JPH04240367A - ice making device - Google Patents
ice making deviceInfo
- Publication number
- JPH04240367A JPH04240367A JP2158491A JP2158491A JPH04240367A JP H04240367 A JPH04240367 A JP H04240367A JP 2158491 A JP2158491 A JP 2158491A JP 2158491 A JP2158491 A JP 2158491A JP H04240367 A JPH04240367 A JP H04240367A
- Authority
- JP
- Japan
- Prior art keywords
- section
- supercooling
- refrigerant
- water
- 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.)
- Granted
Links
Landscapes
- Other Air-Conditioning Systems (AREA)
- Devices That Are Associated With Refrigeration Equipment (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【0001】0001
【産業上の利用分野】本発明は、蓄氷槽の水又は水溶液
を循環させて過冷却したのちその過冷却状態を再冷却に
より解消させてスラリー状の氷化物にするようにした製
氷装置に関し、特に過冷却解消部の冷却性能に関する。[Industrial Field of Application] The present invention relates to an ice making device which circulates water or an aqueous solution in an ice storage tank to supercool it, and then eliminates the supercooled state by recooling to produce a slurry-like frozen product. , especially regarding the cooling performance of the supercooling elimination section.
【0002】従来より、冷却装置に接続された熱交換器
と蓄氷槽との間で蓄氷槽の水を循環させる水循環回路を
設け、熱交換器により蓄氷槽の水をスラリー状の氷化物
に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ごとく、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、熱交換器をこの樋間に介設して、水循環路で熱
交換器により過冷却された水を樋の出口で過冷却状態を
解消させてスラリー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ものは公知の技術である。また、
実開平1−112345号公報に開示されるごとく、邪
魔板及び傾斜樋を設置して、熱交換器で過冷却された水
を大気に放出して邪魔板に衝突させ、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
せるものも公知の技術である。Conventionally, a water circulation circuit for circulating water in the ice storage tank between a heat exchanger connected to a cooling device and an ice storage tank has been provided, and the heat exchanger converts the water in the ice storage tank into slurry ice. For example, as an ice making device that makes ice
As disclosed in Japanese Patent Publication No. 217171, the outlet side of the water circulation path is an inclined gutter that faces downward on the upstream side and is formed such that the outlet end opens at a certain height above the water surface of the ice storage tank, and the water circulation path is a sloped gutter that is formed to open at a certain height above the water surface of the ice storage tank. A container is placed between these gutters, and the water that has been supercooled by a heat exchanger in the water circulation path is de-supercooled at the outlet of the gutters and becomes frozen into a slurry, and this frozen product is stored in an ice storage tank. This is a known technique. Also,
As disclosed in Japanese Utility Model Application Publication No. 1-112345, a baffle plate and an inclined gutter are installed, and the supercooled water in the heat exchanger is discharged into the atmosphere and collides with the baffle plate, thereby reducing the supercooled state of the water. It is also a known technique to melt the ice, turn the water into ice, and drop it into the ice storage tank through the gutter.
【0003】0003
【発明が解決しようとする課題】これら従来の技術では
、樋を用いて落下により水又は水溶液を移送するため、
機器の配置等の設計上の制約があった。これを解決する
ものとして、出願人は特願平2−105952号におい
て、蓄氷槽の水又は水溶液を循環させるための水循環路
の途中の管路に、再冷却による過冷却解消部を設け、そ
のままスラリー状で水又は水溶液の氷化物を閉管路内に
より蓄氷槽まで送ることを提案した。このスラリー状の
氷化物を沈降させずに流すには、ある程度の流速が必要
であり、管路内壁への氷の付着を防止するためにも、こ
の流速は速いほうがよい。しかしながら、流速が速いと
過冷却解消部で水又は水溶液の温度が十分に下がりきる
前に流れ去る。これを防止するには、過冷却解消部の温
度を下げて、水又は水溶液との温度差を大きくして冷却
能力を高くすること、または過冷却解消部の伝熱面積を
大きくして冷却能力を高くすることが考えられるが、前
者は過冷却解消部の冷却用に特に低温の冷熱源を発生す
るための装置が必要となり、後者は装置が大容量になる
欠点がある。本発明はかかる点に鑑みてなされたもので
あり、その目的は、水又は水溶液の過冷却状態の解消を
小さな装置で効率良く行うことにある。[Problems to be Solved by the Invention] These conventional techniques use a gutter to transfer water or aqueous solution by falling.
