JPS6315049A - Absorption heat pump type heat accumulator - Google Patents
Absorption heat pump type heat accumulatorInfo
- Publication number
- JPS6315049A JPS6315049A JP15943086A JP15943086A JPS6315049A JP S6315049 A JPS6315049 A JP S6315049A JP 15943086 A JP15943086 A JP 15943086A JP 15943086 A JP15943086 A JP 15943086A JP S6315049 A JPS6315049 A JP S6315049A
- Authority
- JP
- Japan
- Prior art keywords
- heat
- chamber
- absorption
- refrigerant
- pump
- 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
Links
- 238000010521 absorption reaction Methods 0.000 title claims description 32
- 238000005338 heat storage Methods 0.000 claims description 24
- 239000007788 liquid Substances 0.000 claims description 24
- 238000001704 evaporation Methods 0.000 claims description 13
- 230000008020 evaporation Effects 0.000 claims description 12
- 230000008929 regeneration Effects 0.000 claims description 11
- 238000011069 regeneration method Methods 0.000 claims description 11
- 238000009833 condensation Methods 0.000 claims description 9
- 230000005494 condensation Effects 0.000 claims description 9
- 239000003507 refrigerant Substances 0.000 description 37
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 30
- 238000010438 heat treatment Methods 0.000 description 16
- 238000004891 communication Methods 0.000 description 12
- 238000001816 cooling Methods 0.000 description 11
- 238000005507 spraying Methods 0.000 description 7
- 238000005192 partition Methods 0.000 description 5
- 238000007906 compression Methods 0.000 description 3
- 230000006835 compression Effects 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 238000004378 air conditioning Methods 0.000 description 2
- 230000003247 decreasing effect Effects 0.000 description 2
- 239000006185 dispersion Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000001965 increasing effect Effects 0.000 description 2
- 230000005855 radiation Effects 0.000 description 2
- 239000007921 spray Substances 0.000 description 2
- 239000002250 absorbent Substances 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- PXBRQCKWGAHEHS-UHFFFAOYSA-N dichlorodifluoromethane Chemical compound FC(F)(Cl)Cl PXBRQCKWGAHEHS-UHFFFAOYSA-N 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 230000003028 elevating effect Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- IPLONMMJNGTUAI-UHFFFAOYSA-M lithium;bromide;hydrate Chemical compound [Li+].O.[Br-] IPLONMMJNGTUAI-UHFFFAOYSA-M 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 125000006850 spacer group Chemical group 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Landscapes
- Sorption Type Refrigeration Machines (AREA)
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】
産業上の利用分野
本発明は、吸収ヒートポンプを利用した蓄熱装置に関す
るものである。DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to a heat storage device using an absorption heat pump.
従来の技術
従来の暖房等の昇温時と冷房等の降温時との兼用の蓄熱
装置として、水の顕熱を利用する方式が知られている。2. Description of the Related Art Conventionally, a method is known in which the sensible heat of water is utilized as a heat storage device that can be used both for heating purposes such as heating and for cooling purposes and decreasing temperatures.
また最近氷蓄熱、リキッドアイス蓄熱などが開発されて
いる。Recently, ice heat storage, liquid ice heat storage, etc. have been developed.
発明が解決しようとする問題点
上記のごとく、従来の昇温、降温兼用蓄熱装置は水の顕
熱を利用しているため、実用的には据付容量を極めて大
きくする必要があり、設備費等が増大する。また氷蓄熱
、リキッドアイス蓄熱は氷の潜熱を利用しているが、昇
温用蓄熱はできない。Problems to be Solved by the Invention As mentioned above, the conventional heat storage device for heating and cooling uses the sensible heat of water, so in practice it is necessary to have an extremely large installation capacity, which reduces equipment costs, etc. increases. In addition, ice heat storage and liquid ice heat storage utilize the latent heat of ice, but they cannot be used to store heat for heating purposes.
