JPS58187765A - Absorption type heat pump device - Google Patents

Absorption type heat pump device

Info

Publication number
JPS58187765A
JPS58187765A JP6909782A JP6909782A JPS58187765A JP S58187765 A JPS58187765 A JP S58187765A JP 6909782 A JP6909782 A JP 6909782A JP 6909782 A JP6909782 A JP 6909782A JP S58187765 A JPS58187765 A JP S58187765A
Authority
JP
Japan
Prior art keywords
temperature
absorber
heat
condenser
coolant
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
JP6909782A
Other languages
Japanese (ja)
Other versions
JPH0321827B2 (en
Inventor
若松 伸彦
功 竹下
山田 穂積
実 田頭
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.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial 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 Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP6909782A priority Critical patent/JPS58187765A/en
Publication of JPS58187765A publication Critical patent/JPS58187765A/en
Publication of JPH0321827B2 publication Critical patent/JPH0321827B2/ja
Granted 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】 本発明は吸収器および凝縮器からの熱を給湯に利用する
吸収式ヒーナポンプ装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an absorption type heater pump device that utilizes heat from an absorber and a condenser for hot water supply.

従来、吸収式ヒートポンプとしては第1図に示すものぴ
゛ある。吸収器1から出た冷媒濃度の高い溶液(以下濃
液と記す)はポンプ2で発生器3に送られ、ここで′加
熱されて冷媒蒸気を発生する。
Conventionally, there are absorption heat pumps such as those shown in FIG. A solution with high refrigerant concentration (hereinafter referred to as concentrated liquid) discharged from the absorber 1 is sent by a pump 2 to a generator 3, where it is heated and generates refrigerant vapor.

暖房の場合はこの冷媒蒸気を室内に送り放熱させれば良
いが、給湯に利用する場合は液タンク4内に凝縮器5を
配設し、ここで凝縮させて、液タンク4内の液媒体を加
熱する。凝縮した液冷媒は膨張弁6を通り蒸発器7で蒸
発し吸収器1に戻る。
In the case of heating, this refrigerant vapor can be sent indoors for heat dissipation, but when used for hot water supply, a condenser 5 is installed in the liquid tank 4, where it is condensed and the liquid medium in the liquid tank 4 is heat up. The condensed liquid refrigerant passes through the expansion valve 6, evaporates in the evaporator 7, and returns to the absorber 1.

一方、発生器3から出る冷媒濃度の低い溶液(以下希液
と記す)は、減圧弁8を経て吸収器1に流入し、冷媒蒸
気を吸収して濃液を再生する。この時吸収熱を発生する
ので、すみやかに除去する必要があり、冷却液を水ポン
プ9で循環させている。
On the other hand, a solution with a low refrigerant concentration (hereinafter referred to as a dilute solution) coming out of the generator 3 flows into the absorber 1 via a pressure reducing valve 8, absorbs refrigerant vapor, and regenerates a concentrated solution. Since absorption heat is generated at this time, it is necessary to remove it promptly, and the cooling liquid is circulated by a water pump 9.

吸収器ηゝら出た冷却液は昇温しでいるので再度吸収器
の冷却に使用する為にはどこかで放熱しなければならな
い。吸収熱を利用しない場合は′空冷によって外部放出
する場合もあるが、給湯に利用する場合は、第1図のよ
うに温水熱交換器1oで熱交換させて、昇温した冷却液
の温度降下を図ると共に、市水11の温度を上げている
。ここで昇温した冷却液は液タンク4の上部人口12よ
り入り、熱交換して温度が低下した後は下部出口13か
ら水ポンプ9により循環するようになっている。
Since the temperature of the coolant discharged from the absorber η has risen, the heat must be dissipated somewhere in order to be used again to cool the absorber. If the absorbed heat is not used, it may be released to the outside by air cooling, but if it is used for hot water supply, it is exchanged with the hot water heat exchanger 1o as shown in Figure 1, and the temperature of the coolant that has been raised is lowered. At the same time, the temperature of city water 11 is being raised. The coolant whose temperature has been raised here enters the liquid tank 4 from the upper part 12, and after the temperature has decreased through heat exchange, it is circulated from the lower part outlet 13 by the water pump 9.

いま、外気温が低く、市水11り温度も低く長期間使用
していないような場合、液タンク4下部の水温は低く、
液タンク4下部に凝縮器5を設けてあっても液タンク4
下部の冷却液温は容易に上昇しない。そのため吸収器1
の冷却液温が低すぎる状態が生じる。吸収器10入口冷
却液温が低すぎるとサイクルの低圧も下がり過ぎる。そ
うすると必然的に吸収器1の最高温度も低下し吸収器出
口冷却液温も低下する。これは給湯の性質上、高い温度
を得たい目的とは反してはなはだ都合が悪い。
If the outside temperature is low and the city water 11 temperature is low and the water has not been used for a long time, the water temperature at the bottom of the liquid tank 4 will be low.
Even if the condenser 5 is provided at the bottom of the liquid tank 4, the liquid tank 4
The temperature of the coolant at the bottom does not rise easily. Therefore, absorber 1
A situation occurs where the coolant temperature is too low. If the absorber 10 inlet coolant temperature is too low, the low pressure of the cycle will also be too low. If this happens, the maximum temperature of the absorber 1 will inevitably decrease, and the temperature of the coolant at the outlet of the absorber will also decrease. Due to the nature of hot water supply, this is extremely inconvenient as it goes against the goal of obtaining a high temperature.

