JP3367274B2 - Ice storage device - Google Patents

Ice storage device

Info

Publication number
JP3367274B2
JP3367274B2 JP12362195A JP12362195A JP3367274B2 JP 3367274 B2 JP3367274 B2 JP 3367274B2 JP 12362195 A JP12362195 A JP 12362195A JP 12362195 A JP12362195 A JP 12362195A JP 3367274 B2 JP3367274 B2 JP 3367274B2
Authority
JP
Japan
Prior art keywords
ice
water
heat storage
storage tank
aqueous solution
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 - Fee Related
Application number
JP12362195A
Other languages
Japanese (ja)
Other versions
JPH08313017A (en
Inventor
慎一 若本
寿守務 吉村
一成 中尾
直樹 田中
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.)
Mitsubishi Electric Corp
Original Assignee
Mitsubishi Electric Corp
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 Mitsubishi Electric Corp filed Critical Mitsubishi Electric Corp
Priority to JP12362195A priority Critical patent/JP3367274B2/en
Publication of JPH08313017A publication Critical patent/JPH08313017A/en
Application granted granted Critical
Publication of JP3367274B2 publication Critical patent/JP3367274B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明はビル空調、地域冷房や氷
温にて冷却、冷蔵される食品生産、加工に用いる氷蓄熱
装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an ice heat storage device for use in building air conditioning, district cooling and ice-cooled food production and processing.

【0002】[0002]

【従来の技術】図12は、例えば特開平3−91635
号公報に記載の、第1の従来の氷蓄熱装置を示す構成図
である。図において、1は冷凍機であり、圧縮機2、凝
縮器3、流量制御弁4、蒸発器5を主要構成機器として
備えている。6は過冷却を安定して大きくとれるような
添加物、例えばカリウム塩またはナトリウム塩を添加し
た水溶液、7は水溶液6に浮遊したシャーベット状の
氷、8は水溶液6と微細な氷粒子からなるシャーベット
状の氷7を蓄える蓄熱槽、9は蒸発器5により過冷却さ
れた水溶液の過冷却を解除し、シャーベット状の氷7を
生成させる過冷却解除手段であり、例えば所定の大きさ
の氷塊で過冷却水溶液の出口近傍に設けられている。1
0は水溶液6を循環させる水循環ポンプ、11は一方を
蓄熱槽8に接続し、水循環ポンプ10、蒸発器5を順次
接続して、蒸発器5によって過冷却された水溶液6を過
冷却解除手段9へ導く水循環路である。なお、水溶液6
は添加物を加えず、単に水のみを使用する場合もある。
2. Description of the Related Art FIG. 12 shows, for example, Japanese Patent Laid-Open No. 3-91635.
It is a block diagram which shows the 1st conventional ice heat storage device of the publication. In the figure, reference numeral 1 denotes a refrigerator, which includes a compressor 2, a condenser 3, a flow control valve 4, and an evaporator 5 as main constituent devices. 6 is an aqueous solution to which an additive such as potassium salt or sodium salt is added so that supercooling can be stably taken large, 7 is sherbet-like ice suspended in the aqueous solution 6, and 8 is a sherbet composed of the aqueous solution 6 and fine ice particles. A heat storage tank for storing ice-shaped ice 7, and 9 is a supercooling releasing means for releasing supercooling of the aqueous solution supercooled by the evaporator 5 and generating sherbet-shaped ice 7, for example, an ice block of a predetermined size. It is provided near the outlet of the supercooled aqueous solution. 1
0 is a water circulation pump for circulating the aqueous solution 6, 11 is one of which is connected to the heat storage tank 8, the water circulation pump 10 and the evaporator 5 are sequentially connected, and the aqueous solution 6 supercooled by the evaporator 5 is supercooled releasing means 9 It is a water circuit leading to. The aqueous solution 6
In some cases, no additives are added and only water is used.

【0003】次に動作について説明する。冷凍機1の蒸
発器5により氷点以下数度(約−2℃程度)まで過冷却
された水溶液6は、水循環路11を通って蓄熱槽8上部
に設けられた過冷却解除手段9である、所定の大きさの
氷塊により過冷却状態が破られて過冷却熱量に相当する
シャーベット状の氷7となる。このシャーベット状の氷
7は、氷とならなかった残りの水溶液6とともに蓄熱槽
8に流入し、蓄熱槽8内で氷点温度0℃の水溶液6の上
部に浮遊する。蓄熱槽8の下部の水溶液6は水循環ポン
プ10によって冷凍機1に送水され、サイクルを構成し
ている。
Next, the operation will be described. The aqueous solution 6 supercooled to several degrees below the freezing point (about −2 ° C.) by the evaporator 5 of the refrigerator 1 is the supercooling releasing means 9 provided on the upper part of the heat storage tank 8 through the water circulation path 11. The supercooled state is broken by an ice lump of a predetermined size, and sherbet-shaped ice 7 corresponding to the amount of heat of supercooling is obtained. The sorbet-shaped ice 7 flows into the heat storage tank 8 together with the remaining aqueous solution 6 that has not turned into ice, and floats in the heat storage tank 8 above the aqueous solution 6 having a freezing point temperature of 0 ° C. The aqueous solution 6 in the lower part of the heat storage tank 8 is sent to the refrigerator 1 by the water circulation pump 10 to form a cycle.

【0004】さらに、図13は例えば実公平4ー381
78号公報に記載の、第2の従来の氷蓄熱装置を示す構
成図である。図において、1は冷凍機であり、圧縮機
2、凝縮器3、第1流量制御弁4、第1蒸発器5を主要
構成機器として備えている。6は水溶液、7は水溶液6
に浮遊したシャーベット状の氷、8は水溶液6とシャー
ベット状の氷7を蓄える蓄熱槽である。10は水溶液6
を循環させる第1水循環ポンプ、11は一方を蓄熱槽8
に接続し、第1水循環ポンプ10、第1蒸発器5を順次
接続して、第1蒸発器5によって冷却された水溶液6を
蓄熱槽8へ導く第1水循環路、12bは熱負荷、13b
は蓄熱槽8に蓄えた水溶液6を熱負荷12bに送る第2
水循環ポンプ、14bは一方を蓄熱槽8に接続し、第2
水循環ポンプ13b、熱負荷12bを順次接続して、冷
凍機1で冷却され、蓄熱槽8に蓄えた水溶液6を熱負荷
12bへ導く第2水循環路である。さらに、15bは蓄
熱槽8内に設置し、蓄熱槽8に蓄えた水溶液6を冷却す
る第2蒸発器、16は第2蒸発器の外周に生成した氷塊
状の氷、17bは第2蒸発器15bを流れる冷媒量を制
御する第2流量制御弁、18bは一方を凝縮器3と第1
流量制御弁4の間に接続し、第2流量制御弁17b、第
2蒸発器15bを順次接続し、他方を第1蒸発器5と圧
縮機2の間に接続した冷媒バイパス流路であり、第2蒸
発器15b及び第2流量制御弁17bは、第1蒸発器5
及び第1流量制御弁4と並列接続されている。
Further, FIG. 13 shows, for example, actual fairness 4-381.
It is a block diagram which shows the 2nd conventional ice heat storage apparatus of the 78th publication. In the figure, reference numeral 1 denotes a refrigerator, which includes a compressor 2, a condenser 3, a first flow rate control valve 4, and a first evaporator 5 as main components. 6 is an aqueous solution, 7 is an aqueous solution 6
Sherbet-like ice floating on the surface, and 8 is a heat storage tank for storing the aqueous solution 6 and the sherbet-like ice 7. 10 is an aqueous solution 6
Water circulation pump for circulating water, 11 is one of the heat storage tanks 8
, A first water circulation pump 10 and a first evaporator 5 are sequentially connected to guide the aqueous solution 6 cooled by the first evaporator 5 to the heat storage tank 8, 12b is a heat load, 13b
Is the second for sending the aqueous solution 6 stored in the heat storage tank 8 to the heat load 12b.
One of the water circulation pump, 14b is connected to the heat storage tank 8, and the second
This is a second water circulation path in which the water circulation pump 13b and the heat load 12b are sequentially connected, and the aqueous solution 6 cooled by the refrigerator 1 and stored in the heat storage tank 8 is guided to the heat load 12b. Further, 15b is a second evaporator that is installed in the heat storage tank 8 and cools the aqueous solution 6 stored in the heat storage tank 8, 16 is ice block-like ice generated on the outer periphery of the second evaporator, and 17b is a second evaporator. A second flow control valve for controlling the amount of the refrigerant flowing through 15b, and 18b is provided with one of the condenser 3 and the first
Is a refrigerant bypass flow path connected between the flow rate control valve 4, the second flow rate control valve 17b and the second evaporator 15b are sequentially connected, and the other is connected between the first evaporator 5 and the compressor 2; The second evaporator 15b and the second flow control valve 17b are connected to the first evaporator 5
And the first flow control valve 4 are connected in parallel.

【0005】次に動作について説明する。冷凍機1の第
1蒸発器5により氷点以下数度(約−2℃程度)まで過
冷却された水溶液6は、第1水循環路11を通って蓄熱
槽8に導かれ、蓄熱槽8内で過冷却状態が破られて過冷
却熱量に相当するシャーベット状の氷7となる。このシ
ャーベット状の氷7は、氷とならなかった残りの水溶液
6とともに蓄熱槽8に流入し、蓄熱槽8内で氷点温度0
℃の水溶液6の上部に浮遊する。蓄熱槽8の下部の水溶
液6は第1水循環ポンプ10によって冷凍機1に送水さ
れサイクルを構成している。同時に蓄熱槽8内の水溶液
6は第2蒸発器15bによって冷却され、第2蒸発器1
5bの外周に氷塊状氷16を生成する。
Next, the operation will be described. The aqueous solution 6 supercooled to a few degrees below the freezing point (about −2 ° C.) by the first evaporator 5 of the refrigerator 1 is guided to the heat storage tank 8 through the first water circulation path 11 and is stored in the heat storage tank 8. The supercooled state is broken to become sherbet-shaped ice 7 corresponding to the amount of supercooled heat. The sorbet-shaped ice 7 flows into the heat storage tank 8 together with the remaining aqueous solution 6 that has not turned into ice, and the freezing point temperature 0 is set in the heat storage tank 8.
Float above the aqueous solution 6 at 0 ° C. The aqueous solution 6 in the lower part of the heat storage tank 8 is sent to the refrigerator 1 by the first water circulation pump 10 to form a cycle. At the same time, the aqueous solution 6 in the heat storage tank 8 is cooled by the second evaporator 15b, and the second evaporator 1b
Ice block ice 16 is generated on the outer periphery of 5b.

【0006】[0006]

【発明が解決しようとする課題】従来の氷蓄熱装置は以
上のように構成されており、第1の従来の氷蓄熱装置に
おいては、蓄熱槽に蓄えられた氷はすべて過冷却水から
生成した氷である。この氷は、氷粒子と氷粒子の間に多
量の水分を含んだシャーベット状の氷であることから (1)蓄熱槽に蓄えられる氷の量が少ない。これによ
り、熱負荷に相当する熱量を蓄熱するためには、大きな
蓄熱槽が必要である。 (2)上記の課題を解消するために、氷の濃度を蓄熱槽
全体にわたって一様にしようとして、攪拌機などの氷水
混合手段を蓄熱槽に設置して蓄熱槽内の氷と水溶液をか
き混ぜると、水溶液を過冷却する蒸発器の中にごみや微
細な氷が大量に流入して過冷却が破れ、流路が凍結した
り、またはごみや氷の流入を防ぐフィルタなどの氷除去
装置の目詰まりなどを生じる。 (3)シャーベット状の氷と水溶液を混ぜた氷水は、非
常に流動性に優れていることから、熱負荷に氷水を送
れ、氷の大きな融解潜熱を利用できるため、ポンプに要
する動力を大幅に低減できる。しかし、従来の装置で
は、氷水を蓄熱槽から熱負荷に送るために、蓄熱槽内の
氷と水溶液をかき混ぜる攪拌機などの氷水混合手段を設
置する必要があり、この場合、上記と同様の問題を生じ
る。などの欠点があった。
The conventional ice heat storage device is configured as described above, and in the first conventional ice heat storage device, all the ice stored in the heat storage tank is generated from the supercooled water. It's ice. Since this ice is sherbet-like ice containing a large amount of water between the ice particles, (1) the amount of ice stored in the heat storage tank is small. As a result, a large heat storage tank is required to store the amount of heat corresponding to the heat load. (2) In order to solve the above problems, if ice water mixing means such as a stirrer is installed in the heat storage tank and the ice and the aqueous solution in the heat storage tank are stirred to try to make the ice concentration uniform throughout the heat storage tank, A large amount of dust and fine ice flow into the evaporator that supercools the aqueous solution and breaks the supercooling, freezing the flow path or clogging the ice removal device such as a filter that prevents the inflow of dust and ice. And so on. (3) Ice water, which is a mixture of sherbet-like ice and an aqueous solution, has very good fluidity, so ice water can be sent to a heat load and a large latent heat of melting of ice can be used, so that the power required for the pump is greatly increased. It can be reduced. However, in the conventional device, in order to send the ice water from the heat storage tank to the heat load, it is necessary to install an ice water mixing means such as a stirrer that stirs the ice and the aqueous solution in the heat storage tank. Occurs. There were drawbacks such as.

【0007】また、第2の従来の氷蓄熱装置は、蓄熱槽
の中にシャーベット状の氷と氷塊状氷が共存し、シャー
ベット状の氷が第2蒸発器の外周に生成した氷塊状氷と
付着するため、 (1)氷塊状氷の上部にシャーベット状の氷が山のよう
に盛り上がるほか、水溶液中で大きな氷の固まりができ
ることから、蓄熱槽内に一様に氷を蓄えることができな
い。したがって、熱負荷に相当する熱量を蓄熱するため
に、大きな蓄熱槽が必要となる。 (2)シャーベット状の氷は非常に微細で、氷塊状氷に
比べて融けやすいため熱負荷に対する追随性が非常に良
いが、該氷蓄熱装置では上記(1)の理由から、この長
所がなくなり追随性が悪い。 (3)蓄熱槽に蓄えた氷が堅い固まりとなるため、容易
に熱負荷に氷水を送ることができないため、第2水循環
ポンプに要する動力が大きい。などの欠点があった。
In the second conventional ice heat storage device, sherbet-like ice and ice block ice coexist in the heat storage tank, and the sherbet ice and ice block ice generated on the outer periphery of the second evaporator. As a result, (1) sherbet-like ice rises like a mountain above the ice block-like ice, and large ice blocks form in the aqueous solution, which makes it impossible to store the ice uniformly in the heat storage tank. Therefore, a large heat storage tank is required to store the amount of heat corresponding to the heat load. (2) Sherbet-shaped ice is very fine and melts more easily than ice-massed ice, so it has very good followability to heat load. However, the ice heat storage device does not have this advantage due to the reason (1) above. The followability is poor. (3) Since the ice stored in the heat storage tank becomes a hard mass, ice water cannot be easily sent to the heat load, so that the second water circulation pump requires a large amount of power. There were drawbacks such as.

【0008】本発明はこのような問題点を解消するため
になされたものであり、 (1)蓄熱槽が小型。 (2)熱負荷で利用する熱量の変化に対する追随性がよ
い。 (3)熱負荷に氷と水溶液を混ぜて送り、ポンプ動力が
低減できる。 (4)水溶液を安定して過冷却できる。 を実現できる氷蓄熱装置を得ることを目的とする。
The present invention has been made to solve the above problems, and (1) the heat storage tank is small. (2) Good followability to changes in the amount of heat used under heat load. (3) Pump power can be reduced by sending ice load and an aqueous solution mixed with the heat load. (4) The aqueous solution can be stably supercooled. An object is to obtain an ice heat storage device that can realize the above.

