JPH05149653A - Ice making device - Google Patents

Ice making device

Info

Publication number
JPH05149653A
JPH05149653A JP31236791A JP31236791A JPH05149653A JP H05149653 A JPH05149653 A JP H05149653A JP 31236791 A JP31236791 A JP 31236791A JP 31236791 A JP31236791 A JP 31236791A JP H05149653 A JPH05149653 A JP H05149653A
Authority
JP
Japan
Prior art keywords
water
supercooling
heat exchanger
elimination
storage tank
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP31236791A
Other languages
Japanese (ja)
Other versions
JP2946889B2 (en
Inventor
Koji Matsuoka
弘二 松岡
Shinji Matsuura
伸二 松浦
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 JP31236791A priority Critical patent/JP2946889B2/en
Publication of JPH05149653A publication Critical patent/JPH05149653A/en
Application granted granted Critical
Publication of JP2946889B2 publication Critical patent/JP2946889B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Abstract

PURPOSE:To extend degree of freedom in design by shortening the length of a pipe downstream of a supercooling part in an ice making device wherein water or the like of an ice storage tank is circulated through a water circulation line and supercooling and elimination of supercooling is effected to turn the water into ice in a slurry-like state. CONSTITUTION:In a water circulation line 51 through which water or aqueous solution of an ice storage tank is circulated, there are provided a supercooling generating heat exchanger 22 and a supercooling eliminating part 8 for eliminating supercooled state on the downstream side of the exchanger 22. Further, a supercooling elimination completion part 9 with a sharply expanded section 9a which is formed by sharply expanding the diameter of the line 51 is provided downstream of the part 8. By an agitating action due to turbulent flow caused by the part 9a, the length of line needed for completing the elimination of supercooling of water or the like can be shortened and at the same time heating area required for prevention of attachment of freezed matters to pipe walls can be reduced, resulting in reduced cost. A plurality of parts 9a are provided or an impingement member is provided downstream of the part 9a, whereby effects thereof can be improved.

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、蓄氷槽の水等を熱交換
器で過冷却して氷化するようにした製氷装置に係り、特
に過冷却の解消完了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 in which water or the like in an ice storage tank is supercooled by a heat exchanger to be iced, and more particularly to measures for improving supercooling elimination completion performance.

【0002】[0002]

【従来の技術】従来より、蓄氷槽の水を循環させる水循
環路を設け、熱交換器で水を過冷却させてスラリ―状の
氷化物を生成するようにした製氷装置として、例えば特
開昭63―217171号公報に開示される如く、水循
環路の出口側を上流側で下方に向かいかつ出口端が蓄氷
槽の水面より一定高さだけ上方で開口するように形成さ
れた傾斜樋とし、熱交換器を該樋間に介設して、水循環
路で熱交換器により冷却された水を樋の出口で過冷却状
態を解消させてスラリ―状に氷化するとともに、この氷
化物を蓄氷槽に落下させることにより、水の氷化の進行
による水循環路の凍結を防止しようとするものは公知の
技術である。
2. Description of the Related Art Conventionally, as an ice making device, a water circulation passage for circulating water in an ice storage tank is provided, and the water is supercooled by a heat exchanger to produce slurry-like iced matter, for example, Japanese Patent Application Laid-Open As disclosed in Japanese Patent Laid-Open No. 63-217171, an inclined gutter formed so that the outlet side of the water circulation path is directed downward on the upstream side and the outlet end is opened at a certain height above the water surface of the ice storage tank. , A heat exchanger is provided between the gutters, and the water cooled by the heat exchangers in the water circulation path is melted at the outlet of the gutter to eliminate the supercooled state, and is frozen in a slurry form. It is a well-known technique to prevent freezing of the water circulation path due to the progress of freezing of water by dropping it in an ice storage tank.

【0003】また、実開平1―112345号公報に開
示される如く、水循環路の出口端を蓄氷槽の上方に開口
させ、その前方に邪魔板を有する傾斜樋を設置して、熱
交換器で過冷却された水を大気中に放出して邪魔板に衝
突させることにより、水の過冷却状態を解消させて水を
氷化させ、樋を介して蓄氷槽内に落下させることによ
り、より確実に水循環路の凍結を防止しようとするもの
も公知の技術である。
Further, as disclosed in Japanese Utility Model Laid-Open No. 1-112345, a heat exchanger is provided by opening an outlet end of a water circulation path above an ice storage tank and installing an inclined gutter having a baffle plate in front of it. By releasing the supercooled water into the atmosphere and colliding with the baffle plate, the supercooled state of the water is canceled and the water is frozen, and it is dropped into the ice storage tank through the gutter. It is a known technique to more reliably prevent the freezing of the water circulation path.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、上記従
来のもののうち後者のものでは、蓄氷槽の上方に過冷却
解消部が設けられているために、熱交換器と過冷却解消
部までの距離が長いとその間の配管で過冷却状態が解消
してしまう虞れがある。したがって、熱交換器を蓄氷槽
の近くに設けなければならないので、水配管を曲げる等
の加工が困難となる等、設計上の制約が大きいという問
題がある。
However, in the latter of the above-mentioned conventional ones, since the supercooling elimination section is provided above the ice storage tank, the distance between the heat exchanger and the subcooling elimination section is large. If it is long, there is a risk that the supercooled state will be eliminated in the pipe between them. Therefore, since the heat exchanger has to be provided near the ice storage tank, there is a problem that design restrictions are large, such as difficulty in processing such as bending the water pipe.

