JPS58187767A - Absorption type heat pump air-conditioning hot-water supply system - Google Patents

Absorption type heat pump air-conditioning hot-water supply system

Info

Publication number
JPS58187767A
JPS58187767A JP6909982A JP6909982A JPS58187767A JP S58187767 A JPS58187767 A JP S58187767A JP 6909982 A JP6909982 A JP 6909982A JP 6909982 A JP6909982 A JP 6909982A JP S58187767 A JPS58187767 A JP S58187767A
Authority
JP
Japan
Prior art keywords
heat
hot water
heat exchanger
storage tank
water supply
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
JP6909982A
Other languages
Japanese (ja)
Other versions
JPS6311582B2 (en
Inventor
実 田頭
山田 穂積
若松 伸彦
功 竹下
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 JP6909982A priority Critical patent/JPS58187767A/en
Publication of JPS58187767A publication Critical patent/JPS58187767A/en
Publication of JPS6311582B2 publication Critical patent/JPS6311582B2/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、吸収式ヒートポンプ冷暖給湯システムに関す
る。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an absorption heat pump cooling/heating hot water supply system.

従来、この種装置としては、第1図に示すようなものが
あった。第1図について説明する。
Conventionally, there has been a device of this type as shown in FIG. FIG. 1 will be explained.

発生器1内でバーナ17により加熱された濃液から発生
した冷媒ガスは、管路2を通り四方弁3の実線部を通り
管路4から凝縮熱用熱交換器5に入り貯湯槽30内の給
水と熱交換した冷媒ガスは凝縮し高圧の液冷媒となる。
The refrigerant gas generated from the concentrated liquid heated by the burner 17 in the generator 1 passes through the pipe 2, passes through the solid line part of the four-way valve 3, enters the condensation heat heat exchanger 5 from the pipe 4, and enters the hot water storage tank 30. The refrigerant gas that exchanged heat with the supplied water condenses and becomes a high-pressure liquid refrigerant.

三方弁60口6aから入った液冷媒は口6cよシ三方弁
7のロアaに入り7Cに出、膨張弁8で減圧され熱交換
器9で蒸発し、ファン18により空気から蒸発熱を奪い
冷房が行なわれる。
The liquid refrigerant entering from the port 6a of the three-way valve 60 enters the lower a of the three-way valve 7 through the port 6c and exits to 7C, is depressurized by the expansion valve 8, evaporates in the heat exchanger 9, and removes evaporation heat from the air by the fan 18. Cooling is performed.

蒸発した低圧冷媒ガスは、管路1oを通り四方弁3の実
線部を通り管路11から混合器12に入る。
The evaporated low-pressure refrigerant gas passes through the pipe line 1o, passes through the solid line portion of the four-way valve 3, and enters the mixer 12 from the pipe line 11.

一方、発生器1で冷媒ガスのうすくなった希液は、管路
13を通り混合器12に入り冷媒ガスと混合され吸収器
14に入る。吸収器14内で冷媒ガスを吸収し終った濃
液は、管路15を通り溶液ポンプ16により発生器1に
送られる。吸収器14内で発生する吸収熱は、冷却熱媒
体(例えば不凍液等)に伝えられ温水となシ循環ポンプ
22により管路21を通り貯湯槽3o内の熱交換器23
に入り、貯湯槽30内で給水ど熱交換した後三方弁24
の口24aから入り、口24cに出、管路26を通り吸
収器14に入る。給湯口29を開は給湯すると、給水管
28から市水が貯湯槽3o内に入り凝縮熱用熱交換器5
と熱交換器23とにより自然対流で加熱され、給湯口2
9から給湯される。
On the other hand, the diluted refrigerant gas in the generator 1 enters the mixer 12 through the pipe line 13, is mixed with the refrigerant gas, and enters the absorber 14. The concentrated liquid that has absorbed the refrigerant gas in the absorber 14 is sent to the generator 1 through a pipe 15 by a solution pump 16. The absorbed heat generated in the absorber 14 is transferred to a cooling heat medium (for example, antifreeze, etc.) and converted into hot water.
After entering the hot water storage tank 30 and exchanging heat with the water, the three-way valve 24
The water enters from the port 24a, exits from the port 24c, passes through the pipe line 26, and enters the absorber 14. When the hot water supply port 29 is opened to supply hot water, city water enters the hot water storage tank 3o from the water supply pipe 28 and enters the condensing heat heat exchanger 5.
The hot water is heated by natural convection by the heat exchanger 23 and the hot water supply port 2.
Hot water is supplied from 9 onwards.