【0009】[0009]

【課題を解決するための手段】本発明の請求項1に係る
氷蓄熱装置は、第1蒸発器と第2蒸発器を有する冷凍
機、第1蒸発器により過冷却される水または水に添加物
を添加した水溶液の過冷却を解除し、シャーベット状の
氷を生成させる過冷却解除手段、上記シャーベット状の
氷を蓄える第1蓄熱槽、第1蓄熱槽内の水または水溶液
を第1蒸発器に送り循環させる第1水循環ポンプ、第1
蓄熱槽内の水もしくは水溶液、またはシャーベット状の
氷が混合した氷水を熱負荷に送り循環させる第2水循環
ポンプ、第2蒸発器を槽内に配し、第2蒸発器の外周に
生成する氷塊状の氷を蓄える第2蓄熱槽、並びに第1蓄
熱槽と第2蓄熱槽を接続する連通管を備え、第2蓄熱
槽、第1水循環ポンプ、第1蒸発器、第1蓄熱槽、連通
管の順で上記水または水溶液が循環する第1水循環路
と、第1蓄熱槽、第2水循環ポンプ、熱負荷、第2蓄熱
槽、連通管の順で上記水もしくは水溶液、または上記氷
水が循環する第2水循環路を構成したものである。
An ice heat storage device according to claim 1 of the present invention is a refrigerator having a first evaporator and a second evaporator, water supercooled by the first evaporator, or added to water. Supercooling releasing means for releasing supercooling of the aqueous solution containing the substances to generate sherbet-like ice, a first heat storage tank for storing the sherbet-like ice, and a first evaporator for water or aqueous solution in the first heat storage tank. First water circulation pump to feed and circulate to
A second water circulation pump that sends water or an aqueous solution in a heat storage tank or ice water mixed with sherbet-like ice to a heat load and circulates it, and arranges a second evaporator in the tank, and an ice block that forms on the outer periphery of the second evaporator Second heat storage tank for storing ice-like ice, and a communication pipe connecting the first heat storage tank and the second heat storage tank, the second heat storage tank, the first water circulation pump, the first evaporator, the first heat storage tank, the communication pipe The water or aqueous solution or the ice water circulates in the order of the first water circulation path through which the water or aqueous solution circulates, the first heat storage tank, the second water circulation pump, the heat load, the second heat storage tank, and the communication pipe. The second water circulation path is configured.

【0010】本発明の請求項2に係る氷蓄熱装置は、第
1蒸発器を流れる冷媒の流量と第2蒸発器を流れる冷媒
の流量を制御する制御手段を設けたものである。
The ice heat storage device according to claim 2 of the present invention is provided with a control means for controlling the flow rate of the refrigerant flowing through the first evaporator and the flow rate of the refrigerant flowing through the second evaporator.

【0011】本発明の請求項3に係る氷蓄熱装置は、蒸
発器を有し、少なくとも0℃において凝固しない不凍液
を冷却する冷凍機、この冷凍機により冷却された上記不
凍液と、水または水に添加物を添加した水溶液を熱交換
させて上記水または水溶液を過冷却する過冷却水生成熱
交換器、上記冷凍機により冷却された上記不凍液と、水
または水に添加物を添加した水溶液を熱交換させて氷塊
状の氷を生成する氷塊状氷生成熱交換器、上記過冷却水
生成熱交換器及び上記氷塊状氷生成熱交換器に上記不凍
液を送る不凍液循環ポンプ、過冷却された上記水または
水溶液の過冷却を解除し、シャーベット状の氷を生成さ
せる過冷却解除手段、上記シャーベット状の氷を蓄える
第1蓄熱槽、第1蓄熱槽内の水または水溶液を上記過冷
却水生成熱交換器に送り循環させる第1水循環ポンプ、
第1蓄熱槽内の水もしくは水溶液、またはシャーベット
状の氷が混合した氷水を熱負荷に送り循環させる第2水
循環ポンプ、上記氷塊状氷生成熱交換器を槽内に配し、
上記氷塊状氷生成熱交換器の外周に生成する氷塊状の氷
を蓄える第2蓄熱槽、並びに第1蓄熱槽と第2蓄熱槽を
接続する連通管を備え、上記蒸発器、不凍液循環ポン
プ、氷塊状氷生成熱交換器及び過冷却水生成熱交換器の
順で上記不凍液が循環する不凍液循環路と、第2蓄熱
槽、第1水循環ポンプ、過冷却水生成熱交換器、第1蓄
熱槽、連通管の順で上記水または水溶液が循環する第1
水循環路と、第1蓄熱槽、第2水循環ポンプ、熱負荷、
第2蓄熱槽、連通管の順で上記水もしくは水溶液、また
は上記氷水が循環する第2水循環路を構成したものであ
る。
According to a third aspect of the present invention, there is provided an ice heat storage device, which has an evaporator and cools an antifreeze liquid that does not solidify at least 0 ° C., and the antifreeze liquid cooled by the refrigerator and water or water. A supercooled water generation heat exchanger that heat-exchanges an aqueous solution containing an additive to supercool the water or the aqueous solution, heats the antifreeze solution cooled by the refrigerator, and water or an aqueous solution containing the additive added to the water. An ice block ice generation heat exchanger for exchanging to generate ice block ice, the supercooled water generation heat exchanger and an antifreeze circulation pump for sending the antifreeze liquid to the ice block ice generation heat exchanger, the supercooled water Alternatively, a supercooling releasing means for releasing supercooling of the aqueous solution to generate sherbet-like ice, a first heat storage tank for storing the sherbet-like ice, and water or an aqueous solution in the first heat storage tank for the supercooled water generation heat exchange vessel The first water circulation pump for feeding circulation,
A second water circulation pump for sending water or an aqueous solution in the first heat storage tank or ice water mixed with sherbet-like ice to a heat load to circulate it, and arranging the ice-lumped ice-generating heat exchanger in the tank,
The evaporator, the antifreeze circulation pump, the second heat storage tank for storing the ice-lump-like ice generated on the outer circumference of the ice-lump-shaped ice generation heat exchanger, and the communication pipe connecting the first heat storage tank and the second heat storage tank, An antifreeze liquid circulation path through which the above antifreeze liquid circulates in the order of an ice block ice formation heat exchanger and a supercooling water generation heat exchanger, a second heat storage tank, a first water circulation pump, a supercooling water generation heat exchanger, and a first heat storage tank. First, the water or aqueous solution is circulated in the order of the communication pipe
Water circulation path, first heat storage tank, second water circulation pump, heat load,
A second heat storage tank and a communication pipe constitute a second water circulation path in which the water or the aqueous solution or the ice water is circulated in this order.

【0012】本発明の請求項4に係る氷蓄熱装置は、氷
塊状氷生成熱交換器を流れる不凍液の流量と、過冷却水
生成熱交換器を流れる不凍液の流量を制御する制御手段
を設けたものである。
According to a fourth aspect of the present invention, the ice heat storage device is provided with a control means for controlling the flow rate of the antifreeze liquid flowing through the ice block ice generating heat exchanger and the flow rate of the antifreeze liquid flowing through the supercooled water generating heat exchanger. It is a thing.

【0013】本発明の請求項5に係る氷蓄熱装置は、第
1蓄熱槽内に、第1蓄熱槽内のシャーベット状の氷と水
または水溶液とを混合する氷水混合手段を設けたもので
ある。
According to a fifth aspect of the present invention, there is provided the ice heat storage device, wherein the first heat storage tank is provided with ice water mixing means for mixing the sherbet-shaped ice in the first heat storage tank with water or an aqueous solution. .

【0014】本発明の請求項6に係る氷蓄熱装置は、第
2水循環路に、水または水溶液が熱負荷から第1蓄熱槽
に送水される流路を設けるとともに、上記熱負荷から第
1蓄熱槽に送水される流路と上記熱負荷から第2蓄熱槽
に送水される流路とを切り替える流路切り替え手段を設
けたものである。
According to a sixth aspect of the present invention, there is provided an ice heat storage device, wherein the second water circulation path is provided with a flow path through which water or an aqueous solution is fed from the heat load to the first heat storage tank, and the first heat storage is carried out from the heat load. A flow path switching means is provided for switching between a flow path of water supplied to the tank and a flow path of water supplied from the heat load to the second heat storage tank.

【0015】本発明の請求項7に係る氷蓄熱装置は、第
1水循環路に、水または水溶液が第1蒸発器または過冷
却水生成熱交換器から第2蓄熱槽に送水される流路を設
けるとともに、第1蒸発器または過冷却水生成熱交換器
から第2蓄熱槽に送水される流路と、第1蒸発器または
過冷却水生成熱交換器から第1蓄熱槽に送水される流路
とを切り替える流路切り替え手段を設けたものである。
According to a seventh aspect of the present invention, in the ice heat storage device, the first water circulation path has a flow path through which water or an aqueous solution is fed from the first evaporator or the supercooled water generation heat exchanger to the second heat storage tank. A flow path for providing water to the second heat storage tank from the first evaporator or supercooling water generation heat exchanger and a flow of water to be supplied from the first evaporator or supercooling water generation heat exchanger to the first heat storage tank A flow path switching means for switching between the path and the path is provided.

【0016】本発明の請求項8に係る氷蓄熱装置は、第
1水循環路に、水または水溶液が第1蓄熱槽から第1蒸
発器または過冷却水生成熱交換器に送水される流路を設
けるとともに、第1蓄熱槽から第1蒸発器または過冷却
水生成熱交換器に送水される流路と、第2蓄熱槽から第
1蒸発器または過冷却水生成熱交換器に送水される流路
とを切り替える流路切り替え手段を設けたものである。
In the ice heat storage device according to the eighth aspect of the present invention, the first water circulation path has a flow path through which water or an aqueous solution is sent from the first heat storage tank to the first evaporator or the supercooled water generation heat exchanger. A flow path for providing water from the first heat storage tank to the first evaporator or the supercooling water generation heat exchanger, and a flow for supplying water from the second heat storage tank to the first evaporator or the supercooling water generation heat exchanger A flow path switching means for switching between the path and the path is provided.

【0017】本発明の請求項9に係る氷蓄熱装置は、請
求項8に係る氷蓄熱装置の、第2水循環路に、水または
水溶液が熱負荷から第1蓄熱槽に送水される流路を設け
るとともに、上記熱負荷から第1蓄熱槽に送水される流
路と上記熱負荷から第2蓄熱槽に送水される流路とを切
り替える流路切り替え手段を設けたものである。
According to a ninth aspect of the present invention, there is provided an ice heat storage device according to the eighth aspect, wherein the second water circulation passage has a flow path through which water or an aqueous solution is fed from a heat load to the first heat storage tank. Along with being provided, a flow passage switching means is provided for switching between a flow passage from the heat load to the first heat storage tank and a flow passage from the heat load to the second heat storage tank.

【0018】[0018]

【作用】請求項1に係わる氷蓄熱装置では、第1蓄熱槽
に、第1蒸発器で水または水溶液を過冷却し、過冷却解
除手段で水または水溶液の過冷却を解除して生成したシ
ャーベット状の氷を蓄える。また第2蓄熱槽に、第2蒸
発器の外周に生成した氷塊状の氷を蓄える。従って、 (1)第1蓄熱槽に蓄えたシャーベット状の氷は大きな
固まりにならず、流動性を保つことができる。また、シ
ャーベット状の氷は氷の粒径が小さいため、熱負荷に対
する追随性がよい。 (2)第1蓄熱槽内にシャーベット状の氷を一様に蓄え
ることができ、かつ氷塊状氷をシャーベット状の氷より
高い氷充填率で第2蓄熱槽に蓄えることができるため、
蓄熱槽を小型化できる。 (3)第2蓄熱槽に蓄えた氷塊状氷は、第1蓄熱槽から
第2水循環ポンプで熱負荷に送られ熱交換して0℃以上
に温度が上昇した水または水溶液を冷却するために利用
する。このため、当然のことながら第2蓄熱槽には熱負
荷に氷水を送るための装置、たとえばシャーベット状の
氷と水または水溶液とを混ぜる攪拌機などの氷水混合装
置が不要である。 (4)第2蓄熱槽に蓄えられた氷塊状氷が微細な氷やゴ
ミを捕獲するなどの効果が生じ、第2蓄熱槽から蒸発器
に送られ過冷却される水には、ごみ、氷や、解除されな
かった過冷却水が混ざらない。または、ごみ、氷の流入
を防ぐために第2蓄熱槽から蒸発器にいたる流路にフィ
ルタなどの氷除去装置を設けても目詰まりなどを生じな
い。これにより、蒸発器で安定して水または水溶液を過
冷却でき、連続的にシャーベット状の氷を生成できると
ともに、高効率な冷凍機の運転が行える。
In the ice heat storage device according to the first aspect of the present invention, in the first heat storage tank, the sorbet generated by supercooling the water or the aqueous solution by the first evaporator and releasing the supercooling of the water or the aqueous solution by the supercooling releasing means. Store ice cubes. In addition, the ice cube-shaped ice generated on the outer periphery of the second evaporator is stored in the second heat storage tank. Therefore, (1) the sherbet-shaped ice stored in the first heat storage tank does not form a large lump and the fluidity can be maintained. Further, the sherbet-like ice has a small ice particle size, and therefore has a good followability to a heat load. (2) Since sherbet-shaped ice can be uniformly stored in the first heat storage tank, and ice block ice can be stored in the second heat storage tank at a higher ice filling rate than that of the sherbet-shaped ice.
The heat storage tank can be miniaturized. (3) In order to cool the water or the aqueous solution whose ice block-like ice stored in the second heat storage tank is sent from the first heat storage tank to the heat load by the second water circulation pump and exchanges heat to raise the temperature to 0 ° C. or higher. To use. Therefore, it goes without saying that the second heat storage tank does not require a device for sending ice water to a heat load, for example, an ice water mixing device such as a stirrer for mixing sherbet-shaped ice with water or an aqueous solution. (4) The ice block-like ice stored in the second heat storage tank has the effect of capturing fine ice and dust, and the water sent from the second heat storage tank to the evaporator and supercooled contains dust and ice. Or, the supercooled water that was not released does not mix. Alternatively, even if an ice removing device such as a filter is provided in the flow path from the second heat storage tank to the evaporator to prevent the inflow of dust and ice, clogging does not occur. As a result, it is possible to stably supercool the water or the aqueous solution in the evaporator, continuously generate sherbet-like ice, and operate the refrigerator with high efficiency.

【0019】請求項2に係わる氷蓄熱装置では、第1及
び第2蒸発器内の冷媒の流量を制御して、安定に水を過
冷却できる。また蒸発器内で過冷却が破れて流路が凍結
した場合でも、冷媒を第1蒸発器で液化させ、第2蒸発
器でガス化させるように制御することにより、凍結して
流路を塞いだ氷を加熱、融解させながら、第2蓄熱槽に
氷塊状氷を蓄えることができ、高効率な冷凍機の運転が
行える。
In the ice heat storage device according to the second aspect, the flow rate of the refrigerant in the first and second evaporators can be controlled to stably supercool the water. Even if the supercooling is broken in the evaporator and the flow path is frozen, the refrigerant is liquefied by the first evaporator and gasified by the second evaporator, so that the flow path is frozen and the flow path is blocked. While heating and melting the ice cubes, it is possible to store the ice blocks in the second heat storage tank, and it is possible to operate the refrigerator with high efficiency.