There were design constraints such as equipment placement. In order to solve this problem, the applicant proposed in Japanese Patent Application No. 105952/1997 that a supercooling eliminating section by recooling is provided in a pipe in the middle of a water circulation path for circulating water or an aqueous solution in an ice storage tank. We proposed to send frozen water or aqueous solution in slurry form to the ice storage tank through a closed pipe. A certain flow rate is required to flow this slurry-like frozen product without sedimentation, and it is better to have a higher flow rate in order to prevent ice from adhering to the inner wall of the pipe. However, if the flow rate is high, the water or aqueous solution will flow away before the temperature of the water or aqueous solution is sufficiently lowered in the supercooling elimination section. To prevent this, lower the temperature of the supercooling elimination section to increase the temperature difference with the water or aqueous solution to increase the cooling capacity, or increase the heat transfer area of the supercooling elimination section to increase the cooling capacity. It is conceivable to increase the temperature, but the former requires a device to generate a particularly low-temperature cold source for cooling the supercooling elimination section, and the latter has the disadvantage that the device has a large capacity. The present invention has been made in view of these points, and its purpose is to efficiently eliminate the supercooled state of water or an aqueous solution using a small device.
【0004】0004
【課題を解決するための手段】上記目的を達成するため
本発明の解決手段は、図1に示すように、水又は水溶液
のスラリー状の氷化物を貯溜するための蓄氷槽(5)と
、冷却装置(2)に接続され、水又は水溶液を過冷却す
るための主熱交換器(22)と、上記主熱交換器(22
)と蓄氷槽(5)とを接続する復管路(51B)内の流
路中に介設され、水又は水溶液の過冷却状態を解消させ
てスラリー状の氷化物にするための過冷却解消部(8)
とを備えた製氷装置を前提とする。[Means for Solving the Problems] In order to achieve the above object, the solution means of the present invention, as shown in FIG. , a main heat exchanger (22) connected to the cooling device (2) for supercooling water or an aqueous solution, and the main heat exchanger (22)
) and the ice storage tank (5) are interposed in the flow path in the return pipe (51B) to eliminate the supercooled state of water or aqueous solution and turn it into a slurry-like frozen product. Elimination part (8)
An ice making device equipped with
【0005】第1の解決手段は、図3〜図12に示すよ
うに、過冷却解消部(8)の構成として、復管路(51
B)の管内表面に対し外方に膨出する窪み部(83)を
形成して、この窪み部(83)内面を過冷却解消部(8
)の冷却伝熱面(81)としたものである。[0005] The first solution, as shown in FIGS. 3 to 12, includes a return pipe (51
A recess (83) that bulges outward is formed on the inner surface of the pipe of B), and the inner surface of this recess (83) is used as a supercooling eliminating section (8).
) as the cooling heat transfer surface (81).
【0006】第2の解決手段は、図13〜図18に示す
ように、過冷却解消部(8)の冷却伝熱面(81)の周
りに設けられ、冷却伝熱面(81)付近での水又は水溶
液の流速を局所的に遅くするための障壁部(82)を備
えたものである。The second solution is, as shown in FIGS. 13 to 18, provided around the cooling heat transfer surface (81) of the supercooling elimination section (8), and near the cooling heat transfer surface (81). It is equipped with a barrier part (82) for locally slowing down the flow rate of water or aqueous solution.