本発明は、吸収ヒートポンプを利用した、非常に小型化
できる昇温、降温兼用蓄熱装置を提供しようとするもの
である。The present invention aims to provide a heat storage device that uses an absorption heat pump and can be extremely miniaturized for both heating and cooling.
問題点を解決するための手段
本発明の吸収ヒートポンプ式蓄熱装置は、外部の熱源と
熱交換した液体と真空条件下で熱交換する、再生兼吸収
室と凝縮兼蒸発室とを備えた吸収ヒートポンプの、前記
各室内の伝熱管と各外部熱源の熱交換器との間の熱伝達
用の液体の循環管路を切換弁を介して連通したことを特
徴とするものである。Means for Solving the Problems The absorption heat pump type heat storage device of the present invention is an absorption heat pump equipped with a regeneration/absorption chamber and a condensation/evaporation chamber that exchanges heat under vacuum conditions with a liquid that has exchanged heat with an external heat source. The heat exchanger tube in each of the chambers and the heat exchanger of each external heat source are characterized in that a circulation pipe for a heat transfer liquid is communicated through a switching valve.
作用
上記の構成において、熱伝達用液体の循環管路の切換弁
を切換えることにより、吸収ヒートポンプで蓄熱し、昇
温用、降温用に放熱することができる。すなわち、冷房
、暖房等の負荷のない時間帯における熱源あるいは温廃
液等と熱交換して昇温した熱伝達用の液体を、吸収ヒー
トポンプの再生兼吸収室内の伝熱管へ導いて、冷媒溶液
を加熱し、再生して蓄熱を行ない、凝縮兼蒸発室におい
て再生兼吸収室からの冷媒蒸気を凝縮し、その際の熱は
管路内を循環する熱伝達用の液体により外部へ放散する
。暖房等の昇温用に放熱する際は、凝縮兼蒸発室におい
て外部熱源(低温熱源)で熱交換した、管路内を循環す
る熱伝達用の液体により冷媒を加熱し、発生する蒸気を
再生兼吸収室へ導いて冷媒溶液に吸収させ、発生する熱
で管路内を循環する熱伝達用の液体を加熱し、昇降負荷
と熱交換させる。また冷房等の降温用に放熱する際は、
降温負荷で昇温しだ液体を、凝縮兼蒸発室において冷媒
の蒸発により吸熱して冷却し、降温負荷との間で循環さ
せ、蒸発した冷媒は再生兼吸収室で冷媒溶液に吸収させ
、発生する熱は管路を循環する熱伝達用の液体により外
部へ放熱する。Effect In the above configuration, by switching the switching valve of the circulation pipe for the heat transfer liquid, heat can be stored in the absorption heat pump and radiated for raising or lowering the temperature. In other words, the heat transfer liquid heated by exchanging heat with a heat source or heated waste liquid during times when there is no load such as cooling or heating is guided to the heat transfer tube in the regeneration/absorption chamber of the absorption heat pump, and the refrigerant solution is The refrigerant vapor from the regeneration and absorption chamber is condensed in the condensation and evaporation chamber, and the heat is dissipated to the outside by the heat transfer liquid circulating in the pipes. When dissipating heat for heating purposes such as heating, the refrigerant is heated by the heat transfer liquid circulating in the pipes, which has been exchanged with an external heat source (low-temperature heat source) in the condensation/evaporation chamber, and the generated vapor is regenerated. The heat is guided to the absorption chamber and absorbed by the refrigerant solution, and the generated heat heats the heat transfer liquid circulating in the pipes, which exchanges heat with the lifting load. Also, when dissipating heat for cooling etc.,
The liquid whose temperature rises due to the temperature-lowering load is cooled by absorbing heat through the evaporation of the refrigerant in the condensing/evaporation chamber, and then circulated between the temperature-lowering load and the evaporated refrigerant is absorbed into the refrigerant solution in the regeneration/absorption chamber. The heat generated is radiated to the outside by a heat transfer liquid that circulates through the pipes.
