipe that transfers the refrigerant liquid to the absorber, and a concentrated absorption liquid transfer pipe that transfers the concentrated absorbent liquid that has been regenerated in the regenerator to the absorber.

【0003】0003

【発明が解決しようとする課題】上記従来の構成による
と、例えば停電などにより、溶液ポンプや再生器の加熱
装置が停止した場合、吸収液に溶けている金属塩化合物
などが結晶化し、装置の再起動が困難になるという問題
があった。
[Problems to be Solved by the Invention] According to the above-mentioned conventional configuration, when the solution pump or the heating device of the regenerator is stopped due to a power outage, for example, metal salt compounds dissolved in the absorption liquid crystallize, causing the equipment to malfunction. There was a problem that restarting was difficult.

【0004】そこで、本発明は上記問題を解消し得る吸
収式ヒートポンプ装置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 an absorption heat pump device that can solve the above problems.

【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
、本発明の第1の手段は、冷媒を蒸発させる蒸発器と、
この蒸発器で蒸発された冷媒蒸気を吸収液に吸収する吸
収器と、この吸収器で冷媒を吸収して濃度が薄くなった
稀吸収液を加熱して冷媒蒸気を分離するための再生器と
、この再生器で分離された冷媒蒸気を凝縮させる凝縮器
と、蒸発器内の冷媒蒸気を吸収器に移送する冷媒蒸気移
送管と、吸収器内の稀吸収液を再生器に移送する稀吸収
液移送管と、再生器で分離された冷媒蒸気を凝縮器に移
送する冷媒蒸気移送管と、凝縮器で凝縮された冷媒液を
蒸発器に移送する冷媒液移送管と、再生器で再生されて
濃度が濃くなった濃吸収液を吸収器に移送する濃吸収液
移送管とを有する吸収式ヒートポンプ装置において、少
なくとも再生器を蒸発器よりも下方位置に配置し、上記
蒸発器内の冷媒液を再生器内に供給する希釈用冷媒液移
送管を設けるとともに、この希釈用冷媒液移送管の途中
に非常停止時に開状態となる開閉弁を設けた吸収式ヒー
トポンプ装置である。
[Means for Solving the Problems] In order to solve the above problems, a first means of the present invention includes an evaporator that evaporates a refrigerant;
an absorber that absorbs the refrigerant vapor evaporated by this evaporator into an absorption liquid; and a regenerator that absorbs the refrigerant in this absorber and heats the diluted absorption liquid to separate the refrigerant vapor. , a condenser that condenses the refrigerant vapor separated by this regenerator, a refrigerant vapor transfer pipe that transfers the refrigerant vapor in the evaporator to the absorber, and a rare absorber that transfers the dilute absorption liquid in the absorber to the regenerator. A liquid transfer pipe, a refrigerant vapor transfer pipe that transfers the refrigerant vapor separated in the regenerator to the condenser, a refrigerant liquid transfer pipe that transfers the refrigerant liquid condensed in the condenser to the evaporator, and a refrigerant liquid transfer pipe that transfers the refrigerant vapor separated in the regenerator to the evaporator. In an absorption heat pump device having a concentrated absorption liquid transfer pipe that transfers the concentrated absorption liquid whose concentration has been increased by This is an absorption heat pump device that is provided with a dilution refrigerant liquid transfer pipe that supplies the refrigerant into the regenerator, and an on-off valve that is opened during an emergency stop in the middle of this dilution refrigerant liquid transfer pipe.