【0007】第3の解決手段は、図19〜図22に示す
ように、上記第1又は第2の解決手段に加えて、過冷却
解消部(8)に近接して設けられ、過冷却解消部(8)
で生じた氷化物の管壁への付着を解離させるよう復管路
(51B)を加熱する凍結防止部(9)とを備えたもの
である。As shown in FIGS. 19 to 22, a third solution means, in addition to the first or second solution means, is provided in the vicinity of the supercooling elimination section (8) and eliminates supercooling. Part (8)
The pipe is equipped with a freeze prevention section (9) that heats the return pipe (51B) so as to break up the adhesion of frozen substances to the pipe wall.
【0008】第4の解決手段は、図2及び図23に示す
ように、上記第1又は第2の解決手段に加えて、冷却装
置(2)を、圧縮機(11),(21)、凝縮器(12
)、減圧機構(23)及び蒸発器として作用する主熱交
換器(22)を順次接続してなる冷媒回路(1)を備え
た冷却装置(2)とし、過冷却解消部(8)は上記冷媒
回路(1)の冷媒との熱交換により過冷却状態の水又は
水溶液を冷却するものであり、冷媒回路(1)の液管部
(35)と過冷却解消部(8)の冷媒入口端(86)と
の間を減圧部(C4)を介して接続するとともに、過冷
却解消部(8)の冷媒出口端(87)は冷媒回路(1)
の低圧部(25)に接続する構成としたものである。[0008] As shown in FIGS. 2 and 23, a fourth solution means, in addition to the first or second solution means, replaces the cooling device (2) with compressors (11), (21), Condenser (12
), a decompression mechanism (23), and a main heat exchanger (22) functioning as an evaporator are sequentially connected to each other to form a refrigerant circuit (1). It cools supercooled water or aqueous solution by heat exchange with the refrigerant in the refrigerant circuit (1), and the refrigerant inlet end of the liquid pipe section (35) and supercooling elimination section (8) of the refrigerant circuit (1) (86) via the pressure reduction part (C4), and the refrigerant outlet end (87) of the supercooling elimination part (8) is connected to the refrigerant circuit (1).
The structure is such that it is connected to the low pressure section (25) of the.
【0009】第5の解決手段は、図2及び図24に示す
ように、上記第3の解決手段に加えて、冷却装置(2)
を、圧縮機(11),(21)、凝縮器(12)、減圧
機構(23)及び蒸発器として作用する主熱交換器(2
2)を順次接続してなる冷媒回路(1)を備えた冷却装
置(2)とし、過冷却解消部(8)は上記冷媒回路(1
)の冷媒との熱交換により過冷却状態の水又は水溶液を
冷却するものであり、凍結防止部(9)は上記冷媒回路
(1)の冷媒との熱交換により過冷却解消部(8)に近
接する管壁を加熱するものであり、凍結防止部(9)の
冷媒入口端(96)を冷媒回路(1)の液管部(35)
に接続し、過冷却解消部(8)の冷媒出口端(87)を
冷媒回路(1)の低圧部(25)に接続するとともに、
凍結防止部(9)の冷媒出口端(97)と過冷却解消部
(8)の冷媒入口端(86)との間は減圧部(C4)を
介して接続するものである。A fifth solution, as shown in FIGS. 2 and 24, includes a cooling device (2) in addition to the third solution described above.
, compressors (11), (21), condenser (12), pressure reduction mechanism (23), and main heat exchanger (2) that acts as an evaporator.
A cooling device (2) is provided with a refrigerant circuit (1) formed by sequentially connecting the refrigerant circuits (1) to
) to cool water or aqueous solution in a supercooled state by heat exchange with the refrigerant in the refrigerant circuit (1), and the antifreeze section (9) cools the supercooled water or aqueous solution by heat exchange with the refrigerant in the refrigerant circuit (1). It heats the adjacent pipe wall, and connects the refrigerant inlet end (96) of the antifreeze section (9) to the liquid pipe section (35) of the refrigerant circuit (1).
and connect the refrigerant outlet end (87) of the supercooling elimination section (8) to the low pressure section (25) of the refrigerant circuit (1),
The refrigerant outlet end (97) of the freeze prevention section (9) and the refrigerant inlet end (86) of the supercooling elimination section (8) are connected via a pressure reducing section (C4).
