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JPH0799303B2 - Ice making equipment - Google Patents
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JPH0799303B2 - Ice making equipment - Google Patents

Ice making equipment

Info

Publication number
JPH0799303B2
JPH0799303B2 JP2158092A JP15809290A JPH0799303B2 JP H0799303 B2 JPH0799303 B2 JP H0799303B2 JP 2158092 A JP2158092 A JP 2158092A JP 15809290 A JP15809290 A JP 15809290A JP H0799303 B2 JPH0799303 B2 JP H0799303B2
Authority
JP
Japan
Prior art keywords
heat exchanger
water
refrigerant
main heat
refrigerant circuit
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
JP2158092A
Other languages
Japanese (ja)
Other versions
JPH0448174A (en
Inventor
功 近藤
弘二 松岡
伸二 松浦
優司 仲沢
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.)
Daikin Industries Ltd
Original Assignee
Daikin Industries Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Daikin Industries Ltd filed Critical Daikin Industries Ltd
Priority to JP2158092A priority Critical patent/JPH0799303B2/en
Publication of JPH0448174A publication Critical patent/JPH0448174A/en
Publication of JPH0799303B2 publication Critical patent/JPH0799303B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

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  • Production, Working, Storing, Or Distribution Of Ice (AREA)
  • Other Air-Conditioning Systems (AREA)

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、水等のスラリー状の氷化物を生成して蓄氷槽
に貯溜するようにした製氷装置に係り、特に性能の向上
対策に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an ice making device that produces a slurry-like iced substance such as water and stores it in an ice storage tank, and particularly relates to measures for improving performance. .

(従来の技術) 従来より、例えば実開平1−144722号公報に開示される
如く、冷媒回路に介設される熱交換器と蓄氷槽との間で
蓄氷槽の水を循環させる水循環路を設け、冷媒回路の冷
媒との熱交換により蓄氷槽の水等をスラリー状の氷にす
るようにした製氷装置において、水循環路の出口側に開
放して、過冷却状態にある水を蓄水槽の水面より一定高
さに設置された傾斜樋に落下させ、この傾斜樋を通過す
る間に水をスラリー状に氷化させて、下方の蓄氷槽に氷
化物を貯溜しようとするものは公知の技術である。
(Prior Art) Conventionally, for example, as disclosed in Japanese Utility Model Laid-Open No. 1-144722, a water circulation path for circulating water in an ice storage tank between a heat exchanger and an ice storage tank provided in a refrigerant circuit. In the ice making device in which the water in the ice storage tank is turned into slurry ice by heat exchange with the refrigerant in the refrigerant circuit, the water is opened in the outlet side of the water circulation path to store the water in the supercooled state. The ones that drop ice into a slant gutter installed at a certain height above the water surface of the water tank, ice the water into a slurry while passing through this slant gutter, and store iced substances in the ice storage tank below This is a known technique.

また、同公報において、上記冷媒回路の冷媒等を利用し
て水をさらに過冷却する過冷却ゾーンを上記傾斜樋の途
中に設けることにより、水の過冷却状態を解消させて氷
化を生ずるようにすることも開示されている。
Further, in the same publication, by providing a supercooling zone for further subcooling water by using the refrigerant or the like of the refrigerant circuit in the middle of the inclined trough, the supercooled state of water is eliminated and ice formation is caused. It is also disclosed.

(発明が解決しようとする課題) しかしながら、上記従来のもののように、水の過冷却状
態を解消する過冷却解消部を蓄氷槽の上方に設けると、
そのためのスペースが必要となり設計上の制約が大きく
なるとともに、いったん空気中に水を晒すことで、空気
中に冷熱が放出され、熱損失が大きいという問題があ
る。
(Problems to be Solved by the Invention) However, when a supercooling elimination section for eliminating a supercooled state of water is provided above the ice storage tank as in the conventional one,
There is a problem in that a space for that is required, design constraints become large, and once the water is exposed to the air, cold heat is released into the air, resulting in a large heat loss.

そこで、水循環路を閉回路とし、水循環路の中で水に過
冷却状態を生ぜしめ、かつその過冷却状態を解消させて
スラリー状の氷化物を生成し、蓄氷槽に循環させること
により、設計上の制約や熱損失を回避することが考えら
れる。
Therefore, by setting the water circulation path as a closed circuit, a supercooled state is produced in the water in the water circulation path, and the supercooled state is eliminated to generate a slurry-like iced substance, which is circulated in the ice storage tank. It is possible to avoid design restrictions and heat loss.

また、水の過冷却状態を解消する手段として、上記従来
のもののように、冷媒回路の冷媒を利用して、過冷却状
態にある水を冷却する手段を設けることが考えられる。
Further, as a means for eliminating the supercooled state of water, it is conceivable to provide a means for cooling the water in the supercooled state by utilizing the refrigerant in the refrigerant circuit, as in the conventional device.

しかるに、上記従来の公報には、具体的に傾斜樋の途中
を冷却する手段が開示されていないので、どのような作
用により、冷却状態の解消が行われうるのかについては
不明である。また、過冷却状態を生ぜしめる熱交換器と
冷媒回路を共用する際の具体的な構成についても不明で
あるために、そのままで過冷却状態を解消するための実
効を得られない虞れがある。
However, since the above-mentioned conventional publication does not specifically disclose means for cooling the middle of the inclined gutter, it is unclear what action can be taken to eliminate the cooled state. Further, since the specific configuration when the heat exchanger and the refrigerant circuit that share the supercooled state are shared is unknown, it may not be possible to obtain the effect for eliminating the supercooled state as it is. .