【0005】一方、上記従来のもののうち前者のもので
は、過冷却解消部として、蓄氷槽の上方に相当の高低差
を持った樋を設置する必要があり、やはり設計上の制約
が大きい。また、大気に晒される時間が長いので大気と
の熱交換による熱の浪費が大きいという問題がある。
On the other hand, in the former one of the above-mentioned conventional ones, it is necessary to install a gutter having a considerable height difference above the ice storage tank as the supercooling elimination portion, which also has a large design restriction. In addition, since it is exposed to the atmosphere for a long time, there is a problem that heat is wasted due to heat exchange with the atmosphere.

【0006】そこで、水循環路の過冷却生成熱交換器下
流側で過冷却された水等が通過する連続した流路内で過
冷却状態を解消させ、スラリー状の氷化物を連続的に生
成していくことが考えられる。
Therefore, the supercooled state is eliminated in the continuous flow path through which the supercooled water or the like passes on the downstream side of the supercooling generation heat exchanger of the water circulation path, and the slurry-like iced substance is continuously generated. It is possible to continue.

【0007】しかるに、その場合、単に自然の流れの中
で再冷却や絞りによる流速の増大等により過冷却状態を
解消させるようにすると、過冷却解消が完了するのに長
い行程と時間とを要し、その間に流路の管壁に氷が付
着,成長して管路を詰まらせる確率が増大する。また、
過冷却状態が残存した水等が蓄氷槽まで戻され、再び過
冷却生成熱交換器に循環すると、熱交換器の凍結に至る
虞れも生じる。
However, in that case, if the supercooled state is eliminated by simply recooling or increasing the flow velocity by throttling in a natural flow, it takes a long process and time to complete the supercooling elimination. However, during that time, the probability that ice adheres to and grows on the pipe wall of the flow passage to clog the pipe passage increases. Also,
If water or the like remaining in the supercooled state is returned to the ice storage tank and is circulated again in the subcooling generation heat exchanger, the heat exchanger may be frozen.

【0008】本発明は斯かる点に鑑みてなされたもので
あり、その目的は、過冷却状態の解消の完了を促進する
手段を講ずることにより、過冷却解消完了部の行程を短
縮して、凍結,目詰まりの虞れを解消しながら、設計上
の自由度の向上を図ることにある。
The present invention has been made in view of the above points, and an object thereof is to shorten the stroke of the supercooling elimination completion portion by providing means for promoting completion of elimination of the supercooling state, It is to improve the degree of freedom in design while eliminating the risk of freezing and clogging.

【0009】[0009]

【課題を解決するための手段】上記目的を達成するた
め、請求項1の発明の講じた手段は、図1に示すよう
に、水又は水溶液のスラリ―状の氷化物を貯溜するため
の蓄氷槽(5)と、冷却装置に接続され、水又は水溶液
を過冷却するための過冷却生成熱交換器(22)と、該
過冷却生成熱交換器(22)に蓄氷槽(5)の水又は水
溶液を強制循環させるための水循環路(51)と、該水
循環路(51)の上記熱交換器(22)下流側に設けら
れ、水又は水溶液の過冷却状態を解消するための過冷却
解消部(8)とを備えた製氷装置を対象とする。
Means for Solving the Problems To achieve the above object, the means of the present invention as set forth in claim 1 is, as shown in FIG. An ice bath (5) and a subcooling generation heat exchanger (22) connected to a cooling device for supercooling water or an aqueous solution, and an ice storage tank (5) in the subcooling generation heat exchanger (22). Water circulation path (51) for forcibly circulating the water or aqueous solution of the above, and a water circulation path (51) provided downstream of the heat exchanger (22) and provided with a supercooling means for eliminating a supercooled state of the water or aqueous solution. The object is an ice making device provided with a cooling elimination unit (8).

【0010】そして、上記水循環路(51)の上記過冷
却解消部(8)下流側に、水循環路(51)の管径を急
激に拡大させてなる急拡大部(9a)を有する過冷却解
消完了部(9)を設ける構成としたものである。
Then, the supercooling elimination having a sudden expansion portion (9a) formed by abruptly increasing the pipe diameter of the water circulation passage (51) is provided downstream of the supercooling elimination portion (8) of the water circulation passage (51). The completion unit (9) is provided.

【0011】請求項2の発明の講じた手段は、図4に示
すように、上記請求項1の発明において、過冷却解消完
了部(9)に、複数個の急拡大部(9a1),(9a2)を
設けたものである。
As shown in FIG. 4, the means taken by the invention of claim 2 is, in the invention of claim 1 described above, a plurality of sudden expansion parts (9a1), ( 9a2) is provided.

【0012】請求項3の発明の講じた手段は、図5に示
すように、上記請求項1又は2記載の製氷装置におい
て、過冷却解消完了部(9)に、水循環路(51)の急
拡大部(9a)の下流側に水又は水溶液の流れと衝突す
る衝突部材(9c)を設けたものである。
As shown in FIG. 5, the means taken by the invention of claim 3 is the ice making device according to claim 1 or 2, wherein the supercooling elimination completion portion (9) is provided with a rapid water circulation path (51). A collision member (9c) that collides with the flow of water or an aqueous solution is provided on the downstream side of the enlarged portion (9a).