実施例 本発明の一実施例を図面に基づいて説明する。Example An embodiment of the present invention will be described based on the drawings.
第1図において、1は吸収ヒートポンプであり、本体2
は密閉構造からなり1本体内下部は冷媒溶液貯槽3とし
て冷媒溶液4が貯えられ、冷媒溶液4の上部空間は立設
した隔壁5により2分割され。In Fig. 1, 1 is an absorption heat pump, and the main body 2
has a sealed structure, and a refrigerant solution 4 is stored in the lower part of the main body as a refrigerant solution storage tank 3, and the upper space of the refrigerant solution 4 is divided into two by an upright partition wall 5.
前記隔ri5には蒸気流通孔6が設けられている。A steam communication hole 6 is provided in the spacer ri5.
なお前記冷媒溶液4の上部空間は、真空ポンプ7により
真空状態が保たれるようになっている。前記隔壁5によ
る分割で形成された第1室8および第2室9のうち、第
1室8内の上部に、冷媒溶液4を散布する散布装置10
を設けて、冷媒溶液貯槽3の下部との間に、溶液ポンプ
11を介して冷媒溶液循環管路が形成されている。また
第2室9内の上部に、冷媒12を散布する散布装置13
を設け、かつ下部に冷媒貯槽14を設けて、前記散布装
置13と冷媒貯槽14との間に冷媒ポンプ15を介して
冷媒循環管路が形成されている。さらに前記第1室8内
には、散布装置10と冷媒溶液4の液面との間に伝熱管
16が配設されている。この伝熱管16と、外部熱源と
熱を受授する熱交換器17どの間に、循環ポンプ18お
よび、外部負荷(L)への供給へラダ19、戻りへラダ
20を介して、熱伝達用液体の循環管路21が形成され
ている。また前記第2室9内には、散布装置13と冷媒
貯槽14との間に伝熱管22が配設されている。この伝
熱管22と、外部熱源と熱の受授をする熱交換器23と
の間に、循環ポンプ24を介して熱伝達用液体の循環管
路25が形成されている。Note that the space above the refrigerant solution 4 is kept in a vacuum state by a vacuum pump 7. A spraying device 10 that sprays the refrigerant solution 4 to the upper part of the first chamber 8 of the first chamber 8 and the second chamber 9 formed by the partition wall 5;
A refrigerant solution circulation pipe is formed between the refrigerant solution storage tank 3 and the lower part of the refrigerant solution storage tank 3 via a solution pump 11 . Further, a spraying device 13 that sprays the refrigerant 12 on the upper part of the second chamber 9
, and a refrigerant storage tank 14 is provided in the lower part, and a refrigerant circulation pipe is formed between the distribution device 13 and the refrigerant storage tank 14 via a refrigerant pump 15 . Further, in the first chamber 8, a heat transfer tube 16 is disposed between the spraying device 10 and the liquid level of the refrigerant solution 4. Between this heat exchanger tube 16 and a heat exchanger 17 that receives and receives heat from an external heat source, there is a circulation pump 18, a ladder 19 for supplying to the external load (L), and a ladder 20 for returning, for heat transfer. A liquid circulation pipe 21 is formed. Further, in the second chamber 9, a heat transfer tube 22 is disposed between the dispersion device 13 and the refrigerant storage tank 14. A circulation pipe 25 for a heat transfer liquid is formed via a circulation pump 24 between the heat transfer tube 22 and a heat exchanger 23 that receives and receives heat from an external heat source.
さらに循環管路21の循環ポンプ18のサクション側で
、第1室8内の伝熱管16との間に、循環ポンプ18側
から順に切換弁26.27.28が配設されている。Furthermore, switching valves 26, 27, and 28 are disposed in order from the circulation pump 18 side on the circulation pipe 21 on the suction side of the circulation pump 18 and between the circulation pipe 21 and the heat transfer tube 16 in the first chamber 8.