【0010】0010
【作用】以上の解決手段により、請求項1の発明では、
過冷却解消部(8)の窪み部(83)において、水又は
水溶液の流れが淀んで遅くなる、いわゆる準静止状態に
なる。冷却伝熱面を通して冷却するときには、水又は水
溶液は流れが速いと、温度が十分に下がる前に流れ去る
。しかし、本発明の過冷却解消部(8)の窪み部(83
)においては、水又は水溶液の流速が遅くなるので、窪
み部(83)内面の冷却伝熱面(81)により、水又は
水溶液の温度も十分に下がるので、冷却能力は向上し、
過冷却の解消は効率よく行われる。また、水又は水溶液
全部の流速を遅くするものではないので、生成した氷化
物の流れが悪くなることによる復管路(51)内の閉塞
も生じない。なお、水又は水溶液全部を再冷却すること
なく、水又は水溶液全部の過冷却状態を解消できるのは
、窪み部(83)において氷化物ができ、この氷化物が
核となるからである。[Operation] With the above solution, in the invention of claim 1,
In the recess (83) of the supercooling elimination section (8), the flow of water or aqueous solution becomes stagnant and slow, resulting in a so-called quasi-stationary state. When cooling through a cooled heat transfer surface, if the water or aqueous solution is flowing quickly, it will run off before the temperature has dropped sufficiently. However, the recessed portion (83) of the supercooling eliminating portion (8) of the present invention
), the flow rate of the water or aqueous solution is slowed down, so the temperature of the water or aqueous solution is sufficiently lowered by the cooling heat transfer surface (81) on the inner surface of the recess (83), so the cooling capacity is improved.
Elimination of supercooling is performed efficiently. In addition, since the flow rate of the entire water or aqueous solution is not slowed down, there will be no blockage in the return pipe (51) due to a slow flow of generated frozen substances. Note that the reason why the supercooled state of the entire water or aqueous solution can be eliminated without recooling the entire water or aqueous solution is that a frozen product is formed in the depression (83) and this frozen product becomes a core.
【0011】請求項2の発明では、過冷却解消部(8)
の周りの障壁部(82)が水又は水溶液の流れを妨げる
ので、過冷却解消部(8)の冷却伝熱面(81)に接す
る所で水又は水溶液の流速が遅くなる。また、水又は水
溶液の全体の流速を遅くするものではないので、請求項
1の発明と同様に、冷却能力は向上し、過冷却の解消は
効率よく行われ、氷化物の流れが悪くなることによる復
管路(51B)内の閉塞も生じない。[0011] In the invention of claim 2, the supercooling eliminating section (8)
Since the barrier section (82) around the supercooling section (82) obstructs the flow of the water or aqueous solution, the flow rate of the water or aqueous solution becomes slow at the point where it contacts the cooling heat transfer surface (81) of the supercooling elimination section (8). Further, since the overall flow rate of water or aqueous solution is not slowed down, the cooling capacity is improved, supercooling is efficiently eliminated, and the flow of frozen substances is worsened, as in the invention of claim 1. Also, no blockage occurs in the return pipe (51B).
【0012】請求項3の発明では、上記請求項1又は請
求項2の発明に加えて、過冷却解消部(8)の周りの管
壁を加熱する凍結防止部(9)により、過冷却解消部(
8)で生成した氷化物が過冷却解消部(8)付近の管壁
に付着するのを解離して、過冷却解消部(8)及びこの
付近の管壁の凍結を阻止し、製氷効率を向上させる。In the invention of claim 3, in addition to the invention of claim 1 or claim 2, supercooling is eliminated by a freeze prevention section (9) that heats the tube wall around the supercooling elimination section (8). Department (
The frozen product generated in step 8) is dissociated from adhering to the tube wall near the supercooling eliminating section (8), preventing the supercooling eliminating section (8) and the tube wall in this vicinity from freezing, and improving ice making efficiency. Improve.