【0013】[0013]

【作用】以上の構成により、請求項1の発明では、水循
環路(51)において、水等が過冷却生成熱交換器(2
2)で過冷却され、この過冷却状態にある水等が過冷却
解消部(8)で再冷却等により過冷却状態の解消を開始
し、過冷却解消完了部(9)で過冷却状態の解消を完了
すると、スラリー状の氷化物となって蓄氷槽(5)に戻
る。そのとき、過冷却解消部(8)の下流側に管径を急
激に拡大させてなる急拡大部(9a)を有する過冷却解
消完了部(9)が設けられているので、この急拡大部
(9a)で、水等の流れの急激な拡大により乱流が生
じ、この乱流による攪拌作用で過冷却解消の完了が促進
される。したがって、過冷却解消部(8)下流側の管路
長が短縮され、設計上の自由度が拡大することになる。
また、管路長の短縮により、氷化物の管壁への付着防止
のための加熱量が減少するので、コストも低減すること
になる。
With the above construction, in the invention of claim 1, in the water circulation path (51), water or the like is supercooled to generate heat exchanger (2).
The supercooled water is supercooled in 2), and water in the supercooled state is started to be recooled in the supercooling elimination section (8) to eliminate the supercooled state. When the elimination is completed, it turns into a slurry-like frozen product and returns to the ice storage tank (5). At that time, since the supercooling elimination completion portion (9) having the sudden enlargement portion (9a) formed by rapidly enlarging the pipe diameter is provided on the downstream side of the supercooling elimination portion (8), this sudden enlargement portion is provided. At (9a), a turbulent flow occurs due to the rapid expansion of the flow of water or the like, and the stirring action of this turbulent flow promotes the completion of elimination of supercooling. Therefore, the pipeline length on the downstream side of the supercooling elimination portion (8) is shortened, and the degree of freedom in design is expanded.
Further, since the length of the pipe line is shortened, the amount of heating for preventing the adhesion of the iced substance to the pipe wall is reduced, so that the cost is also reduced.

【0014】請求項2の発明では、過冷却解消完了部
(9)に複数の急拡大部(9a1),(9a2)が設けられ
ているので、水等の流れを攪拌する作用がより増大し、
過冷却解消の完了が促進する。
According to the second aspect of the invention, since the supercooling elimination completion section (9) is provided with a plurality of sudden expansion sections (9a1), (9a2), the action of stirring the flow of water or the like is further increased. ,
The completion of elimination of supercooling is promoted.

【0015】請求項3の発明では、急拡大部(9a)と
衝突部材(9c)とによる流れの攪拌作用により、過冷
却解消の完了がさらに促進される。
According to the third aspect of the invention, the completion of the supercooling elimination is further promoted by the stirring action of the flow by the sudden expansion portion (9a) and the collision member (9c).

【0016】[0016]

【実施例】以下、本発明の実施例について図面に基づき
説明する。
Embodiments of the present invention will be described below with reference to the drawings.

【0017】図2は請求項1の発明に係る第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)は該室外熱交換器(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)は第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 according to the invention of claim 1, and (11)
Is a first compressor, (12) is an outdoor heat exchanger that is arranged on the discharge side of the first compressor (11) and exchanges heat between the refrigerant and outdoor air, and (13) is the outdoor heat exchanger ( 12) An outdoor electric expansion valve for adjusting the refrigerant flow rate of 12) or for reducing the pressure, wherein the above-mentioned devices (11) to (13) are connected in series in a first conduit (14).

【0018】また、(21)は第2圧縮機、(22)は
該第2圧縮機(21)の吐出側に配置され、後述の蓄氷
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 a second compressor, and (22) is arranged on the discharge side of the second compressor (21) to supercool water or an aqueous solution in an ice storage tank (5) described later. The water heat exchanger, which is the main heat exchanger of (23), regulates the refrigerant flow rate when the water heat exchanger (22) functions as a condenser, and depressurizes the refrigerant when the water heat exchanger (22) functions as an evaporator. In the electric expansion valve, the devices (21) to (23) are connected in series in the second pipe line (24).

【0019】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(RT1 ),(RT2 )に
それぞれ介設された減圧用キャピラリチュ―ブである。
Incidentally, (SD1) and (SD2) are oil separators provided in the discharge pipes of the compressors (11) and (21), and (C1) and (C2) are oil separators (SD1). ),
The pressure reducing capillary tubes are respectively provided in oil return pipes (RT1) and (RT2) provided on the suction sides of the compressors (11) and (21) from (SD2).

【0020】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. The devices (32) and (33) are each connected in series, and their respective sets are connected in parallel in the third conduit (34).

【0021】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、(Ac)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―タである。
The first pipeline (14) and the second pipeline (24) are connected in parallel with the third pipeline (34). In addition, (Ac) is each compressor (11), (21)
It is an accumulator provided in the third conduit (34) on the suction side of.