【0020】請求項3に係わる氷蓄熱装置では、冷凍機
で冷却された不凍液を不凍液循環ポンプで氷塊状氷生成
熱交換器と過冷却水生成熱交換器に送り、第1蓄熱槽に
は過冷却水生成熱交換器で水または水溶液を過冷却し、
過冷却解除手段で水または水溶液の過冷却を解除して生
成したシャーベット状の氷を蓄え、同時に第2蓄熱槽に
は氷塊状氷生成熱交換器の外周に生成した氷塊状の氷を
蓄えることにより、請求項1に係わる氷蓄熱装置と同様
のものが得られる。
In the ice heat storage device according to the third aspect, the antifreeze liquid cooled by the refrigerator is sent to the ice block-like ice formation heat exchanger and the supercooled water generation heat exchanger by the antifreeze liquid circulation pump, and the first heat storage tank stores the excess heat. Supercool water or aqueous solution with a cooling water generation heat exchanger,
To store sherbet-like ice generated by removing supercooling of water or an aqueous solution by the supercooling releasing means, and at the same time store ice-like ice formed in the outer periphery of the ice-lumped ice-generating heat exchanger in the second heat storage tank. As a result, the same device as the ice heat storage device according to the first aspect can be obtained.

【0021】請求項4に係わる氷蓄熱装置では、氷塊状
氷生成熱交換器を流れる不凍液の流量と、過冷却水生成
熱交換器を流れる不凍液の流量を制御して、安定に水を
過冷却できる。
According to the fourth aspect of the present invention, in the ice heat storage device, the flow rate of the antifreezing liquid flowing through the ice block ice generating heat exchanger and the flow rate of the antifreezing liquid flowing through the supercooled water generating heat exchanger are controlled to stably supercool the water. it can.

【0022】請求項5に係わる氷蓄熱装置では、第1蓄
熱槽内に氷水混合手段を設けるので、シャーベット状の
氷と水または水溶液とが混合した氷水を熱負荷に送るこ
とができ、水循環ポンプに要する動力を大幅に低減でき
る。また、上記氷水混合手段により第1蓄熱槽内の氷と
水溶液をかき混ぜることにより水溶液中に発生するごみ
や微細な氷は、第2蓄熱槽に蓄えられた氷塊状氷により
捕獲されるため、上記と同様、水溶液を安定して過冷却
でき、高効率な冷凍機の運転が行える。
In the ice heat storage device according to the fifth aspect, since the ice water mixing means is provided in the first heat storage tank, the ice water in which the sherbet-like ice and water or the aqueous solution are mixed can be sent to the heat load, and the water circulation pump. The power required for can be greatly reduced. Further, dust and fine ice generated in the aqueous solution by stirring the ice in the first heat storage tank with the aqueous solution by the ice water mixing means are captured by the ice block ice stored in the second heat storage tank. Similarly, the aqueous solution can be stably supercooled, and the refrigerator can be operated with high efficiency.

【0023】請求項6に係わる氷蓄熱装置では、熱負荷
出口の水または水溶液の温度が0℃以下の場合に第1蓄
熱槽に送水する流路に切り替え、0℃を越える温度の場
合に第2蓄熱槽に送水する流路に切り替えることができ
る。これにより、第1蓄熱槽に蓄えたシャーベット状の
氷を溶かすことなく利用でき、長い時間氷水を熱負荷に
送り続けることができ、流量が小さくできるので、第2
水循環ポンプに要する動力を低減できる。さらに、第2
蓄熱槽に蓄えられた水または水溶液の温度を第1蓄熱槽
に蓄えられた水または水溶液の温度より高くできるた
め、高い温度の水または水溶液を蒸発器に送水でき、高
効率な冷凍機の運転が行える。
In the ice heat storage device according to the sixth aspect, when the temperature of the water or aqueous solution at the heat load outlet is 0 ° C. or lower, the flow path is switched to the water flow to the first heat storage tank, and when the temperature exceeds 0 ° C. 2 It is possible to switch to a flow path for supplying water to the heat storage tank. As a result, the sherbet-shaped ice stored in the first heat storage tank can be used without melting, the ice water can be continuously sent to the heat load for a long time, and the flow rate can be reduced.
The power required for the water circulation pump can be reduced. Furthermore, the second
Since the temperature of the water or aqueous solution stored in the heat storage tank can be made higher than the temperature of the water or aqueous solution stored in the first heat storage tank, it is possible to send the water or aqueous solution of high temperature to the evaporator, and operate the refrigerator with high efficiency. Can be done.

【0024】請求項7に係わる氷蓄熱装置では、第1蒸
発器または過冷却水生成熱交換器で冷却された過冷却水
または冷水が0℃を越える温度の場合、第2蓄熱槽に送
水する流路に切り替え、0℃以下の場合、第1蓄熱槽に
送水する流路に切り替えることができる。これにより請
求項6に係わる氷蓄熱装置と同様のものが得られる。
In the ice heat storage device according to the seventh aspect, when the supercooled water or the cold water cooled by the first evaporator or the supercooled water generation heat exchanger has a temperature exceeding 0 ° C., the water is sent to the second heat storage tank. If the temperature is 0 ° C. or lower, it is possible to switch to the flow path for supplying water to the first heat storage tank. As a result, the same device as the ice heat storage device according to claim 6 is obtained.

【0025】請求項8に係わる氷蓄熱装置では、第2蓄
熱槽に蓄えられた水または水溶液と第1蓄熱槽に蓄えら
れた水または水溶液の温度を比較して、高い温度の水ま
たは水溶液を第1蒸発器または過冷却水生成熱交換器に
送水するよう流路を切り替えることができる。これによ
り、高効率な冷凍機の運転が行える。
In the ice heat storage device according to the eighth aspect, the temperatures of the water or the aqueous solution stored in the second heat storage tank and the water or the aqueous solution stored in the first heat storage tank are compared with each other, and the high temperature water or the aqueous solution is stored. The flow path can be switched to feed water to the first evaporator or the supercooled water generation heat exchanger. This allows highly efficient operation of the refrigerator.

【0026】請求項9に係わる氷蓄熱装置では、請求項
8の作用に加え、第2蓄熱槽に蓄えられた水または水溶
液の温度が所定の温度を越える場合は、水または水溶液
を第1蓄熱槽から蒸発器に送水でき、第2蓄熱槽を水循
環路から分離できる。
In the ice heat storage device according to the ninth aspect, in addition to the operation of the eighth aspect, when the temperature of the water or the aqueous solution stored in the second heat storage tank exceeds a predetermined temperature, the water or the aqueous solution is stored as the first heat storage. Water can be sent from the tank to the evaporator, and the second heat storage tank can be separated from the water circulation path.

【0027】[0027]

【実施例】【Example】

実施例1.以下、本発明の一実施例を図について説明す
る。図1は本発明の実施例1による氷蓄熱装置を示す構
成図であり、図において、15aは圧縮機2と第1蒸発
器5の間に設けた第2蒸発器、20は第2蒸発器15a
を槽内に設け、この第2蒸発器15aの外周に生成する
氷塊状の氷16を蓄える第2蓄熱槽、21は一方を第1
蓄熱槽8に接続し、他方を第2蓄熱槽20に接続した連
通管、11は第2蓄熱槽20、第1水循環ポンプ10、
第1蒸発器5、第1蓄熱槽8、連通管21、第2蓄熱槽
20の順で循環するように構成した第1水循環路、22
は水または水溶液6にシャーベット状の氷7を混合する
氷水混合手段、12aは熱負荷、13aはこの熱負荷1
2aに氷水混合手段22で混合した水または水溶液6と
シャーベット状の氷7を混ぜた氷水を送る第2水循環ポ
ンプ、14aは第1蓄熱槽8、第2水循環ポンプ13
a、熱負荷12a、第2蓄熱槽20、連通管21、第1
蓄熱槽8の順で循環するように構成した第2水循環路で
ある。なお、その他の構成については第1の従来例と同
様につき説明を省略する。
Example 1. An embodiment of the present invention will be described below with reference to the drawings. 1 is a configuration diagram showing an ice heat storage device according to a first embodiment of the present invention. In the figure, 15a is a second evaporator provided between a compressor 2 and a first evaporator 5, and 20 is a second evaporator. 15a
Is provided in the tank, and the second heat storage tank 21 for storing the ice-lump-shaped ice 16 generated on the outer periphery of the second evaporator 15a, one of which is the first
A communication pipe connected to the heat storage tank 8 and the other to the second heat storage tank 20, 11 denotes the second heat storage tank 20, the first water circulation pump 10,
A first water circulation passage 22 configured to circulate in the order of the first evaporator 5, the first heat storage tank 8, the communication pipe 21, and the second heat storage tank 20,
Is an ice water mixing means for mixing the sherbet-like ice 7 with water or the aqueous solution 6, 12a is a heat load, 13a is this heat load 1
A second water circulation pump that sends ice water obtained by mixing the water or the aqueous solution 6 mixed by the ice water mixing means 22 and the sherbet-shaped ice 7 to 2a, 14a is the first heat storage tank 8, and the second water circulation pump 13
a, heat load 12a, second heat storage tank 20, communication pipe 21, first
It is a second water circulation passage configured to circulate in the order of the heat storage tank 8. The other configurations are the same as those in the first conventional example, and the description thereof will be omitted.

【0028】次に動作について説明する。第2蓄熱槽2
0に蓄えられた水または水溶液6は、冷凍機1の第1蒸
発器5で氷点以下数度(−2〜−5℃程度)まで過冷却
され、第1水循環路11を通って第1蓄熱槽8上部に設
けられた過冷却解除手段9である所定の大きさの氷塊に
より過冷却状態が破られて過冷却熱量に相当するシャー
ベット状の氷7になる。このシャーベット状の氷7は、
氷とならなかった残りの水溶液6とともに第1蓄熱槽8
に流入し、第1蓄熱槽8内で氷点温度0℃の水溶液6の
上部に浮遊する。第1蓄熱槽8の下部の水溶液6は連通
管21を通り、第2蓄熱槽20に流入し、第2蒸発器1
5aで冷却され、氷塊状の氷16になる。氷塊状の氷1
6とならなかった残りの水溶液6は、第1水循環ポンプ
10によって冷凍機1の第1蒸発器5に送られサイクル
を構成する。
Next, the operation will be described. Second heat storage tank 2
The water or aqueous solution 6 stored in 0 is supercooled to several degrees below the freezing point (about −2 to −5 ° C.) in the first evaporator 5 of the refrigerator 1, and passes through the first water circulation path 11 to generate the first heat storage. The supercooled state is broken by an ice block having a predetermined size, which is the supercooling releasing means 9 provided on the upper portion of the tank 8, and the sherbet-shaped ice 7 corresponding to the supercooling heat amount is obtained. This sherbet ice 7
The first heat storage tank 8 together with the remaining aqueous solution 6 that did not become ice
And floats above the aqueous solution 6 having a freezing point temperature of 0 ° C. in the first heat storage tank 8. The aqueous solution 6 in the lower part of the first heat storage tank 8 passes through the communication pipe 21 and flows into the second heat storage tank 20, and the second evaporator 1
It is cooled in 5a and becomes ice 16 in the form of ice blocks. Ice block ice 1
The remaining aqueous solution 6 that did not become 6 is sent to the first evaporator 5 of the refrigerator 1 by the first water circulation pump 10 to form a cycle.

【0029】一方、第1蓄熱槽8に蓄えられたシャーベ
ット状の氷7は、氷水混合手段22で水または水溶液6
と混ぜて熱負荷12aに送られ、室内の空気または室内
を冷却する水と熱交換し、シャーベット状の氷7が融け
て第2水循環路14aを通って第2蓄熱槽20に送水さ
れる。そして、第2蓄熱槽20内に設置した第2蒸発器
15aで冷却された後、連通管21を通り第1蓄熱槽8
に戻される。この水は再び氷水混合手段22でシャーベ
ット状の氷7と混ぜて、第2水循環ポンプ13aによっ
て熱負荷12aに送られサイクルを構成する。
On the other hand, the sherbet-shaped ice 7 stored in the first heat storage tank 8 is mixed with water or an aqueous solution 6 by the ice water mixing means 22.
Is mixed with and sent to the heat load 12a to exchange heat with the air in the room or the water for cooling the room, and the sherbet ice 7 is melted and sent to the second heat storage tank 20 through the second water circulation path 14a. Then, after being cooled by the second evaporator 15a installed in the second heat storage tank 20, the first heat storage tank 8 passes through the communication pipe 21.
Returned to. This water is mixed with the sherbet-shaped ice 7 again by the ice water mixing means 22, and is sent to the heat load 12a by the second water circulation pump 13a to form a cycle.

【0030】冷凍機1の動作を説明する。圧縮機2から
吐出されたガス冷媒は凝縮器3で冷却し液化して、流量
制御弁4で低圧まで減圧する。この低圧となった冷媒は
第1蒸発器5に流入し、第2蓄熱槽20から第1水循環
ポンプ10で送水される水または水溶液6と熱交換し、
さらに第2蒸発器15aに流入し、第2蓄熱槽20に蓄
えられている水または水溶液6と熱交換してガス状態と
なって再び圧縮機2に吸入される。
The operation of the refrigerator 1 will be described. The gas refrigerant discharged from the compressor 2 is cooled and liquefied by the condenser 3 and depressurized to a low pressure by the flow control valve 4. This low-pressure refrigerant flows into the first evaporator 5 and exchanges heat with the water or aqueous solution 6 sent from the second heat storage tank 20 by the first water circulation pump 10,
Further, it flows into the second evaporator 15a, exchanges heat with the water or the aqueous solution 6 stored in the second heat storage tank 20, becomes a gas state, and is sucked into the compressor 2 again.

【0031】以上のように、この実施例においては、第
1蓄熱槽8に、第1蒸発器5で水または水溶液6を過冷
却し、過冷却解除手段9で水または水溶液6の過冷却を
解除して生成したシャーベット状の氷7を蓄えると同時
に、第2蓄熱槽20に第2蒸発器15aの外周に生成し
た氷塊状氷16を蓄えることができる。このため、第1
蓄熱槽8に蓄えたシャーベット状の氷7は大きな固まり
にならず、流動性を保つことができるため、第1蓄熱槽
8内にシャーベット状の氷7を一様に蓄えることができ
る。同時に、氷塊状の氷16をシャーベット状の氷7よ
り高い氷充填率で第2蓄熱槽20に蓄えることができる
ため、第1蓄熱槽8を小型化できる。さらに、シャーベ
ット状の氷7は氷の粒径が小さいため、熱負荷に対する
追随性がよい。また、攪拌機などの氷水混合手段22
で、容易に水または水溶液6とシャーベット状の氷7を
混ぜて熱負荷12aに送れるため、第2水循環ポンプ1
3aに要する動力を大幅に低減できる。さらに、第2蓄
熱槽20に蓄えた氷塊状氷16は、第1蓄熱槽8から熱
負荷12aに送られ熱交換して0℃以上に温度が上昇し
た水または水溶液6を冷却するためだけに利用できる。
このため、当然のことながら第2蓄熱槽20にはシャー
ベット状の氷7と水または水溶液とを混ぜる攪拌機など
の氷水混合手段が不要である。一方、第1蓄熱槽8に上
記氷水混合手段を設置し、第1蓄熱槽内の氷と水溶液を
かき混ぜても、第2蓄熱槽20に蓄えられた氷塊状氷1
6が微細な氷を捕獲するなどの効果が生じるため、第2
蓄熱槽20から第1蒸発器5に送られ過冷却される水に
は、ごみ、氷や解除されなかった過冷却水が混ざらな
い。またはごみ、氷の流入を完全に防ぐために第2蓄熱
槽20から第1蒸発器5にいたる流路にフィルタなどの
氷除去装置を設けても目詰まりを生じない。これによ
り、第1蒸発器5では水または水溶液6を安定して過冷
却でき、連続にシャーベット状の氷7を生成できるとと
もに、高効率な冷凍機1の運転が行える。
As described above, in this embodiment, in the first heat storage tank 8, the water or aqueous solution 6 is supercooled by the first evaporator 5, and the water or aqueous solution 6 is supercooled by the supercooling releasing means 9. It is possible to store the sherbet-shaped ice 7 generated by releasing it and at the same time store the ice block-shaped ice 16 generated on the outer periphery of the second evaporator 15a in the second heat storage tank 20. Therefore, the first
Since the sherbet-shaped ice 7 stored in the heat storage tank 8 does not form a large lump and can maintain fluidity, the sherbet-shaped ice 7 can be stored uniformly in the first heat storage tank 8. At the same time, the ice block-shaped ice 16 can be stored in the second heat storage tank 20 at an ice filling rate higher than that of the sherbet-shaped ice 7, so that the first heat storage tank 8 can be downsized. Furthermore, since the sherbet-shaped ice 7 has a small ice grain size, it has good followability to heat load. In addition, ice water mixing means 22 such as a stirrer
Since the water or the aqueous solution 6 and the sherbet-shaped ice 7 can be easily mixed and sent to the heat load 12a, the second water circulation pump 1
The power required for 3a can be greatly reduced. Further, the ice block ice 16 stored in the second heat storage tank 20 is sent from the first heat storage tank 8 to the heat load 12a and exchanges heat to cool the water or the aqueous solution 6 whose temperature has risen to 0 ° C. or higher. Available.
Therefore, as a matter of course, the second heat storage tank 20 does not require an ice water mixing means such as a stirrer for mixing the sherbet-shaped ice 7 with water or an aqueous solution. On the other hand, even if the ice water mixing means is installed in the first heat storage tank 8 and the ice and the aqueous solution in the first heat storage tank are stirred, the ice block-shaped ice 1 stored in the second heat storage tank 20
Since 6 has the effect of capturing fine ice, the second
The water sent from the heat storage tank 20 to the first evaporator 5 and supercooled does not contain dust, ice, or uncooled supercooled water. Even if an ice removing device such as a filter is provided in the flow path from the second heat storage tank 20 to the first evaporator 5 to completely prevent the inflow of dust and ice, clogging does not occur. As a result, the first evaporator 5 can stably supercool the water or the aqueous solution 6, continuously generate sherbet-like ice 7, and operate the refrigerator 1 with high efficiency.