そして循環管路21に、切換弁26を介して外部負荷(
L)からの熱伝達用の液体の戻り管路29が連通され、
切換弁27と戻りヘッダ20との間に連通管3゜が設け
られ、切換弁28と循環管路25の循環ポンプ24のサ
クション側〔第2室9内の伝熱管22と熱交換器23と
の間〕に配設された切換弁31との間に、連通管32が
設けられている。また循環管路21の、伝熱管16とへ
ラダ19との間に切換弁33が配設され。Then, an external load (
A return line 29 of a liquid for heat transfer from L) is connected,
A communication pipe 3° is provided between the switching valve 27 and the return header 20, and a communication pipe 3° is provided between the switching valve 28 and the circulation pipe 25 on the suction side of the circulation pump 24 [between the heat transfer tube 22 and the heat exchanger 23 in the second chamber 9]. A communication pipe 32 is provided between the switching valve 31 and the switching valve 31 disposed between the two. Further, a switching valve 33 is disposed between the heat transfer tube 16 and the heat exchanger 19 in the circulation pipe line 21 .
かつ循環管路25の循環ポンプ24のデリベリ側に切換
弁34が配設され、この切換弁33と切換弁34との間
に連通管35が設けられている。また循環管路25には
、前記伝熱管22と切換弁31の間に切換弁36が設け
られて、この切換弁36と供給ヘッダ19との間に連通
管37が設けられ、かつ伝熱管22と切換弁34との間
に切換弁38が設けられて、戻りヘッダ20との間に連
通管39が設けられている。A switching valve 34 is provided on the delivery side of the circulation pump 24 of the circulation pipe 25, and a communication pipe 35 is provided between the switching valve 33 and the switching valve 34. Further, in the circulation pipe line 25, a switching valve 36 is provided between the heat transfer pipe 22 and the switching valve 31, a communication pipe 37 is provided between the switching valve 36 and the supply header 19, and a communication pipe 37 is provided between the heat transfer pipe 22 and the switching valve 31. A switching valve 38 is provided between the switching valve 34 and the switching valve 34, and a communication pipe 39 is provided between the return header 20 and the switching valve 34.
40は熱交換器17で熱伝達用の液体と熱交換する外部
熱源であり、本実施例では、外部負荷(L)が冷暖房で
あるため、圧縮式ヒートポンプを用いている。すなわち
、圧縮器41.熱交換器17で熱交換する凝縮器兼蒸発
器42.蒸発器兼凝縮器43、冷媒管路44、およ゛び
四方弁45で構成されている。Reference numeral 40 denotes an external heat source that exchanges heat with a heat transfer liquid in the heat exchanger 17. In this embodiment, since the external load (L) is air conditioning, a compression heat pump is used. That is, the compressor 41. A condenser/evaporator 42 that exchanges heat with a heat exchanger 17. It is composed of an evaporator/condenser 43, a refrigerant pipe 44, and a four-way valve 45.
上記のごとく構成された蓄熱装置の動作について説明す
る。なお吸収ヒートポンプ1において冷媒−吸収剤系は
、水−臭化リチウム系が一般的であり、熱伝達用の液体
としては通常水が用いられる。外部負荷(L)は冷暖房
とする。The operation of the heat storage device configured as described above will be explained. In the absorption heat pump 1, the refrigerant-absorbent system is generally a water-lithium bromide system, and water is usually used as the heat transfer liquid. The external load (L) is air conditioning.
(i)蓄熱(第1図参照)
外部熱源40の圧縮ヒートポンプを、たとえば夜間電力
を利用して運転し、凝縮器兼蒸発器42で発生する熱で
、熱交換器17において熱伝達液体(以下水という)が
加熱され、昇温された水は循環管路21内で循環されて
、吸収ヒートポンプ1の第1室(再生兼吸収室)8内の
伝熱管16で放熱する。(i) Heat storage (see FIG. 1) The compression heat pump of the external heat source 40 is operated, for example, using nighttime electricity, and the heat generated in the condenser/evaporator 42 is used to store the heat transfer liquid (hereinafter referred to as The heated water is circulated in the circulation pipe 21 and radiates heat in the heat transfer tube 16 in the first chamber (regeneration and absorption chamber) 8 of the absorption heat pump 1.