【0022】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),(21)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(3
2),(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, in (2), the gas pipe of the outdoor heat exchanger (12) and the gas pipes of the indoor heat exchangers (32) and (32) are connected to the discharge sides of the compressors (11) and (21) or A four-way switching valve (2) that is switched so as to be alternately communicated with the intake side. When the four-way switching valve (2) is switched to the solid line side in the figure, the outdoor heat exchanger (12) is a condenser, an indoor unit. Heat exchanger (32),
While (32) functions as an evaporator to perform cooling operation indoors, when the four-way switching valve (2) is switched to the broken line side in the figure, the outdoor heat exchanger (12) is an evaporator and an indoor heat exchanger. (3
2) and (32) function as a condenser to perform heating operation in the room.

【0023】さらに、該水熱交換器(22)のガス管と
各圧縮機(11),(21)の吸入管とをバイパス接続
する分岐路(25)と、水熱交換器(22)のガス管を
上記第2圧縮機(21)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―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―ト側の配管に介設さ
れたキャピラリチュ―ブである。
Further, a branch passage (25) for bypass-connecting the gas pipe of the water heat exchanger (22) and the suction pipes of the compressors (11) and (21) and the water heat exchanger (22). A water side switching valve (26) for alternately connecting the gas pipe to the discharge pipe of the second compressor (21) and the branch passage (25) is provided. The water side switching valve (26) utilizes 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 water heat exchanger (22 ) Is connected to the branch passage (25) side, that is, the suction side of each of the compressors (11) and (21), and 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, the gas pipe of the water heat exchanger (22) communicates with the discharge pipe of the second compressor (21) so that the water heat exchanger (22) functions as a condenser. Has been done. In addition, (C3)
Is a capillary tube provided in the dead port side pipe of the water side switching valve (26).

【0024】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。
Further, a bypass passage (3) for connecting the discharge pipes of the first compressor (11) and the second compressor (21) is provided, and the second compressor is provided in the bypass passage (3). A check valve (4) which allows only refrigerant flow from the discharge pipe side of (21) to the discharge pipe side of the first compressor (11) is interposed.

【0025】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)における凝縮温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(1
2)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, if the condensation temperature in the water heat exchanger (22) is high and the pressure is high, the second compression The gas discharged from the machine (21) is used as an outdoor heat exchanger (1
The amount of heat radiation can be distributed by letting it escape to the 2) side.

【0026】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―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、該蓄氷槽(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(2
2)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―状の
氷化物を戻す復管路(51B)とからなっており、往管
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-like iced product of water or an aqueous solution as a heat storage medium, and the ice storage tank (5). The water and the water heat exchanger (22) are connected by a water circulation path (51) so that water or an aqueous solution can circulate. The water circulation path (51) extends from the bottom of the ice storage tank (5) to the water heat exchanger (2).
Outgoing line (51A) for supplying water etc. to 2) and returning line (51B) for returning slurry-like iced substances such as water from the water heat exchanger (22) to the upper part of the ice storage tank (5) The pump (52) provided in the forward path (51A) forcibly circulates the water or the aqueous solution in the ice storage tank (5) in the water circulation path (51).

【0027】そして、水循環路(51)の往管路(51
A)のポンプ(52)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―ナ(53)が介設され、さらに、該ストレ―ナ
(53)の下流側には、水熱交換器(22)に供給され
る水等を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 forward path (51) of the water circulation path (51)
On the downstream side of the pump (52) of A), the water circulation path (51)
A strainer (53) for removing solid matters such as iced matter and dust in the water or the aqueous solution of the above is interposed, and further, a water heat exchanger (22) is provided on the downstream side of the strainer (53). A preheat heat exchanger (6) for preheating water or the like supplied to the is installed. On the other hand, the liquid line of the refrigerant circuit (1) is provided with a preheating bypass passage (61) for circulating a part of the liquid refrigerant to the preheat heat exchanger (6) by bypassing the water side electric expansion valve (23). Further, a preheat electric expansion valve (62) having a refrigerant decompression function and a flow rate control function is provided downstream of the preheat exchanger (6) in the preheat bypass passage (61). 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.

【0028】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(2
2)で過冷却された水等の過冷却状態を解消させる過冷
却状態解消部としての再冷却器(8)と、該再冷却器
(8)による水等の過冷却解消を完了させるための過冷
却解消完了部(9)とが上流側から順に設けられてい
る。なお、(7)は、上記再冷却器(8)と水熱交換器
(22)との間に介設され、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である。
Further, in the return pipe (51B) of the water circulation passage (51), the water or the like in the return pipe (51B) is cooled downstream of the water heat exchanger (22) to cool the water heat exchanger. (2
A recooler (8) as a supercooled state eliminating unit for eliminating the supercooled state of water or the like supercooled in 2), and for completing the elimination of supercooled state of water or the like by the recooler (8). A subcooling elimination completion section (9) is provided in order from the upstream side. In addition, (7) is interposed between the recooler (8) and the water heat exchanger (22), and the freezing of the return conduit (51B) progresses to the water heat exchanger (22). It is a heat retention heat exchanger as a freezing progress prevention unit for preventing the above.

【0029】そして、冷媒回路(1)の液ラインと、各
圧縮機(11),(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―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―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。
A water heat exchanger (22) is provided between the liquid line of the refrigerant circuit (1) and the branch passage (gas line) on the suction side of each compressor (11), (21). A recooling bypass passage (81) for bypassing and circulating the refrigerant is provided, and the recooling bypass passage (81) is provided with the recooling capillary tube (C4) and the recooler (in order from the upstream side). 8) is installed. That is, recooler (8)
A low-temperature refrigerant whose pressure has been reduced by a re-cooling capillary tube (C4) is circulated in the water, and heat exchange with the refrigerant is performed to re-cool water and the like supercooled in the water heat exchanger (22). There is.

