JPS6231824Y2 - - Google Patents
Info
- Publication number
- JPS6231824Y2 JPS6231824Y2 JP13492486U JP13492486U JPS6231824Y2 JP S6231824 Y2 JPS6231824 Y2 JP S6231824Y2 JP 13492486 U JP13492486 U JP 13492486U JP 13492486 U JP13492486 U JP 13492486U JP S6231824 Y2 JPS6231824 Y2 JP S6231824Y2
- Authority
- JP
- Japan
- Prior art keywords
- heat
- temperature side
- water
- heat pump
- low
- 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
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 84
- 239000003507 refrigerant Substances 0.000 claims description 14
- 239000000498 cooling water Substances 0.000 claims description 3
- 239000007788 liquid Substances 0.000 description 11
- 230000006835 compression Effects 0.000 description 9
- 238000007906 compression Methods 0.000 description 9
- 238000010438 heat treatment Methods 0.000 description 7
- 238000001816 cooling Methods 0.000 description 5
- 238000010586 diagram Methods 0.000 description 4
- 238000001704 evaporation Methods 0.000 description 3
- 230000008020 evaporation Effects 0.000 description 3
- 238000005338 heat storage Methods 0.000 description 3
- 230000005855 radiation Effects 0.000 description 3
- 230000007423 decrease Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000004781 supercooling Methods 0.000 description 2
- 239000006096 absorbing agent Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 230000017525 heat dissipation Effects 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 239000008400 supply water Substances 0.000 description 1
Landscapes
- Heat-Pump Type And Storage Water Heaters (AREA)
Description
【考案の詳細な説明】
〔考案の目的〕
(産業上の利用分野)
本考案は、ヒートポンプを夜間運転して熱媒体
に蓄熱し、この蓄積熱量を昼間運転するヒートポ
ンプの蒸発熱の熱源として吸収させることにより
所望の高温度を得るような時間差運転に好適なヒ
ートポンプ装置に関するものである。[Detailed explanation of the invention] [Purpose of the invention] (Field of industrial application) This invention operates a heat pump at night to store heat in a heat medium, and absorbs this accumulated heat as a heat source for the heat of evaporation of the heat pump that operates during the day. The present invention relates to a heat pump device suitable for staggered operation in which a desired high temperature is obtained by
(従来の技術)
この種の技術を温水プールについて考えてみる
に、温水プールの運営については、プール用温水
の温度管理のみならず、シヤワー及び暖房用温水
の温度管理もしなければならないが、従来これ等
の温水はボイラー等を介して重油燃焼により加温
する例が多く見られた。しかしながら燃焼加温よ
りもヒートポンプ方式の方が熱効率が良好な場合
があることが知られており、ヒートポンプ方式で
も一段圧縮よりも二段圧縮の方が効率が高いこと
は言うまでもない。(Conventional technology) If we consider this type of technology for heated pools, we can see that in operating a heated pool, it is necessary not only to control the temperature of hot water for the pool, but also to control the temperature of hot water for showers and heating. In many cases, this hot water was heated by burning heavy oil in a boiler or the like. However, it is known that the heat pump method may have better thermal efficiency than combustion heating, and it goes without saying that even in the heat pump method, two-stage compression has higher efficiency than single-stage compression.
しかしながら、第2図に示すような二段圧縮機
によるヒートポンプサイクルは、第3図に示すモ
リエル線図で明らかなように、線は一段圧縮
機低段圧縮、線は中間冷却器による中間
冷却、線は二段圧縮機高段圧縮、線は凝
縮器による凝縮、線は管V内の液の過冷
却、線は第一膨脹弁による膨脹、線は中
間冷却器による過冷却、線は第二膨脹弁
による膨脹、及びは蒸発器及び中間冷却
器による一段及び二段圧縮の蒸発の各状態変化
を遂行する。この場合、線を中間冷却器を介
して外部からの熱による冷却であるとするなら
ば、ヒートポンプの熱勘定から言つてエンタルピ
ーの損失となる。 However, in a heat pump cycle using a two-stage compressor as shown in Fig. 2, as is clear from the Mollier diagram shown in Fig. 3, the line indicates low-stage compression by the single-stage compressor, the line indicates intercooling by the intercooler, and the line indicates intercooling by the intercooler. The line is high-stage compression in the two-stage compressor, the line is condensation by the condenser, the line is supercooling of the liquid in pipe V, the line is expansion by the first expansion valve, the line is supercooling by the intercooler, the line is second Each state change of evaporation is performed: expansion by an expansion valve, and one-stage and two-stage compression by an evaporator and an intercooler. In this case, if the line is cooled by heat from the outside via an intercooler, there will be an enthalpy loss from the heat pump's heat account.