【0032】なお、上記実施例では、氷水混合手段22
でシャーベット状の氷7を水または水溶液6と混ぜて氷
水とし、熱負荷12aに送る装置について説明したが、
氷水混合手段22を用いず、第1蓄熱槽8に蓄えた水ま
たは水溶液6のみを熱負荷12aに送る装置について
も、第2水循環ポンプ13aに要する動力を低減する効
果以外は、同様の効果を得ることができる。
In the above embodiment, the ice water mixing means 22
In the above, a device for mixing the sherbet-shaped ice 7 with water or the aqueous solution 6 to form ice water and sending it to the heat load 12a has been described.
A device that sends only the water or the aqueous solution 6 stored in the first heat storage tank 8 to the heat load 12a without using the ice water mixing means 22 has the same effect except that the power required for the second water circulation pump 13a is reduced. Obtainable.

【0033】また、上記実施例では、第1蒸発器5と第
2蒸発器15aに一定量のシャーベット状の氷7と氷塊
状の氷16を生成する装置について説明したが、第2蒸
発器15aの出口に温度センサ−を設けて、その出口温
度、つまり冷媒の過熱度を所定の値に制御することによ
り、上記実施例の効果に加えて、熱負荷12aに送るた
めに蓄えるシャーベット状の氷7を所定の量蓄えなが
ら、熱負荷12aで必要な熱負荷量に応じて氷塊状の氷
16の量のみを調整できる。
Further, in the above-mentioned embodiment, the device for producing a certain amount of sherbet-shaped ice 7 and ice block-shaped ice 16 in the first evaporator 5 and the second evaporator 15a has been described, but the second evaporator 15a is described. In addition to the effect of the above-mentioned embodiment by providing a temperature sensor at the outlet of the device and controlling the temperature of the outlet, that is, the degree of superheat of the refrigerant, a sherbet-like ice to be stored for sending to the heat load 12a. It is possible to adjust only the amount of ice blocks 16 in accordance with the heat load required by the heat load 12a while storing 7 in a predetermined amount.

【0034】また、冷凍機1の容量制御手段、たとえば
圧縮機2の周波数制御手段などを設けることにより、熱
負荷12aに送るために蓄えるシャーベット状の氷7を
所定の量蓄えながら、熱負荷12aで必要な熱負荷量に
応じて氷塊状の氷16の量のみを調整できる。
Further, by providing the capacity control means of the refrigerator 1, for example, the frequency control means of the compressor 2, etc., the heat load 12a can be stored while storing a predetermined amount of sherbet-like ice 7 to be stored for sending to the heat load 12a. It is possible to adjust only the amount of ice cube-shaped ice 16 according to the required heat load.

【0035】また、上記実施例では第1蒸発器5と第2
蒸発器15aを直列に接続したものを示したが、第2の
従来例のように、並列接続した構成の冷凍機に対して、
本実施例と同様、第2蒸発器15aを槽内に配した第2
蓄熱槽20を設け、第2蓄熱槽、第1水循環ポンプ、第
1蒸発器、第1蓄熱槽、連通管の順で水または水溶液が
循環する第1水循環路と、第1蓄熱槽、第2水循環ポン
プ、熱負荷、第2蓄熱槽、連通管の順で水もしくは水溶
液、または氷水が循環する第2水循環路を構成しても良
い。
In the above embodiment, the first evaporator 5 and the second evaporator 5
Although the evaporators 15a connected in series are shown, as in the second conventional example, a refrigerator having a configuration in which they are connected in parallel is
As in the present embodiment, the second evaporator 15a in which the second evaporator 15a is arranged in the tank is used.
A heat storage tank 20 is provided, and a second heat storage tank, a first water circulation pump, a first evaporator, a first heat storage tank, and a communication pipe in which water or an aqueous solution circulates in that order, a first heat storage tank, and a second heat storage tank. A water circulation pump, a heat load, a second heat storage tank, and a communication pipe may be arranged in this order to form a second water circulation path through which water or an aqueous solution or ice water circulates.

【0036】実施例2.図2は本発明の実施例2による
氷蓄熱装置を示す構成図である。実施例1では、第1蒸
発器5と第2蒸発器15aにほぼ同じ圧力の冷媒が流入
する装置について説明したが、この実施例2の氷蓄熱装
置では、第1蒸発器5と第2蒸発器15aの間に第2流
量制御弁30を設け、第1蒸発器5を流れる冷媒の流量
と第2蒸発器15aを流れる冷媒の流量を制御する。な
お、その他の構成については実施例1と同様につき説明
を省略する。
Example 2. Second Embodiment FIG. 2 is a configuration diagram showing an ice heat storage device according to a second embodiment of the present invention. Although the device in which the refrigerant having substantially the same pressure flows into the first evaporator 5 and the second evaporator 15a has been described in the first embodiment, the ice heat storage device of the second embodiment includes the first evaporator 5 and the second evaporator. A second flow rate control valve 30 is provided between the evaporators 15a to control the flow rate of the refrigerant flowing through the first evaporator 5 and the flow rate of the refrigerant flowing through the second evaporator 15a. The other configurations are similar to those of the first embodiment, and the description thereof is omitted.

【0037】次に動作について説明する。第2水循環路
14a内の氷水の動作は、実施例1と同じであるが、冷
凍機1と第1水循環路11内の水または水溶液の動作が
異なるため、冷凍機1と第1水循環路11内の水または
水溶液6の動作について、主に説明する。
Next, the operation will be described. The operation of the ice water in the second water circulation passage 14a is the same as that of the first embodiment, but the operation of the water or the aqueous solution in the refrigerator 1 and the first water circulation passage 11 is different, so the refrigerator 1 and the first water circulation passage 11 are different. The operation of the water or the aqueous solution 6 therein will be mainly described.

【0038】この氷蓄熱装置には、第1蒸発器5内の水
または水溶液6が安定して過冷却状態まで冷却される場
合の第1の運転モードと、第1蒸発器5内で過冷却が破
れ、第1蒸発器5内の流路が凍結した場合の第2の運転
モードがある。以下、それぞれの運転モードについて説
明する。
The ice heat storage device has a first operation mode in which the water or aqueous solution 6 in the first evaporator 5 is stably cooled to a supercooled state, and a subcooling in the first evaporator 5. Is broken and the flow path in the first evaporator 5 is frozen, there is a second operation mode. Hereinafter, each operation mode will be described.

【0039】第1の運転モード(安定した過冷却水の生
成運転)では、図3の圧力−エンタルピ図に示すよう
に、第1蒸発器5でガス化しながら水または水溶液6と
熱交換する冷媒の圧力(図中のA→B間の圧力)を、水
または水溶液6が安定して過冷却できる圧力になるよう
に第2流量制御弁30で制御する。他の動作について
は、実施例1と同様につき説明を省略する。
In the first operation mode (stable operation of producing supercooled water), as shown in the pressure-enthalpy diagram of FIG. 3, a refrigerant that heat-exchanges with the water or aqueous solution 6 while being gasified in the first evaporator 5. The pressure (the pressure between A and B in the figure) is controlled by the second flow control valve 30 so that the water or the aqueous solution 6 can be stably supercooled. The other operations are similar to those of the first embodiment, and the description thereof will be omitted.

【0040】第2の運転モード(凍結時の運転)では、
第1流量制御弁4を全開し、図4の圧力−エンタルピ図
に示すように、凝縮器3から流出した冷媒(図中のA*
点)の冷媒は減圧されることなく、第1蒸発器5に流入
し(図中のA* 点)、第1蒸発器5内で流路を塞いだ氷
を加熱しながら液化して(図中のB* 点)、さらに第2
流量制御弁30で低圧まで減圧される(図中のC
* 点)。そして、この低圧となった冷媒は第2蒸発器1
5aに流入して(図中のC* 点)、第2蓄熱槽20に蓄
えられた水または水溶液6と熱交換してガス状態となっ
て(図中のD* 点)、圧縮機2に吸入される。また、水
循環ポンプ10は、停止した状態である。第2水循環路
内の氷水の動作については、実施例1と同様につき説明
を省略する。
In the second operation mode (operation during freezing),
The first flow rate control valve 4 is fully opened, and as shown in the pressure-enthalpy diagram of FIG. 4, the refrigerant flowing out from the condenser 3 (A * in the figure )
The refrigerant at the point) flows into the first evaporator 5 without being decompressed (point A * in the figure), and liquefies while heating the ice blocking the flow path in the first evaporator 5 (see the figure). (B * point in the middle), and second
The pressure is reduced to a low pressure by the flow control valve 30 (C in the figure).
* Point). Then, the low-pressure refrigerant becomes the second evaporator 1
5a (C * point in the figure) and exchanges heat with the water or the aqueous solution 6 stored in the second heat storage tank 20 to become a gas state (D * point in the figure), and enters the compressor 2. Inhaled. Further, the water circulation pump 10 is in a stopped state. The operation of the ice water in the second water circulation path is the same as that of the first embodiment, and the description thereof is omitted.

【0041】このように構成した氷蓄熱装置は、第1蒸
発器5内の冷媒の圧力を第2流量制御弁30で安定に水
を過冷却できる圧力に制御でき、同時に第2蒸発器15
aの圧力を冷凍機1が効率よく運転できる圧力に制御で
きるため、実施例1の効果に加えて、さらに安定してシ
ャーベット状の氷7を生成できる。さらに、第1蒸発器
5内で過冷却が破れて流路が凍結した場合でも、冷媒を
第1蒸発器5で液化させ第2蒸発器15aでガス化させ
るように、第1流量制御弁4と第2流量制御弁30を制
御することにより、凍結して流路を塞いだ氷を加熱、融
解させながら、第2蓄熱槽20に氷塊状氷16を蓄える
ことができ、高効率な冷凍機1の運転が行える。
In the ice heat storage device thus configured, the pressure of the refrigerant in the first evaporator 5 can be controlled by the second flow rate control valve 30 to a pressure at which water can be stably supercooled, and at the same time, the second evaporator 15 can be controlled.
Since the pressure of a can be controlled to a pressure at which the refrigerator 1 can be efficiently operated, in addition to the effect of the first embodiment, the sherbet-shaped ice 7 can be generated more stably. Further, even when the subcooling is broken in the first evaporator 5 and the flow path is frozen, the first flow control valve 4 is configured so that the refrigerant is liquefied in the first evaporator 5 and gasified in the second evaporator 15a. By controlling the second flow rate control valve 30 and the second flow control valve 30, the ice block ice 16 can be stored in the second heat storage tank 20 while heating and melting the ice that has frozen and blocked the flow path. 1 operation can be performed.

【0042】また、上記実施例では第2流量制御弁30
を設ける装置について説明したが、この第2流量制御弁
30のかわりに、毛細管などの減圧手段を設けても同様
の効果がある。
In the above embodiment, the second flow control valve 30 is used.
Although the device for providing the above has been described, the same effect can be obtained by providing a pressure reducing means such as a capillary tube instead of the second flow rate control valve 30.

【0043】実施例3.上記実施例2では、第1蒸発器
5内で過冷却が破れて流路が凍結した場合に、凝縮器3
と第1蒸発器5で冷媒を液化させて流路を塞いだ氷を加
熱する装置について説明したが、この実施例3の氷蓄熱
装置では、図5の構成図に示すように、一方を圧縮機2
と凝縮器3の間に接続し、他方を第1流量制御弁4と第
1蒸発器5の間に接続した冷媒バイパス流路31と、こ
の冷媒バイパス流路31の途中に開閉弁32を設けた構
成とする。なお、その他の構成については実施例2と同
様につき説明を省略する。
Example 3. In the second embodiment, when the subcooling is broken in the first evaporator 5 and the flow path is frozen, the condenser 3
The device for heating the ice that has liquefied the refrigerant in the first evaporator 5 and blocked the flow path has been described. However, in the ice heat storage device of the third embodiment, one is compressed as shown in the configuration diagram of FIG. Machine 2
And a condenser 3 and the other is connected between the first flow rate control valve 4 and the first evaporator 5, and a shutoff valve 32 is provided in the middle of the refrigerant bypass passage 31. It has a different configuration. The other configurations are the same as those in the second embodiment, and the description thereof is omitted.

【0044】次に動作について説明する。第2水循環路
14a内の氷水と第1水循環路11内の水または水溶液
の動作は、実施例2と全く同じであるが、冷凍機1の動
作が異なるため、冷凍機1の動作について、主に説明す
る。
Next, the operation will be described. The operations of the ice water in the second water circulation path 14a and the water or the aqueous solution in the first water circulation path 11 are exactly the same as those in the second embodiment, but the operation of the refrigerator 1 is different, so that the operation of the refrigerator 1 will be mainly described. Explained.

【0045】この氷蓄熱装置には、第1蒸発器5内の水
または水溶液6が安定して過冷却状態まで冷却される場
合の第1の運転モードと、第1蒸発器5内で過冷却が破
れ、第1蒸発器5内の流路が凍結した場合の第2の運転
モードがある。以下、それぞれの運転モードについて説
明する。
This ice heat storage device has a first operation mode in which the water or aqueous solution 6 in the first evaporator 5 is stably cooled to a supercooled state and a subcooling in the first evaporator 5. Is broken and the flow path in the first evaporator 5 is frozen, there is a second operation mode. Hereinafter, each operation mode will be described.

【0046】第1の運転モード(安定した過冷却水の生
成運転)では、開閉弁32を閉じる以外は、実施例2と
同様である。
The first operation mode (stable supercooling water generation operation) is the same as that of the second embodiment except that the on-off valve 32 is closed.