貯湯槽3o内が充分昇温されると貯湯槽30内の凝縮熱
用熱交換器6と熱交換器23とでの自然対流による熱交
換が行なわれにくくなるので三方弁24が動作し空冷熱
交換器26、ファ/27により吸収器14の吸収熱を放
熱する。また三方弁7が動作し空冷熱交換器19、ファ
ン2oにより凝縮熱を放熱する。
When the temperature inside the hot water storage tank 3o rises sufficiently, it becomes difficult to exchange heat by natural convection between the condensation heat heat exchanger 6 and the heat exchanger 23 in the hot water storage tank 30, so the three-way valve 24 operates and the air-cooled heat is transferred. The heat absorbed by the absorber 14 is radiated by the exchanger 26 and the F/27. In addition, the three-way valve 7 operates, and the condensation heat is radiated by the air-cooled heat exchanger 19 and fan 2o.

暖房時は、四方弁3が動作し発生器1で発生した高温・
高圧の冷媒ガスは管路2を通り四方弁3の破線部を通過
して管路10より熱交換器9に入りファン18により凝
縮熱を放熱し暖房する。凝縮熱を放熱し高圧液冷媒とな
り、膨張弁8を通り減圧され、空冷の熱交換器19に入
りファン20により外気から吸熱し蒸発し低圧の冷媒ガ
ス、となる。その後三方弁7のロアbよりロアdを通り
三方弁6の口6Cから6bに出て、管路4を通り四方弁
3の破線を通り、管路11から混合器12に入る。溶液
の循環は冷房時と同じである。吸収器14内で発生する
吸収熱は、冷房時と同じく熱交換器23で貯湯槽30内
の給水を加熱する。
During heating, the four-way valve 3 operates to remove the high temperature and heat generated by the generator 1.
The high-pressure refrigerant gas passes through the conduit 2, passes through the broken line portion of the four-way valve 3, enters the heat exchanger 9 through the conduit 10, and radiates condensed heat by the fan 18, thereby heating the room. The heat of condensation is radiated to become a high-pressure liquid refrigerant, which is depressurized through an expansion valve 8, enters an air-cooled heat exchanger 19, absorbs heat from the outside air by a fan 20, and evaporates to become a low-pressure refrigerant gas. Thereafter, it passes through the lower b and lower d of the three-way valve 7, exits from the mouth 6C of the three-way valve 6 to 6b, passes through the conduit 4, passes through the broken line of the four-way valve 3, and enters the mixer 12 through the conduit 11. The circulation of the solution is the same as during cooling. The absorbed heat generated in the absorber 14 heats the water supplied in the hot water storage tank 30 in the heat exchanger 23, as in the case of cooling.

以上説明したように貯湯槽3o内に吸収器14の冷却熱
媒体と熱交換するための熱交換器23を設け、その下層
に凝縮器熱交換器6を設け、貯湯槽30内の水を自然対
流により加熱し給水管28から市水を給水し給湯口29
から給湯しているものは既にあった。しかし貯湯槽30
内の水を加熱するのは凝縮熱用熱交換器6と熱交換器2
3の2個で、自然対流により加熱しているため、熱伝達
率が悪く貯湯槽3o内の給水温の上昇に時間がかかり、
また貯湯槽30内の水温が上昇すると、凝縮熱用熱交換
器6.熱交換器23との温度差が少なくなり、熱交換量
が低下する。従って加熱源温度まで上昇させるためには
時間がかかる。貯湯槽30内の水温が充分上昇してない
時に給湯、されると冷たい給湯となってしまう等の問題
がある。
As explained above, the heat exchanger 23 for exchanging heat with the cooling heat medium of the absorber 14 is provided in the hot water storage tank 3o, and the condenser heat exchanger 6 is provided in the lower layer of the heat exchanger 23, so that the water in the hot water storage tank 30 is naturally drained. City water is heated by convection and supplied from the water supply pipe 28 to the hot water supply port 29
There were already some that were supplying hot water from. However, the hot water tank 30
Heat exchanger 6 for condensing heat and heat exchanger 2 heat the water inside.
3, heating is done by natural convection, so the heat transfer rate is poor and it takes time for the temperature of the water supply in the hot water storage tank 3o to rise.
Further, when the water temperature in the hot water storage tank 30 rises, the condensing heat heat exchanger 6. The temperature difference with the heat exchanger 23 decreases, and the amount of heat exchange decreases. Therefore, it takes time to raise the temperature to the heating source temperature. If hot water is supplied when the water temperature in the hot water storage tank 30 has not risen sufficiently, there are problems such as cold water being supplied.