本発明は、過冷却状態にある水等がさらにその温度より
も低温になるよう再冷却されることにより、過冷却され
た水等の中で発生,消滅する氷の結晶の芽の径が成長に
向かうに十分な所定の臨界径に達する確率が高くなる点
に着目し、冷媒回路から冷却用の熱交換器にバイパスさ
せた冷媒の蒸発温度を熱交換器側よりも低くする手段を
講ずることにより、熱交換器で過冷却された水等の過冷
却状態を迅速に解消させ、もって、製氷装置の性能の向
上を図ることにある。
INDUSTRIAL APPLICABILITY According to the present invention, by supercooling water or the like which is further cooled to a temperature lower than that temperature, the diameter of buds of ice crystals that grow and disappear in the supercooled water grows. Paying attention to the fact that the probability of reaching the predetermined critical diameter that is sufficient to reach the temperature will increase, and measures will be taken to lower the evaporation temperature of the refrigerant bypassed from the refrigerant circuit to the cooling heat exchanger than the heat exchanger side. Thus, the supercooled state of water or the like supercooled by the heat exchanger can be promptly eliminated, and the performance of the ice making device can be improved.

(課題を解決するための手段) 上記目的を達成するため本発明の第1の解決手段は、第
1図に示すように、製氷装置に、水又は水溶液のスラリ
ー状の氷化物を貯溜するための製氷槽(5)と、水又は
水溶液を過冷却するための主熱交換器(22)と、閉環状
の断面を有する管部材で構成され上記主熱交換器(22)
と製氷槽(5)との間で水又は水溶液を強制循環させる
ための水循環炉(51)と、上記主熱交換器(22)下流側
の水循環路(51)に配置され主熱交換器(1)で過冷却
された水又は水溶液の過冷却状態を解消させるようさら
に低温の状態まで再冷却する副熱交換器(8)と、圧縮
機,凝縮器及び蒸発器となる上記主熱交換器(22)を順
次接続してなる閉回路の冷媒回路(1)と、上記冷媒回
路(1)の主熱交換器(22)の出口側配管となるガスラ
インに配置され通過する冷媒に圧力損失を与える減圧手
段と、上記冷媒回路(1)の液ラインとガスラインとの
間を上記主熱交換器(22)及び減圧手段をバイパスしか
つ蒸発器となる上記副熱交換器(8)を介して接続する
バイパス路(81)とを設け、上記副熱交換器(8)にお
ける冷媒の蒸発温度は上記主熱交換器(22)における冷
媒の蒸発温度よりも低くする構成としたものである。
(Means for Solving the Problem) In order to achieve the above object, the first means for solving the problems is to store a slurry of iced water or an aqueous solution in an ice making device as shown in FIG. The ice making tank (5), a main heat exchanger (22) for supercooling water or an aqueous solution, and a pipe member having a closed ring-shaped cross section, the main heat exchanger (22)
And a water circulation furnace (51) for forcibly circulating water or an aqueous solution between the ice making tank (5) and the main heat exchanger (51) arranged in the water circulation path (51) on the downstream side of the main heat exchanger (22). A sub heat exchanger (8) for recooling to a lower temperature state so as to eliminate the supercooled state of the water or aqueous solution supercooled in 1), and the main heat exchanger serving as a compressor, a condenser and an evaporator. Pressure loss to the passing refrigerant which is arranged in the closed circuit refrigerant circuit (1) in which (22) are sequentially connected and the gas line serving as the outlet side pipe of the main heat exchanger (22) of the refrigerant circuit (1). The decompressing means for supplying the refrigerant and the sub-heat exchanger (8) serving as an evaporator by bypassing the main heat exchanger (22) and the decompressing means between the liquid line and the gas line of the refrigerant circuit (1). A bypass path (81) connected via the above is provided, and the evaporation temperature of the refrigerant in the sub heat exchanger (8) is It is obtained by a configuration to be lower than the evaporation temperature of the refrigerant in the serial main heat exchanger (22).

第2の解決手段は、上記第1の解決手段において、冷媒
回路(1)にガスラインにアキュムレータ(Ac)を介設
し、減圧手段をこのアキュムレータ(Ac)で構成したも
のである。
A second solving means is the above first solving means, wherein an accumulator (Ac) is provided in the gas line in the refrigerant circuit (1) and the depressurizing means is constituted by this accumulator (Ac).

(作用) 以上の構成により、請求項(1)の発明では、主熱交換
器(22)下流の復管路(51B)において、副熱交換器
(8)で、減圧手段(C4)を介して冷媒回路(1)の液
ラインからバイパスされた冷媒との熱交換により、水等
が冷却される。
(Operation) With the above configuration, in the invention of claim (1), the decompression means (C 4 ) is provided in the auxiliary heat exchanger (8) in the return conduit (51B) downstream of the main heat exchanger (22). Water or the like is cooled by heat exchange with the refrigerant bypassed from the liquid line of the refrigerant circuit (1) via the.

その場合、水等は主熱交換器(22)によりすでに過冷却
されているため、この過冷却状態を解消させるには、さ
らに低温に冷却することが必要となる。ここで、本発明
では、副熱交換器(8)は冷媒回路(1)の液ラインか
ら冷媒をバイパスさせる冷却用バイパス路(81)に介設
され、副熱交換器(8)と主熱交換器(22)とは、冷却
回路(1)の液ラインとガスラインとの間で互いに並列
に接続されたことになり、主熱交換器(22)側のガスラ
インには、冷媒の圧力損失を与える減圧手段が設けら
れ、副熱交換器(8)における冷媒の蒸発温度は主熱交
換器(22)における冷媒の蒸発温度よりも低く維持され
ている。したがって、副熱交換器(8)において、過冷
却状態にある水等がさらに低温に冷却され、過冷却状態
が解消されて、スラリー状に氷化することになる。
In this case, since water and the like have already been supercooled by the main heat exchanger (22), it is necessary to cool the water to a lower temperature in order to eliminate this supercooled state. Here, in the present invention, the sub heat exchanger (8) is provided in the cooling bypass passage (81) for bypassing the refrigerant from the liquid line of the refrigerant circuit (1), and the sub heat exchanger (8) and the main heat The exchanger (22) means that the liquid line and the gas line of the cooling circuit (1) are connected in parallel with each other, and the pressure of the refrigerant is added to the gas line on the main heat exchanger (22) side. A pressure reducing means for giving a loss is provided, and the evaporation temperature of the refrigerant in the sub heat exchanger (8) is kept lower than the evaporation temperature of the refrigerant in the main heat exchanger (22). Therefore, in the sub heat exchanger (8), water or the like in a supercooled state is further cooled to a lower temperature, the supercooled state is eliminated, and it is frozen into a slurry.