【0013】請求項4の発明では、上記請求項1又は請
求項2の発明に加えて、主熱交換器(22)が冷却装置
(2)の冷媒回路(1)に接続されていて、過冷却解消
部(8)には、上記冷媒回路(1)の液冷媒を減圧部(
C4)で減圧した低温の冷媒を流通して冷却するので、
別途冷却装置を設けることなく、過冷却解消が行われる
。In the invention of claim 4, in addition to the invention of claim 1 or claim 2, the main heat exchanger (22) is connected to the refrigerant circuit (1) of the cooling device (2), and The cooling elimination section (8) supplies the liquid refrigerant of the refrigerant circuit (1) to the decompression section (
Since the low-temperature refrigerant depressurized by C4) is circulated and cooled,
Supercooling can be eliminated without providing a separate cooling device.
【0014】請求項5の発明では、上記請求項3の発明
に加えて、主熱交換器(22)が冷却装置(2)の冷媒
回路(1)に接続されていて、凍結防止部(9)には冷
媒回路(1)の比較的高温の液冷媒が流通する一方、過
冷却解消部(8)には凍結防止部(9)で冷媒との熱交
換により冷却され、さらに減圧部(C4)で減圧された
低温の冷媒が流通するので、別途加熱冷却装置を設ける
ことなく、過冷却解消と凍結防止が行われる。In the invention of claim 5, in addition to the invention of claim 3, the main heat exchanger (22) is connected to the refrigerant circuit (1) of the cooling device (2), and the antifreeze section (9) is connected to the refrigerant circuit (1) of the cooling device (2). ), the relatively high-temperature liquid refrigerant from the refrigerant circuit (1) flows through the supercooling elimination section (8), where it is cooled by heat exchange with the refrigerant at the anti-freezing section (9), and further flows through the decompression section (C4 ), the low-temperature refrigerant is circulated, so supercooling can be eliminated and freezing can be prevented without the need for a separate heating and cooling device.
【0015】[0015]
【実施例】以下、本発明の実施例について、図2以下の
図面に基づき説明する。図2は本発明の製氷装置を備え
た空気調和装置の実施例を示し、冷却装置(2)の冷媒
回路(1)は下記のように構成している。(11)は第
1圧縮機、(12)はこの第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)はこの室外熱交換器(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。また、(21)は第2圧縮機、(
22)はこの第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、(23)はこの主熱交換器(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。Embodiments Hereinafter, embodiments of the present invention will be described with reference to FIG. 2 and subsequent drawings. FIG. 2 shows an embodiment of an air conditioner equipped with an ice making device of the present invention, and the refrigerant circuit (1) of the cooling device (2) is configured as follows. (11) is the first compressor, (12) is an outdoor heat exchanger that is arranged on the discharge side of this first compressor (11) and exchanges heat between the refrigerant and outdoor air, and (13) is this outdoor heat exchanger. An outdoor motorized expansion valve that adjusts the refrigerant flow rate of the exchanger (12) or reduces the pressure, and the above-mentioned devices (11) to (13) are connected in series in the first pipe line (14). . In addition, (21) is the second compressor, (
22) is arranged on the discharge side of this second compressor (21),
A main heat exchanger (23) for supercooling water or aqueous solution in an ice storage tank (5), which will be described later, adjusts the refrigerant flow rate when the main heat exchanger (22) functions as a condenser, and It is a water-side electric expansion valve that reduces the pressure of the refrigerant when functioning as a
24) are connected in series within.