すなわち、二段圧縮によるヒートポンプで凝縮
熱量の線を得ようとするとき、線に相当す
る熱量が損失となる欠点を有する。一方、中間冷
却を外部からの熱による冷却でなく自己冷媒方式
によつて線に相当する熱量を冷却するとして
も、線に相当する熱量だけ二段圧縮機の熱容
量を大にしなければならず、従つて、二段圧縮機
がその分だけ大型となる欠点を有することにな
る。 That is, when trying to obtain a line of condensed heat using a heat pump using two-stage compression, there is a drawback that the amount of heat corresponding to the line is lost. On the other hand, even if intercooling is performed using a self-refrigerant system rather than external heat, the heat capacity of the two-stage compressor must be increased by the amount of heat equivalent to the line. Therefore, the two-stage compressor has the disadvantage of being correspondingly larger.
また、従来の二段圧縮機を用いる冷凍装置例え
ば実開昭54−60754号公報所載のものは低段側と
高段側の圧縮機を同時運転しなければならないも
のであるから、これをヒートポンプに応用しても
低段側を高段側より先行運転させて夜間の安い電
力料金を利用して熱量を蓄積するような作動をさ
せることはできない。 In addition, conventional refrigeration equipment using two-stage compressors, such as the one described in Japanese Utility Model Application Publication No. 1983-60754, requires the low-stage and high-stage compressors to be operated simultaneously; Even when applied to a heat pump, it is not possible to operate the low-stage side in advance of the high-stage side and accumulate heat by taking advantage of the low electricity rates at night.
(考案が解決しようとする問題点)
本考案は、前記従来技術の欠点を解決し、熱効
率がよく、圧縮機が小型化でき、電力の平準化に
とつても望ましい経済的な効率的な昇温を実施で
きるヒートポンプ装置を提供することを目的とす
る。(Problems to be Solved by the Invention) The present invention solves the drawbacks of the prior art, has good thermal efficiency, can downsize the compressor, and provides an economical and efficient increase that is desirable for power leveling. The purpose of the present invention is to provide a heat pump device that can perform heating.
(問題点を解決するための手段)
本考案のヒートポンプ装置は前記の問題点を解
決するために、低段側の圧縮機と、蒸発器と、前
記圧縮機から吐出された冷媒ガスを凝縮させる低
温側加熱器と、前記低温側加熱器と第1送水管に
より連結される温水設備とを有する低温側ヒート
ポンプサイクルと、前記第1送水管から分岐され
る第2送水管が連通する水熱源蒸発器と、高温側
加熱器と、前記水熱源蒸発器から冷媒ガスを吸入
し圧縮して前記高温側加熱器に吐出する高段側の
圧縮機と、前記高温側加熱器と第3送水管により
連結される貯湯槽とを有する高温側ヒートポンプ
サイクルとからなるものである。
(Means for Solving the Problems) In order to solve the above problems, the heat pump device of the present invention includes a low-stage compressor, an evaporator, and condenses refrigerant gas discharged from the compressor. A low temperature side heat pump cycle having a low temperature side heater and a hot water facility connected to the low temperature side heater by a first water pipe, and a water heat source evaporation in which a second water pipe branched from the first water pipe communicates with each other. a high-temperature side heater, a high-stage compressor that sucks refrigerant gas from the water heat source evaporator, compresses it, and discharges it to the high-temperature side heater, and the high-temperature side heater and a third water pipe. It consists of a high temperature side heat pump cycle having a hot water storage tank connected thereto.