【0047】第2の運転モード(凍結時の運転)では、
第1流量制御弁4を全閉し、冷媒バイパス流路31の途
中に設けた開閉弁32を全開にして、圧縮機2を流出し
た冷媒は高温高圧の冷媒ガスとして第1蒸発器5に流入
し、第1蒸発器5内で流路を塞いだ氷を加熱しながら液
化して、第2流量制御弁30で低圧まで減圧される。そ
して、この低圧となった冷媒は第2蒸発器15aに流入
して、第2蓄熱槽20に蓄えられた水または水溶液6と
熱交換してガス状態となって、圧縮機2に吸入される。
第2水循環路内の氷水と水循環路内の水または水溶液の
動作については、実施例1と同様につき説明を省略す
る。
In the second operation mode (operation during freezing),
The first flow rate control valve 4 is fully closed, the on-off valve 32 provided in the middle of the refrigerant bypass passage 31 is fully opened, and the refrigerant flowing out of the compressor 2 flows into the first evaporator 5 as a high-temperature and high-pressure refrigerant gas. Then, the ice blocking the flow path in the first evaporator 5 is liquefied while being heated, and the pressure is reduced to a low pressure by the second flow rate control valve 30. Then, the low-pressure refrigerant flows into the second evaporator 15 a, exchanges heat with the water or the aqueous solution 6 stored in the second heat storage tank 20, becomes a gas state, and is sucked into the compressor 2. .
The operations of the ice water in the second water circulation path and the water or the aqueous solution in the water circulation path are the same as those in the first embodiment, and the description thereof is omitted.

【0048】このように構成した氷蓄熱装置は、実施例
2の効果に加えて、さらに効率よく凍結した流路を塞い
だ氷を加熱、融解させながら、第2蓄熱槽20に氷塊状
の氷16を蓄えることができる。
In addition to the effect of the second embodiment, the ice heat storage device configured as described above more efficiently heats and melts the ice that has blocked the frozen flow passage, while the second heat storage tank 20 holds the ice block-shaped ice. Can store 16.

【0049】また、上記実施例では第2流量制御弁30
を設ける装置について説明したが、この第2流量制御弁
30のかわりに、毛細管などの減圧手段を設けても同様
の効果がある。
Further, in the above embodiment, the second flow control valve 30
Although the device for providing the above has been described, the same effect can be obtained by providing a pressure reducing means such as a capillary tube instead of the second flow rate control valve 30.

【0050】実施例4.図6は本発明の実施例4による
氷蓄熱装置を示す構成図であり、図において、1は少な
くとも0℃において凝固しない不凍液を冷却する冷凍
機、40は冷凍機1により冷却された不凍液と水または
水溶液6を熱交換させて水または水溶液をを過冷却する
過冷却水生成熱交換器、41は過冷却水熱交換器40に
不凍液を送る不凍液循環ポンプ、42は第2蓄熱槽20
の槽内に設けられ、不凍液と、水または水溶液6を熱交
換させて氷塊状の氷を外周に生成する氷塊状氷生成熱交
換器、43は過冷却水生成熱交換器40、蒸発器5、不
凍液循環ポンプ41、氷塊状氷生成熱交換器42の順で
循環するように構成した不凍液循環路である。なお、そ
の他の構成については実施例1と同様につき説明を省略
する。
Example 4. FIG. 6 is a configuration diagram showing an ice heat storage device according to a fourth embodiment of the present invention. In the figure, 1 is a refrigerator for cooling an antifreeze liquid that does not solidify at 0 ° C., 40 is an antifreeze liquid and water cooled by the refrigerator 1. Alternatively, a supercooled water generation heat exchanger that heat-exchanges the aqueous solution 6 to supercool the water or the aqueous solution, 41 is an antifreeze circulation pump that sends an antifreeze solution to the supercooled water heat exchanger 40, and 42 is the second heat storage tank 20.
Is provided in the tank of No. 3, and an ice block-shaped ice generation heat exchanger that heat-exchanges the antifreeze liquid with water or aqueous solution 6 to generate ice block-shaped ice on the outer periphery, 43 is a supercooled water generation heat exchanger 40, and an evaporator 5 , An antifreeze liquid circulation pump 41, and an ice block-like ice forming heat exchanger 42 in this order. The other configurations are similar to those of the first embodiment, and the description thereof is omitted.

【0051】次に動作について説明する。冷凍機1の動
作は第1の従来例と同様につき説明を省略する。また、
第1水循環路11内の水の動作、および第2水循環路1
4a内の氷水の動作は実施例1と同様につき、不凍液循
環路43内の不凍液の動作について説明する。
Next, the operation will be described. Since the operation of the refrigerator 1 is the same as that of the first conventional example, description thereof will be omitted. Also,
Operation of water in the first water circuit 11, and second water circuit 1
Since the operation of the ice water in 4a is the same as that of the first embodiment, the operation of the antifreeze liquid in the antifreeze liquid circulation path 43 will be described.

【0052】この氷蓄熱装置では、冷凍機1の蒸発器5
で不凍液を冷却し、この不凍液を、不凍液循環ポンプ4
1で第2蓄熱槽20に備えられた氷塊状氷生成熱交換器
42、過冷却水生成熱交換器40の順で循環させて、氷
塊状氷生成熱交換器42の外周に氷塊状の氷16を生成
し、過冷却水生成熱交換器40では水または水溶液7を
過冷却まで冷却する。このように構成した氷蓄熱装置
も、実施例1と同様の効果が得られる。
In this ice heat storage device, the evaporator 5 of the refrigerator 1
The antifreeze liquid is cooled with the antifreeze liquid circulation pump 4
1, the ice lump ice generation heat exchanger 42 and the supercooled water generation heat exchanger 40 provided in the second heat storage tank 20 are circulated in this order, and ice lump ice is formed around the ice lump ice generation heat exchanger 42. 16 is generated, and the water or aqueous solution 7 is cooled to supercool in the supercooled water generation heat exchanger 40. The ice heat storage device configured in this manner also has the same effects as those of the first embodiment.

【0053】なお、本実施例では氷塊状氷生成熱交換器
42と過冷却水生成熱交換器40を直列に接続したもの
を示したが、並列接続した構成のものでもよく、冷凍機
1の蒸発器5で不凍液を冷却し、この不凍液を、不凍液
循環ポンプ41で氷塊状氷生成熱交換器42に送るとと
もに、並列接続された過冷却水生成熱交換器40に送る
よう、不凍液循環路を構成しても良い。
In this embodiment, the ice lump-like ice forming heat exchanger 42 and the supercooled water forming heat exchanger 40 are connected in series, but they may be connected in parallel to each other and the refrigerator 1 may be used. The antifreeze liquid is cooled by the evaporator 5, the antifreeze liquid is sent by the antifreeze liquid circulation pump 41 to the ice block-like ice formation heat exchanger 42, and the antifreeze circulation passage is connected to the supercooled water formation heat exchanger 40 connected in parallel. It may be configured.

【0054】実施例5.図7は本発明の実施例5による
氷蓄熱装置を示す構成図である。上記実施例4では、過
冷却水生成熱交換器40と氷塊状氷生成熱交換器42に
同流量の不凍液が流入する装置について説明したが、こ
の実施例5の氷蓄熱装置では図7の構成図に示すよう
に、一方を氷塊状氷生成熱交換器42と過冷却水生成熱
交換器40の間に接続し、他方を過冷却水生成熱交換器
40と蒸発器5の間に接続した不凍液バイパス流路45
と、この不凍液バイパス流路45を流れる不凍液の流量
を調整する不凍液流量制御弁46を設け、氷塊状氷生成
熱交換器42を流れる不凍液の流量と、過冷却水生成熱
交換器40を流れる不凍液の流量を制御する。なお、そ
の他の構成については実施例4と同様につき説明を省略
する。
Example 5. FIG. 7 is a configuration diagram showing an ice heat storage device according to a fifth embodiment of the present invention. In the above-described fourth embodiment, the device in which the same flow rate of the antifreeze liquid flows into the supercooled water generation heat exchanger 40 and the ice block ice generation heat exchanger 42 has been described, but the ice heat storage device of the fifth embodiment has the configuration of FIG. 7. As shown in the figure, one is connected between the ice block-like ice generation heat exchanger 42 and the supercooled water generation heat exchanger 40, and the other is connected between the supercooled water generation heat exchanger 40 and the evaporator 5. Antifreeze bypass flow path 45
And an antifreeze liquid flow control valve 46 for adjusting the flow amount of the antifreeze liquid flowing through the antifreeze liquid bypass passage 45, and the flow rate of the antifreeze liquid flowing through the ice block ice generation heat exchanger 42 and the antifreeze liquid flowing through the supercooling water generation heat exchanger 40. Control the flow rate of. The other configurations are similar to those in the fourth embodiment, and the description thereof is omitted.

【0055】このように構成した氷蓄熱装置は、過冷却
水生成熱交換器40に流入する不凍液の流量を不凍液流
量制御弁46で制御して、安定に水または水溶液6を過
冷却でき、同時に氷塊状氷生成熱交換器42では冷凍機
1を効率よく運転できる流量に制御できるため、実施例
4の効果に加えて、安定してシャーベット状の氷7を生
成できるとともに、高効率な冷凍機1の運転が行える。
In the ice heat storage device configured as described above, the flow rate of the antifreeze liquid flowing into the supercooled water generation heat exchanger 40 is controlled by the antifreeze liquid flow control valve 46, and the water or the aqueous solution 6 can be stably supercooled, and at the same time. In the ice block ice generation heat exchanger 42, the flow rate of the refrigerator 1 can be controlled so that the refrigerator 1 can be efficiently operated. Therefore, in addition to the effect of the fourth embodiment, the sherbet-like ice 7 can be stably generated and the refrigerator is highly efficient. 1 operation can be performed.

【0056】実施例6.図8は本発明の実施例6による
氷蓄熱装置を示す構成図である。本実施例においては、
第2水循環路14aに、水または水溶液6が熱負荷12
aから第1蓄熱槽8に送水される流路を加え、この熱負
荷12aから第1蓄熱槽8に送水される流路と、熱負荷
12aから第2蓄熱槽20に送水される流路とを切り替
える流路切り替え手段50を設けたものである。なお、
その他の構成については実施例1と同様である。
Example 6. FIG. 8 is a configuration diagram showing an ice heat storage device according to a sixth embodiment of the present invention. In this embodiment,
The water or the aqueous solution 6 has a heat load 12 on the second water circulation path 14a.
A flow path for supplying water from a to the first heat storage tank 8 is added, and a flow path for supplying water from the heat load 12a to the first heat storage tank 8 and a flow path for supplying water from the heat load 12a to the second heat storage tank 20. The flow path switching means 50 for switching between is provided. In addition,
Other configurations are similar to those of the first embodiment.

【0057】次に動作について説明する。この氷蓄熱装
置には、(1)熱負荷12aの出口の水または水溶液6
の温度が0℃以下の第1の運転モードと、(2)熱負荷
12aの出口の水または水溶液6の温度が0℃を越える
場合の第2の運転モードがある。以下、それぞれの運転
モードについて説明する。
Next, the operation will be described. This ice heat storage device includes (1) water or aqueous solution 6 at the outlet of the heat load 12a.
There is a first operation mode in which the temperature is 0 ° C. or less, and (2) a second operation mode in which the temperature of the water or aqueous solution 6 at the outlet of the heat load 12a exceeds 0 ° C. Hereinafter, each operation mode will be described.

【0058】第1の運転モードでは、流路切り替え手段
50を熱負荷12aから第1蓄熱槽8に送水する流路に
切り替える。第1蓄熱槽8に蓄えたシャーベット状の氷
7は氷水混合手段22で水または水溶液6と混ぜて、第
2水循環ポンプ13aで熱負荷12aに送られ、室内空
気または室内空気を冷却する水などと熱交換して、第1
蓄熱槽8に送られる。この水は、第1蓄熱槽8に蓄えら
れ再びシャーベット状の氷7と混ぜて熱負荷5に送られ
てサイクルを構成する。なお、冷凍機1および第1水循
環ポンプ10の運転は、実施例1と同様につき説明を省
略する。
In the first operation mode, the flow path switching means 50 is switched to the flow path for supplying water from the heat load 12a to the first heat storage tank 8. The sherbet-shaped ice 7 stored in the first heat storage tank 8 is mixed with water or the aqueous solution 6 by the ice water mixing means 22 and sent to the heat load 12a by the second water circulation pump 13a to cool the indoor air or the water for cooling the indoor air. Heat exchange with
It is sent to the heat storage tank 8. This water is stored in the first heat storage tank 8, mixed again with the sherbet-shaped ice 7, and sent to the heat load 5 to form a cycle. The operation of the refrigerator 1 and the first water circulation pump 10 is the same as that of the first embodiment, and the description thereof is omitted.

【0059】第2の運転モードでは、流路切り替え手段
50を第2蓄熱槽20に送水する流路に切り替える。第
1蓄熱槽8に蓄えられたシャーベット状の氷7は、水ま
たは水溶液6と混ぜて第2水循環ポンプ13aで熱負荷
12aに送られ、室内空気または室内空気を冷却する水
などと熱交換して、0℃以上の温度、たとえば12℃程
度の水となる。この水は、流路切り替え手段50を通っ
て第2蓄熱槽20に送水され、第2蓄熱槽20に蓄えら
れた氷塊状氷16を融かしながら0℃程度まで冷却され
第2蓄熱槽20に蓄えられる。そして、この水または水
溶液6の一部は、連通管21を通り第1蓄熱槽8に蓄え
られる。なお、冷凍機1および第1水循環ポンプ10の
運転は、実施例1と同様につき説明を省略する。
In the second operation mode, the flow path switching means 50 is switched to the flow path for supplying water to the second heat storage tank 20. The sherbet-shaped ice 7 stored in the first heat storage tank 8 is mixed with water or the aqueous solution 6 and sent to the heat load 12a by the second water circulation pump 13a to exchange heat with room air or water for cooling the room air. As a result, water has a temperature of 0 ° C. or higher, for example, about 12 ° C. This water is sent to the second heat storage tank 20 through the flow path switching means 50, and is cooled to about 0 ° C. while melting the ice block ice 16 stored in the second heat storage tank 20 and then the second heat storage tank 20. Stored in. Then, a part of the water or the aqueous solution 6 passes through the communication pipe 21 and is stored in the first heat storage tank 8. The operation of the refrigerator 1 and the first water circulation pump 10 is the same as that of the first embodiment, and the description thereof is omitted.

【0060】以上のように、この実施例においては、実
施例1の効果に加えて、熱負荷12a出口の水または水
溶液6の温度に応じて熱負荷12aで熱交換した後の水
または水溶液6の流路を第1蓄熱槽8に至る流路、また
は第2蓄熱槽20に至る流路のいずれかに切り替えるこ
とができ、熱負荷12aに送るために蓄えたシャーベッ
ト状の氷7を熱負荷12aからの水または水溶液6で溶
かすことなく、効率的に利用でき、長い時間氷水を送り
続けて、少ない流量で熱負荷の冷却が行えるので第2水
循環ポンプ13aに要する動力が低減できる。さらに、
第2蓄熱槽20に蓄えられた水または水溶液6の温度は
第1蓄熱槽8に蓄えられた水または水溶液6の温度より
高くでき、冷凍機1に送水する水または水溶液6の温度
が高く、冷凍機1を効率的に運転できる。
As described above, in this embodiment, in addition to the effects of the first embodiment, the water or aqueous solution 6 after heat exchange with the heat load 12a according to the temperature of the water or aqueous solution 6 at the outlet of the heat load 12a is performed. Can be switched to either the flow path leading to the first heat storage tank 8 or the flow path reaching the second heat storage tank 20, and the sherbet-shaped ice 7 stored for sending to the heat load 12a is subjected to the heat load. It can be efficiently used without being melted with the water or the aqueous solution 6 from 12a, the ice water can be continuously sent for a long time, and the heat load can be cooled with a small flow rate, so that the power required for the second water circulation pump 13a can be reduced. further,
The temperature of the water or the aqueous solution 6 stored in the second heat storage tank 20 can be higher than the temperature of the water or the aqueous solution 6 stored in the first heat storage tank 8, and the temperature of the water or the aqueous solution 6 sent to the refrigerator 1 is high, The refrigerator 1 can be operated efficiently.