【0016】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)はこの油分離器(SD1),
(SD2)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のキャ
ピラリーチューブである。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、上
記各機器(32),(33)はそれぞれ直列に接続され
、かつその各組が第3管路(34)中で並列に接続され
ている。また、(35)は室外電動膨張弁(13)と水
側電動膨張弁(23)とをつなぐ液管部である。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ームレーターである。
また、(10)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(1
1),(21)の吐出側又は吸入側に切換連通させる四
路切換弁(10)であって、この四路切換弁(10)が
図中実線側に切り換わったときには室外熱交換器(12
)が凝縮器、主熱交換器(22)又は室内熱交換器(3
2),(32)が蒸発器として機能する一方、四路切換
弁(10)が図中波線側に切り換わったときには室外熱
交換器(12)が蒸発器、主熱交換器(22)又は室内
熱交換器(32),(32)が凝縮蒸器として機能する
。さらに、各圧縮機(11),(21)の吸入側をバイ
パス接続する低圧部(25)と、主熱交換器(22)の
ガス管を上記第2圧縮機(21)の吐出管と低圧部(2
5)とに切換連通させる水側切換弁(26)とが設けら
れている。この水側切換弁(26)は四路切換弁のうち
の3つのポートを利用して、水側切換弁(26)が図中
実線側に切り換わったときには主熱交換器(22)が蒸
発器として機能する一方、水側切換弁(26)が図中破
線側に切り換わったときには主熱交換器(22)のガス
管が第2圧縮機(21)の吐出管に連通し、主熱交換器
(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ーチューブである。Note that (SD1) and (SD2) are oil separators installed in the discharge pipes of the compressors (11) and (21), respectively, and (C1) and (C2) are the oil separators (SD1). ,
Oil return pipes (R) provided on the suction side of (SD2)
These are capillary tubes for depressurization installed in T1) and (RT2), respectively. Furthermore, (32), (32)
are indoor heat exchangers placed in each room, (33), (33
) is an indoor electric expansion valve as a pressure reducing valve for reducing the pressure of the refrigerant, each of the above devices (32) and (33) is connected in series, and each set thereof is connected in parallel in the third pipe (34). ing. Further, (35) is a liquid pipe section that connects the outdoor electric expansion valve (13) and the water side electric expansion valve (23). The first pipe line (14) and the second pipe line (24) are connected in parallel to the third pipe line (34). In addition, (A
C) is the third compressor on the suction side of each compressor (11), (21).
This is an accumulator provided in the conduit (34). In addition, (10) connects the gas pipes of the outdoor heat exchanger (12) and the gas pipes of the indoor heat exchangers (32), (32) to each compressor (1).
A four-way switching valve (10) that switches between the discharge side and the suction side of 1) and (21), and when the four-way switching valve (10) switches to the solid line side in the figure, the outdoor heat exchanger ( 12
) is the condenser, main heat exchanger (22) or indoor heat exchanger (3
2) and (32) function as an evaporator, while when the four-way switching valve (10) switches to the dotted line side in the figure, the outdoor heat exchanger (12) functions as an evaporator, main heat exchanger (22), or Indoor heat exchangers (32), (32) function as condensing steamers. Furthermore, a low pressure section (25) that bypass-connects the suction side of each compressor (11), (21), and a gas pipe of the main heat exchanger (22) are connected to the discharge pipe of the second compressor (21) and the low pressure section. Part (2
5) is provided with a water side switching valve (26) for switching communication with the water side switching valve (26). This water side switching valve (26) uses three ports of the four-way switching valve, and when the water side switching valve (26) switches to the solid line side in the figure, the main heat exchanger (22) evaporates. On the other hand, when the water side switching valve (26) switches to the side shown by the broken line in the figure, the gas pipe of the main heat exchanger (22) communicates with the discharge pipe of the second compressor (21), and the main heat An exchanger (22) is adapted to function as a condenser. Note that (C3) is a capillary tube interposed in the pipe on the dead port side of the water side switching valve (26).