(作用)
低段側の圧縮機を運転することによつて冷媒が
蒸発器において熱を吸上げて低温側加熱器にヒー
トポンプサイクルとして熱を供給し、温水設備内
の第一熱媒体に十分の熱量を貯えることができ
る。また、高段側の圧縮機を運転することによつ
て、第1送水管から分岐される第2送水管を介し
て低温側ヒートポンプサイクルの第一熱媒体の保
有する熱量の一部が水熱源蒸発器に導入されるの
で該蒸発器内で冷媒が該熱を吸上げて高温側加熱
器にヒートポンプサイクルとして熱を供給し、貯
湯槽内の第二の熱媒体の温度を高温に上昇させる
ことができる。そして、低段側の圧縮機を夜間運
転して第一熱媒体に十分の熱量を貯えることによ
り該熱媒体が昼間の使用時に必要とする温度より
も高い温度にまで上昇させておけば、昼間におい
て低段側と高段側の両方の圧縮機を共に運転して
前記第一熱媒体の温度を昼間使用時の温度まで下
げる熱量分を利用して第二熱媒体の温度を高温に
上昇させることができる。(Function) By operating the low-stage compressor, the refrigerant absorbs heat in the evaporator and supplies heat to the low-temperature side heater as a heat pump cycle. Can store heat. In addition, by operating the compressor on the high stage side, a part of the heat held by the first heat medium of the low temperature side heat pump cycle is transferred to the water heat source through the second water pipe branched from the first water pipe. Since the refrigerant is introduced into the evaporator, the refrigerant absorbs the heat in the evaporator and supplies the heat to the high temperature side heater as a heat pump cycle, thereby raising the temperature of the second heat medium in the hot water storage tank to a high temperature. Can be done. Then, if the compressor on the lower stage side is operated at night to store sufficient heat in the first heat medium and raise the temperature of the heat medium to a temperature higher than that required during daytime use, it is possible to In this step, both the low-stage and high-stage compressors are operated to lower the temperature of the first heat medium to the temperature during daytime use, and the amount of heat is used to raise the temperature of the second heat medium to a high temperature. be able to.
(実施例) 本考案の実施例を図に基づいて説明する。(Example) An embodiment of the present invention will be described based on the drawings.
第4図において、低温側のヒートポンプはサイ
クルを画いている。冷媒ガスは圧力P1から
圧力P3に昇圧し(線)、線の熱量を凝縮器
で放熱し、更に、過冷却器により線に相当す
る熱量を放熱する。次に膨脹弁により線に沿
つて圧力P3からP1に減圧し、蒸発器により線
の熱量を吸収し熱サイクルを終了する。一方、高
温側のヒートポンプは、サイクルを画いて
いる。すなわち、高温側の冷媒は圧力P2からP4に
昇圧し(線)、線(OP)の熱量を凝縮器で放
熱し、更に過冷却器により線に相当する熱量
を放熱過冷却する。次に膨脹弁により線に沿
つて圧力P4からP2に減圧し、蒸発器により線
の熱量を吸収し熱サイクルを終了する。 In FIG. 4, the heat pump on the low temperature side is in a cycle. The refrigerant gas is pressurized from pressure P 1 to pressure P 3 (line), the heat of the line is radiated by the condenser, and the heat equivalent to the line is further radiated by the supercooler. Next, the pressure is reduced from P 3 to P 1 along the line by the expansion valve, and the heat of the line is absorbed by the evaporator to complete the thermal cycle. On the other hand, the heat pump on the high temperature side operates in a cycle. That is, the refrigerant on the high temperature side increases the pressure from P 2 to P 4 (line), radiates the heat in the line (OP) in the condenser, and then radiates and supercools the heat equivalent to the line in the supercooler. Next, the pressure is reduced from P 4 to P 2 along the line by the expansion valve, and the heat of the line is absorbed by the evaporator, completing the thermal cycle.
そして、高温側のヒートポンプサイクルの吸熱
作用(線)において吸熱するための熱源と、
低温側のヒートポンプサイクルの放熱作用(線
)において放熱するための被加熱源とを同一
の第一の熱媒体とすることによつて、低温側及び
高温側のヒートポンプサイクルは、それぞれを低
圧縮比で効率よく運転しながら、高温側のヒート
ポンプサイクルの放熱作用(線)により第二
の熱媒体に容易に高温の熱を与えることができ
る。 and a heat source for absorbing heat in the endothermic action (line) of the heat pump cycle on the high temperature side;
By using the same first heat medium as the heated source for heat radiation in the heat radiation action (line) of the low temperature side heat pump cycle, the low temperature side and high temperature side heat pump cycles each have a low compression ratio. While operating efficiently, high-temperature heat can be easily given to the second heat medium by the heat dissipation action (line) of the heat pump cycle on the high temperature side.