そして前記第1室8内で、散布装置1oにより冷媒溶液
を散布して、前記伝熱管16によりその冷媒溶液を加熱
して、冷媒である水を蒸発させて濃縮するとともに、発
生した水蒸気は隔壁5に設けられた蒸気流通孔6を通っ
て、第2室(凝縮兼蒸発室)9内に入り、伝熱管22で
冷却して凝縮する。一方伝熱管22内で熱伝達用の液体
が加熱され、循環管路25を通って、熱交換器23でそ
の熱を外部へ放散して冷却され、循環ポンプ24により
伝熱管22へ送られて、循環する6以上の一連の動作に
より、吸収ヒートポンプ1′において、冷媒溶液の濃縮
が進行して、蓄熱が行なわれる。Then, in the first chamber 8, the refrigerant solution is sprayed by the spraying device 1o, and the refrigerant solution is heated by the heat transfer tube 16 to evaporate and concentrate the water that is the refrigerant, and the generated water vapor is The vapor enters the second chamber (condensing and evaporating chamber) 9 through the vapor distribution hole 6 provided in the tube 5, and is cooled and condensed by the heat transfer tube 22. On the other hand, the heat transfer liquid is heated in the heat transfer tube 22, passes through the circulation pipe 25, is cooled by dissipating the heat to the outside in the heat exchanger 23, and is sent to the heat transfer tube 22 by the circulation pump 24. Through a series of six or more circulating operations, the refrigerant solution is concentrated and heat is stored in the absorption heat pump 1'.
(ii)暖房(昇降負荷)(第2図参照)暖房負荷にお
いて、たとえば基本負荷に対しては、外部熱源40から
のエネルギーにより、すなわち、凝縮器兼蒸発器42で
の凝縮に伴う発熱により、熱交換器17で温水を作成し
、切換弁26を切換えて負荷へ循環して対応し、負荷の
ピーク時にその増加分に対して、上記蓄熱装置で蓄熱さ
れた熱エネルギーを次のように放出して対応することが
できる。すなわち、循環管路25内を循環する水を、熱
交換器23により外部熱源(たとえば廃熱)と熱交換し
て加熱すれば、吸収ヒートポンプ1の第2室(!i縮兼
蒸発室)9内の伝熱管22により、冷媒ポンプ15を経
て散布装置13から散布される冷媒が加熱されて蒸発を
続け、蒸気は隔壁5の蒸気流通孔6を通って第1室(再
生兼吸収室)8内へ入り、溶液ポンプ11を経て散布装
置10がら散布されている冷媒溶液に吸収され、その際
放出される蒸気潜熱により伝熱管16内の水が加熱され
る。そして、伝熱管I6内で加熱された水を、循環管路
21のうちの切換弁27を切換えて、連通管3oにより
戻りヘッダと接続し、さらに外部負荷(L)とで形成し
た管路を循環させて、外部負荷(L)において熱を放出
(暖房)する。(ii) Heating (elevating load) (see Figure 2) In the heating load, for example, for the basic load, energy from the external heat source 40, that is, heat generated by condensation in the condenser/evaporator 42, Hot water is created in the heat exchanger 17 and circulated to the load by switching the switching valve 26 to cope with the increase, and at the peak of the load, the thermal energy stored in the heat storage device is released as follows. You can respond accordingly. That is, if the water circulating in the circulation pipe 25 is heated by exchanging heat with an external heat source (for example, waste heat) by the heat exchanger 23, the second chamber (!i compression and evaporation chamber) 9 of the absorption heat pump 1 is heated. The refrigerant sprayed from the dispersion device 13 via the refrigerant pump 15 is heated by the heat transfer tube 22 inside and continues to evaporate, and the vapor passes through the vapor distribution hole 6 of the partition wall 5 to the first chamber (regeneration and absorption chamber) 8. The water in the heat exchanger tubes 16 is absorbed by the refrigerant solution being sprayed from the spraying device 10 via the solution pump 11, and the water in the heat transfer tubes 16 is heated by the vapor latent heat released at this time. Then, the water heated in the heat transfer tube I6 is connected to the return header through the communication pipe 3o by switching the switching valve 27 of the circulation pipe 21, and then connected to the pipe line formed by the external load (L). It circulates and releases heat (heating) at the external load (L).