【0030】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 this case, the gas side pipe of the water heat exchanger (22) is connected to the branch passage (25) via the water side switching valve (26) while the gas side of the recooler (8) is directly connected. The water side switching valve (26) by connecting to the branch passage (25)
A pressure loss is caused in the water heat exchanger (22) by the flow resistance due to the passage of water, and the evaporation temperature of the recooler (8) is maintained at a temperature lower than that of the water heat exchanger (22). (22)
The subcooled water or the like can be further cooled to a lower temperature by the recooler (8).

【0031】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。
In addition, the heat insulation bypass passage (71) for bypassing and circulating the liquid refrigerant from the liquid line of the refrigerant circuit (1) to the heat insulation heat exchanger (7) and returning it to the liquid line.
In the heat retention heat exchanger (7), the return pipe (51B) is heated by heat exchange with the liquid refrigerant in the liquid line, and the recooler (8) and the return pipe (51B) are heated. In this case, it is possible to prevent the iced substance generated by the elimination of supercooling of water or the like from adhering to the pipe wall of the return pipe (51B) and freezing to the water heat exchanger (22).

【0032】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内熱交換
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 side of the solid line 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, the compressors (11), (21)
After the refrigerant discharged from each of them is condensed in the outdoor heat exchanger (12), it is evaporated in each of the indoor heat exchangers (32) and (32) to cool the room. Further, 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 of (1) flows into the water heat exchanger (22), is condensed, and then circulates so as to be evaporated in the indoor heat exchangers (32) and (32).

【0033】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(2
3)(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。
When the electric power is cheap at night or the like, the cold storage operation for storing the 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, and the indoor electric expansion valves (33), (33) are switched.
And the refrigerant discharged from the compressors (11) and (21) is condensed in the outdoor heat exchanger (12), and the water-side electric expansion valve (2
3) (or preheat electric expansion valve (62)) to reduce pressure and evaporate in water heat exchanger (22) to supercool water or aqueous solution in ice storage tank (5) to ice, Cold heat is stored in (5).

【0034】ここで、本発明の特徴として、図3に示す
ように、上記過冷却解消完了部(9)は、復管路(51
B)の管径を急激につまり段付円筒状に拡大してなる大
径の急拡大部(9a)と、その後管径を拡大前の径まで
テーパ状に連続的に絞る絞り部(9b)とを備えてお
り、上記再冷却器(8)で再冷却されて過冷却状態を解
消しつつある水等の流れを急激に拡大させて乱流を生ぜ
しめ、その攪拌作用により、過冷却解消の完了を促進す
るようになされている。
Here, as a feature of the present invention, as shown in FIG. 3, the subcooling elimination completion section (9) has a return pipe (51).
A large diameter sudden expansion portion (9a) that is formed by rapidly expanding the pipe diameter of B), that is, a stepped cylindrical shape, and then a narrowing portion (9b) that continuously narrows the pipe diameter to the diameter before expansion. Which is recooled by the recooler (8) to eliminate the supercooled state and rapidly expands the flow of water or the like to generate a turbulent flow, and eliminates the supercooling by its stirring action. Is designed to facilitate the completion of.

【0035】上記第1実施例では、水循環路(51)に
おいて、水熱交換器(22)で水等が過冷却された後、
復管路(51B)の再冷却器(8)で過冷却状態にある
水等が再冷却されることにより、過冷却状態が解消さ
れ、スラリー状の氷化物となって蓄氷槽(5)に戻る。
そのとき、単に過冷却状態を解消すべく再冷却しても、
再冷却による過冷却解消作用だけでは、過冷却解消が完
了するのに長い時間つまり行程を要する。このため、再
冷却器(8)から蓄氷槽(5)迄の管路長が長くなっ
て、設計上の制約が生じるが、上記第1実施例では、再
冷却器(8)下流側に急拡大部(9a)を有する過冷却
解消完了部(9)が設けられているので、この急拡大部
(9a)で、水等の流れが急激に拡大して乱流を生じ、
この乱流による攪拌作用で過冷却解消の完了が促進され
る。したがって、再冷却器(8)下流側の管路長を短縮
することができ、設計上の自由度が拡大するとともに、
管路長の短縮により、氷化物の管壁への付着による凍結
防止のための加熱量が減少するので、コストの低減を図
ることができる。
In the first embodiment described above, after water and the like are supercooled in the water heat exchanger (22) in the water circulation path (51),
By recooling the water or the like in the supercooled state in the recooler (8) of the return conduit (51B), the supercooled state is eliminated, and it becomes a frosted product in the form of slurry and the ice storage tank (5). Return to.
At that time, even if it is simply recooled to eliminate the supercooled state,
It takes a long time, that is, a stroke, to complete the elimination of supercooling only by the action of eliminating subcooling by recooling. For this reason, the pipe length from the recooler (8) to the ice storage tank (5) becomes long, which causes a restriction in design. However, in the first embodiment, the recooler (8) is provided downstream. Since the subcooling elimination completion portion (9) having the sudden expansion portion (9a) is provided, the flow of water or the like rapidly expands at this sudden expansion portion (9a) to generate a turbulent flow.
Completion of elimination of supercooling is promoted by the stirring action by this turbulent flow. Therefore, the pipeline length on the downstream side of the recooler (8) can be shortened, and the degree of freedom in design is expanded, and
By reducing the pipe length, the amount of heating for preventing freezing due to the adhesion of the iced substance to the pipe wall is reduced, so that the cost can be reduced.