次に、前記のヒートポンプサイクルを温水プー
ルに適用した一実施例につき説明する。第1図に
おいて、低段側の圧縮機1は、吐出管2を介して
低温側加熱器(凝縮器)3に連通され、液管4は
途中に液過冷却器35及び膨脹弁5を介して空気
熱源蒸発器6又はその他の吸熱器に接続され、前
記空気熱源蒸発器6と低段側の圧縮機1との間は
吸入ガス管7で連通されている。液管4は途中で
分岐管8により分岐され、膨脹弁9を介して冷房
用水冷却器又は他の目的の冷却器10に連通さ
れ、ガス管11は前記ガス管7に合流されてい
る。一方、高段側の圧縮機12は、吐出管13を
介し高温側加熱器(凝縮器)14に連通され、液
管15は途中に液過冷却器36及び膨脹弁16を
介して水熱源蒸発器17に連通される。ガス管3
4はこの水熱源蒸発器17と高段側の圧縮機12
を連通している。さて、低温側加熱器3と温水プ
ール18とは、第1送水管19,20により連通
され、この第1送水管19,20より分岐し夫々
適宜の開閉弁を有する第2送水管21,22は高
温側の水熱源蒸発器17に連通されている。ま
た、第1送水管19は分岐管23を介してクーリ
ングタワー24に連通し、このクーリングタワー
24は途中にポンプ25を介し分岐管26に次い
で第1送水管20に連通されている。クーリング
タワー24は温水プールの温度上昇又は下降を調
整し、熱の過不足を補足する役目をする。温水プ
ール18の第1送水管20には図示していないポ
ンプ、浄化装置等が配設されている。 Next, an example in which the heat pump cycle described above is applied to a hot water pool will be described. In FIG. 1, a low-stage compressor 1 is connected to a low-temperature side heater (condenser) 3 via a discharge pipe 2, and a liquid pipe 4 is connected to a liquid subcooler 35 and an expansion valve 5 on the way. The air heat source evaporator 6 is connected to the air heat source evaporator 6 or another heat absorber, and the air heat source evaporator 6 and the lower stage compressor 1 are communicated through an intake gas pipe 7. The liquid pipe 4 is branched by a branch pipe 8 in the middle and communicated with a cooling water cooler or a cooler 10 for other purposes via an expansion valve 9, and a gas pipe 11 is joined to the gas pipe 7. On the other hand, the high-stage compressor 12 is connected to a high-temperature side heater (condenser) 14 via a discharge pipe 13, and a liquid pipe 15 is connected to a water heat source evaporator via a liquid supercooler 36 and an expansion valve 16 on the way. It is communicated with the container 17. gas pipe 3
4 is this water heat source evaporator 17 and the compressor 12 on the high stage side.
are communicating. Now, the low-temperature side heater 3 and the hot water pool 18 are communicated through first water pipes 19 and 20, and second water pipes 21 and 22 branch from the first water pipes 19 and 20 and have appropriate on-off valves, respectively. is connected to the water heat source evaporator 17 on the high temperature side. Further, the first water pipe 19 communicates with a cooling tower 24 via a branch pipe 23, and this cooling tower 24 is connected to a branch pipe 26 and then to the first water pipe 20 via a pump 25 along the way. The cooling tower 24 serves to adjust the temperature rise or fall of the hot water pool and compensate for excess or deficiency in heat. The first water pipe 20 of the hot water pool 18 is provided with a pump, a purification device, etc. (not shown).