【0061】実施例7.図9は本発明の実施例7による
氷蓄熱装置を示す構成図である。本実施例においては、
第1水循環路11に、水または水溶液6が第1蒸発器5
から第2蓄熱槽20に送水される流路を加え、この第1
蒸発器5から第2蓄熱槽20に送水される流路と、第1
蒸発器5から第1蓄熱槽8に送水される流路とを切り替
える流路切り替え手段60を設けたものである。なお、
その他の構成については実施例1と同様である。
Example 7. FIG. 9 is a configuration diagram showing an ice heat storage device according to a seventh embodiment of the present invention. In this embodiment,
In the first water circulation path 11, water or an aqueous solution 6 is added to the first evaporator 5
A flow path from the first heat storage tank 20 to the second heat storage tank 20 is added.
A flow path for sending water from the evaporator 5 to the second heat storage tank 20;
The flow path switching means 60 is provided to switch the flow path from the evaporator 5 to the water supplied to the first heat storage tank 8. In addition,
Other configurations are similar to those of the first embodiment.

【0062】次に動作について説明する。この氷蓄熱装
置には、(1)第1蒸発器5の出口の水または水溶液6
の温度が0℃以下の第1の運転モードと、(2)第1蒸
発器5の出口の水または水溶液6の温度が0℃を越える
場合の第2の運転モードがある。以下、それぞれの運転
モードについて説明する。
Next, the operation will be described. This ice heat storage device includes (1) water or aqueous solution 6 at the outlet of the first evaporator 5.
There is a first operation mode in which the temperature is 0 ° C. or lower, and (2) a second operation mode when the temperature of the water or aqueous solution 6 at the outlet of the first evaporator 5 exceeds 0 ° C. Hereinafter, each operation mode will be described.

【0063】第1の運転モードでは、流路切り替え手段
60を第1蒸発器5から第1蓄熱槽8に送水する流路に
切り替え、過冷却解除手段9により水または水溶液6の
過冷却を解除してシャーベット状の氷7を生成する。シ
ャーベット状の氷7とならなかった水または水溶液6
は、連通管20を通り第2蓄熱槽20に流入し、再び第
1水循環ポンプ10で冷凍機1の第1蒸発器5に送水さ
れてサイクルを構成する。なお、冷凍機1、第2水循環
ポンプ15aと氷水混合手段22の運転は、実施例1と
同様につき説明を省略する。
In the first operation mode, the flow path switching means 60 is switched to the flow path for feeding water from the first evaporator 5 to the first heat storage tank 8, and the supercooling canceling means 9 cancels the supercooling of the water or the aqueous solution 6. Then, sherbet-shaped ice 7 is generated. Sherbet-like ice 7 Water or aqueous solution 6
Flows into the second heat storage tank 20 through the communication pipe 20, and is again sent to the first evaporator 5 of the refrigerator 1 by the first water circulation pump 10 to form a cycle. The operations of the refrigerator 1, the second water circulation pump 15a, and the ice water mixing means 22 are the same as those in the first embodiment, and a description thereof will be omitted.

【0064】第2の運転モードでは、流路切り替え手段
60を第2蓄熱槽20に送水する流路に切り替える。第
1蓄熱槽8に蓄えられたシャーベット状の氷7は、水ま
たは水溶液6と混ぜて第2水循環ポンプ13aで熱負荷
12aに送られ、室内空気または室内空気を冷却する水
などと熱交換して、0℃以上の温度、たとえば12℃程
度の水となる。この水は第2蓄熱槽20に送水され、第
2蓄熱槽20に蓄えられた氷塊状氷16を融かしながら
0℃程度まで冷却され第2蓄熱槽20に蓄えられる。そ
して、この水または水溶液6の一部は、連通管21を通
り第1蓄熱槽8に蓄えられる。なお、冷凍機1、第2水
循環ポンプ15aと氷水混合手段22の運転は実施例1
と同様につき説明を省略する。
In the second operation mode, the flow passage switching means 60 is switched to the flow passage for supplying water to the second heat storage tank 20. The sherbet-shaped ice 7 stored in the first heat storage tank 8 is mixed with water or the aqueous solution 6 and sent to the heat load 12a by the second water circulation pump 13a to exchange heat with room air or water for cooling the room air. As a result, water has a temperature of 0 ° C. or higher, for example, about 12 ° C. This water is sent to the second heat storage tank 20, and is cooled to about 0 ° C. while melting the ice block ice 16 stored in the second heat storage tank 20 and stored in the second heat storage tank 20. Then, a part of the water or the aqueous solution 6 passes through the communication pipe 21 and is stored in the first heat storage tank 8. The operation of the refrigerator 1, the second water circulation pump 15a and the ice water mixing means 22 is the same as that of the first embodiment.
The explanation is omitted because it is the same as the above.

【0065】以上のように、この実施例においては、実
施例1の効果に加えて、第1蒸発器5出口の水または水
溶液6の温度に応じて、第1蒸発器5で冷却された水ま
たは水溶液6の流路を、第1蓄熱槽8に至る流路または
第2蓄熱槽20に至る流路のいずれかに切り替えること
ができるため、熱負荷12aに送るために蓄えたシャー
ベット状の氷7を第1蒸発器5からの水または水溶液6
で溶かすことなく、効率的に利用でき、長い時間氷水を
送り続けて、少ない流量で熱負荷の冷却が行えるので第
2水循環ポンプ13aに要する動力が低減できる。さら
に、第2蓄熱槽20に蓄えられた水または水溶液6の温
度は第1蓄熱槽8に蓄えられた水または水溶液6の温度
より高くでき、冷凍機1に送水する水または水溶液6の
温度が高く、冷凍機1を効率的に運転できる。
As described above, in this embodiment, in addition to the effect of the first embodiment, the water cooled by the first evaporator 5 is changed according to the temperature of the water or the aqueous solution 6 at the outlet of the first evaporator 5. Alternatively, since the flow path of the aqueous solution 6 can be switched to either the flow path to the first heat storage tank 8 or the flow path to the second heat storage tank 20, sherbet-like ice stored for sending to the heat load 12a. 7 is water or aqueous solution 6 from the first evaporator 5.
Since the ice water can be efficiently used without being melted and the ice water can be continuously sent for a long time to cool the heat load with a small flow rate, the power required for the second water circulation pump 13a can be reduced. Further, the temperature of the water or the aqueous solution 6 stored in the second heat storage tank 20 can be higher than the temperature of the water or the aqueous solution 6 stored in the first heat storage tank 8, and the temperature of the water or the aqueous solution 6 sent to the refrigerator 1 can be increased. It is high, and the refrigerator 1 can be operated efficiently.

【0066】実施例8.図10は本発明の実施例8によ
る氷蓄熱装置を示す構成図である。本実施例では第1水
循環路11に、水または水溶液6が第1蓄熱槽8から第
1蒸発器5に送水されるバイパス流路71を設けるとと
もに、この第1蓄熱槽8から第1蒸発器5に送水される
流路と第2蓄熱槽20から第1蒸発器5に送水される流
路とを切り替える流路切り替え手段70を設けたもので
ある。なお、その他の構成については実施例1と同様で
ある。
Example 8. FIG. 10 is a configuration diagram showing an ice heat storage device according to Embodiment 8 of the present invention. In the present embodiment, the first water circulation passage 11 is provided with a bypass passage 71 through which the water or the aqueous solution 6 is fed from the first heat storage tank 8 to the first evaporator 5, and the first heat storage tank 8 is passed through the first evaporator. The flow path switching means 70 is provided for switching between the flow path for supplying water to the water tank 5 and the flow path for supplying water to the first evaporator 5 from the second heat storage tank 20. The other configurations are similar to those of the first embodiment.

【0067】次に動作について説明する。この氷蓄熱装
置には、(1)第2蓄熱槽20に蓄えられた水または水
溶液6の温度が、第1蓄熱槽8に蓄えられた水または水
溶液6の温度より高い場合の第1の運転モードと、
(2)第2蓄熱槽20に蓄えられた水または水溶液6の
温度が、蓄熱槽8に蓄えられた水または水溶液6の温度
より低い場合の第2の運転モードがある。以下、それぞ
れの運転モードについて説明する。
Next, the operation will be described. In this ice heat storage device, (1) the first operation when the temperature of the water or the aqueous solution 6 stored in the second heat storage tank 20 is higher than the temperature of the water or the aqueous solution 6 stored in the first heat storage tank 8 Mode,
(2) There is a second operation mode in which the temperature of the water or the aqueous solution 6 stored in the second heat storage tank 20 is lower than the temperature of the water or the aqueous solution 6 stored in the heat storage tank 8. Hereinafter, each operation mode will be described.

【0068】第1の運転モードでは、流路切り替え手段
70を第2蓄熱槽20から第1水循環ポンプ10を通り
第1蒸発器5に至る流路71に切り替える。その他の動
作は実施例1と同様につき省略する。
In the first operation mode, the flow path switching means 70 is switched to the flow path 71 from the second heat storage tank 20 to the first evaporator 5 through the first water circulation pump 10. Since other operations are the same as those in the first embodiment, the description thereof will be omitted.

【0069】第2の運転モードでは、流路切り替え手段
70を第1蓄熱槽8から第1水循環ポンプ10を通り第
1蒸発器5にいたるバイパス流路71に切り替える。第
1蓄熱槽8に蓄えられた水または水溶液6は、バイパス
流路71を通り第1蒸発器5で冷却された後、再び第1
蓄熱槽8に送水される。なお、その他の動作は実施例1
と同様につき説明を省略する。
In the second operation mode, the flow passage switching means 70 is switched from the first heat storage tank 8 to the bypass flow passage 71 which passes through the first water circulation pump 10 and reaches the first evaporator 5. The water or the aqueous solution 6 stored in the first heat storage tank 8 passes through the bypass passage 71, is cooled by the first evaporator 5, and is then again returned to the first heat storage tank 6.
Water is sent to the heat storage tank 8. The other operations are the same as those in the first embodiment.
The explanation is omitted because it is the same as the above.

【0070】以上のように、この実施例においては、実
施例1の効果に加えて、第2蓄熱槽20に蓄えられた水
または水溶液6と第1蓄熱槽8に蓄えられた水または水
溶液6の温度を比較して、高い温度の水または水溶液6
を1蒸発器5に送水することができるため、冷凍機を効
率的に運転できる。
As described above, in this embodiment, in addition to the effects of the first embodiment, the water or aqueous solution 6 stored in the second heat storage tank 20 and the water or aqueous solution 6 stored in the first heat storage tank 8 are added. Compare the temperatures of water and water at higher temperatures 6
Since the water can be sent to one evaporator 5, the refrigerator can be operated efficiently.

【0071】実施例9.図11は本発明の実施例8によ
る氷蓄熱装置を示す構成図である。本実施例において
は、実施例6と同様、第2水循環路14aに、水または
水溶液6が熱負荷12aから第1蓄熱槽8に送水される
流路を加え、この熱負荷12aから第1蓄熱槽8に送水
される流路と、熱負荷12aから第2蓄熱槽20に送水
される流路とを切り替える流路切り替え手段80を設け
るとともに、実施例8と同様、第1水循環路11に、水
または水溶液6が第1蓄熱槽8から第1蒸発器5に送水
されるバイパス流路81を設け、この第1蓄熱槽8から
第1蒸発器5に送水される流路と第2蓄熱槽20から第
1蒸発器5に送水される流路とを切り替える第2流路切
り替え手段82を設けたものである。なお、その他の構
成については実施例1と同様である。
Example 9. FIG. 11 is a configuration diagram showing an ice heat storage device according to Embodiment 8 of the present invention. In the present embodiment, as in the case of the sixth embodiment, a flow path through which the water or the aqueous solution 6 is sent from the heat load 12a to the first heat storage tank 8 is added to the second water circulation path 14a, and the first heat storage from the heat load 12a is added. A flow passage switching means 80 for switching between a flow passage for supplying water to the tank 8 and a flow passage for supplying water from the heat load 12a to the second heat storage tank 20 is provided, and like the eighth embodiment, the first water circulation passage 11 is provided with: A bypass flow path 81 is provided through which water or aqueous solution 6 is sent from the first heat storage tank 8 to the first evaporator 5, and a flow path through which water is sent from the first heat storage tank 8 to the first evaporator 5 and the second heat storage tank. The second flow path switching means 82 for switching the flow path from 20 to the water flow to the first evaporator 5 is provided. The other configurations are similar to those of the first embodiment.

【0072】次に動作について説明する。この氷蓄熱装
置には、(1)第2蓄熱槽20に蓄えられた水または水
溶液6の温度が利用できる上限の温度、たとえば12℃
以下の場合の第1の運転モードと、(2)第2蓄熱槽2
0に蓄えられた水または水溶液6の温度が利用できる上
限の温度、たとえば12℃を越える場合の第2の運転モ
ードがある。以下、それぞれの運転モードについて説明
する。
Next, the operation will be described. In this ice heat storage device, (1) an upper limit temperature at which the temperature of the water or the aqueous solution 6 stored in the second heat storage tank 20 can be used, for example, 12 ° C.
The first operation mode in the following cases, and (2) the second heat storage tank 2
There is a second operating mode when the temperature of the water or aqueous solution 6 stored at 0 exceeds the upper limit temperature that can be used, for example 12 ° C. Hereinafter, each operation mode will be described.

【0073】第1の運転モードでは、流路切り替え手段
80を熱負荷12aから第2蓄熱槽20に至る流路に切
り替え、第2流路切り替え手段82を第2蓄熱槽20か
ら第1水循環ポンプ10に至る流路に切り替える。その
他の動作は実施例1と同様につき省略する。
In the first operation mode, the flow path switching means 80 is switched to the flow path from the heat load 12a to the second heat storage tank 20, and the second flow path switching means 82 is moved from the second heat storage tank 20 to the first water circulation pump. Switch to the flow path up to 10. Since other operations are the same as those in the first embodiment, the description thereof will be omitted.

【0074】第2の運転モードでは、流路切り替え手段
80を熱負荷12aから第1蓄熱槽8に至る流路に切り
替え、第2流路切り替え手段82を第1蓄熱槽8から第
1水循環ポンプ10にいたるバイパス流路81に切り替
える。第1蓄熱槽8に蓄えられた水または水溶液6は、
バイパス流路81を通り第1蒸発器5で冷却された後、
再び第1蓄熱槽8に送水されるとともに、第2の水循環
ポンプ13aで熱負荷12aに送水される。なお、冷凍
機1の運転は実施例1と同様につき説明を省略する。
In the second operation mode, the flow path switching means 80 is switched to the flow path from the heat load 12a to the first heat storage tank 8, and the second flow path switching means 82 is switched from the first heat storage tank 8 to the first water circulation pump. Switch to the bypass passage 81 up to 10. The water or aqueous solution 6 stored in the first heat storage tank 8 is
After being cooled by the first evaporator 5 through the bypass passage 81,
The water is again sent to the first heat storage tank 8 and is also sent to the heat load 12a by the second water circulation pump 13a. The operation of the refrigerator 1 is the same as that of the first embodiment, and a description thereof will be omitted.