【0006】また、上記課題を解決するため、本発明の
第2の手段は、冷媒を蒸発させる蒸発器と、この蒸発器
で蒸発された冷媒蒸気を吸収液に吸収する吸収器と、こ
の吸収器で冷媒を吸収して濃度が薄くなった稀吸収液を
加熱して冷媒蒸気を分離するための再生器と、この再生
器で分離された冷媒蒸気を凝縮させる凝縮器と、蒸発器
内の冷媒蒸気を吸収器に移送する冷媒蒸気移送管と、吸
収器内の稀吸収液を再生器に移送する稀吸収液移送管と
、再生器で分離された冷媒蒸気を凝縮器に移送する冷媒
蒸気移送管と、凝縮器で凝縮された冷媒液を蒸発器に移
送する冷媒液移送管と、再生器で再生されて濃度が濃く
なった濃吸収液を吸収器に移送する濃吸収液移送管とを
有する吸収式ヒートポンプ装置において、少なくとも再
生器を蒸発器よりも下方位置に配置し、上記凝縮器内の
冷媒液を再生器内に供給する希釈用冷媒液移送管を設け
るとともに、この希釈用冷媒液移送管の途中に非常停止
時に開状態となる開閉弁を設けた吸収式ヒートポンプ装
置である。
[0006] In order to solve the above-mentioned problems, the second means of the present invention includes an evaporator for evaporating a refrigerant, an absorber for absorbing the refrigerant vapor evaporated by the evaporator into an absorption liquid, and a A regenerator for separating the refrigerant vapor by heating the diluted absorption liquid that absorbs the refrigerant in the regenerator, a condenser for condensing the refrigerant vapor separated by the regenerator, and a A refrigerant vapor transfer pipe that transfers refrigerant vapor to the absorber, a dilute absorption liquid transfer pipe that transfers the dilute absorption liquid in the absorber to the regenerator, and a refrigerant vapor that transfers the refrigerant vapor separated in the regenerator to the condenser. A transfer pipe, a refrigerant liquid transfer pipe that transfers the refrigerant liquid condensed in the condenser to the evaporator, and a concentrated absorption liquid transfer pipe that transfers the concentrated absorption liquid that has been regenerated and concentrated in the regenerator to the absorber. In an absorption heat pump device having at least a regenerator located below the evaporator, a refrigerant liquid transfer pipe for dilution is provided to supply the refrigerant liquid in the condenser to the regenerator, and the refrigerant for dilution is This is an absorption heat pump device that is equipped with an on-off valve that opens during an emergency stop in the middle of the liquid transfer pipe.

【0007】また、上記課題を解決するため、本発明の
第3の手段は、上記第1または第2の手段の構成におい
て、再生器で分離された冷媒蒸気を凝縮器に移送する冷
媒蒸気移送管の途中に、凝縮器側からの逆流を防止する
ための逆止弁を設けた吸収式ヒートポンプ装置である。
Further, in order to solve the above-mentioned problem, a third means of the present invention is a refrigerant vapor transfer system in which the refrigerant vapor separated in the regenerator is transferred to the condenser in the configuration of the first or second means. This is an absorption heat pump device that is equipped with a check valve in the middle of the pipe to prevent backflow from the condenser side.

【0008】また、上記課題を解決するため、本発明の
第4の手段は、第1または第2の手段の構成において、
再生器内に冷媒液を供給するための希釈用冷媒液移送管
の再生器内に突設される冷媒液の吹出し管部に多数の噴
射穴を形成した吸収式ヒートポンプ装置である。
[0008] Furthermore, in order to solve the above-mentioned problem, a fourth means of the present invention is provided in the configuration of the first or second means,
This is an absorption heat pump device in which a large number of injection holes are formed in the refrigerant liquid blow-off pipe section of the refrigerant liquid transfer pipe for dilution that is protruded into the regenerator for supplying the refrigerant liquid into the regenerator.

【0009】さらに、上記課題を解決するため、本発明
の第5の手段は、上記第1または第2の手段の構成にお
いて、再生器内に冷媒液を供給するための希釈用冷媒液
移送管の途中および再生器内に突設された部分に逆止弁
を設けた吸収式ヒートポンプ装置である。
Furthermore, in order to solve the above-mentioned problem, a fifth means of the present invention is a dilution refrigerant liquid transfer pipe for supplying refrigerant liquid into the regenerator in the configuration of the above-mentioned first or second means. This is an absorption heat pump device that is equipped with a check valve in the middle of the regenerator and in a protruding part inside the regenerator.

【0010】0010

【作用】上記の構成によると、装置が停止した場合、希
釈用冷媒液移送管途中に設けられた開閉弁が開状態とな
り、蒸発器内または凝縮器内の冷媒液がそれぞれの希釈
用冷媒液移送管を介して再生器内に流入する。
[Operation] According to the above configuration, when the device is stopped, the on-off valve provided in the middle of the dilution refrigerant liquid transfer pipe is opened, and the refrigerant liquid in the evaporator or condenser is transferred to the dilution refrigerant liquid. It flows into the regenerator via the transfer pipe.