次に、高温加熱器14は第3送水管27,28
により貯湯槽29に連通し、第3送水管27には
複数個のシヤワー30暖房その他の高温水使用部
及び圧力調整弁31が配設され、第3送水管28
にはポンプ32が配設されている。符号33は貯
湯槽29へ水を補給する補給水管を示している。 Next, the high temperature heater 14
The third water pipe 27 is connected to a hot water storage tank 29, and the third water pipe 27 is provided with a plurality of showers 30 for heating and other high-temperature water usage parts, and a pressure regulating valve 31.
A pump 32 is disposed at. Reference numeral 33 indicates a supply water pipe that supplies water to the hot water tank 29.
以上のように構成されたヒートポンプの作用に
ついて説明する。 The operation of the heat pump configured as above will be explained.
冷媒は、低段側の圧縮機1により、第4図にあ
る如く圧力P1から圧力P3に昇圧して吐出管2を通
つて低温側加熱器3に入り、温水プールの第一熱
媒体たる温水と熱交換を行ない、凝縮液は液管4
に入り、液過冷却器35を通り、一部は膨脹弁5
を介して空気熱源蒸発器6に入つて外気空気等熱
源と熱交換し、他部は膨脹弁9を介して冷房用水
冷却器10に入つて、図示していない空調器用水
と熱交換し再び圧縮機1戻る。この場合、冷却器
10はスケートリンク等の負荷であつてもよい。 The refrigerant is pressurized from pressure P 1 to pressure P 3 by the compressor 1 on the low stage side, as shown in Fig. 4, enters the low temperature side heater 3 through the discharge pipe 2, and becomes the first heat medium of the hot water pool. Heat exchange is performed with the hot water in the barrel, and the condensate is transferred to liquid pipe 4.
enters the liquid, passes through the liquid supercooler 35, and a portion passes through the expansion valve 5.
The air enters the heat source evaporator 6 through the air and exchanges heat with a heat source such as outside air, and the other part enters the cooling water cooler 10 through the expansion valve 9 and exchanges heat with air conditioner water (not shown) again. Compressor 1 return. In this case, the cooler 10 may be a load such as a skating rink.
次に、高段側の圧縮機12のサイクルの冷媒
は、圧力P2から圧力P4に昇圧し、吐出管13を通
つて高温側加熱器(凝縮器)14に入り、貯湯槽
29からの第二熱媒体たる温水と熱交換を行な
い、液管15及び液過冷却器36を経て、膨脹弁
16により減圧し水熱源蒸発器17に入る。この
水熱源蒸発器17において、冷媒は前記温水プー
ル18からの蓄熱分温水と熱交換し再び圧縮機1
2に戻る。すなわち、低段側の圧縮機1は空気熱
源蒸発器6及び冷房用冷却器、及びその他の熱源
10からそれぞれ外気熱源及び冷房負荷を吸上
げ、熱源として低温側加熱器3にヒートポンプサ
イクルとして熱量を与え、プールの水を温水とす
る。夜間プール使用停止の負荷のない中には前記
低段側の圧縮機1のみの運転続行によりプール水
温は、日中のプールの使用負荷の減少により例え
ばほぼ29℃のプールの常用温度からほぼ33℃に昇
温される。 Next, the refrigerant in the cycle of the high stage compressor 12 is increased from pressure P 2 to pressure P 4 , enters the high temperature side heater (condenser) 14 through the discharge pipe 13, and is discharged from the hot water storage tank 29. It exchanges heat with hot water as a second heat medium, passes through a liquid pipe 15 and a liquid subcooler 36, is depressurized by an expansion valve 16, and enters a water heat source evaporator 17. In this water heat source evaporator 17, the refrigerant exchanges heat with the stored heat water from the hot water pool 18 and returns to the compressor 1.
Return to 2. That is, the low-stage compressor 1 sucks up the outside air heat source and the cooling load from the air heat source evaporator 6, cooling cooler, and other heat sources 10, respectively, and transfers the amount of heat to the low-temperature side heater 3 as a heat source in a heat pump cycle. to warm the pool water. During the night when there is no load when the pool is not used, only the compressor 1 on the low stage side continues to operate, and the pool water temperature decreases from the normal pool temperature of approximately 29℃ to approximately 33℃ due to the reduction in the pool usage load during the day. The temperature is raised to ℃.