請求項(2)の発明では、上記請求項(1)の発明にお
いて、冷却回路(1)のガスラインにアキュムレータ
(Ac)が介設されており、このアキュムレータ(Ac)が
主熱交換器(22)側の冷媒の流れに対する減圧手段とし
て機能するので、主熱交換器(22)の蒸発温度よりも副
熱交換器(8)の蒸発温度が低温に維持され、別途圧力
損失を与える手段を設けることなく、上記請求項(1)
の発明の作用が得られることになる。
According to the invention of claim (2), in the invention of claim (1), an accumulator (Ac) is provided in the gas line of the cooling circuit (1), and the accumulator (Ac) is the main heat exchanger (Ac). Since it functions as a pressure reducing means for the flow of the refrigerant on the 22) side, the evaporation temperature of the sub heat exchanger (8) is kept lower than the evaporation temperature of the main heat exchanger (22), and a means for separately providing a pressure loss is provided. Claim (1) above without provision
The effect of the invention can be obtained.

(実施例) 以下、本発明の実施例について、第2図以下の図面に基
づき説明する。
(Embodiment) An embodiment of the present invention will be described below with reference to the drawings starting from FIG.

第2図は第1実施例の空気調和装置の冷媒回路(1)の
構成を示し、(11)は第1圧縮機、(12)は該第1圧縮
機(11)の吐出側に配置され、冷媒と室外空気との熱交
換を行う室外熱交換器、(13)は該室該熱交換器(12)
の冷媒流量を調節し、又は減圧を行う室外電動膨張弁で
あって、上記各機器(11)〜(13)を第1管路(14)中
で直列に接続されている。
FIG. 2 shows the configuration of the refrigerant circuit (1) of the air conditioner of the first embodiment, where (11) is the first compressor and (12) is the discharge side of the first compressor (11). An outdoor heat exchanger for exchanging heat between the refrigerant and the outdoor air, (13) the heat exchanger (12)
Is an outdoor electric expansion valve that adjusts the refrigerant flow rate or reduces the pressure, and the above-mentioned devices (11) to (13) are connected in series in the first conduit (14).

また、(21)は第2圧縮機、(22)は該第2圧縮機(2
1)の吐出側に配置され、後述の蓄水槽(5)の水又は
水溶液を過冷却するための主熱交換器である水熱交換
器、(23)は該水熱交換器(22)が凝縮器として機能す
るときには冷媒流量を調節し、蒸発器として機能すると
きには冷媒の減圧を行う水側電動膨張弁であって、上記
各機器(21)〜(23)は第2管路(24)中で直列に接続
されている。
Further, (21) is the second compressor, (22) is the second compressor (2
A water heat exchanger, which is arranged on the discharge side of 1) and is a main heat exchanger for supercooling water or an aqueous solution in a water storage tank (5) described later, and (23) is a water heat exchanger (22). A water-side electric expansion valve that regulates the flow rate of the refrigerant when functioning as a condenser, and decompresses the refrigerant when functioning as an evaporator, and each of the devices (21) to (23) is a second conduit (24). Are connected in series inside.

なお、(SD1),(SD2)はそれぞれ各圧縮機(11),
(21)の吐出管に設けられた油分離器、(C1),(C2
は該各油分離器(SD1),(SD2)から各圧縮機(11),
(21)の吸入側にそれぞれ設けられた油戻し管(R
T1),(RT2)にそれぞれ介設された減圧用キャピラリ
チューブである。
Note that (SD 1 ) and (SD 2 ) are each compressor (11),
Oil separator provided in the discharge pipe of (21), (C 1 ), (C 2 )
From the oil separators (SD 1 ) and (SD 2 ) to the compressors (11) and
Oil return pipes (R) provided on the suction side of (21)
It is a capillary tube for decompression, which is provided in each of T 1 ) and (RT 2 ).

さらに、(32),(32)は各室内に配置される室内熱交
換器、(33),(33)は冷媒を減圧する減圧弁としての
室内電動膨張弁であって、上記各機器(32),(33)は
各々直列に接続され、かつその各組が第3管路(34)中
で並列に接続されている。
Further, (32) and (32) are indoor heat exchangers arranged in each room, and (33) and (33) are indoor electric expansion valves as pressure reducing valves for reducing the pressure of the refrigerant, and the above-mentioned devices (32). ) And (33) are connected in series, and each set is connected in parallel in the third conduit (34).

そして、上記第1管路(14)及び第2管路(24)は第3
管路(34)に対して並列に接続されている。なお、(A
c)は各圧縮機(11),(21)の吸入側となる第3管路
(34)に設けられたアキュムレータである。
The first pipeline (14) and the second pipeline (24) are the third
It is connected in parallel to the pipe line (34). Note that (A
c) is an accumulator provided in the third conduit (34) on the suction side of each compressor (11), (21).