【0011】したがって、再生器内の吸収液の濃度が薄
められるため、吸収液の結晶化が防止される。また、希
釈用冷媒液移送管途中に逆止弁を設けることにより、再
生器内の吸収液が蒸発器または凝縮器内に逆流するのを
防止することができる。
[0011] Therefore, since the concentration of the absorption liquid in the regenerator is diluted, crystallization of the absorption liquid is prevented. Further, by providing a check valve in the middle of the dilution refrigerant liquid transfer pipe, it is possible to prevent the absorption liquid in the regenerator from flowing back into the evaporator or condenser.

【0012】0012

【実施例】以下、本発明の一実施例を図1に基づき説明
する。図1に示すように、本実施例における吸収式ヒー
トポンプ装置は、冷媒を蒸発させる蒸発器1と、この蒸
発器1で蒸発された冷媒蒸気を吸収液に吸収する吸収器
2と、この吸収器2で冷媒を吸収して濃度が薄くなった
稀吸収液を加熱して冷媒蒸気を分離するための再生器3
と、この再生器3で分離された冷媒蒸気を凝縮させる凝
縮器4と、蒸発器1内の冷媒蒸気を吸収器2に移送する
冷媒蒸気移送管11と、途中に溶液ポンプ21を有して
吸収器内2の稀吸収液を再生器3に移送する稀吸収液移
送管12と、途中に逆止弁22を有して再生器3で分離
された冷媒蒸気を凝縮器4に移送する冷媒蒸気移送管1
3と、途中に通電時に開状態となる電磁開閉弁23を有
して凝縮器4で凝縮された冷媒液を蒸発器1に移送する
冷媒液移送管14と、再生器3で再生されて濃度が濃く
なった濃吸収液を吸収器2に移送する濃吸収液移送管1
5と、この濃吸収液移送管15と稀吸収液移送管12と
の間で熱交換を行うための熱交換器16と、途中に非常
停止時に開状態となる電磁開閉弁24および逆止弁25
を有して、上記蒸発器1内の冷媒液を再生器3内に供給
する第1希釈用冷媒液移送管17と、途中に非常停止時
に開状態となる電磁開閉弁26および逆止弁27を有し
て、上記凝縮器4内の冷媒液を再生器3内に供給する第
2希釈用冷媒液移送管18とから構成され、さらに上記
再生器3および凝縮器4が蒸発器1および吸収器2より
も下方に配置されたものである。
[Embodiment] An embodiment of the present invention will be described below with reference to FIG. As shown in FIG. 1, the absorption heat pump device in this embodiment includes an evaporator 1 that evaporates refrigerant, an absorber 2 that absorbs the refrigerant vapor evaporated in the evaporator 1 into an absorption liquid, and Regenerator 3 for heating the diluted absorption liquid that absorbed the refrigerant in step 2 and separating the refrigerant vapor.
It has a condenser 4 that condenses the refrigerant vapor separated by the regenerator 3, a refrigerant vapor transfer pipe 11 that transfers the refrigerant vapor in the evaporator 1 to the absorber 2, and a solution pump 21 in the middle. A dilute absorption liquid transfer pipe 12 that transfers the dilute absorption liquid in the absorber 2 to the regenerator 3, and a refrigerant that has a check valve 22 in the middle to transfer the refrigerant vapor separated in the regenerator 3 to the condenser 4. Steam transfer pipe 1
3, a refrigerant liquid transfer pipe 14 which has an electromagnetic on-off valve 23 that opens when energized and transfers the refrigerant liquid condensed in the condenser 4 to the evaporator 1; A concentrated absorption liquid transfer pipe 1 that transfers the concentrated absorption liquid to the absorber 2
5, a heat exchanger 16 for exchanging heat between the concentrated absorption liquid transfer pipe 15 and the dilute absorption liquid transfer pipe 12, and an electromagnetic on-off valve 24 and a check valve that are opened during an emergency stop. 25
A first dilution refrigerant liquid transfer pipe 17 that supplies the refrigerant liquid in the evaporator 1 to the regenerator 3, and an electromagnetic on-off valve 26 and a check valve 27 that are opened during an emergency stop. and a second dilution refrigerant liquid transfer pipe 18 that supplies the refrigerant liquid in the condenser 4 to the regenerator 3, and the regenerator 3 and condenser 4 are connected to the evaporator 1 and the absorber 3. It is placed below the vessel 2.