【0036】ここで、過冷却解消完了の促進効果につい
て説明する。過冷却度が1.5degの水中で粒径0.5m
mの球状の氷核が2倍の大きさに成長するのに要する時
間は、攪拌がない場合には6.9秒、攪拌を行った場合
には1.9秒となる。したがって、水等の流量が100
l/min とすると、過冷却解消が完了するに必要な管路
長は、管径が40mmで拡大部が無いときには9.15
m、管径が40mmから60mmに拡大する拡大部を設けた
ときには、1.12mとなり、氷核の付着を防止すべく
加熱する管壁の面積は、拡大部が無いときには1.15
2 、拡大部があるときには0.21m2 となって、管
路長及び加熱面積の短縮が著しいことが分かる。
The effect of accelerating the completion of supercooling elimination will be described below. Particle diameter 0.5m in water with supercooling degree of 1.5deg
The time required for the spherical ice nuclei of m to grow to twice the size is 6.9 seconds without stirring and 1.9 seconds with stirring. Therefore, the flow rate of water etc. is 100
If the flow rate is 1 / min, the pipe length required to complete elimination of supercooling is 9.15 when the pipe diameter is 40 mm and there is no enlarged portion.
m, the diameter of the pipe is 1.12 m when the enlarged portion is enlarged from 40 mm to 60 mm, and the area of the tube wall heated to prevent the adhesion of ice nuclei is 1.15 m when there is no enlarged portion.
m 2, and a 0.21 m 2 when there is a larger portion, it can be seen a significant shortening of the pipe length and the heating area.

【0037】次に、請求項2の発明に係る第2実施例に
ついて説明する。本実施例においても、冷媒回路
(1),水循環路(51)等の構成は上記第1実施例と
同様である。図4は、第2実施例における過冷却解消完
了部(9)の急拡大部(9a)の形状を示し、急拡大部
(9a)は、再冷却器(8)下流側の管径を急激に拡大
させてなるやや大径の第1拡大部(9a1 )と、該第1
拡大部(9a1)をさらに急激に拡大させてなる大径の第
2拡大部(9a2)とを備えている。
Next, a second embodiment according to the invention of claim 2 will be described. Also in this embodiment, the configurations of the refrigerant circuit (1), the water circulation path (51) and the like are the same as those in the first embodiment. FIG. 4 shows the shape of the sudden expansion portion (9a) of the supercooling elimination completion portion (9) in the second embodiment, where the sudden expansion portion (9a) sharply reduces the pipe diameter on the downstream side of the recooler (8). A slightly larger diameter first enlarged portion (9a1) and the first enlarged portion (9a1).
It is provided with a large-diameter second enlarged portion (9a2) obtained by further rapidly enlarging the enlarged portion (9a1).

【0038】本第2実施例では、このような複数の急拡
大部(9a1),(9a2)を設けることで、流れの攪拌作
用をより増大させることができ、著効を発揮することが
できる。なお、急拡大部(9a)を3個以上設けてもよ
いことはいうまでもない。
In the second embodiment, by providing a plurality of such abruptly expanding portions (9a1), (9a2), the stirring action of the flow can be further increased and a remarkable effect can be exhibited. .. Needless to say, three or more sudden expansion portions (9a) may be provided.

【0039】次に、請求項3の発明に係る第3実施例に
ついて説明する。本実施例においても、冷媒回路(1)
及び水循環路(51)の構成は上記第1実施例と同様で
ある。図5は、本実施例における過冷却解消完了部
(9)の構成を示し、急拡大部(9a)の下流側におい
て、管路の中央部には、流れと衝突することにより乱流
を生ぜしめるための衝突部材(9c)が配設されてい
る。
Next, a third embodiment according to the invention of claim 3 will be described. Also in this embodiment, the refrigerant circuit (1)
The structure of the water circulation path (51) is similar to that of the first embodiment. FIG. 5 shows the structure of the supercooling elimination completion section (9) in the present embodiment, in which the turbulent flow is generated in the central portion of the pipeline on the downstream side of the rapid expansion section (9a) by colliding with the flow. A collision member (9c) for tightening is provided.

【0040】本第3実施例では、急拡大部(9a)と衝
突部材(9c)とによる流れの攪拌作用により過冷却状
態解消完了の促進が図られ、著効を発揮することができ
る。
In the third embodiment, the agitating action of the flow by the sudden expansion portion (9a) and the collision member (9c) promotes completion of elimination of the supercooled state, and can exert a remarkable effect.

【0041】なお、上記各実施例における再冷却器
(8)は、冷媒回路(1)の冷媒との熱交換により水等
を再冷却するものとしたが、本発明はかかる実施例に限
定されるものではなく、例えばサーモパイル等で冷却す
るようにしてもよいことはいうまでもない。
Although the recooler (8) in each of the above-mentioned embodiments is designed to recool water by heat exchange with the refrigerant in the refrigerant circuit (1), the present invention is not limited to such embodiments. Needless to say, it may be cooled by, for example, a thermopile.