また、(2)は室外熱交換器(12)のガス管と室内熱交
換器(32),(32)のガス管とを各圧縮機(11),(2
1)の吐出側又は吸入側に交互に連通させるよう切換え
る四路切換弁(2)であって、該四路切換弁(2)が図
中実線側に切換わったときには室外熱交換器(12)が凝
縮器、室内熱交換器(32),(32)が蒸発器として機能
して室内で冷房運転を行う一方、四路切換弁(2)が図
中破線側に切換わったときには室外熱交換器(12)が蒸
発器、室内熱交換器(32),(32)が凝縮器として機能
して室内で暖房運転を行うようになされている。
Further, (2) includes a gas pipe of the outdoor heat exchanger (12) and gas pipes of the indoor heat exchangers (32) and (32) in the compressors (11) and (2
A four-way switching valve (2) which is switched so as to alternately communicate with the discharge side or the suction side of 1), and when the four-way switching valve (2) is switched to the solid line side in the figure, the outdoor heat exchanger (12 ) Functions as a condenser and the indoor heat exchangers (32) and (32) function as evaporators to perform indoor cooling operation, while the four-way switching valve (2) switches to the side of the broken line in the figure, the outdoor heat The exchanger (12) functions as an evaporator, and the indoor heat exchangers (32), (32) function as condensers to perform indoor heating operation.

さらに、該水熱交換器(22)のガス管と各圧縮機(1
1),(21)の吸入管とをバイパス接続する分岐路(2
5)と、水熱交換器(22)のガス管を上記第2圧縮機(2
1)の吐出管と分岐路(25)とに交互に連通させる水側
切換弁(26)とが設けられている。該水側切換弁(26)
は四路切換弁のうちの3つのポートを利用しており、水
側切換弁(26)が図中実線側に切換わったときには水熱
交換器(22)のガス管が分岐路(25)側つまり各圧縮機
(11),(21)の吸入側に連通し、水熱交換器(22)が
蒸発器として機能する一方、水側切換弁(26)が図中破
線側に切換わったときには水熱交換器(22)のガス管が
第2圧縮機(21)の吐出管に連通し、水熱交換器(22)
が凝縮器として機能するようになされている。なお、
(C3)は水側切換弁(26)のデッドポート側の配管に介
設されたキャピラリチューブである。
Further, the gas pipe of the water heat exchanger (22) and each compressor (1
Branch path (2) that bypass-connects the suction pipes of 1) and (21)
5) and the gas pipe of the water heat exchanger (22) to the second compressor (2
A water side switching valve (26) for alternately communicating with the discharge pipe of 1) and the branch passage (25) is provided. The water side switching valve (26)
Uses three ports of the four-way switching valve, and when the water side switching valve (26) is switched to the solid line side in the figure, the gas pipe of the water heat exchanger (22) has a branch path (25). Side, that is, communicating with the suction side of each compressor (11), (21), the water heat exchanger (22) functions as an evaporator, while the water side switching valve (26) is switched to the broken line side in the figure. Sometimes the gas pipe of the water heat exchanger (22) communicates with the discharge pipe of the second compressor (21), and the water heat exchanger (22)
Is designed to function as a condenser. In addition,
(C 3 ) is a capillary tube provided in the pipe on the dead port side of the water side switching valve (26).

さらに、第1圧縮機(11)及び第2圧縮機(21)の吐出
管同士を接続するバイパス路(3)が設けられていて、
該バイパス路(3)には第2圧縮機(21)の吐出管側か
ら第1圧縮機(11)の吐出管側への冷媒流通のみを許容
する逆止弁(4)が介設されている。
Furthermore, a bypass passage (3) for connecting the discharge pipes of the first compressor (11) and the second compressor (21) is provided,
A check valve (4) which allows only refrigerant flow from the discharge pipe side of the second compressor (21) to the discharge pipe side of the first compressor (11) is provided in the bypass passage (3). There is.

すなわち、室外熱交換器(12)及び水熱交換器(22)が
凝縮器として機能する際、水熱交換器(22)における凝
縮濃度が高く圧力が高くなった場合、第2圧縮機(21)
の吐出ガスを室外熱交換器(12)側に逃がすことによ
り、放熱量を分配しうるようになされている。
That is, when the outdoor heat exchanger (12) and the water heat exchanger (22) function as condensers, when the condensation concentration in the water heat exchanger (22) is high and the pressure is high, the second compressor (21 )
The discharged gas is discharged to the outdoor heat exchanger (12) side so that the heat radiation amount can be distributed.

ここで、空気調和装置には、蓄熱媒体としての水又は水
溶液のスラリー状の氷化物を貯溜するための蓄氷槽
(5)が配置されていて、該蓄水槽(5)と水熱交換器
(22)との間は、水循環路(51)により水又は水溶液の
循環可能に接続されている。該水循環路(51)は、蓄氷
槽(5)の底部から水熱交換器(22)に水等を供給する
往管路(51A)と、水熱交換器(22)から蓄氷槽(5)
の上部に水等のスラリー状の氷化物を戻す復管路(51
B)とからなっており、往復路(51A)に介設されたポン
プ(52)により、水循環路(51)内で蓄氷槽(5)の水
又は水溶液を強制循環させるようになされている。
Here, the air conditioner is provided with an ice storage tank (5) for storing a slurry iced product of water or an aqueous solution as a heat storage medium, and the water storage tank (5) and the water heat exchanger. A water circulation path (51) is connected to the (22) so that water or an aqueous solution can circulate. The water circulation path (51) includes a forward path (51A) for supplying water and the like from the bottom of the ice storage tank (5) to the water heat exchanger (22), and an ice storage tank (22) from the water heat exchanger (22). 5)
Return conduit (51
B) and is configured to forcibly circulate the water or aqueous solution in the ice storage tank (5) in the water circulation path (51) by the pump (52) provided in the reciprocating path (51A). .