【0013】なお、上記逆止弁22,24はそれぞれ再
生器3側からの吸収液の逆流を防止するためのものであ
る。上記構成において、吸収サイクルの作動中に、例え
ば停電により装置が非常停止した場合、電磁開閉弁23
が閉状態となるとともに、残りの電磁開閉弁24,26
が開状態となり、蒸発器1内および凝縮器4内の冷媒液
が第1および第2希釈用冷媒液移送管17,18を介し
て再生器3内に流入する。
Note that the check valves 22 and 24 are for preventing backflow of the absorbing liquid from the regenerator 3 side. In the above configuration, if the device comes to an emergency stop due to a power outage while the absorption cycle is in operation, the electromagnetic on-off valve 23
is closed, and the remaining electromagnetic on-off valves 24 and 26 are closed.
is opened, and the refrigerant liquid in the evaporator 1 and the condenser 4 flows into the regenerator 3 via the first and second dilution refrigerant liquid transfer pipes 17 and 18.

【0014】したがって、再生器3内の吸収液の濃度が
薄められるため、たとえ再生器3内の吸収液の温度が低
下した場合でも、吸収液の結晶化が防止される。なお、
冷媒液が再生器3内の流入すると、沸騰蒸気の消滅によ
り、激しい溶液運動、すなわち蒸気爆発やウォータハン
マーなどの現象が起こるが、再生器3内に設けられてい
る冷媒液の吹出し管部17a,18aに形成する噴出穴
を多数設けて、再生器3内に均一に冷媒液を吹き出すこ
とにより、抑制することができる。
[0014] Therefore, since the concentration of the absorption liquid in the regenerator 3 is diluted, even if the temperature of the absorption liquid in the regenerator 3 decreases, crystallization of the absorption liquid is prevented. In addition,
When the refrigerant liquid flows into the regenerator 3, intense solution movement occurs due to the disappearance of boiling vapor, such as steam explosion and water hammer. , 18a to uniformly blow out the refrigerant liquid into the regenerator 3, this can be suppressed.

【0015】このように、装置停止時において、吸収液
の結晶化が防止されるため、装置の再起動を容易に行う
ことができる。ところで、上記実施例においては、蒸発
器1および凝縮器4からの冷媒液を再生器3内に供給す
るようにしたが、例えば蒸発器1または凝縮器4のいず
れから冷媒液を再生器3内に供給するようにしてもよい
[0015] In this way, since crystallization of the absorption liquid is prevented when the apparatus is stopped, the apparatus can be restarted easily. Incidentally, in the above embodiment, the refrigerant liquid from the evaporator 1 and the condenser 4 is supplied into the regenerator 3, but for example, the refrigerant liquid is supplied into the regenerator 3 from either the evaporator 1 or the condenser 4. It may also be supplied to

【0016】また、上記実施例においては、各逆止弁2
5,27をそれぞれ希釈用冷媒移送管17,18途中に
設けたが、例えば図1の仮想線で示すように、各希釈用
冷媒移送管17,18の再生器3内に突設された部分、
すなわち各吹出し管部17a,18a部に設けるように
してもよい。
Furthermore, in the above embodiment, each check valve 2
5 and 27 are provided in the middle of the dilution refrigerant transfer pipes 17 and 18, respectively. For example, as shown by the imaginary line in FIG. ,
That is, it may be provided in each of the blow-off pipe portions 17a and 18a.

【0017】[0017]

【発明の効果】以上のように本発明の構成によると、装
置停止時においては、希釈用冷媒液移送管途中の開閉弁
が開くため、蒸発器内または凝縮器内の冷媒液がそれぞ
れの希釈用冷媒液移送管を介して再生器内に流入し、し
たがって再生器内の吸収液の濃度が薄められるため、吸
収液の結晶化が防止される。
As described above, according to the structure of the present invention, when the apparatus is stopped, the on-off valve in the middle of the dilution refrigerant liquid transfer pipe is opened, so that the refrigerant liquid in the evaporator or condenser is diluted. The refrigerant flows into the regenerator through the refrigerant liquid transfer pipe, thus diluting the concentration of the absorption liquid in the regenerator, thereby preventing crystallization of the absorption liquid.

