JPS6311582B2 - - Google Patents

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Publication number
JPS6311582B2
JPS6311582B2 JP6909982A JP6909982A JPS6311582B2 JP S6311582 B2 JPS6311582 B2 JP S6311582B2 JP 6909982 A JP6909982 A JP 6909982A JP 6909982 A JP6909982 A JP 6909982A JP S6311582 B2 JPS6311582 B2 JP S6311582B2
Authority
JP
Japan
Prior art keywords
heat
hot water
heat exchanger
storage tank
water storage
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
Application number
JP6909982A
Other languages
Japanese (ja)
Other versions
JPS58187767A (en
Inventor
Minoru Tagashira
Hozumi Yamada
Nobuhiko Wakamatsu
Isao Takeshita
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

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  • Sorption Type Refrigeration Machines (AREA)

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
なものがあつた。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。三方弁6の口6aか
ら入つた液冷媒は口6cより三方弁7の口7aに
入り7cに出、膨張弁8で減圧され熱交換器9で
蒸発し、フアン18により空気から蒸発熱を奪い
冷房が行なわれる。
Refrigerant gas generated from the concentrated liquid heated by the burner 17 in the generator 1 passes through the pipe 2 and enters the four-way valve 3.
The refrigerant gas enters the condensing heat heat exchanger 5 from the pipe 4 through the solid line portion and exchanges heat with the water supply in the hot water storage tank 30, and is condensed to become a high-pressure liquid refrigerant. The liquid refrigerant that enters from the port 6a of the three-way valve 6 enters the port 7a of the three-way valve 7 from the port 6c and exits to 7c, is depressurized by the expansion valve 8, evaporates in the heat exchanger 9, and removes heat of evaporation from the air by the fan 18. Cooling is performed.

蒸発した低圧冷媒ガスは、管路10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 10 and the solid line portion of the four-way valve 3, and enters the mixer 12 from the pipe 11.

一方、発生器1で冷媒ガスのうすくなつた希液
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
ガスを吸収し終つた濃液は、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1
4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り循環ポンプ22に
より管路21を通り貯湯槽30内の熱交換器23
に入り、貯湯槽30内で給水と熱交換した後三方
弁24の口24aから入り、口24cに出、管路
25を通り吸収器14に入る。給湯口29を開け
給湯すると、給水管28から市水が貯湯槽30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29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. After absorbing the refrigerant gas in the absorber 14, the concentrated liquid is sent to the generator 1 through a pipe 15 by a solution pump 16. Absorber 1
The absorbed heat generated in the hot water tank 4 is transferred to a cooling heat medium (for example, antifreeze liquid, etc.) and becomes hot water, which is passed through the pipe line 21 by the circulation pump 22 to the heat exchanger 23 in the hot water storage tank 30.
After exchanging heat with the supplied water in the hot water storage tank 30, it enters through the port 24a of the three-way valve 24, exits through the port 24c, passes through the pipe 25, 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 30 from the water supply pipe 28, is heated by natural convection by the condensing heat heat exchanger 5 and the heat exchanger 23, and is supplied from the hot water supply port 29.

貯湯槽30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、フアン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、フアン20により
凝縮熱を放熱する。
When the temperature inside the hot water storage tank 30 rises sufficiently, it becomes difficult to exchange heat by natural convection between the condensing heat heat exchanger 5 in the hot water storage tank 30 and the heat exchanger 23, 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 air-cooled heat exchanger 19 and fan 20 radiate condensation heat.

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
りフアン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に入りフアン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の口7bより口7a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 and the high-temperature, high-pressure refrigerant gas generated by the generator 1 passes through the pipe 2 to the four-way valve 3.
It passes through the broken line part and enters the heat exchanger 9 from the conduit 10, and the condensed heat is radiated by the fan 18 for heating. The heat of condensation is radiated to become a high-pressure liquid refrigerant, which is depressurized through the expansion valve 8 and enters the air-cooled heat exchanger 19 into the fan 20.
It absorbs heat from the outside air and evaporates, becoming a low-pressure refrigerant gas. Thereafter, it passes through the port 7b and 7a of the three-way valve 7, exits from the port 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30内に吸収器14
の冷却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5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
は既にあつた。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5と熱交換器23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30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5、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。従つて加熱源温度
まで上昇させるためには時間がかかる。貯湯槽3
0内の水温が充分上昇していない時に給湯される
と冷たい給湯となつてしまう等の問題がある。
As explained above, the absorber 14 is installed in the hot water storage tank 30.
A heat exchanger 23 is provided for exchanging heat with a cooling medium, and a condenser heat exchanger 5 is provided below the heat exchanger 23, and the water in the hot water storage tank 30 is heated by natural convection, and city water is supplied from the water supply pipe 28 to supply hot water. The hot water supplied from port 29 was already hot. However, the water in the hot water storage tank 30 is heated by two units, the condensing heat heat exchanger 5 and the heat exchanger 23, and the heat exchanger 23 is heated by natural convection, so the heat transfer coefficient is poor and the water supply temperature in the hot water storage tank 30 is It takes time for the temperature to rise, and when the water temperature in the hot water storage tank 30 rises, the temperature difference between the condensing heat heat exchanger 5 and the heat exchanger 23 decreases, and the amount of heat exchange decreases. Therefore, it takes time to raise the heating source temperature. Hot water tank 3
If hot water is supplied when the water temperature in the tank 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。なお、第1図と共通する素子には同一番号を
付し重複する部分の説明を省略する。
The present invention will be explained below based on FIG. 2 of the embodiment. Note that elements common to those in FIG. 1 are given the same numbers, and explanations of overlapping parts will be omitted.