そして、水循環路(51)の往管路(51A)のポンプ(5
2)の下流側には、水循環路(51)の水又は水溶液中の
氷結物やゴミ等の固体物を除去するストレーナ(53)が
介設され、さらに、該ストレーナ(53)の下流側には、
水熱交換器(22)に供給される水等が予熱する予熱熱交
換器(6)が介設されている。一方、冷媒回路(1)の
液ラインには、液冷媒の一部を水側電動膨張弁(23)を
バイパスさせて予熱熱交換器(6)に流通させる予熱バ
イパス路(61)が設けられていて、該予熱バイパス路
(61)の予熱熱交換器(6)の下流側には、冷媒の減圧
機能及び流量制御機能を有する予熱電動膨張弁(62)が
介設されている。該予熱電動膨張弁(62)と水側電動膨
張弁(23)とにより、予熱バイパス路(61)の冷媒流量
を調節するとともに、水熱交換器(22)の製氷運転時に
おける冷媒の減圧をも行うようになされている。
Then, the pump (5) of the forward path (51A) of the water circulation path (51)
On the downstream side of 2), a strainer (53) for removing solid matters such as iced matter and dust in the water or aqueous solution of the water circulation path (51) is provided, and further on the downstream side of the strainer (53). Is
A preheat heat exchanger (6) for preheating water or the like supplied to the water heat exchanger (22) is provided. On the other hand, the liquid line of the refrigerant circuit (1) is provided with a preheating bypass passage (61) for flowing a part of the liquid refrigerant to the preheat heat exchanger (6) by bypassing the water side electric expansion valve (23). On the downstream side of the preheat heat exchanger (6) in the preheat bypass passage (61), a preheat electric expansion valve (62) having a refrigerant decompression function and a flow rate control function is provided. The preheat electric expansion valve (62) and the water side electric expansion valve (23) adjust the refrigerant flow rate of the preheat bypass passage (61) and reduce the pressure of the refrigerant during the ice making operation of the water heat exchanger (22). Is also supposed to do.

さらに、上記水循環路(51)の復管路(51B)におい
て、水熱交換器(22)の下流側には、復管路(51B)の
水等を冷却して水熱交換器(22)で過冷却された水等の
過冷却状態を解消させる副熱交換器としての再冷却器
(8)が設けられ、さらに、該再冷却器(8)と水熱交
換器(22)との間には、復管路(51B)の凍結が水熱交
換器(22)まで進展するのを阻止するための凍結進展防
止部としての保温熱交換器(7)が設けられている。
Further, in the return pipe (51B) of the water circulation passage (51), the water or the like in the return pipe (51B) is cooled to the downstream side of the water heat exchanger (22) to cool the water heat exchanger (22). Is provided with a recooler (8) as a sub-heat exchanger for eliminating a supercooled state of water or the like supercooled by the subcooler, and further between the recooler (8) and the water heat exchanger (22). The heat insulation heat exchanger (7) is provided in the as a freezing progress preventing unit for preventing the freezing of the return conduit (51B) from progressing to the water heat exchanger (22).

ここで、冷媒回路(1)の液ラインと、各圧縮機(1
1),(21)の吸入側となる分岐路(ガスライン)との
間には、水熱交換器(22)をバイパスして冷媒を流通さ
せる再冷却バイパス路(81)が設けられていて、該再冷
却バイパス路(81)には、上流側から順に上記再冷却キ
ャピラリチューブ(C4)及び再冷却器(8)が介設され
ている。つまり、再冷却器(8)に再冷却キャピラリチ
ューブ(C4)で減圧された低温の冷媒を流通させ、この
冷媒との熱交換により水熱交換器(22)で過冷却された
水等を再冷却するようになされている。
Here, the liquid line of the refrigerant circuit (1) and each compressor (1
A recooling bypass passage (81) is provided between the branch passage (gas line) on the suction side of 1) and (21) to allow the refrigerant to flow by bypassing the water heat exchanger (22). The recooling bypass passage (81) is provided with the recooling capillary tube (C 4 ) and the recooler (8) in this order from the upstream side. That is, a low-temperature refrigerant whose pressure has been reduced by the re-cooling capillary tube (C 4 ) is circulated in the re-cooling device (8), and the water and the like supercooled in the water heat exchanger (22) are exchanged by heat exchange with this refrigerant. It is designed to recool.

その場合、水熱交換器(22)のガス側配管を上記水側切
換弁(26)を介して分岐路(25)に連通させる一方、再
冷却器(8)のガス側を直接分岐路(25)に連通させる
ことにより、水側切換弁(26)の通過による流通抵抗分
だけ水熱交換器(22)に圧力損失を生ぜしめ、再冷却器
(8)の蒸発温度を水熱交換器(22)よりも低温に維持
して、水熱交換器(22)で過冷却された水等を再冷却器
(8)でさらに低温に冷却しうるようになされている。
In that case, the gas side pipe of the water heat exchanger (22) is connected to the branch passage (25) through the water side switching valve (26), while the gas side of the recooler (8) is directly branched ( By communicating with the water side switching valve (26), pressure loss is caused in the water heat exchanger (22) by the passage of the water side switching valve (26), and the evaporation temperature of the recooler (8) is changed to the water heat exchanger. The temperature is maintained lower than that of (22), and the water and the like supercooled by the water heat exchanger (22) can be further cooled by the recooler (8).

なお、上記冷媒回路(1)の液ラインからこの保温熱交
換器(7)に液冷媒をバイパスして流通させて液ライン
に戻すようにした保温バイパス路(71)が設けられてい
て、保温熱交換器(7)において、液ラインの液冷媒と
の熱交換により復管路(51B)を加熱して、上記再冷却
器(8)や復管路(51B)で水等の過冷却解消により生
じた氷化物が復管路(51B)の管壁に付着して凍結が水
熱交換器(22)まで進展するのを防止するようになされ
ている。
A heat insulation bypass passage (71) is provided to bypass the liquid refrigerant from the liquid line of the refrigerant circuit (1) to the heat insulation heat exchanger (7) and return it to the liquid line. In the heat exchanger (7), the return conduit (51B) is heated by heat exchange with the liquid refrigerant in the liquid line, and the supercooling of water or the like is eliminated in the recooler (8) or the return conduit (51B). It is designed to prevent the frost formed by the above from adhering to the pipe wall of the return pipe (51B) and freezing to the water heat exchanger (22).