次に、翌日の昼間プール使用時には、高段側の
圧縮機12を低段側の圧縮機1と共に運転し、高
温側加熱器12の水熱源蒸発器17の熱源として
前夜プールに蓄熱しておいた33℃の温水を33℃か
ら29℃までの蓄熱量を熱源として利用する。プー
ルの温水は第1送水管19,20より分岐する第
2送水管21,22を介して水熱源蒸発器17と
連通しており、この水熱源蒸発器17おける熱交
換により、温水の温度は33℃からプールの常用保
持温度29℃に低下して温水プール18に戻る。一
方、低温側のヒートポンプはプール温水を29℃に
保持する。すなわち、4℃×(水熱源蒸発器17
と熱交換する温水量)の熱量分が高段側の圧縮機
の熱源として有効に利用されたことになる。高温
側のヒートポンプの水熱源蒸発器17から流出す
る冷媒は、前記熱量に相当する熱分量を吸熱して
高段側の圧縮機12に吸入されるので、高温側加
熱器14で加熱するほぼ45℃〜70℃の高温シヤワ
ー及び暖房用温水は、前記熱量に更に高段側の圧
縮機12の動力熱当量分を加えた熱として高温の
温水(45℃〜70℃)を圧縮比が小さい状態で得る
ことができる。 Next, when the pool is used during the daytime on the next day, the high-stage compressor 12 is operated together with the low-stage compressor 1, and the heat stored in the pool from the previous night is used as a heat source for the water heat source evaporator 17 of the high-temperature side heater 12. The heated water at 33°C is used as a heat source by storing heat from 33°C to 29°C. The hot water in the pool communicates with the water heat source evaporator 17 via second water pipes 21 and 22 that branch from the first water pipes 19 and 20, and the temperature of the hot water decreases by heat exchange in the water heat source evaporator 17. The temperature drops from 33°C to 29°C and returns to the heated pool 18. On the other hand, the heat pump on the low-temperature side maintains the pool hot water at 29°C. That is, 4°C x (water heat source evaporator 17
This means that the amount of heat (the amount of hot water exchanged with The refrigerant flowing out from the water heat source evaporator 17 of the heat pump on the high temperature side absorbs heat equivalent to the above amount of heat and is sucked into the compressor 12 on the high stage side, so that it is heated by the heater 14 on the high temperature side. The hot water for high-temperature showers and heating at a temperature of ℃ to 70℃ is generated by adding the power heat equivalent of the high-stage compressor 12 to the above-mentioned amount of heat, and then converting the high-temperature hot water (45℃ to 70℃) into a state where the compression ratio is small. You can get it at
このように、低温側のヒートポンプでプールに
蓄熱したほぼ33℃の熱量の一部を高温側のヒート
ポンプの吸上げ熱量として使用することができる
から、従来、単段圧縮機による1つのヒートポン
プで外気熱源から温水プールの水温を29℃に昇温
し、また単段圧縮機による他のヒートポンプで同
じく冬期の外気熱源0℃以下からシヤワーや暖房
用温水を45℃〜70℃に昇温する場合に比較して、
高段側の圧縮機の圧縮比は低くすることができる
ので体積効率は高く性能上優れた効果を奏し、一
方前記の夜間の蓄熱分だけ低段側の圧縮機を小型
にすることができる。従つて、VL/VH=2:1
の比を夜間運転の延長により、1:1の容量比で
も稼動できるものであり、高段側の圧縮機を低段
より大なる圧縮機に選定できるものである。ま
た、本実施例では温水プールを蓄熱槽に兼用した
ので、別に蓄熱水槽を設ける必要がなく、廉価に
できる利点を有すると共に、プールは容積が大き
く放熱量も少なくてすむので放熱損失が少なくて
すむ利点も有している。 In this way, part of the approximately 33°C heat stored in the pool by the heat pump on the low temperature side can be used as the heat absorbed by the heat pump on the high temperature side. When raising the water temperature of a heated pool from a heat source to 29℃, or when raising the temperature of hot water for showers or space heating to 45℃ to 70℃ from an outside air heat source of 0℃ or less in winter using another heat pump using a single-stage compressor. Compared to,
Since the compression ratio of the high-stage compressor can be lowered, the volumetric efficiency is high and excellent performance is achieved, while the low-stage compressor can be made smaller by the amount of heat stored during the night. Therefore, V L /V H =2:1
By extending the nighttime operation, it is possible to operate with a capacity ratio of 1:1, and the compressor on the high stage side can be selected as a larger compressor than the compressor on the lower stage. In addition, in this embodiment, the hot water pool is also used as a heat storage tank, so there is no need to provide a separate heat storage tank, which has the advantage of being inexpensive, and the pool has a large volume and requires less heat radiation, so there is less heat loss. It also has the advantage of being able to survive.