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

【図1】本発明の一実施例における吸収式ヒートポンプ
装置の概略構成を示す側面図である。
FIG. 1 is a side view showing a schematic configuration of an absorption heat pump device according to an embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1          蒸発器 2          吸収器 3          再生器 4          凝縮器 11          冷媒蒸気移送管12    
      吸収液移送管13          冷
媒蒸気移送管14          冷媒液移送管1
5          濃吸収液移送管17     
     第1希釈用冷媒液移送管18       
   第2希釈用冷媒液移送管24         
 電磁開閉弁 25          逆止弁 26          電磁開閉弁 27          逆止弁
1 Evaporator 2 Absorber 3 Regenerator 4 Condenser 11 Refrigerant vapor transfer pipe 12
Absorption liquid transfer pipe 13 Refrigerant vapor transfer pipe 14 Refrigerant liquid transfer pipe 1
5 Concentrated absorption liquid transfer pipe 17
First dilution refrigerant liquid transfer pipe 18
Second dilution refrigerant liquid transfer pipe 24
Solenoid on-off valve 25 Check valve 26 Solenoid on-off valve 27 Check valve

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】冷媒を蒸発させる蒸発器と、この蒸発器で
蒸発された冷媒蒸気を吸収液に吸収する吸収器と、この
吸収器で冷媒を吸収して濃度が薄くなった稀吸収液を加
熱して冷媒蒸気を分離するための再生器と、この再生器
で分離された冷媒蒸気を凝縮させる凝縮器と、蒸発器内
の冷媒蒸気を吸収器に移送する冷媒蒸気移送管と、吸収
器内の稀吸収液を再生器に移送する稀吸収液移送管と、
再生器で分離された冷媒蒸気を凝縮器に移送する冷媒蒸
気移送管と、凝縮器で凝縮された冷媒液を蒸発器に移送
する冷媒液移送管と、再生器で再生されて濃度が濃くな
った濃吸収液を吸収器に移送する濃吸収液移送管とを有
する吸収式ヒートポンプ装置において、少なくとも再生
器を蒸発器よりも下方位置に配置し、上記蒸発器内の冷
媒液を再生器内に供給する希釈用冷媒液移送管を設ける
とともに、この希釈用冷媒液移送管の途中に非常停止時
に開状態となる開閉弁を設けたことを特徴とする吸収式
ヒートポンプ装置。
Claim 1: An evaporator that evaporates refrigerant, an absorber that absorbs the refrigerant vapor evaporated by the evaporator into an absorption liquid, and a dilute absorption liquid whose concentration has been reduced by absorbing the refrigerant with the absorber. A regenerator for heating and separating refrigerant vapor, a condenser for condensing the refrigerant vapor separated by this regenerator, a refrigerant vapor transfer pipe for transferring refrigerant vapor in the evaporator to an absorber, and an absorber. a dilute absorption liquid transfer pipe for transferring the dilute absorption liquid in the regenerator;
A refrigerant vapor transfer pipe transfers the refrigerant vapor separated in the regenerator to the condenser, a refrigerant liquid transfer pipe transfers the refrigerant liquid condensed in the condenser to the evaporator, and the refrigerant vapor is regenerated in the regenerator to become more concentrated. In an absorption heat pump device having a concentrated absorption liquid transfer pipe for transferring the concentrated absorption liquid to the absorber, at least a regenerator is disposed below the evaporator, and the refrigerant liquid in the evaporator is transferred into the regenerator. An absorption heat pump device characterized in that a dilution refrigerant liquid transfer pipe is provided, and an on-off valve that is opened during an emergency stop is provided in the middle of the dilution refrigerant liquid transfer pipe.
【請求項2】冷媒を蒸発させる蒸発器と、この蒸発器で
蒸発された冷媒蒸気を吸収液に吸収する吸収器と、この
吸収器で冷媒を吸収して濃度が薄くなった稀吸収液を加
熱して冷媒蒸気を分離するための再生器と、この再生器
で分離された冷媒蒸気を凝縮させる凝縮器と、蒸発器内
の冷媒蒸気を吸収器に移送する冷媒蒸気移送管と、吸収
器内の稀吸収液を再生器に移送する稀吸収液移送管と、
再生器で分離された冷媒蒸気を凝縮器に移送する冷媒蒸
気移送管と、凝縮器で凝縮された冷媒液を蒸発器に移送
する冷媒液移送管と、再生器で再生されて濃度が濃くな
った濃吸収液を吸収器に移送する濃吸収液移送管とを有
する吸収式ヒートポンプ装置において、少なくとも再生
器を蒸発器よりも下方位置に配置し、上記凝縮器内の冷
媒液を再生器内に供給する希釈用冷媒液移送管を設ける
とともに、この希釈用冷媒液移送管の途中に非常停止時
に開状態となる開閉弁を設けたことを特徴とする吸収式
ヒートポンプ装置。
Claim 2: An evaporator that evaporates refrigerant, an absorber that absorbs the refrigerant vapor evaporated by the evaporator into an absorption liquid, and a dilute absorption liquid whose concentration has been reduced by absorbing the refrigerant with the absorber. A regenerator for heating and separating refrigerant vapor, a condenser for condensing the refrigerant vapor separated by this regenerator, a refrigerant vapor transfer pipe for transferring refrigerant vapor in the evaporator to an absorber, and an absorber. a dilute absorption liquid transfer pipe for transferring the dilute absorption liquid in the regenerator;