本発明は上記従来技術における問題点を解消したもので
、貯湯槽30内の給水温が充分上昇していなくても給湯
温度が貯湯槽30内の温度より高い給湯が得られ、また
給湯すれば、熱交換量も増加し給湯をより良くするもの
である。
The present invention solves the above-mentioned problems in the conventional technology, and even if the temperature of the supplied water in the hot water storage tank 30 has not risen sufficiently, hot water can be obtained whose temperature is higher than the temperature in the hot water storage tank 30, and when hot water is supplied, This increases the amount of heat exchange and improves hot water supply.

以下本発明を実施例第2図に基づいて説明するっ発生器
1内でバーナ17により加熱された濃液から発生した冷
媒ガスは、管路2を通9四方弁3の実線部を通り管路4
から構成される第2凝縮熱用熱交換器31に入る。2重
管熱交換器31内の給水と熱交換した冷媒ガスは貯湯槽
30内の凝縮熱用熱交換器6に入り周辺の給水と熱交換
し凝縮し高圧の液冷媒となる。三方弁6の口6aから入
った液冷媒は口6Cよりヰ方弁7のロアaに入り7Cに
出、膨張弁8で減圧され熱交換器9で蒸発し、ファン1
8により空気から蒸発熱をうばい冷房が行なわれる。
The present invention will be described below with reference to FIG. 2. Refrigerant gas generated from a concentrated liquid heated by a burner 17 in a generator 1 passes through a conduit 2 through a solid line portion of a four-way valve 3 and into a pipe. Road 4
The condensation heat enters the second condensation heat heat exchanger 31 composed of. The refrigerant gas that has exchanged heat with the water supply in the double-pipe heat exchanger 31 enters the condensation heat heat exchanger 6 in the hot water storage tank 30, exchanges heat with the surrounding water supply, and condenses to become a high-pressure liquid refrigerant. The liquid refrigerant that entered from the port 6a of the three-way valve 6 enters the lower a of the one-way valve 7 from the port 6C and exits to 7C.
8, cooling is performed by extracting heat of evaporation from the air.

蒸発した低圧冷媒ガスは、管路1oを通り四方弁3の実
線部を通り管路11から混合器12に入る。一方発生器
1で冷媒ガスのうすくなった栢液は、管路13を通り混
合器12に入り冷媒ガスと混合され吸収器14に入る。
The evaporated low-pressure refrigerant gas passes through the pipe line 1o, passes through the solid line portion of the four-way valve 3, and enters the mixer 12 from the pipe line 11. On the other hand, the drying liquid in which the refrigerant gas has been diluted in the generator 1 passes through the pipe 13 and enters the mixer 12, where it is mixed with the refrigerant gas and enters the absorber 14.

吸収器14内で冷媒ガスを吸収し終った濃液は、管路1
5を通り溶液ポンプ16により発生器1に送られる。吸
収器14内で発生する吸収熱は、熱媒体(例えば不凍液
等)に伝えられ温水となり循環ポンプ22により管路2
1を通り構成される第2吸収熱用熱交換器32を通り貯
湯槽3o内の熱交換器23に入り、貯湯槽30内で熱交
換した後三方弁24の口24aから口24cに出、管路
26を通り吸収器14に入る。給湯口29を開は給湯す
ると、給水管28から市水が第2凝縮熱用熱交換器31
に入り内部の高温高圧冷媒ガスと強制循環による対向流
で熱交換を行ない昇温された給水が貯湯槽3o内に入り
凝縮熱用熱交換器5と熱交換器23とにより自然対流で
加熱される。貯湯槽30から・出た給湯は第2凝縮熱用
熱交換器32を通過する時、強制循環による対向流熱交
換でさらに加熱され給湯口29から給湯される。
The concentrated liquid that has absorbed the refrigerant gas in the absorber 14 is transferred to the pipe 1.
5 and is sent to the generator 1 by a solution pump 16. The absorbed heat generated in the absorber 14 is transferred to a heat medium (for example, antifreeze, etc.) and becomes hot water, which is transferred to the pipe line 2 by the circulation pump 22.
1, enters the heat exchanger 23 in the hot water storage tank 3o through the second absorption heat heat exchanger 32, and after exchanging heat in the hot water storage tank 30, exits from the port 24a of the three-way valve 24 to the port 24c, It passes through line 26 and enters absorber 14 . When the hot water supply port 29 is opened to supply hot water, city water flows from the water supply pipe 28 to the second condensing heat heat exchanger 31.
The supplied water enters the hot water storage tank 3o, where it exchanges heat with the internal high-temperature, high-pressure refrigerant gas in counterflow through forced circulation, and the heated water enters the hot water storage tank 3o, where it is heated by natural convection by the condensing heat heat exchanger 5 and the heat exchanger 23. Ru. When the hot water discharged from the hot water storage tank 30 passes through the second condensing heat heat exchanger 32, it is further heated by counterflow heat exchange by forced circulation and is supplied from the hot water supply port 29.