空気調和装置の運転時、室内で冷房運転を行うときに
は、四路切換弁(2)が図中実線側に切換えられる。そ
して、水側切換弁(26)が図中実線側に切換えられてい
るときには、各圧縮機(11),(21)からの吐出冷媒が
いずれも室外熱交換器(12)で凝縮された後、各室内熱
交換器(32),(32)で蒸発することにより、室内の冷
房を行う。また、水側切換弁(26)が図中破線側に切換
えられているときには、第1圧縮機(11)の吐出冷媒が
室外熱交換器(12)に流れる一方、第2圧縮機(21)の
吐出冷媒は水熱交換器(22)に流れ、それぞれ凝縮され
た後各室熱交換器(32),(32)で蒸発するように循環
する。
The four-way switching valve (2) is switched to the solid line side in the figure when the air-conditioning apparatus is operating and the indoor cooling operation is performed. When the water side switching valve (26) is switched to the solid line side in the figure, after the refrigerant discharged from each of the compressors (11) and (21) has been condensed in the outdoor heat exchanger (12). , The indoor heat exchangers (32) and (32) evaporate to cool the room. When the water side switching valve (26) is switched to the broken line side in the figure, the refrigerant discharged from the first compressor (11) flows to the outdoor heat exchanger (12), while the second compressor (21). The discharged refrigerant flows into the water heat exchanger (22), is condensed and circulates so as to evaporate in the heat exchangers (32) and (32) of the chambers.

また、夜間等の電力が安価なときには、蓄氷槽(5)に
冷熱を蓄える蓄冷熱運転が行われる。すなわち、四路切
換弁(2)及び水側切換弁(26)を図中実線側に切換
え、各室内電動膨張弁(33),(33)を閉じて、各圧縮
機(11),(21)の吐出冷媒を室外熱交換器(12)で凝
縮させた後水側電動膨張弁(23)(又は予熱電動膨張弁
(62))で減圧して水熱交換器(22)で蒸発させること
により、蓄氷槽(5)の水又は水溶液を過冷却して氷化
し、蓄氷槽(5)に冷熱を蓄えるようになされている。
Further, when electric power is cheap at night or the like, a cold storage operation for storing cold heat in the ice storage tank (5) is performed. That is, the four-way switching valve (2) and the water side switching valve (26) are switched to the solid line side in the figure, the indoor electric expansion valves (33) and (33) are closed, and the compressors (11) and (21) are closed. ) Is condensed in the outdoor heat exchanger (12) and then decompressed by the water side electric expansion valve (23) (or preheat electric expansion valve (62)) to be evaporated by the water heat exchanger (22). Thus, the water or the aqueous solution in the ice storage tank (5) is supercooled to be iced, and cold heat is stored in the ice storage tank (5).

したがって、本実施例では、上記実施例における製氷運
転時、水熱交換器(主熱交換器)(22)下流側の復管路
(51B)において、水熱交換器(22)で過冷却された水
等が再冷却器(副熱交換器)(8)で再冷却される。
Therefore, in the present embodiment, during the ice making operation in the above embodiment, the water heat exchanger (22) is supercooled in the return pipe (51B) on the downstream side of the water heat exchanger (main heat exchanger) (22). The water or the like is recooled by the recooler (sub heat exchanger) (8).

その場合、水熱交換器(22)により過冷却された水等の
過冷却状態を再冷却により解消させるには、さらに低温
に冷却することが必要となる。ここで、本発明では、再
冷却器(8)にバイパスされる冷媒は冷媒回路(1)の
液ラインからバイパスされていて、再冷却器(8)と氷
熱交換器(22)とは、冷媒回路(1)の液ラインとガス
ラインとに跨って互いに並列に接続されており、また、
水熱交換器(22)のガス側配管に減圧手段となる水側切
換弁(26)を設けられている。そのため、水熱交換器
(22)側のガス冷媒がこの水側切換弁(26)を通過する
ことにより圧力損失が生じ、その分だけ再冷却器(8)
における冷媒の蒸発温度は水熱交換器(22)における冷
媒の蒸発温度よりも低く維持されることになる。
In that case, in order to eliminate the supercooled state of water or the like supercooled by the water heat exchanger (22) by recooling, it is necessary to cool it to a lower temperature. Here, in the present invention, the refrigerant bypassed to the recooler (8) is bypassed from the liquid line of the refrigerant circuit (1), and the recooler (8) and the ice heat exchanger (22) are Are connected in parallel to each other across the liquid line and the gas line of the refrigerant circuit (1), and
The gas side pipe of the water heat exchanger (22) is provided with a water side switching valve (26) serving as a pressure reducing means. Therefore, the gas refrigerant on the side of the water heat exchanger (22) passes through the water side switching valve (26) to cause a pressure loss, and the recooler (8) correspondingly.
The evaporation temperature of the refrigerant in is kept lower than the evaporation temperature of the refrigerant in the water heat exchanger (22).

すなわち、再冷却器(8)において、過冷却状態にある
水等がさらに低温に冷却され、過冷却状態が解消され
て、スラリー状に氷化する。よって、円滑な製氷作用を
得ることができ、製氷装置の性能の向上を図ることがで
きるのである。
That is, in the recooler (8), water or the like in a supercooled state is further cooled to a lower temperature, the supercooled state is eliminated, and the water is slurried. Therefore, a smooth ice-making operation can be obtained, and the performance of the ice-making device can be improved.