(iii)冷房(降温負荷)(第3図参照)冷房負荷に
おいても、暖房負荷の場合と同様に、基本負荷に対して
は外部熱源4oがらのエネルギーにより、すなおち、四
方弁45を切換えて凝縮器兼蒸発器42での蒸発に伴う
吸熱により、熱交換器17で冷水を作成し、循環して対
応し、負荷のピーク時にその増加分に対して、上記蓄熱
装置で蓄熱された熱エネルギーを次のように放出して対
応することができる。すなわち、切換弁36および38
を切換えて、吸収ヒートポンプ1の第2室(凝縮兼蒸発
室)9内の伝熱管22と連通管37.39と供給へラダ
19と戻りヘッダ20および外部負荷(L)との間に冷
水循環系路を形成する。また切換弁28.33および3
1.34を切換えて、第1室(再生兼吸収室)8内の伝
熱管16と連通管32.35と熱交換器23と循環ポン
プ24との間に温水循環系路を形成する。第2室9にお
いて、冷水循環系路により外部負荷(L)からの戻り水
を伝熱管22内に循環すると、冷媒ポンプ15を経て散
布装置13から散布される冷媒が吸熱して蒸発を続ける
。その吸熱により前記冷水循環系路内の送り水が冷却さ
れて、外部負荷(L)へ送られる。前記第2室(凝縮兼
蒸発室)9で蒸発した水蒸気は、隔壁5の蒸気流通孔6
を通って第1室(再生兼吸収室)8内へ入り、溶液ポン
プ11を経て散布装置10から散布されている冷媒溶液
に吸収され、その際放出される熱は伝熱管16に連通さ
れた、前記温水循環系路を循環する水により伝達されて
、熱交換器23で外部へ放出される。(iii) Cooling (temperature-dropping load) (see Figure 3) For the cooling load, as in the case of the heating load, for the basic load, the four-way valve 45 is switched using the energy from the external heat source 4o. By absorbing heat due to evaporation in the condenser/evaporator 42, cold water is created in the heat exchanger 17 and circulated to cope with the increase, and the thermal energy stored in the heat storage device is used for the increased amount at the peak of the load. You can respond by emitting the following: That is, switching valves 36 and 38
, the cold water is circulated between the heat transfer tube 22 in the second chamber (condensation and evaporation chamber) 9 of the absorption heat pump 1, the communication tube 37, 39, the supply ladder 19, the return header 20, and the external load (L). form a system. Also, switching valves 28, 33 and 3
1.34, a hot water circulation path is formed between the heat exchanger tube 16 in the first chamber (regeneration/absorption chamber) 8, the communication tube 32.35, the heat exchanger 23, and the circulation pump 24. In the second chamber 9, when return water from the external load (L) is circulated into the heat transfer tubes 22 through the cold water circulation path, the refrigerant sprayed from the spraying device 13 via the refrigerant pump 15 absorbs heat and continues to evaporate. The feed water in the cold water circulation system is cooled by the heat absorption and sent to the external load (L). The water vapor evaporated in the second chamber (condensation and evaporation chamber) 9 flows through the vapor flow holes 6 of the partition wall 5.
It enters the first chamber (regeneration and absorption chamber) 8 through the solution pump 11 and is absorbed by the refrigerant solution being sprayed from the spraying device 10, and the heat released at this time is communicated to the heat transfer tube 16. The heat is transmitted by the water circulating in the hot water circulation system, and is discharged to the outside by the heat exchanger 23.