本発明は上記従来技術の問題点に鑑み、凝縮熱を利用し
て吸収器冷却液温低下の問題を解決する例 ものである。以下にその詳細を実施に従って説明する。
In view of the problems of the prior art described above, the present invention is an example of solving the problem of a drop in absorber coolant temperature by utilizing condensation heat. The details will be explained below according to implementation.

第2図は本発明の一実施例の要部を示すものでり、液タ
ンク14内には主凝縮器15と温水熱交換器16が配設
されている。ポンプ17で循環される冷却液は吸収器1
8を冷却後、入口19より液タンク14に流入する。液
タンク14内の冷却液は、吸収熱と主凝縮器15の凝縮
熱により昇温すると共に、温水熱交換器16で市水2o
と熱交換して出口21では低温となっている。又、図示
していないが温水熱交換器16を室内に設けて冷却液を
別ポンプで循環させ、暖房た使う場合も同様で液タンク
14下部へ、低温の液で戻ってくる。
FIG. 2 shows the main parts of an embodiment of the present invention, in which a main condenser 15 and a hot water heat exchanger 16 are disposed within the liquid tank 14. The coolant circulated by the pump 17 is supplied to the absorber 1
After cooling the liquid 8, it flows into the liquid tank 14 through the inlet 19. The temperature of the cooling liquid in the liquid tank 14 rises due to the heat of absorption and the heat of condensation from the main condenser 15, and the temperature of the cooling liquid in the liquid tank 14 increases.
The temperature at the outlet 21 is low due to heat exchange. Further, although not shown, a hot water heat exchanger 16 is provided indoors, and the coolant is circulated by a separate pump, and the coolant is returned to the lower part of the liquid tank 14 as a low-temperature liquid in the same manner when used for heating.

この低温の冷却液は、出口21から補助凝縮器22に流
入する。発生器3からの冷媒ガヌは先ずこの補助凝縮器
22に流入して冷却液と熱交換され主凝縮器15に入る
。一方、熱交換によって昇温した冷却液はポンプ1.7
に戻る。
This low temperature cooling liquid flows into the auxiliary condenser 22 from the outlet 21. The refrigerant gas from the generator 3 first flows into this auxiliary condenser 22 and exchanges heat with the cooling liquid before entering the main condenser 15 . On the other hand, the coolant heated by heat exchange is pumped to pump 1.7.
Return to

このように吸収器1gff)入口に戻される冷却液は凝
縮熱の一部を受けるため給湯熱量は若干低下するが、冷
却液の最低温度が凝縮温度より若干低い所定値になるま
で低すぎる市水20の時でも吸収器18の入口冷却液温
が低下しすぎることになく。
In this way, the coolant returned to the absorber 1gff) inlet receives part of the condensation heat, so the amount of hot water supply decreases slightly. 20, the temperature of the coolant at the inlet of the absorber 18 does not drop too much.

吸収式サイクルの低圧が大巾に変動することはない。従
って吸収器出口冷却液温は所定温度で維持することがで
きる。このことは市水2oの出口では常時高温の冷却液
と熱交換することを意味し、スタートから高温の出湯を
得ることができる。
The low pressure of the absorption cycle does not fluctuate widely. Therefore, the absorber outlet coolant temperature can be maintained at a predetermined temperature. This means that at the outlet of the city water 2o, heat is constantly exchanged with the high-temperature cooling liquid, and hot water can be obtained at a high temperature from the start.

第3図は本発明の異なる実施例の要部を示すものであり
第2図と共通する部分には同一番号を付す。温水熱交換
器23を第1の液タンク24に、主凝縮器25を第2の
液タンク26に、出口27とポンプ17の間に補助凝縮
器28とセンサー29を、そして主凝縮器26と補助凝
縮器28の冷媒回路に切換弁30.31を設けたもので
ある。
FIG. 3 shows main parts of a different embodiment of the present invention, and parts common to those in FIG. 2 are given the same numbers. The hot water heat exchanger 23 is connected to the first liquid tank 24, the main condenser 25 is connected to the second liquid tank 26, the auxiliary condenser 28 and the sensor 29 are connected between the outlet 27 and the pump 17, and the main condenser 26 and A switching valve 30, 31 is provided in the refrigerant circuit of the auxiliary condenser 28.