【0042】また、上記各実施例では、過冷却状態解消
を水等の再冷却により行うものについて説明したが、本
発明はかかる実施例に限定されるものではなく、管路を
絞って流速を増大させることにより過冷却状態を解消さ
せるようにしたものについても適用しうる。図6は、か
かる絞りによる過冷却解消を行うようにしたものに本発
明を適用した第4実施例を示し、例えば管径を40mmか
ら20mmに絞ってなる過冷却解消部(8)の下流側で、
管径を40mmに急激に拡大させてなる急拡大部(9a)
を設けた例である。この場合にも、上記第1〜第3実施
例のような過冷却解消完了部(9)を設けることによ
り、過冷却の解消完了を促進することができ、各実施例
と同様の効果を発揮することができる。
Further, in each of the above-mentioned embodiments, the description has been made of the case where the supercooled state is eliminated by re-cooling water or the like, but the present invention is not limited to such an embodiment, and the flow rate is reduced by narrowing the pipeline. It can also be applied to those in which the supercooled state is eliminated by increasing the number. FIG. 6 shows a fourth embodiment in which the present invention is applied to the one in which the supercooling is eliminated by such a throttle. For example, the downstream side of the supercooling elimination unit (8) in which the pipe diameter is reduced from 40 mm to 20 mm. so,
Sudden expansion part (9a) formed by rapidly expanding the pipe diameter to 40 mm
Is an example in which is provided. Also in this case, by providing the subcooling elimination completion section (9) as in the first to third embodiments, the elimination completion of supercooling can be promoted, and the same effect as each embodiment is exhibited. can do.

【0043】さらに、実施例は省略するが、再冷却器
(8)の代わりに、水循環路(51)の往管路(51
A)から水熱交換器(22)下流側までバイパス路を設
け、氷核を導入することにより過冷却を解消するように
したものに対しても、適用することができる。
Further, although the embodiment is omitted, instead of the recooler (8), the forward line (51) of the water circulation path (51) is used.
The present invention can also be applied to a system in which a bypass passage is provided from A) to the downstream side of the water heat exchanger (22) and supercooling is eliminated by introducing ice nuclei.

【0044】[0044]

【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、蓄氷槽の水等を循環路に循環させ、循環路に過冷
却生成熱交換器と過冷却解消部とを設けて、水循環路の
水等を過冷却した後過冷却解消部でその過冷却状態を解
消させてスラリー状の氷化物を連続的に生成するように
した製氷装置において、過冷却解消部の下流側に、水循
環路の管径を急激に拡大してなる急拡大部を有する過冷
却解消完了部を設けたので、流れの乱流化による攪拌作
用で過冷却解消の完了のために要する管路長を低減する
ことができ、よって、設計上の自由度の拡大を図ること
ができるとともに、氷化物の管壁への凍結防止のための
加熱面積の減少によるコストの低減を図ることができ
る。
As described above, according to the first aspect of the invention, the water in the ice storage tank is circulated in the circulation path, and the subcooling generation heat exchanger and the subcooling elimination section are provided in the circulation path. In an ice-making device in which after supercooling water in the water circulation path, the supercooling elimination section eliminates the supercooled state to continuously produce slurry-like iced matter, on the downstream side of the supercooling elimination section. Since the supercooling elimination completion portion having the sudden expansion portion formed by rapidly enlarging the pipe diameter of the water circulation passage is provided, the pipe length required for completing the supercooling elimination by the stirring action due to the turbulent flow Therefore, the degree of freedom in design can be increased, and the cost can be reduced by reducing the heating area for preventing the frozen product from freezing on the tube wall.

【0045】請求項2の発明によれば、上記請求項1の
発明において、過冷却解消完了部に複数の急拡大部を設
けたので、乱流による攪拌効果をより増大することがで
き、過冷却解消の完了の促進をより促進させることがで
きる。
According to the invention of claim 2, in the invention of claim 1, since a plurality of sudden expansion portions are provided in the supercooling elimination completion portion, the stirring effect due to turbulent flow can be further increased. It is possible to further promote the completion of cooling elimination.

【0046】請求項3の発明によれば、上記請求項1又
は2の発明において、過冷却解消完了部の急拡大部下流
側に、水等の流れと衝突して流れを乱す衝突部材を設け
たので、乱流による攪拌効果をさらに増大させることが
でき、よって、著効を発揮することができる。
According to the invention of claim 3, in the invention of claim 1 or 2, a collision member for colliding with the flow of water or the like and disturbing the flow is provided downstream of the rapid expansion part of the supercooling elimination completion part. Therefore, the stirring effect due to the turbulent flow can be further increased, and therefore a remarkable effect can be exhibited.

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

【図1】本発明の構成を示す図である。FIG. 1 is a diagram showing a configuration of the present invention.

【図2】実施例に係る製氷装置及び空気調和装置の配管
系統図である。
FIG. 2 is a piping system diagram of an ice making device and an air conditioner according to an embodiment.

【図3】第1実施例における過冷却解消完了部の構成を
示す図である。
FIG. 3 is a diagram showing a configuration of a supercooling elimination completion unit in the first embodiment.

【図4】第2実施例における過冷却解消完了部の構成を
示す図である。
FIG. 4 is a diagram showing a configuration of a supercooling elimination completion unit in a second embodiment.