このように、本実施例は数多くの優れた効果を
有しているが、本実施は、第一熱媒体としてプー
ル温水に限るものではなく、また熱媒体の温度領
域も29℃や45℃に限定するものでもない。 As described above, this example has many excellent effects, but this implementation is not limited to pool hot water as the first heat medium, and the temperature range of the heat medium is also 29℃ and 45℃. It's not limited either.
すなわち、第一熱媒体は昼間のみ所要の目的に
使用されるものであり、したがつて第一の熱媒体
の不取用時である夜間を利用して、ヒートポンプ
により、第一熱媒体の温度を使用時の常用温度よ
り高い温度にまで上昇させ第一熱媒体を蓄熱用に
利用し、昼間においてはこの余分に蓄積された熱
を利用して昼間のヒートポンプの運転を経済的に
行わせるようにする点に本実施例は特徴がある。
したがつて、このヒートポンプ装置はこのような
第一熱媒体と第二熱媒体とを必要とする色々な目
的にきわめて有利に適用することができる。 In other words, the first heat medium is used for the required purpose only during the day, and therefore, during the night when the first heat medium is not used, the heat pump is used to increase the temperature of the first heat medium. The heat pump is raised to a temperature higher than the normal temperature during use, and the first heat medium is used for heat storage, and during the daytime, this excess accumulated heat is used to economically operate the heat pump during the daytime. This embodiment is characterized by the following points.
Therefore, this heat pump device can be very advantageously applied to various purposes that require such a first heat medium and a second heat medium.
なお、前記実施例において、第一熱媒体を空気
とし、ソーラハウス内の暖気を蓄熱して夜間利用
するものであつてもよく、また、前記実施例にお
けるプール表面から蒸発し、温水プールの室内天
井部に滞溜する暖飽和空気熱を吸熱して利用する
ものであつてもよい。更に、第二熱媒体もシヤワ
ーや暖房用温水に限定するものでないことは勿論
である。 In the above embodiment, air may be used as the first heat medium, and the warm air inside the solar house may be stored and used at night. It may be one that absorbs and utilizes the heat of warm saturated air that accumulates in the ceiling. Furthermore, it goes without saying that the second heat medium is not limited to hot water for showers or heating.
本考案によれば、低段側の圧縮機を運転するこ
とによつて低温側加熱器で温水設備内の第一熱媒
体に十分の熱量を貯えられるとともに、高段側の
圧縮機を運転することによつて第一熱媒体の保有
する熱量の一部が水熱源蒸発器に導入されるので
これにより第二熱媒体の温度を能率よく所要の高
温にまで上昇させることができる。
According to the present invention, by operating the compressor on the low stage side, a sufficient amount of heat can be stored in the first heat medium in the hot water equipment by the heater on the low temperature side, and at the same time, the compressor on the high stage side can be operated. As a result, a part of the heat held by the first heat medium is introduced into the water heat source evaporator, so that the temperature of the second heat medium can be efficiently raised to a required high temperature.
また、低温側ヒートポンプサイクルを夜間運転
して第一熱媒体を昼間において必要とされる温度
より高い中間温度に上昇させる行程を先行して行
わせ、次に低温側と高温側のヒートポンプサイク
ルを共に昼間運転し、夜間運転において余分に蓄
えておいて熱量を高温側ヒートポンプの熱源とし
て使用することができるので、成績係数を向上さ
せ運転するヒートポンプの圧縮機を小型化するこ
とが可能となる。 In addition, the low temperature side heat pump cycle is operated at night to raise the first heat medium to an intermediate temperature higher than the temperature required during the daytime, and then the low temperature side and high temperature side heat pump cycles are operated together. Since it is possible to operate during the day and store excess heat during nighttime operation and use it as a heat source for the high-temperature side heat pump, it is possible to improve the coefficient of performance and downsize the compressor of the operated heat pump.