上記装置により吸収ヒートポンプ1を使用して蓄熱し、
簡単な切換弁の操作により、暖房(昇温負荷)および冷
房(降温負荷)の際利用できるが。The above device stores heat using the absorption heat pump 1,
By simply operating the switching valve, it can be used for heating (temperature increasing load) and cooling (temperature decreasing load).
上記装置では真空条件下で、冷媒(水)蒸気の潜熱を利
用するため、その潜熱も大きく、装置全体を小型化でき
る。Since the above device utilizes the latent heat of the refrigerant (water) vapor under vacuum conditions, the latent heat is also large and the entire device can be downsized.
次に、上記実施例の構成の蓄熱装置における、LOGc
aQの蓄熱熱量を得るための諸条件は、第1表および第
2表のとおりであり、比較のため他の蓄熱装置の場合を
第3表に示す。Next, in the heat storage device having the configuration of the above embodiment, LOGc
The various conditions for obtaining the thermal storage heat amount of aQ are as shown in Tables 1 and 2, and the cases of other heat storage devices are shown in Table 3 for comparison.
〈以下余白〉
(c)他の蓄熱装置
第3表
上記第2表から明らかなごとく、冷房、暖房用に用いる
蓄熱装置として、蓄熱熱量が100calLの場合、稀
冷媒溶液および冷媒の総容量は100〜130イ程度で
十分であるが、第3表に示すごとく、従来の蓄熱装置で
は、冷水、温水の場合2000 rr1″もの容量が必
要であり、またリキッドアイスでも250〜400 r
n”を必要とし、本発明にかかる蓄熱装置は従来の装置
に比べて非常に小型化できる。(Left below) (c) Table 3 of other heat storage devices As is clear from Table 2 above, when a heat storage device used for cooling and heating has a heat storage capacity of 100 calL, the total capacity of the dilute refrigerant solution and refrigerant is 100 calL. ~130 i is sufficient, but as shown in Table 3, conventional heat storage devices require a capacity of 2000 r1'' for cold water and hot water, and 250 to 400 r1'' for liquid ice.
n'', and the heat storage device according to the present invention can be much smaller than conventional devices.
発明の効果
本発明の吸収ヒートポンプ式蓄熱装置においては、真空
条件下で作動する吸収ヒートポンプの。Effects of the Invention In the absorption heat pump heat storage device of the present invention, the absorption heat pump operates under vacuum conditions.
再生兼吸収室内および凝縮兼蒸発室内の各伝熱管と、外
部熱源と熱交換する熱交換器との間の熱伝達用の液体の
循環管路を互に切換弁を介して連通しているので、必要
に応じて前記切換弁を切換えることにより、蓄熱、昇温
(暖房)用放熱、降温(冷房)用放熱を容易に行なうこ
とができ、しかも利用できる冷媒の蒸発潜熱が大きく、
装置全体を、従来の装置に比べて非常に小型化すること
ができる。The heat transfer liquid circulation pipes between the heat exchanger tubes in the regeneration/absorption chamber and the condensation/evaporation chamber and the heat exchanger that exchanges heat with an external heat source are communicated with each other via switching valves. By switching the switching valve as necessary, heat storage, heat radiation for temperature increase (heating), and heat radiation for temperature decrease (cooling) can be easily performed, and the latent heat of vaporization of the available refrigerant is large.
The entire device can be made much smaller than conventional devices.
第1図は本発明の装置の一実施例の全体構成を示すとと
もに蓄熱時の使用態様を示す概略構成図、第2図は第1
図に示す装置の暖房時の使用態様を示す概略構成図、第
3図は第1図に示す装置の冷房時の使用態様を示す概略
構成図である。
1・・・吸収ヒートポンプ、3・・・冷媒溶液貯槽、5
・・・隔壁、6・・・蒸気流通孔、7・・・真空ポンプ
、8・・・第1室(再生兼吸収室)、9・・・第2室(
凝縮兼蒸発室) 、16.22・・・伝熱管、17.2
3・・・熱交換器、18゜24・・・循環ポンプ、21
.25・・・循環管路、 26.27.2g。
31、33.34.36.3g・・・切換弁、30.3
2.35.37゜39・・・連通管FIG. 1 is a schematic configuration diagram showing the overall configuration of one embodiment of the device of the present invention and how it is used during heat storage, and FIG.