なお、圧力損失を与える減圧手段として、上記実施例で
は水側切換弁(26)を利用したが、キャピラリチューブ
等の減圧機器を別途設けてもよい。ただし、上記実施例
のように減圧手段として水側切換弁(26)を利用した場
合、別途圧力損失を与える手段を設けることなく、既存
の設備だけで済むので、コストの増大を回避することが
できる。
Although the water side switching valve (26) is used as the pressure reducing means for giving a pressure loss in the above embodiment, a pressure reducing device such as a capillary tube may be separately provided. However, when the water side switching valve (26) is used as the pressure reducing means as in the above-described embodiment, it is possible to avoid an increase in cost because it is possible to use only existing equipment without providing a means for giving a pressure loss separately. it can.

次に、第2実施例について説明する。第3図は第2実施
例における空気調和装置の冷媒配管系統を示し、本実施
例では、再冷却バイパス路(81)の冷媒入口端は、上記
第1実施例と同様に、冷媒回路(81)の液ラインに接続
されるとともに、再冷却バイパス路(81)の冷媒出口端
はアキュムレータ(Ac)下流側の吸入管(ガスライン)
に接続されている。その他の構成は上記第1実施例と同
様である。
Next, a second embodiment will be described. FIG. 3 shows the refrigerant piping system of the air conditioner in the second embodiment. In this embodiment, the refrigerant inlet end of the recooling bypass passage (81) has the refrigerant circuit (81) as in the first embodiment. ), And the refrigerant outlet end of the re-cooling bypass passage (81) is a suction pipe (gas line) downstream of the accumulator (Ac).
It is connected to the. The other structure is similar to that of the first embodiment.

すなわち、再冷却バイパス路(81)の冷媒出口端をアキ
ュムレータ(Ac)下流側のガスラインに接続することに
より、水熱交換器(22)側のガス冷媒にアキュムレータ
(Ac)の流通抵抗による圧力損失を生ぜしめ、再冷却器
(8)における蒸発温度を水熱交換器(22)における蒸
発温度よりも低く維持するようになされている。すなわ
ち、上記アキュムレータ(Ac)により、水熱交換器(2
2)側の冷媒に圧力損失を与える減圧手段が構成されて
いる。
That is, by connecting the refrigerant outlet end of the recooling bypass passage (81) to the gas line on the downstream side of the accumulator (Ac), the pressure due to the flow resistance of the accumulator (Ac) on the gas refrigerant on the water heat exchanger (22) side. This causes a loss and keeps the evaporation temperature in the recooler (8) lower than the evaporation temperature in the water heat exchanger (22). That is, the water heat exchanger (2
The decompression means that gives pressure loss to the refrigerant on the 2) side is configured.

したがって、本実施例では、水熱交換器(22)側の冷媒
がアキュームレータ(Ac)によって圧力損失を与えるの
で、その分だけ再冷却器(8)の蒸発温度が水熱交換器
(22)の蒸発温度よりもさらに低く維持されることにな
り、よって、別途圧力損失を与える手段を設けることな
く、製氷装置の性能の向上を図ることができる。
Therefore, in the present embodiment, the refrigerant on the side of the water heat exchanger (22) gives a pressure loss due to the accumulator (Ac), so that the evaporation temperature of the recooler (8) corresponds to that of the water heat exchanger (22). Since the temperature is kept lower than the evaporation temperature, the performance of the ice making device can be improved without separately providing a means for giving a pressure loss.

なお、上記各実施例では、冷媒回路(1)の構成とし
て、二台の圧縮機(11),(21)をそれぞれ熱交換器に
直列に接続させたものを利用しているが、本発明は斯か
る実施例に限定されるものではなく、一台の圧縮機のみ
を備えたものについても適用しうることはいうまでもな
い。
In each of the above embodiments, the refrigerant circuit (1) has two compressors (11) and (21) connected in series to heat exchangers, respectively. It is needless to say that the present invention is not limited to such an embodiment and can be applied to a device provided with only one compressor.

(発明の効果) 以上説明したように、請求項(1)の発明によれば、製
氷装置として、蓄氷槽の水等を強制循環させる水循環路
に、冷媒回路の冷媒との熱交換により水等を過冷却する
主熱交換器を設け、さらにその下流側に、過冷却された
水等を再冷却して過冷却状態を解消させるための副熱交
換器を配置し、副熱交換器を冷媒回路の主熱交換器とは
並列ラインとなるバイパス路に介設するとともに、主熱
交換器を通過した後のガス冷媒に圧力損失を与えるよう
にしたので、副熱交換器の蒸発温度を主熱交換器の蒸発
温度よりも低く維持することができ、よって、水等の過
冷却状態を解消してスラリー状に氷化させる製氷作用を
円滑に行うことができ、製氷装置の性能の向上を図るこ
とができる。
(Effects of the Invention) As described above, according to the invention of claim (1), as an ice-making device, water is circulated in the water circulation path for forcibly circulating water or the like in the ice storage tank by heat exchange with the refrigerant in the refrigerant circuit. A main heat exchanger for supercooling etc. is provided, and a sub heat exchanger for recooling the supercooled water etc. to eliminate the supercooled state is arranged further downstream, and the sub heat exchanger is installed. The main heat exchanger of the refrigerant circuit is installed in a bypass line that is a parallel line, and pressure loss is applied to the gas refrigerant after passing through the main heat exchanger, so the evaporation temperature of the sub heat exchanger is It can be kept lower than the evaporation temperature of the main heat exchanger, and therefore the ice making action of eliminating the supercooled state of water etc. and making it into a slurry can be smoothly performed, and the performance of the ice making device is improved. Can be achieved.

請求項(2)の発明では、上記請求項(1)の発明にお
ける圧力損失を与える手段とし、圧縮機の吸入側に配置
されるアキュムレータを利用したので、別途圧力損失を
与えるための手段を設けることなく、請求項(1)の発
明の効果を得ることができ、よって、コストの低減を図
ることができる。
In the invention of claim (2), the means for giving the pressure loss in the invention of the above-mentioned claim (1) uses the accumulator arranged on the suction side of the compressor, so that means for separately giving the pressure loss is provided. Therefore, the effect of the invention of claim (1) can be obtained, and the cost can be reduced.