貯湯槽3o内が充分昇温されると貯湯槽30内の凝縮熱
用熱交換器5と熱交換器23とでの自然対流による熱交
換が行なわれにくくなるので三方弁24が動作し空冷熱
交換器26、ファン27により吸収器14の吸収熱を放
熱する。また三方弁7が動作し空冷熱交換器19、ファ
ン2oにより凝縮熱を放熱する。しかしわずかでも給湯
口29を開き給湯されると、貯湯槽30内ではほとんど
熱交換されなくても第2吸収熱用熱交換器32および第
2凝縮熱用熱交換器31で給湯水は、さらに加熱され、
また市水は予熱される。
When the temperature inside the hot water tank 3o rises sufficiently, it becomes difficult to exchange heat by natural convection between the condensing heat heat exchanger 5 and the heat exchanger 23 in the hot water storage tank 30, so the three-way valve 24 operates and the air-cooled heat is transferred. The heat absorbed by the absorber 14 is radiated by the exchanger 26 and the fan 27. In addition, the three-way valve 7 operates, and the condensation heat is radiated by the air-cooled heat exchanger 19 and fan 2o. However, if the hot water supply port 29 is opened even slightly and hot water is supplied, even if there is almost no heat exchange in the hot water storage tank 30, the hot water is further heated in the second absorption heat heat exchanger 32 and the second condensation heat heat exchanger 31. heated,
City water is also preheated.

暖房時は、四方弁3が動作し発生器1で発生した高温・
高圧の冷媒ガスは管路2を通り四方弁3の破線部を通過
して熱交換器9に入りファン18によシ凝縮熱を放熱し
暖房する。凝縮熱を放熱し高圧液冷媒となり、膨張弁8
を通り減圧され、空冷の熱交換器19に入りファン2o
により外気から吸熱し、蒸発し低圧の冷媒ガスとなる。
During heating, the four-way valve 3 operates to remove the high temperature and heat generated by the generator 1.
The high-pressure refrigerant gas passes through the conduit 2, passes through the broken line portion of the four-way valve 3, enters the heat exchanger 9, and radiates condensed heat through the fan 18 to provide space heating. The heat of condensation is radiated and becomes a high-pressure liquid refrigerant, and the expansion valve 8
The pressure is reduced through the air-cooled heat exchanger 19, and the fan 2o
It absorbs heat from the outside air and evaporates, becoming a low-pressure refrigerant gas.

その後三方弁Tのロアbよりロアaを通り三方弁6の口
線を通り、管路11から混合器12に入る。溶液の循環
は冷房時と同じである。吸収器14内で発生する吸収熱
は、冷房時と同じく熱交換器23で貯湯槽30内の給水
を加熱する。また貯湯槽30から出る給湯水は、第2吸
収熱用熱交換器32でさらに加熱され給湯口29から給
湯される。
Thereafter, it passes through the lower part b of the three-way valve T, passes through the mouth line of the three-way valve 6, and enters the mixer 12 through the conduit 11. The circulation of the solution is the same as during cooling. The absorbed heat generated in the absorber 14 heats the water supplied in the hot water storage tank 30 in the heat exchanger 23, as in the case of cooling. In addition, the hot water coming out of the hot water storage tank 30 is further heated by the second absorption heat exchanger 32 and then supplied from the hot water supply port 29 .

なお、上記実施例においては、貯湯槽30外に2重熱交
換器3.1.32を設けているが、貯湯槽内に設けても
よい。また2重管熱交換器はこの形式にこだわらず他の
形式のものであってもよい。
In the above embodiment, the dual heat exchanger 3.1.32 is provided outside the hot water storage tank 30, but it may be provided inside the hot water storage tank. Further, the double tube heat exchanger is not limited to this type, and may be of other types.

以上のように本発明においては、貯湯槽内に凝縮熱を伝
える熱交換器と吸収熱を伝える熱交換器を設け、それ以
外に前記貯湯槽の出入経路の少なくとも何れか一方に前
記熱交換器と直列に接続した熱交換器を形成しているの
で貯湯槽内の給水が充分昇温されていなくても直列接続
した熱交換器を給湯水が通過することにより第2吸収熱
用熱交換器内部での強制循環による対向流で熱交換が促
進され貯湯槽内の給湯源より高い給湯が得られる。
As described above, in the present invention, a heat exchanger for transmitting condensation heat and a heat exchanger for transmitting absorption heat are provided in the hot water storage tank, and the heat exchanger is provided in at least one of the inlet and output routes of the hot water storage tank. Since the heat exchanger is connected in series with the heat exchanger, even if the temperature of the water supply in the hot water storage tank is not sufficiently raised, the hot water can pass through the heat exchanger connected in series, and the second absorption heat heat exchanger will be activated. Heat exchange is promoted by countercurrent flow due to internal forced circulation, resulting in higher hot water supply than from a hot water source in a hot water storage tank.