A refrigerant vapor transfer pipe transfers the refrigerant vapor separated in the regenerator to the condenser, a refrigerant liquid transfer pipe transfers the refrigerant liquid condensed in the condenser to the evaporator, and the refrigerant vapor is regenerated in the regenerator to become more concentrated. In an absorption heat pump device having a concentrated absorption liquid transfer pipe for transferring concentrated absorption liquid to an absorber, at least a regenerator is disposed at a position below the evaporator, and the refrigerant liquid in the condenser is transferred into the regenerator. An absorption heat pump device characterized in that a dilution refrigerant liquid transfer pipe is provided, and an on-off valve that is opened during an emergency stop is provided in the middle of the dilution refrigerant liquid transfer pipe.
【請求項3】再生器で分離された冷媒蒸気を凝縮器に移
送する冷媒蒸気移送管の途中に、凝縮器側からの逆流を
防止するための逆止弁を設けたことを特徴とする請求項
1または2に記載の吸収式ヒートポンプ装置。
Claim 3: A claim characterized in that a check valve for preventing backflow from the condenser side is provided in the middle of the refrigerant vapor transfer pipe that transfers the refrigerant vapor separated by the regenerator to the condenser. Item 2. Absorption heat pump device according to item 1 or 2.
【請求項4】再生器内に冷媒液を供給するための希釈用
冷媒液移送管の再生器内に突設される冷媒液の吹出し管
部に多数の噴射穴を形成したことを特徴とする請求項1
または2に記載の吸収式ヒートポンプ装置。
4. A diluting refrigerant liquid transfer pipe for supplying refrigerant liquid into the regenerator, the refrigerant liquid blow-out pipe portion protruding into the regenerator is provided with a large number of injection holes. Claim 1
Or the absorption heat pump device according to 2.
【請求項5】再生器内に冷媒液を供給するための希釈用
冷媒液移送管の途中および再生器内に突設された部分に
逆止弁を設けたことを特徴とする請求項1または2に記
載の吸収式ヒートポンプ装置。
5. A check valve as claimed in claim 1 or 2, characterized in that a check valve is provided in the middle of the dilution refrigerant liquid transfer pipe for supplying refrigerant liquid into the regenerator and in a portion protruding into the regenerator. 2. The absorption heat pump device according to 2.
JP3118957A 1991-05-24 1991-05-24 Absorption heat pump device Expired - Lifetime JP2554793B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3118957A JP2554793B2 (en) 1991-05-24 1991-05-24 Absorption heat pump device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3118957A JP2554793B2 (en) 1991-05-24 1991-05-24 Absorption heat pump device

Publications (2)

Publication Number Publication Date
JPH04347464A true JPH04347464A (en) 1992-12-02
JP2554793B2 JP2554793B2 (en) 1996-11-13

Family

ID=14749463

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3118957A Expired - Lifetime JP2554793B2 (en) 1991-05-24 1991-05-24 Absorption heat pump device

Country Status (1)

Country Link
JP (1) JP2554793B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007285649A (en) * 2006-04-19 2007-11-01 Ebara Corp Absorption heating value control method for absorption heat pump device, and absorption heat pump device
JP2010096374A (en) * 2008-10-15 2010-04-30 Ebara Refrigeration Equipment & Systems Co Ltd Absorption heat pump

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007285649A (en) * 2006-04-19 2007-11-01 Ebara Corp Absorption heating value control method for absorption heat pump device, and absorption heat pump device
JP2010096374A (en) * 2008-10-15 2010-04-30 Ebara Refrigeration Equipment & Systems Co Ltd Absorption heat pump

Also Published As

Publication number Publication date
JP2554793B2 (en) 1996-11-13

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