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

第1図は本発明の構成を示すブロック図である。第2図
は第1実施例における空気調和装置の冷媒回路の構成を
示す冷媒配管系統図、第3図は第2実施例における空気
調和装置の冷媒回路の構成を示す冷媒配管系統図であ
る。 1……冷媒回路 5……蓄水槽 8……再冷却器(副熱交換器) 22……水熱交換器(主熱交換器) 51……水循環路 81……再冷却バイパス路 26……水側切換弁(減圧手段) Ac……アキュムレータ(減圧手段)
FIG. 1 is a block diagram showing the configuration of the present invention. FIG. 2 is a refrigerant piping system diagram showing the configuration of the refrigerant circuit of the air conditioning apparatus in the first embodiment, and FIG. 3 is a refrigerant piping system diagram showing the configuration of the refrigerant circuit of the air conditioning apparatus in the second embodiment. 1 …… Refrigerant circuit 5 …… Water tank 8 …… Recooler (sub heat exchanger) 22 …… Water heat exchanger (main heat exchanger) 51 …… Water circulation path 81 …… Recooling bypass path 26 …… Water side switching valve (pressure reducing means) Ac …… Accumulator (pressure reducing means)

───────────────────────────────────────────────────── フロントページの続き (72)発明者 仲沢 優司 大阪府堺市金岡町1304番地 ダイキン工業 株式会社堺製作所金岡工場内 (56)参考文献 実開 平1−144722(JP,U)) ─────────────────────────────────────────────────── ─── Continuation of front page (72) Inventor Yuji Nakazawa 1304 Kanaoka-machi, Sakai-shi, Osaka Daikin Industry Co., Ltd., Kanaoka factory, Sakai Manufacturing Co., Ltd.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】水又は水溶液のスラリー状の氷化物を貯溜
するための製氷槽(5)と、水又は水溶液を過冷却する
ための主熱交換器(22)と、 閉環状の断面を有する管部材で構成され上記主熱交換器
(22)と製氷槽(5)との間で水又は水溶液を強制循環
させるための水循環路(51)と、上記主熱交換器(22)
下流側の水循環路(51)に配置され主熱交換器(1)で
過冷却された水又は水溶液の過冷却状態を解消させるよ
うさらに低温の状態まで再冷却する副熱交換器(8)
と、 圧縮機,凝縮器及び蒸発器となる上記主熱交換器(22)
を順次接続してなる閉回路の冷媒回路(1)と、 上記冷媒回路(1)の主熱交換器(22)の出口側配管と
なるガスラインに配置され通過する冷媒に圧力損失を与
える減圧手段と、 上記冷媒回路(1)の液ラインとガスラインとの間を上
記主熱交換器(22)及び減圧手段をバイパスしかつ蒸発
器となる上記副熱交換器(8)を介して接続するバイパ
ス路(81)とを備え、 上記副熱交換器(8)における冷媒の蒸発温度は上記主
熱交換器(22)における冷媒の蒸発温度よりも低いこと
を特徴とする製氷装置。
1. An ice making tank (5) for storing a slurry of iced water or an aqueous solution, a main heat exchanger (22) for supercooling water or an aqueous solution, and a closed ring cross section. A water circulation path (51) composed of a pipe member for forcibly circulating water or an aqueous solution between the main heat exchanger (22) and the ice making tank (5), and the main heat exchanger (22)
A sub heat exchanger (8) arranged in the water circulation path (51) on the downstream side and recooled to a lower temperature state so as to eliminate the supercooled state of the water or aqueous solution supercooled by the main heat exchanger (1).
And the main heat exchanger (22) that serves as a compressor, condenser, and evaporator.
A closed circuit refrigerant circuit (1) that is connected in sequence with a refrigerant circuit (1) and a gas line that is a gas line that serves as an outlet side pipe of the main heat exchanger (22) of the refrigerant circuit (1) and that causes pressure loss to the passing refrigerant. And the liquid line and the gas line of the refrigerant circuit (1) are connected via the main heat exchanger (22) and the depressurizing means and the auxiliary heat exchanger (8) serving as an evaporator. And a bypass passage (81) for performing cooling, the evaporation temperature of the refrigerant in the sub heat exchanger (8) being lower than the evaporation temperature of the refrigerant in the main heat exchanger (22).
【請求項2】請求項(1)において、 上記冷媒回路(1)はガスラインにアキュムレータ(A
c)を介設しているものであり、 上記減圧手段は上記アキュムレータ(Ac)であることを
特徴とする製氷装置。
2. The refrigerant circuit (1) according to claim (1), wherein an accumulator (A) is installed in a gas line.
c), wherein the depressurizing means is the accumulator (Ac).
JP2158092A 1990-06-15 1990-06-15 Ice making equipment Expired - Fee Related JPH0799303B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2158092A JPH0799303B2 (en) 1990-06-15 1990-06-15 Ice making equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2158092A JPH0799303B2 (en) 1990-06-15 1990-06-15 Ice making equipment

Publications (2)

Publication Number Publication Date
JPH0448174A JPH0448174A (en) 1992-02-18
JPH0799303B2 true JPH0799303B2 (en) 1995-10-25

Family

ID=15664127

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2158092A Expired - Fee Related JPH0799303B2 (en) 1990-06-15 1990-06-15 Ice making equipment

Country Status (1)

Country Link
JP (1) JPH0799303B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105042972B (en) * 2015-06-24 2017-04-12 广州高菱机电工程有限公司 Sub-cooled water type dynamic ice making system with preheating cold energy recovery mechanism

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH065536Y2 (en) * 1988-03-28 1994-02-09 高砂熱学工業株式会社 Device for releasing supercooled water

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
実開平1−144722(JP,U))

Also Published As

Publication number Publication date
JPH0448174A (en) 1992-02-18

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