また給水側も給湯側と同じように、給水管より市水が第
2凝縮熱用熱交換器31を通過することにより凝縮熱を
もらい昇温し貯湯槽内に入る。すなわち、給湯回路に瞬
間湯沸的な要素を持たせることにより、吸収式ヒートポ
ンプ装置の吸収熱O凝縮熱を有効に利用しより高温の給
湯が得られる等の効果を奏するものである。
Similarly to the hot water supply side, on the water supply side, city water from the water supply pipe passes through the second condensation heat heat exchanger 31, receives condensation heat, raises the temperature, and enters the hot water storage tank. That is, by providing the hot water supply circuit with an instantaneous water boiling element, the absorption heat O condensation heat of the absorption heat pump device can be effectively utilized to provide hot water at a higher temperature.

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

第1図は従来の一実施例の吸収式ヒートポンプ冷暖給湯
システムの一例を示す図、第2図は本発明の一実施例の
吸収式ヒートポンプ冷暖給湯システムの一実施例を示す
図である。 1 、、、、、、発生器、6・・・・・・凝縮熱用熱交
換器、14 、、、、、、吸収器、16 、、、、、、
溶液ポンプ、2381110.吸収熱用熱交換器、2 
B 、、、、、、給水管、29・・・・・・給湯口−%
30・・・・・・貯湯槽131・・・・・・・・・第2
凝縮熱用熱交換器132・・・・・・第2吸収熱用熱交
換器。
FIG. 1 is a diagram showing an example of a conventional absorption type heat pump cooling/heating hot water supply system, and FIG. 2 is a diagram showing an example of an absorption type heat pump cooling/heating hot water supply system according to an embodiment of the present invention. 1. Generator, 6. Heat exchanger for condensing heat, 14. Absorber, 16.
Solution pump, 2381110. Heat exchanger for absorption heat, 2
B , , , , Water supply pipe, 29...Hot water inlet -%
30...Hot water tank 131...2nd
Condensation heat heat exchanger 132...Second absorption heat heat exchanger.

Claims (1)

【特許請求の範囲】[Claims] 市水の入口と湯水の出口を設けた貯湯槽内に吸収器の冷
却熱媒体と熱交換するための吸収熱用熱交換器と前記吸
収熱用熱交換器よりも前記入口側湯水と熱交換する第2
吸収熱用熱交換器と前記凝縮熱用熱交換器と直列接続し
前記貯湯槽へ入る水と熱交換する第2凝縮熱用熱交換器
の少なくとも一方を付加した吸収式ヒートポンプ冷暖給
湯システム。
An absorption heat heat exchanger for exchanging heat with the cooling heat medium of the absorber in a hot water storage tank having an inlet for city water and an outlet for hot water; and an absorption heat heat exchanger for exchanging heat with the hot water on the inlet side of the absorption heat heat exchanger. Second to do
An absorption heat pump cooling/heating hot water system that includes at least one of an absorption heat heat exchanger and a second condensation heat heat exchanger that is connected in series with the condensation heat heat exchanger and exchanges heat with water entering the hot water storage tank.
JP6909982A 1982-04-23 1982-04-23 Absorption type heat pump air-conditioning hot-water supply system Granted JPS58187767A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6909982A JPS58187767A (en) 1982-04-23 1982-04-23 Absorption type heat pump air-conditioning hot-water supply system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6909982A JPS58187767A (en) 1982-04-23 1982-04-23 Absorption type heat pump air-conditioning hot-water supply system

Publications (2)

Publication Number Publication Date
JPS58187767A true JPS58187767A (en) 1983-11-02
JPS6311582B2 JPS6311582B2 (en) 1988-03-15

Family

ID=13392833

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6909982A Granted JPS58187767A (en) 1982-04-23 1982-04-23 Absorption type heat pump air-conditioning hot-water supply system

Country Status (1)

Country Link
JP (1) JPS58187767A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6245647U (en) * 1985-09-07 1987-03-19

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6245647U (en) * 1985-09-07 1987-03-19

Also Published As

Publication number Publication date
JPS6311582B2 (en) 1988-03-15

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