【0075】以上のように、この実施例においては、実
施例1の効果に加えて、第2蓄熱槽20に蓄えられた水
または水溶液6の温度に応じて、水または水溶液6の流
路を、第1蓄熱槽8から第1蒸発器5に至る流路、また
は第2蓄熱槽20から第1蒸発器5に至る流路のいずれ
かに切り替え、さらに熱負荷12aで熱交換した後の水
または水溶液6の流路を第1蓄熱槽8に至る流路、また
は第2蓄熱槽20に至る流路に切り替えることができる
ため、第2蓄熱槽20に蓄えられた水または水溶液6の
温度が所定の温度を越える場合に、第2蓄熱槽20を第
1水循環路11および第2の水循環路から切り離すこと
ができ、熱負荷12aに送るために蓄えたシャーベット
状の氷を溶かすことなく、効率よくシャーベット状の氷
7を熱負荷12aに送ることができ、第2水循環ポンプ
13aに要する動力を低減できる。
As described above, in this embodiment, in addition to the effect of the first embodiment, the flow path of the water or the aqueous solution 6 is changed depending on the temperature of the water or the aqueous solution 6 stored in the second heat storage tank 20. , Water after switching to either the flow path from the first heat storage tank 8 to the first evaporator 5 or the flow path from the second heat storage tank 20 to the first evaporator 5 and further performing heat exchange with the heat load 12a Alternatively, since the flow path of the aqueous solution 6 can be switched to the flow path to the first heat storage tank 8 or the flow path to the second heat storage tank 20, the temperature of the water or the aqueous solution 6 stored in the second heat storage tank 20 is changed. When the temperature exceeds a predetermined temperature, the second heat storage tank 20 can be separated from the first water circulation path 11 and the second water circulation path, and the sherbet-shaped ice stored for sending to the heat load 12a is not melted, and the efficiency is improved. A sherbet-like ice 7 is often loaded with heat 12a It can be sent, thereby reducing the power required for the second water circulation pump 13a.

【0076】[0076]

【発明の効果】以上のように本発明の請求項1記載の発
明によれば、第1蒸発器と第2蒸発器を有する冷凍機、
第1蒸発器により過冷却される水または水に添加物を添
加した水溶液の過冷却を解除し、シャーベット状の氷を
生成させる過冷却解除手段、上記シャーベット状の氷を
蓄える第1蓄熱槽、第1蓄熱槽内の水または水溶液を第
1蒸発器に送り循環させる第1水循環ポンプ、第1蓄熱
槽内の水もしくは水溶液、またはシャーベット状の氷が
混合した氷水を熱負荷に送り循環させる第2水循環ポン
プ、第2蒸発器を槽内に配し、第2蒸発器の外周に生成
する氷塊状の氷を蓄える第2蓄熱槽、並びに第1蓄熱槽
と第2蓄熱槽を接続する連通管により氷蓄熱装置を構成
するとともに、第2蓄熱槽、第1水循環ポンプ、第1蒸
発器、第1蓄熱槽、連通管の順で上記水または水溶液が
循環する第1水循環路と、第1蓄熱槽、第2水循環ポン
プ、熱負荷、第2蓄熱槽、連通管の順で上記水もしくは
水溶液、または上記氷水が循環する第2水循環路を構成
したので、第1蓄熱槽内に流動性のあるシャーベット状
の氷を一様に蓄えることができ、熱負荷に対し追従性の
よい装置が得られる。また、氷塊状氷をシャーベット状
の氷より高い氷充填率で第2蓄熱槽に蓄えることがで
き、蓄熱槽が小型化できる。また、第2蓄熱槽に蓄えら
れた氷塊状氷が微細な氷を捕獲する効果があり、第1蒸
発器で安定して水または水溶液を過冷却でき、高効率な
冷凍機の運転が行える。
As described above, according to the first aspect of the present invention, a refrigerator having a first evaporator and a second evaporator,
Supercooling releasing means for releasing supercooling of water supercooled by the first evaporator or an aqueous solution obtained by adding an additive to water to generate sherbet-like ice; a first heat storage tank for storing the sherbet-like ice; A first water circulation pump for sending and circulating water or an aqueous solution in the first heat storage tank to the first evaporator; water or an aqueous solution in the first heat storage tank, or ice water in which sherbet-like ice is mixed, for sending and circulating to a heat load; 2 water circulation pump, 2nd evaporator is arrange | positioned in a tank, the 2nd heat storage tank which stores the ice block-like ice produced in the outer periphery of a 2nd evaporator, and the communication pipe which connects a 1st heat storage tank and a 2nd heat storage tank And a first water circulation path in which the water or the aqueous solution circulates in the order of the second heat storage tank, the first water circulation pump, the first evaporator, the first heat storage tank, and the communication pipe, and the first heat storage. Tank, second water circulation pump, heat load, second Since the second water circulation path in which the water or the aqueous solution or the ice water is circulated in the order of the heat tank and the communication pipe is configured, it is possible to uniformly store fluidized sherbet-like ice in the first heat storage tank. As a result, a device having good followability with respect to heat load can be obtained. Further, the ice lump ice can be stored in the second heat storage tank at a higher ice filling rate than the sherbet-shaped ice, and the heat storage tank can be downsized. In addition, the ice block-like ice stored in the second heat storage tank has an effect of capturing fine ice, and the first evaporator can stably supercool the water or the aqueous solution, and can operate the refrigerator with high efficiency.

【0077】また、請求項2記載の発明によれば、請求
項1記載の氷蓄熱装置に対し、第1蒸発器を流れる冷媒
の流量と第2蒸発器を流れる冷媒の流量を制御する制御
手段を設けたので、さらに安定してシャーベット状の氷
を生成できる。
Further, according to the invention of claim 2, in the ice heat storage device of claim 1, the control means for controlling the flow rate of the refrigerant flowing through the first evaporator and the flow rate of the refrigerant flowing through the second evaporator. With the provision of, the sherbet-like ice can be generated more stably.

【0078】また、請求項3記載の発明によれば、蒸発
器を有し、少なくとも0℃において凝固しない不凍液を
冷却する冷凍機、この冷凍機により冷却された不凍液
と、水または水に添加物を添加した水溶液を熱交換させ
て水または水溶液を過冷却する過冷却水生成熱交換器、
上記冷凍機により冷却された不凍液と、水または水に添
加物を添加した水溶液を熱交換させて氷塊状の氷を生成
する氷塊状氷生成熱交換器、上記過冷却水生成熱交換器
及び上記氷塊状氷生成熱交換器に不凍液を送る不凍液循
環ポンプ、過冷却された水または水溶液の過冷却を解除
し、シャーベット状の氷を生成させる過冷却解除手段、
上記シャーベット状の氷を蓄える第1蓄熱槽、第1蓄熱
槽内の水または水溶液を上記過冷却水生成熱交換器に送
り循環させる第1水循環ポンプ、第1蓄熱槽内の水もし
くは水溶液、またはシャーベット状の氷が混合した氷水
を熱負荷に送り循環させる第2水循環ポンプ、上記氷塊
状氷生成熱交換器を槽内に配し、上記氷塊状氷生成熱交
換器の外周に生成する氷塊状の氷を蓄える第2蓄熱槽、
並びに第1蓄熱槽と第2蓄熱槽を接続する連通管で氷蓄
熱装置を構成するとともに、蒸発器、不凍液循環ポン
プ、氷塊状氷生成熱交換器及び過冷却水生成熱交換器の
順で不凍液が循環する不凍液循環路と、第2蓄熱槽、第
1水循環ポンプ、過冷却水生成熱交換器、第1蓄熱槽、
連通管の順で水または水溶液が循環する第1水循環路
と、第1蓄熱槽、第2水循環ポンプ、熱負荷、第2蓄熱
槽、連通管の順で水もしくは水溶液、または氷水が循環
する第2水循環路を構成したので、請求項1記載の氷蓄
熱装置と同様の効果がある。
According to the third aspect of the present invention, a refrigerator having an evaporator for cooling an antifreeze liquid which does not solidify at least at 0 ° C., an antifreeze liquid cooled by the refrigerator, and water or an additive to water. A subcooled water generation heat exchanger that heat-exchanges the added aqueous solution to supercool water or the aqueous solution,
The antifreeze liquid cooled by the refrigerator and water or an aqueous solution obtained by adding an additive to water is heat-exchanged to generate ice-lump ice, and the ice-lump ice generation heat exchanger, the supercooled water generation heat exchanger, and the above An antifreeze liquid circulation pump that sends an antifreeze liquid to an ice block ice formation heat exchanger, a supercooling releasing means for releasing supercooling of supercooled water or an aqueous solution, and generating sherbet-like ice,
A first heat storage tank for storing the sherbet-like ice, a first water circulation pump for sending and circulating water or an aqueous solution in the first heat storage tank to the supercooled water generation heat exchanger, water or an aqueous solution in the first heat storage tank, or A second water circulation pump for sending ice water mixed with sherbet-like ice to a heat load to circulate the ice water, the ice-mass ice-generating heat exchanger is arranged in a tank, and the ice-mass ice-mass generated on the outer periphery of the ice-mass ice-generating heat exchanger Second heat storage tank for storing ice
In addition, the ice heat storage device is configured by a communication pipe that connects the first heat storage tank and the second heat storage tank, and the antifreeze liquid is formed in the order of the evaporator, the antifreeze liquid circulation pump, the ice lump ice formation heat exchanger, and the supercooled water generation heat exchanger. Circulating antifreeze liquid, second heat storage tank, first water circulation pump, supercooled water generation heat exchanger, first heat storage tank,
A first water circulation path in which water or an aqueous solution circulates in the order of a communication pipe, and a first heat storage tank, a second water circulation pump, a heat load, a second heat storage tank, a water or aqueous solution or an ice water circulates in the order of a communication tube. Since the two water circulation paths are configured, the same effect as the ice heat storage device according to the first aspect is obtained.

【0079】また、請求項4記載の発明によれば、請求
項3記載の氷蓄熱装置に対し、氷塊状氷生成熱交換器を
流れる不凍液の流量と、過冷却水生成熱交換器を流れる
不凍液の流量を制御する制御手段を設けたので、さらに
安定してシャーベット状の氷を生成できる。
Further, according to the invention described in claim 4, in the ice heat storage device according to claim 3, the flow rate of the antifreezing liquid flowing through the ice block ice-generating heat exchanger and the antifreezing liquid flowing through the supercooling water generating heat exchanger. Since the control means for controlling the flow rate is provided, the sherbet-like ice can be generated more stably.

【0080】また、請求項5記載の発明によれば、上記
各氷蓄熱装置の第1蓄熱槽内に、シャーベット状の氷
と、水または水溶液とを混合する氷水混合手段を設けた
ので、第2水循環ポンプに要する動力を大幅に低減でき
る。
According to the fifth aspect of the invention, the ice water mixing means for mixing the sherbet-shaped ice and water or an aqueous solution is provided in the first heat storage tank of each of the ice heat storage devices. 2 The power required for the water circulation pump can be greatly reduced.

【0081】また、請求項6記載の発明によれば、上記
各氷蓄熱装置の第2水循環路に、水または水溶液が熱負
荷から第1蓄熱槽に送水される流路を設けるとともに、
上記熱負荷から第1蓄熱槽に送水される流路と上記熱負
荷から第2蓄熱槽に送水される流路とを切り替える流路
切り替え手段を設けたので、第1蓄熱槽に蓄えたシャー
ベット状の氷を溶かすことなく利用でき、第2水循環ポ
ンプに要する動力を低減できる。
According to the sixth aspect of the invention, the second water circulation path of each of the ice heat storage devices is provided with a flow path through which water or an aqueous solution is sent from the heat load to the first heat storage tank.
Since the flow path switching means for switching the flow path from the heat load to the first heat storage tank and the flow path from the heat load to the second heat storage tank is provided, the sherbet shape stored in the first heat storage tank is provided. The ice can be used without melting, and the power required for the second water circulation pump can be reduced.

【0082】また、請求項7記載の発明によれば、上記
各氷蓄熱装置の第1水循環路に、水または水溶液が第1
蒸発器または過冷却水生成熱交換器から第2蓄熱槽に送
水される流路を設けるとともに、第1蒸発器または過冷
却水生成熱交換器から第2蓄熱槽に送水される流路と、
第1蒸発器または過冷却水生成熱交換器から第1蓄熱槽
に送水される流路とを切り替える流路切り替え手段を設
けたので、請求項6記載の氷蓄熱装置と同様の効果があ
る。
According to the invention described in claim 7, water or an aqueous solution is the first in the first water circulation path of each of the ice heat storage devices.
A flow path for supplying water from the evaporator or the supercooled water generation heat exchanger to the second heat storage tank is provided, and a flow path for supplying water from the first evaporator or the supercooled water generation heat exchanger to the second heat storage tank,
Since the flow path switching means for switching the flow path from the first evaporator or the supercooled water generation heat exchanger to the water flow to the first heat storage tank is provided, the same effect as the ice heat storage device according to the sixth aspect is provided.

【0083】また、請求項8記載の発明によれば、上記
各氷蓄熱装置の第1水循環路に、水または水溶液が第1
蓄熱槽から第1蒸発器または過冷却水生成熱交換器に送
水される流路を設けるとともに、第1蓄熱槽から第1蒸
発器または過冷却水生成熱交換器に送水される流路と、
第2蓄熱槽から第1蒸発器または過冷却水生成熱交換器
に送水される流路とを切り替える流路切り替え手段を設
けたので、冷凍機を効率的に運転できる。
According to the invention of claim 8, water or an aqueous solution is first in the first water circulation path of each of the ice heat storage devices.
A flow path for supplying water from the heat storage tank to the first evaporator or the supercooled water generation heat exchanger, and a flow path for supplying water from the first heat storage tank to the first evaporator or the supercooled water generation heat exchanger,
Since the flow path switching means for switching the flow path from the second heat storage tank to the water flow to the first evaporator or the supercooled water generation heat exchanger is provided, the refrigerator can be operated efficiently.

【0084】また、請求項9記載の発明によれば、請求
項8記載の氷蓄熱装置に対し、さらに第2水循環路に、
水または水溶液が熱負荷から第1蓄熱槽に送水される流
路を設けるとともに、熱負荷から第1蓄熱槽に送水され
る流路と熱負荷から第2蓄熱槽に送水される流路とを切
り替える流路切り替え手段を設けたので、シャーベット
状の氷を融かすことなく、効率よく熱負荷に送ることが
でき、第2水循環ポンプに要する動力を低減できる。
Further, according to the invention of claim 9, in addition to the ice heat storage device of claim 8, in the second water circulation path,
A flow path for sending water or an aqueous solution from the heat load to the first heat storage tank is provided, and a flow path for sending water from the heat load to the first heat storage tank and a flow path for sending water from the heat load to the second heat storage tank are provided. Since the flow path switching means for switching is provided, the sherbet-shaped ice can be efficiently sent to the heat load without melting, and the power required for the second water circulation pump can be reduced.

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

【図1】 本発明の実施例1による氷蓄熱装置を示す構
成図である。
FIG. 1 is a configuration diagram showing an ice heat storage device according to a first embodiment of the present invention.

【図2】 本発明の実施例2による氷蓄熱装置を示す構
成図である。
FIG. 2 is a configuration diagram showing an ice heat storage device according to a second embodiment of the present invention.

【図3】 本発明の実施例2に係わる冷凍機の動作(過
冷却水生成時の運転)を表す圧力−エンタルピー線図で
ある。
FIG. 3 is a pressure-enthalpy diagram showing the operation of the refrigerator according to the second embodiment of the present invention (operation during generation of supercooled water).

【図4】 本発明の実施例2に係わる冷凍機の動作(凍
結時の運転)を表す圧力−エンタルピー線図である。
FIG. 4 is a pressure-enthalpy diagram showing the operation (operation during freezing) of the refrigerator according to the second embodiment of the present invention.

【図5】 本発明の実施例3による氷蓄熱装置を示す構
成図である。
FIG. 5 is a configuration diagram showing an ice heat storage device according to a third embodiment of the present invention.

【図6】 本発明の実施例4による氷蓄熱装置を示す構
成図である。
FIG. 6 is a configuration diagram showing an ice heat storage device according to a fourth embodiment of the present invention.

【図7】 本発明の実施例5による氷蓄熱装置を示す構
成図である。
FIG. 7 is a configuration diagram showing an ice heat storage device according to a fifth embodiment of the present invention.

【図8】 本発明の実施例6による氷蓄熱装置を示す構
成図である。
FIG. 8 is a configuration diagram showing an ice heat storage device according to a sixth embodiment of the present invention.