冷媒回路は切換弁3〇−主凝縮器26−切換弁31と、
切換弁30−補助凝縮器28−切換弁31と、切換弁3
〇−補助凝縮器28−主凝縮器26−切換弁31との3
回路に切換ができる。従ってセンサー29で検出した温
度により設定値以下では補助凝縮器28を通し、設定値
以上であれば主凝縮器25のみに、極端に低い場合は補
助凝縮器28のみに冷媒を流すように切換えることによ
り、冷却液の温度低下を防ぎ、サイクルの低圧の維持、
即ち吸収器出口液温の維持を図ることができる。
The refrigerant circuit includes a switching valve 30 - a main condenser 26 - a switching valve 31,
Switching valve 30 - auxiliary condenser 28 - switching valve 31 and switching valve 3
〇-Auxiliary condenser 28-Main condenser 26-Switching valve 31
The circuit can be switched. Therefore, depending on the temperature detected by the sensor 29, the refrigerant can be switched to flow through the auxiliary condenser 28 if it is below the set value, only to the main condenser 25 if it is above the set value, and only to the auxiliary condenser 28 if it is extremely low. This prevents coolant temperature from dropping and maintains low pressure in the cycle.
In other words, the temperature of the absorber outlet liquid can be maintained.

以上のように本発明は吸収式ヒートポンプサイクルの吸
収器の冷却液流路に設けた液タンク冷却液流路に凝縮熱
との熱交換回路を設けることによって、冷却液温が低い
時や市水温度が低く結果的に冷却液温が低すぎる時でも
、吸収器出口冷却液温の維持を図り、高い給湯温度の確
保ができる。
As described above, the present invention provides a heat exchange circuit with condensation heat in the liquid tank coolant flow path provided in the coolant flow path of the absorber of an absorption heat pump cycle, so that it can be used when the coolant temperature is low or when the city water Even when the temperature is low and as a result, the coolant temperature is too low, the absorber outlet coolant temperature can be maintained and a high hot water supply temperature can be ensured.

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

第1図は従来例の一実施例の吸収式ヒートポンプ装置の
構成図、第2図は本発明の一実施例の要部を示す図、第
3図は本発明の異なる実施例の要部を示す図である。 18・・・・・・吸収器、14液タンク、16・・・・
・・温水熱交換器、15・・・・・・主凝縮器、22・
・・・・・補助凝縮器。 代理人の氏名 弁理士 中 尾 敏 男 ほか1名第1
図 第2図 第3図 2
Fig. 1 is a block diagram of an absorption heat pump device according to an embodiment of the conventional example, Fig. 2 is a diagram showing a main part of an embodiment of the present invention, and Fig. 3 is a diagram showing main parts of a different embodiment of the present invention. FIG. 18...Absorber, 14 liquid tank, 16...
...Hot water heat exchanger, 15...Main condenser, 22.
...Auxiliary condenser. Name of agent: Patent attorney Toshio Nakao and 1 other person No. 1
Figure 2 Figure 3 Figure 2

Claims (3)

【特許請求の範囲】[Claims] (1)発生器、凝縮器、蒸発器、吸収器を少なくと一媒
体出口から前記吸収器までの流路に前記液媒体と熱交換
する補助凝縮器を設けたことを特徴とする吸収式ヒート
ポンプ装置。
(1) An absorption heat pump characterized in that a generator, a condenser, an evaporator, and an absorber are provided with an auxiliary condenser that exchanges heat with the liquid medium in a flow path from at least one medium outlet to the absorber. Device.
(2)前記補助凝縮器は前記凝縮器から分岐したもので
あ゛る特許請求の範囲第1項に記載の吸収式ヒートポン
プ装置。
(2) The absorption heat pump device according to claim 1, wherein the auxiliary condenser is branched from the condenser.
(3)前記液媒体タンクは前記凝縮器の凝縮熱および前
記吸収器の吸収熱と前記液媒体間で熱交換させる熱交換
器を有する特許請求の範囲第1項または第2項に記載の
吸収式ヒートポンプ装置。
(3) The absorber according to claim 1 or 2, wherein the liquid medium tank has a heat exchanger that exchanges heat between the liquid medium and the condensation heat of the condenser and the absorption heat of the absorber. type heat pump device.
JP6909782A 1982-04-23 1982-04-23 Absorption type heat pump device Granted JPS58187765A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6909782A JPS58187765A (en) 1982-04-23 1982-04-23 Absorption type heat pump device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6909782A JPS58187765A (en) 1982-04-23 1982-04-23 Absorption type heat pump device

Publications (2)

Publication Number Publication Date
JPS58187765A true JPS58187765A (en) 1983-11-02
JPH0321827B2 JPH0321827B2 (en) 1991-03-25

Family

ID=13392767

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6909782A Granted JPS58187765A (en) 1982-04-23 1982-04-23 Absorption type heat pump device

Country Status (1)

Country Link
JP (1) JPS58187765A (en)

Also Published As

Publication number Publication date
JPH0321827B2 (en) 1991-03-25

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