第1図は本考案のヒートポンプ装置の一実施例
のフローシートダイヤグラム、第2図は従来技術
のヒートポンプ装置のフローシートダイヤグラ
ム、第3図と第4図はそれぞれ第2図と第1図の
状態変化を示すモリエル線図である。
1……低段側の圧縮機、3……低温側加熱器、
6……蒸発器としての空気熱源蒸発器、10……
蒸発器としての冷却器、12……高段側の圧縮
機、14……高温側加熱器、17……水熱源蒸発
器、18……温水設備としての温水プール、1
9,20……第1送水管、21,22……第2送
水管、27,28……第3送水管、29……貯湯
槽。
Fig. 1 is a flow sheet diagram of an embodiment of the heat pump device of the present invention, Fig. 2 is a flow sheet diagram of a conventional heat pump device, and Figs. 3 and 4 are the states of Fig. 2 and Fig. 1, respectively. It is a Mollier diagram showing changes. 1...low stage side compressor, 3...low temperature side heater,
6... Air heat source evaporator as an evaporator, 10...
Cooler as evaporator, 12... Compressor on high stage side, 14... High temperature side heater, 17... Water heat source evaporator, 18... Hot water pool as hot water equipment, 1
9, 20...first water pipe, 21,22...second water pipe, 27,28...third water pipe, 29...hot water tank.
Claims (1)
ら吐出された冷媒ガスを凝縮させる低温側加熱
器と、前記低温側加熱器と第1送水管により連
結される温水設備とを有する低温側ヒートポン
プサイクルと、前記第1送水管から分岐される
第2送水管が連通する水熱源蒸発器と、高温側
加熱器と、前記水熱源蒸発器から冷媒ガスを吸
入し圧縮して前記高温側加熱器に吐出する高段
側の圧縮機と、前記高温側加熱器と第3送水管
により連結される貯湯槽とを有する高温側ヒー
トポンプサイクルとからなることを特徴とする
ヒートポンプ装置。 (2) 低温側ヒートポンプサイクルの蒸発器が空気
熱源蒸発器と冷房用水冷却器とからなり、温水
設備が温水プールであることを特徴とする実用
新案登録請求の範囲第1項記載のヒートポンプ
装置。 (3) 高温側ヒートポンプサイクルの第3送水管に
シヤワーを有することを特徴とする実用新案登
録請求の範囲第2項記載のヒートポンプ装置。[Claims for Utility Model Registration] (1) A low-stage compressor, an evaporator, a low-temperature side heater for condensing refrigerant gas discharged from the compressor, the low-temperature side heater, and a first A low temperature side heat pump cycle having hot water equipment connected by a water pipe, a water heat source evaporator communicating with a second water pipe branched from the first water pipe, a high temperature side heater, and the water heat source evaporator. It consists of a high-stage compressor that sucks refrigerant gas, compresses it, and discharges it to the high-temperature side heater, and a high-temperature side heat pump cycle that has a hot water storage tank connected to the high-temperature side heater by a third water pipe. A heat pump device characterized by: (2) The heat pump device according to claim 1, wherein the evaporator of the low-temperature side heat pump cycle comprises an air heat source evaporator and a cooling water cooler, and the hot water facility is a hot water pool. (3) The heat pump device according to claim 2 of the utility model registration, characterized in that the third water pipe of the high temperature side heat pump cycle has a shower.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13492486U JPS6231824Y2 (en) | 1986-09-03 | 1986-09-03 |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13492486U JPS6231824Y2 (en) | 1986-09-03 | 1986-09-03 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6250461U JPS6250461U (en) | 1987-03-28 |
| JPS6231824Y2 true JPS6231824Y2 (en) | 1987-08-14 |
Family
ID=31036624
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP13492486U Expired JPS6231824Y2 (en) | 1986-09-03 | 1986-09-03 |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6231824Y2 (en) |
-
1986
- 1986-09-03 JP JP13492486U patent/JPS6231824Y2/ja not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6250461U (en) | 1987-03-28 |
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