【図5】第3実施例における過冷却解消完了部の構成を
示す図である。
FIG. 5 is a diagram showing a configuration of a supercooling elimination completion unit in a third embodiment.

【図6】第4実施例における過冷却解消部と過冷却解消
完了部との構成を示す図である。
FIG. 6 is a diagram showing a configuration of a supercooling elimination unit and a supercooling elimination completion unit in the fourth embodiment.

【符号の説明】[Explanation of symbols]

1 冷媒回路 5 蓄氷槽 22 水熱交換器(過冷却生成熱交換器) 8 再冷却器(過冷却解消部) 9 過冷却解消完了部 9a 急拡大部 9c 衝突部材 51 水循環路 DESCRIPTION OF SYMBOLS 1 Refrigerant circuit 5 Ice storage tank 22 Water heat exchanger (supercooling generation heat exchanger) 8 Recooler (supercooling elimination part) 9 Supercooling elimination completion part 9a Rapid expansion part 9c Collision member 51 Water circulation path

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 水又は水溶液のスラリ―状の氷化物を貯
溜するための蓄氷槽(5)と、冷却装置に接続され、水
又は水溶液を過冷却するための過冷却生成熱交換器(2
2)と、該過冷却生成熱交換器(22)に蓄氷槽(5)
の水又は水溶液を強制循環させるための水循環路(5
1)と、該水循環路(51)の上記熱交換器(22)下
流側に設けられ、水又は水溶液の過冷却状態を解消する
ための過冷却解消部(8)とを備えた製氷装置におい
て、 上記水循環路(51)の上記過冷却解消部(8)下流側
に設けられ、水循環路(51)の管径を急激に拡大させ
てなる急拡大部(9a)を有する過冷却解消完了部
(9)を備えたことを特徴とする製氷装置。
1. A subcooling generation heat exchanger for supercooling water or an aqueous solution, which is connected to an ice storage tank (5) for storing a slurry-like iced product of water or an aqueous solution and a cooling device ( Two
2) and an ice storage tank (5) in the supercooling generation heat exchanger (22).
Water circulation path for forced circulation of water or aqueous solution (5)
1) and an ice making device comprising a water cooling passage (51) downstream of the heat exchanger (22) and a supercooling elimination section (8) for eliminating a supercooled state of water or an aqueous solution. , A supercooling elimination completion portion which is provided on the downstream side of the supercooling elimination portion (8) of the water circulation passageway (51) and has a sudden enlargement portion (9a) formed by rapidly increasing the pipe diameter of the water circulation passageway (51). An ice making device comprising (9).
【請求項2】 請求項1記載の製氷装置において、 上記過冷却解消完了部(9)は、複数個の急拡大部(9
a1),(9a2)を有することを特徴とする製氷装置。
2. The ice making device according to claim 1, wherein the supercooling elimination completion section (9) includes a plurality of sudden expansion sections (9).
An ice making device comprising a1) and (9a2).
【請求項3】 請求項1又は2記載の製氷装置におい
て、 上記過冷却解消完了部(9)は、水循環路(51)の急
拡大部(9a)の下流側に水又は水溶液の流れと衝突す
る衝突部材(9c)を有することを特徴とする製氷装
置。
3. The ice making device according to claim 1, wherein the supercooling elimination completion section (9) collides with a flow of water or an aqueous solution on a downstream side of the sudden expansion section (9a) of the water circulation path (51). An ice making device having a collision member (9c) for
JP31236791A 1991-11-27 1991-11-27 Ice making equipment Expired - Lifetime JP2946889B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP31236791A JP2946889B2 (en) 1991-11-27 1991-11-27 Ice making equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP31236791A JP2946889B2 (en) 1991-11-27 1991-11-27 Ice making equipment

Publications (2)

Publication Number Publication Date
JPH05149653A true JPH05149653A (en) 1993-06-15
JP2946889B2 JP2946889B2 (en) 1999-09-06

Family

ID=18028407

Family Applications (1)

Application Number Title Priority Date Filing Date
JP31236791A Expired - Lifetime JP2946889B2 (en) 1991-11-27 1991-11-27 Ice making equipment

Country Status (1)

Country Link
JP (1) JP2946889B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH074801A (en) * 1993-06-18 1995-01-10 Shinryo Corp Ice-maker
WO2003031887A1 (en) * 2001-09-26 2003-04-17 The Kansai Electric Power Co., Inc. Method and system for making ice by underwater supercooling release and low temperature water supply system comprising it
CN102003856A (en) * 2010-11-04 2011-04-06 广州鑫誉蓄能科技有限公司 Jet type anti-ice crystal transmitter

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH074801A (en) * 1993-06-18 1995-01-10 Shinryo Corp Ice-maker
WO2003031887A1 (en) * 2001-09-26 2003-04-17 The Kansai Electric Power Co., Inc. Method and system for making ice by underwater supercooling release and low temperature water supply system comprising it
KR100774604B1 (en) * 2001-09-26 2007-11-09 간사이 덴료쿠 가부시키가이샤 Method and system for making ice by underwater supercooling release and low temperature water supply system comprising it
CN102003856A (en) * 2010-11-04 2011-04-06 广州鑫誉蓄能科技有限公司 Jet type anti-ice crystal transmitter

Also Published As

Publication number Publication date
JP2946889B2 (en) 1999-09-06

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