FIG. 3 is a schematic configuration diagram showing how the device shown in FIG. 1 is used during heating, and FIG. 3 is a schematic configuration diagram showing how the device shown in FIG. 1 is used during cooling. 1... Absorption heat pump, 3... Refrigerant solution storage tank, 5
...Partition wall, 6...Steam flow hole, 7...Vacuum pump, 8...1st chamber (regeneration and absorption chamber), 9...2nd chamber (
condensation and evaporation chamber), 16.22...heat exchanger tube, 17.2
3... Heat exchanger, 18° 24... Circulation pump, 21
.. 25...Circulation pipe, 26.27.2g. 31, 33.34.36.3g...Switching valve, 30.3
2.35.37゜39...Communication pipe
Claims (1)
する、再生兼吸収室と凝縮兼蒸発室とを備えた吸収ヒー
トポンプの、前記各室内の伝熱管と各外部熱源の熱交換
器との間の熱伝達用液体の循環管路を切換弁を介して連
通したことを特徴とする吸収ヒートポンプ式蓄熱装置。1. A heat exchanger between the heat exchanger tubes in each chamber and each external heat source of an absorption heat pump equipped with a regeneration/absorption chamber and a condensation/evaporation chamber that exchanges heat under vacuum conditions with a liquid that has exchanged heat with an external heat source. An absorption heat pump type heat storage device, characterized in that a circulation pipe for a heat transfer liquid between the two is connected through a switching valve.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61159430A JPH0678860B2 (en) | 1986-07-07 | 1986-07-07 | Absorption heat pump type heat storage device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61159430A JPH0678860B2 (en) | 1986-07-07 | 1986-07-07 | Absorption heat pump type heat storage device |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6315049A true JPS6315049A (en) | 1988-01-22 |
JPH0678860B2 JPH0678860B2 (en) | 1994-10-05 |
Family
ID=15693571
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP61159430A Expired - Lifetime JPH0678860B2 (en) | 1986-07-07 | 1986-07-07 | Absorption heat pump type heat storage device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0678860B2 (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH02122169A (en) * | 1988-11-01 | 1990-05-09 | Hitachi Ltd | Chemical heat pump |
JPH0270854U (en) * | 1988-10-07 | 1990-05-30 | ||
CN108534213A (en) * | 2018-05-11 | 2018-09-14 | 宋世海 | A kind of low ebb electric heat storage composite adsorption type air source heat pump circulating heating system |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS60238657A (en) * | 1984-05-11 | 1985-11-27 | 株式会社クボタ | Air conditioner |
JPS61110856A (en) * | 1984-11-02 | 1986-05-29 | 株式会社日立製作所 | Chemical heat accumulating system |
-
1986
- 1986-07-07 JP JP61159430A patent/JPH0678860B2/en not_active Expired - Lifetime
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS60238657A (en) * | 1984-05-11 | 1985-11-27 | 株式会社クボタ | Air conditioner |
JPS61110856A (en) * | 1984-11-02 | 1986-05-29 | 株式会社日立製作所 | Chemical heat accumulating system |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0270854U (en) * | 1988-10-07 | 1990-05-30 | ||
JPH02122169A (en) * | 1988-11-01 | 1990-05-09 | Hitachi Ltd | Chemical heat pump |
CN108534213A (en) * | 2018-05-11 | 2018-09-14 | 宋世海 | A kind of low ebb electric heat storage composite adsorption type air source heat pump circulating heating system |
Also Published As
Publication number | Publication date |
---|---|
JPH0678860B2 (en) | 1994-10-05 |
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