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5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
つた液冷媒は口6cより三方弁7の口7aに入り
7cに出、膨張弁8で減圧され熱交換器9で蒸発
し、フアン18により空気から蒸発熱をうばい冷
房が行なわれる。
Refrigerant gas generated from the concentrated liquid heated by the burner 17 in the generator 1 passes through the pipe 2 and enters the four-way valve 3.
It passes through the solid line part and enters the second condensation heat heat exchanger 31 composed of the pipe line 4. The refrigerant gas that has exchanged heat with the water supply in the double-pipe heat exchanger 31 enters the condensation heat heat exchanger 5 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 enters from the port 6a of the three-way valve 6 enters the port 7a of the three-way valve 7 from the port 6c and exits to 7c, is depressurized by the expansion valve 8, evaporates in the heat exchanger 9, and removes the heat of evaporation from the air by the fan 18. Cooling is performed.

蒸発した低圧冷媒ガスは、管路10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つた希液
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
ガスを吸収し終つた濃液は、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1
4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21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30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24
aから口24cに出、管路25を通り吸収器14
に入る。給湯口29を開け給湯すると、給水管2
8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30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 evaporated low-pressure refrigerant gas passes through the pipe 10 and the solid line portion of the four-way valve 3, and enters the mixer 12 from the pipe 11. On the other hand, the diluted refrigerant gas in the generator 1 passes through a pipe 13 and enters a mixer 12, where it is mixed with refrigerant gas and enters an absorber 14. After absorbing the refrigerant gas in the absorber 14, the concentrated liquid is sent to the generator 1 through a pipe 15 by a solution pump 16. Absorber 1
The absorbed heat generated in the hot water storage tank 30 is transferred to a heat medium (for example, antifreeze, etc.) and becomes hot water. Enters the exchanger 23,
After heat exchange in the hot water storage tank 30, the opening 24 of the three-way valve 24
a to the port 24c and passes through the pipe 25 to the absorber 14.
to go into. When the hot water supply port 29 is opened and hot water is supplied, the water supply pipe 2
City water enters the second heat exchanger 31 for condensing heat from 8 and exchanges heat with the internal high-temperature, high-pressure refrigerant gas in a counterflow by forced circulation, and the heated supply water enters the hot water storage tank 30 for heat exchange for condensing heat. It is heated by natural convection by the container 5 and the heat exchanger 23. 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30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、フアン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、フアン20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 storage tank 30 rises sufficiently, it becomes difficult to exchange heat by natural convection between the condensing heat heat exchanger 5 in the hot water storage tank 30 and the heat exchanger 23, 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 air-cooled heat exchanger 19 and fan 20 radiate condensation heat. However, even if it is only a little, the hot water supply port 29
When the hot water tank is opened and hot water is supplied, the hot water is further heated in the second absorption heat heat exchanger 32 and the second condensation heat heat exchanger 31 even though there is almost no heat exchange in the hot water storage tank 30. is 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に入りフアン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に入りフアン20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の口7bより口7aを通り三方弁6の口6
c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。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。
During heating, the four-way valve 3 operates and the high-temperature, high-pressure refrigerant gas generated by the generator 1 passes through the pipe 2 to the four-way valve 3.
It passes through the broken line part and enters the heat exchanger 9 and enters the fan 18.
The condensed heat is radiated to provide space for heating. 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 through a fan 20, and evaporates to become a low-pressure refrigerant gas. After that, it passes from the port 7b of the three-way valve 7 to the port 7a, and the port 6 of the three-way valve 6
It exits from c to 6b, passes through conduit 4, passes through the broken line of four-way valve 3, and enters mixer 12 through 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31,32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つてもよい。
In the above embodiment, the dual heat exchangers 31 and 32 are provided outside the hot water storage tank 30, but they 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温より高い給湯が得られ
る。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・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。
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 counterflow caused by forced circulation inside the tank, resulting in hot water that is higher in temperature than the hot water in the hot water storage tank. 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 and condensation heat of the absorption heat pump device can be effectively used to produce hot water at a higher temperature.

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

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、5……凝縮熱用熱交換器、14
……吸収器、16……溶液ポンプ、23……吸収
熱用熱交換器、28……給水管、29……給湯
口、30……貯湯槽、31……第2凝縮熱用熱交
換器、32……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, 5... Heat exchanger for condensing heat, 14
...absorber, 16 ... solution pump, 23 ... heat exchanger for absorption heat, 28 ... water supply pipe, 29 ... hot water supply port, 30 ... hot water storage tank, 31 ... heat exchanger for second condensation heat , 32... second heat exchanger for absorption heat.

Claims (1)

【特許請求の範囲】[Claims] 1 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
側に位置させた凝縮熱用熱交換器を設け、前記吸
収熱用熱交換器と直列に接続し前記吸収器の貯湯
槽から出た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。
1. An absorption heat heat exchanger for exchanging heat with the cooling heat medium of the absorber in a hot water storage tank provided with a city water inlet and a hot water outlet, and a heat exchanger located on the inlet side of the absorption heat heat exchanger. a second absorption heat heat exchanger connected in series with the absorption heat heat exchanger to exchange heat with hot water discharged from the hot water storage tank of the absorber; and the condensation heat heat exchanger. An absorption heat pump cooling/heating hot water system that includes at least one of a second condensing heat heat exchanger that is connected in series with the 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 JPS58187767A (en) 1983-11-02
JPS6311582B2 true 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)

Families Citing this family (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
JPS58187767A (en) 1983-11-02

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