【図9】 本発明の実施例7による氷蓄熱装置を示す構
成図である。
FIG. 9 is a configuration diagram showing an ice heat storage device according to a seventh embodiment of the present invention.

【図10】 本発明の実施例8による氷蓄熱装置を示す
構成図である。
FIG. 10 is a configuration diagram showing an ice heat storage device according to Embodiment 8 of the present invention.

【図11】 本発明の実施例9による氷蓄熱装置を示す
構成図である。
FIG. 11 is a configuration diagram showing an ice heat storage device according to a ninth embodiment of the present invention.

【図12】 第1の従来の氷蓄熱装置を示す構成図であ
る。
FIG. 12 is a configuration diagram showing a first conventional ice heat storage device.

【図13】 第2の従来の氷蓄熱装置を示す構成図であ
る。
FIG. 13 is a configuration diagram showing a second conventional ice heat storage device.

【符号の説明】[Explanation of symbols]

1 冷凍機、2 圧縮機、3 凝縮器、4 第1流量制
御弁、5 第1蒸発器、6 水または水溶液、7 シャ
ーベット状の氷、8 第1蓄熱槽、9 過冷却解除手
段、10 第1水循環ポンプ、11 第1水循環路、1
2a,12b 熱負荷、13a,13b 第2水循環ポ
ンプ、14a,14b 第2水循環路、15a,15b
第2蒸発器、16 氷塊状氷、17b 第2流量制御
弁、18b冷媒バイパス流路、20 第2蓄熱槽、21
連通管、22 氷水混合手段、30 第2流量制御
弁、31 冷媒バイパス流路、32 開閉弁、40 過
冷却水生成熱交換器、41 不凍液循環ポンプ、42
氷塊状氷生成熱交換器、43不凍液循環路、45 不凍
液バイパス流路、46不凍液流量制御弁、50 流路切
り替え手段、60 流量切り替え手段、70 流路切り
替え手段、71 バイパス流路、80 流路切り替え手
段、81 バイパス流路、82 第2流路切り替え手
段。
1 Refrigerator, 2 Compressor, 3 Condenser, 4 1st flow control valve, 5 1st evaporator, 6 Water or aqueous solution, 7 Sherbet-shaped ice, 8 1st heat storage tank, 9 Supercooling cancellation means, 10th 1 water circulation pump, 11 1st water circulation path, 1
2a, 12b heat load, 13a, 13b second water circulation pump, 14a, 14b second water circulation path, 15a, 15b
2nd evaporator, 16 ice block ice, 17b 2nd flow control valve, 18b refrigerant bypass flow path, 20 2nd heat storage tank, 21
Communication pipe, 22 Ice water mixing means, 30 Second flow rate control valve, 31 Refrigerant bypass flow path, 32 Open / close valve, 40 Supercooling water generation heat exchanger, 41 Antifreeze circulation pump, 42
Ice block ice generation heat exchanger, 43 antifreeze circulation passage, 45 antifreeze bypass flow passage, 46 antifreeze flow control valve, 50 flow passage switching means, 60 flow passage switching means, 70 flow passage switching means, 71 bypass flow passage, 80 flow passage Switching means, 81 bypass flow path, 82 second flow path switching means.

フロントページの続き (72)発明者 田中 直樹 静岡市小鹿三丁目18番1号 三菱電機株 式会社 住環境エンジニアリング統括セ ンター内 (56)参考文献 特開 昭64−75869(JP,A) 特開 平3−91635(JP,A) 特開 平6−347144(JP,A) 特開 平2−166330(JP,A) 特開 平5−346246(JP,A) 実開 昭63−2022(JP,U) 実公 平4−38178(JP,Y2) (58)調査した分野(Int.Cl.7,DB名) F24F 5/00 102 F25C 1/00 Front page continuation (72) Inventor Naoki Tanaka 3-18-1, Oga, Shizuoka City Mitsubishi Electric Co., Ltd. In the Center for Living Environment Engineering (56) Reference JP-A-64-75869 (JP, A) JP Japanese Unexamined Patent Publication No. 3-91635 (JP, A) Japanese Unexamined Patent Publication No. 6-347144 (JP, A) Japanese Unexamined Patent Publication No. 2-166330 (JP, A) Japanese Unexamined Patent Publication No. 5-346246 (JP, A) Actual Development Sho 63-2022 (JP , U) J. Kohei 4-38178 (JP, Y2) (58) Fields investigated (Int.Cl. 7 , DB name) F24F 5/00 102 F25C 1/00

Claims (9)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 第1蒸発器と第2蒸発器を有する冷凍
機、第1蒸発器により過冷却される水または水に添加物
を添加した水溶液の過冷却を解除し、シャーベット状の
氷を生成させる過冷却解除手段、上記シャーベット状の
氷を蓄える第1蓄熱槽、第1蓄熱槽内の水または水溶液
を第1蒸発器に送り循環させる第1水循環ポンプ、第1
蓄熱槽内の水もしくは水溶液、またはシャーベット状の
氷が混合した氷水を熱負荷に送り循環させる第2水循環
ポンプ、第2蒸発器を槽内に配し、第2蒸発器の外周に
生成する氷塊状の氷を蓄える第2蓄熱槽、並びに第1蓄
熱槽と第2蓄熱槽を接続する連通管を備え、第2蓄熱
槽、第1水循環ポンプ、第1蒸発器、第1蓄熱槽、連通
管の順で上記水または水溶液が循環する第1水循環路
と、第1蓄熱槽、第2水循環ポンプ、熱負荷、第2蓄熱
槽、連通管の順で上記水もしくは水溶液、または上記氷
水が循環する第2水循環路を構成した氷蓄熱装置。
1. A refrigerator having a first evaporator and a second evaporator, water that is supercooled by the first evaporator or an aqueous solution obtained by adding an additive to water is released from supercooling, and sherbet-like ice is removed. Supercooling releasing means for generating, a first heat storage tank for storing the sherbet-like ice, a first water circulation pump for sending and circulating water or an aqueous solution in the first heat storage tank to the first evaporator, first
A second water circulation pump that sends water or an aqueous solution in a heat storage tank or ice water mixed with sherbet-like ice to a heat load and circulates it, and arranges a second evaporator in the tank, and an ice block that forms on the outer periphery of the second evaporator Second heat storage tank for storing ice-like ice, and a communication pipe connecting the first heat storage tank and the second heat storage tank, the second heat storage tank, the first water circulation pump, the first evaporator, the first heat storage tank, the communication pipe The water or aqueous solution or the ice water circulates in the order of the first water circulation path through which the water or aqueous solution circulates, the first heat storage tank, the second water circulation pump, the heat load, the second heat storage tank, and the communication pipe. An ice heat storage device that constitutes a second water circulation path.
【請求項2】 請求項1記載の氷蓄熱装置において、第
1蒸発器を流れる冷媒の流量と第2蒸発器を流れる冷媒
の流量を制御する制御手段を設けたことを特徴とする氷
蓄熱装置。
2. The ice heat storage device according to claim 1, further comprising control means for controlling a flow rate of the refrigerant flowing through the first evaporator and a flow rate of the refrigerant flowing through the second evaporator. .
【請求項3】 蒸発器を有し、少なくとも0℃において
凝固しない不凍液を冷却する冷凍機、この冷凍機により
冷却された上記不凍液と、水または水に添加物を添加し
た水溶液を熱交換させて上記水または水溶液を過冷却す
る過冷却水生成熱交換器、上記冷凍機により冷却された
上記不凍液と、水または水に添加物を添加した水溶液を
熱交換させて氷塊状の氷を生成する氷塊状氷生成熱交換
器、上記過冷却水生成熱交換器及び上記氷塊状氷生成熱
交換器に上記不凍液を送る不凍液循環ポンプ、過冷却さ
れた上記水または水溶液の過冷却を解除し、シャーベッ
ト状の氷を生成させる過冷却解除手段、上記シャーベッ
ト状の氷を蓄える第1蓄熱槽、第1蓄熱槽内の水または
水溶液を上記過冷却水生成熱交換器に送り循環させる第
1水循環ポンプ、第1蓄熱槽内の水もしくは水溶液、ま
たはシャーベット状の氷が混合した氷水を熱負荷に送り
循環させる第2水循環ポンプ、上記氷塊状氷生成熱交換
器を槽内に配し、上記氷塊状氷生成熱交換器の外周に生
成する氷塊状の氷を蓄える第2蓄熱槽、並びに第1蓄熱
槽と第2蓄熱槽を接続する連通管を備え、上記蒸発器、
不凍液循環ポンプ、氷塊状氷生成熱交換器及び過冷却水
生成熱交換器の順で上記不凍液が循環する不凍液循環路
と、第2蓄熱槽、第1水循環ポンプ、過冷却水生成熱交
換器、第1蓄熱槽、連通管の順で上記水または水溶液が
循環する第1水循環路と、第1蓄熱槽、第2水循環ポン
プ、熱負荷、第2蓄熱槽、連通管の順で上記水もしくは
水溶液、または上記氷水が循環する第2水循環路を構成
した氷蓄熱装置。
3. A refrigerator having an evaporator, which cools an antifreeze liquid that does not solidify at least 0 ° C., and heat exchange is performed between the antifreeze liquid cooled by the refrigerator and water or an aqueous solution obtained by adding an additive to water. A supercooled water generation heat exchanger that supercools the water or the aqueous solution, the antifreeze liquid cooled by the refrigerator, and an ice mass that generates ice mass ice by heat exchange of water or an aqueous solution in which an additive is added to water. Ice-cooling pump, an antifreeze circulation pump for sending the antifreeze to the ice-cooled ice-cooling heat exchanger, the ice-cooled ice-cooling heat exchanger, and the supercooled water or aqueous solution to remove the supercooling. Means for generating ice, a first heat storage tank for storing the sherbet-like ice, a first water circulation pump for circulating water or an aqueous solution in the first heat storage tank to the supercooled water generation heat exchanger, 1) Water or aqueous solution in heat storage tank, or second water circulation pump for sending and circulating ice water mixed with sherbet-like ice to heat load, the above ice block ice formation heat exchanger is arranged in the tank, and above ice block ice formation An evaporator having a second heat storage tank for storing ice-lump-like ice generated on the outer periphery of the heat exchanger, and a communication pipe connecting the first heat storage tank and the second heat storage tank,
An antifreeze liquid circulation passage through which the above antifreeze liquid circulates in the order of an antifreeze liquid circulation pump, an ice block ice formation heat exchanger, and a supercooled water formation heat exchanger, a second heat storage tank, a first water circulation pump, a supercooled water generation heat exchanger, A first water circulation path in which the water or aqueous solution circulates in the order of the first heat storage tank and the communication pipe, and the water or aqueous solution in the order of the first heat storage tank, the second water circulation pump, the heat load, the second heat storage tank, and the communication pipe. Or an ice heat storage device that constitutes a second water circulation path through which the ice water circulates.
【請求項4】 請求項3記載の氷蓄熱装置において、氷
塊状氷生成熱交換器を流れる不凍液の流量と、過冷却水
生成熱交換器を流れる不凍液の流量を制御する制御手段
を設けたことを特徴とする氷蓄熱装置。
4. The ice heat storage device according to claim 3, further comprising a control means for controlling a flow rate of the antifreeze liquid flowing through the ice block ice generating heat exchanger and a flow rate of the antifreeze liquid flowing through the supercooled water generating heat exchanger. An ice heat storage device characterized by.
【請求項5】 請求項1または3記載の氷蓄熱装置にお
いて、第1蓄熱槽内に、第1蓄熱槽内のシャーベット状
の氷と水または水溶液とを混合する氷水混合手段を設け
たことを特徴とする氷蓄熱装置。
5. The ice heat storage device according to claim 1 or 3, wherein ice water mixing means for mixing the sherbet-shaped ice in the first heat storage tank with water or an aqueous solution is provided in the first heat storage tank. A characteristic ice heat storage device.
【請求項6】 請求項1または3記載の氷蓄熱装置にお
いて、第2水循環路に、水または水溶液が熱負荷から第
1蓄熱槽に送水される流路を設けるとともに、上記熱負
荷から第1蓄熱槽に送水される流路と上記熱負荷から第
2蓄熱槽に送水される流路とを切り替える流路切り替え
手段を設けたことを特徴とする氷蓄熱装置。
6. The ice heat storage device according to claim 1 or 3, wherein the second water circulation passage is provided with a flow path for sending water or an aqueous solution from a heat load to the first heat storage tank, and the first heat storage device is connected to the first heat storage tank. An ice heat storage device comprising flow path switching means for switching between a flow path for supplying water to the heat storage tank and a flow path for supplying water to the second heat storage tank from the heat load.
【請求項7】 請求項1または3に記載の氷蓄熱装置に
おいて、第1水循環路に、水または水溶液が第1蒸発器
または過冷却水生成熱交換器から第2蓄熱槽に送水され
る流路を設けるとともに、第1蒸発器または過冷却水生
成熱交換器から第2蓄熱槽に送水される流路と、第1蒸
発器または過冷却水生成熱交換器から第1蓄熱槽に送水
される流路とを切り替える流路切り替え手段を設けたこ
とを特徴とする氷蓄熱装置。
7. The ice heat storage device according to claim 1 or 3, wherein water or an aqueous solution is fed to the first water circulation path from the first evaporator or the supercooled water generation heat exchanger to the second heat storage tank. A channel is provided, and a flow path for sending water from the first evaporator or supercooled water generation heat exchanger to the second heat storage tank, and a flow path for water from the first evaporator or supercooled water generation heat exchanger to the first heat storage tank An ice heat storage device, characterized in that it is provided with a flow path switching means for switching between the flow path and the flow path.
【請求項8】 請求項1または3に記載の氷蓄熱装置に
おいて、第1水循環路に、水または水溶液が第1蓄熱槽
から第1蒸発器または過冷却水生成熱交換器に送水され
る流路を設けるとともに、第1蓄熱槽から第1蒸発器ま
たは過冷却水生成熱交換器に送水される流路と、第2蓄
熱槽から第1蒸発器または過冷却水生成熱交換器に送水
される流路とを切り替える流路切り替え手段を設けたこ
とを特徴とする氷蓄熱装置。
8. The ice heat storage device according to claim 1 or 3, wherein water or an aqueous solution is sent to the first water circulation path from the first heat storage tank to the first evaporator or the supercooled water generation heat exchanger. A channel is provided, and a flow path from the first heat storage tank to the first evaporator or the supercooled water generation heat exchanger, and a flow path from the second heat storage tank to the first evaporator or the supercooled water generation heat exchanger. An ice heat storage device, characterized in that it is provided with a flow path switching means for switching between the flow path and the flow path.
【請求項9】 請求項8記載の氷蓄熱装置において、第
2水循環路に、水または水溶液が熱負荷から第1蓄熱槽
に送水される流路を設けるとともに、上記熱負荷から第
1蓄熱槽に送水される流路と上記熱負荷から第2蓄熱槽
に送水される流路とを切り替える流路切り替え手段を設
けたことを特徴とする氷蓄熱装置。
9. The ice heat storage device according to claim 8, wherein the second water circulation path is provided with a flow path through which water or an aqueous solution is fed from a heat load to the first heat storage tank, and the heat load is used to supply the first heat storage tank. An ice heat storage device, characterized in that a flow path switching means is provided for switching between a flow path for supplying water to the second heat storage tank and a flow path for supplying water to the second heat storage tank.
JP12362195A 1995-05-23 1995-05-23 Ice storage device Expired - Fee Related JP3367274B2 (en)

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JP12362195A JP3367274B2 (en) 1995-05-23 1995-05-23 Ice storage device

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Publication Number Publication Date
JPH08313017A JPH08313017A (en) 1996-11-29
JP3367274B2 true JP3367274B2 (en) 2003-01-14

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CN104279724A (en) * 2014-08-25 2015-01-14 广西申能达智能技术有限公司 Heat pump control method and heat pump control system of energy-saving air conditioner

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