【0017】さらに、第1圧縮機(11)及び第2圧縮
機(21)の吐出管どうしを接続するバイパス路(3)
が設けられていて、このバイパス路(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。すなわち、室外熱交換器(12)及び主熱交換
器(22)が凝縮器として機能する際、主熱交換器(2
2)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(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。ここで、製氷装置には、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、この蓄氷槽(5)と主熱交換
器(22)との間は、水循環路(51)により水又は水
溶液が循環するように接続されている。この水循環路(
51)は、蓄氷槽(5)の低部から主熱交換器(22)
に水又は水溶液を供給する往管路(51A)と、主熱交
換器(22)から蓄氷槽(5)の上部に水又は水溶液の
スラリー状の氷化物を戻す復管路(51B)とからなっ
ており、往管路(51A)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化物やゴミ
等の固体物を除去するストレーナー(53)が介設され
、さらに、このストレーナー(53)の下流側には、主
熱交換器(22)に供給される水又は水溶液を予熱する
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)が設けられていて、この予
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(62)を有する
予熱電動膨張弁(62)が介設されている。この予熱電
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
、主熱交換器(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。Furthermore, a bypass passage (3) connects the discharge pipes of the first compressor (11) and the second compressor (21).
The bypass passage (3) is provided with a check valve (4) that allows refrigerant to flow only from the discharge pipe side of the second compressor (21) to the discharge pipe side of the first compressor (11). ) is provided. That is, when the outdoor heat exchanger (12) and the main heat exchanger (22) function as a condenser, the main heat exchanger (22)
When the condensation temperature and pressure in step 2) become high, the amount of heat released can be distributed by releasing the gas discharged from the second compressor (21) to the outdoor heat exchanger (12). Here, an ice storage tank (5) for storing a slurry-like frozen product of water or an aqueous solution as a heat storage medium is arranged in the ice making device, and the ice storage tank (5) and the main heat exchanger (22) is connected through a water circulation path (51) so that water or an aqueous solution circulates therethrough. This water circulation path (
51) is the main heat exchanger (22) from the lower part of the ice storage tank (5).
an outgoing pipe (51A) that supplies water or an aqueous solution to the ice storage tank (5), and a return pipe (51B) that returns a frozen product in the form of a slurry of water or an aqueous solution from the main heat exchanger (22) to the upper part of the ice storage tank (5). A strainer (53) is installed downstream of the pump (52) in the outgoing pipe (51A) to remove solid matter such as frozen matter and dirt from the water or aqueous solution in the water circulation path (51). Furthermore, a preheating heat exchanger (6) for preheating the water or aqueous solution supplied to the main heat exchanger (22) is interposed downstream of the strainer (53). On the other hand, the liquid line of the refrigerant circuit (1) is provided with a preheating bypass passage (61) that allows a part of the liquid refrigerant to bypass the water side electric expansion valve (23) and flow to the preheating heat exchanger (6). A preheating electric expansion valve (62) having a refrigerant pressure reduction function and a flow rate control function (62) is installed on the downstream side of the preheating heat exchanger (6) in this preheating bypass path (61). . With this preheating electric expansion valve (62) and the water side electric expansion valve (23),
The refrigerant flow rate in the preheating bypass passage (61) is adjusted, and the pressure of the refrigerant is also reduced during the ice-making operation of the main heat exchanger (22).
【0018】さらに、上記水循環路(51)の復管路(
51B)において、主熱交換器(22)の下流側には、
復管路(51B)の水又は水溶液を冷却して主熱交換器
(22)で過冷却された水又は水溶液の過冷却状態を解
消させる過冷却解消部(8)としての再冷却器が設けら
れ、この過冷却解消部(8)の周囲には、管路の凍結を
防止するための加熱伝熱面(91)を有する凍結防止部
(9)が設けられ、さらに、この過冷却解消部(8)と
主熱交換器(22)との間には、復管路(51B)の凍
結が主熱交換器(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。また、上記冷媒回路(1)の液管部(35)
から保温熱交換器(7)に液冷媒を流通させる一方、こ
の液管部(35)から分岐して解消バイパス路(85)
が延び、この解消バイパス路(85)は、図24に示す
ように凍結防止部(9)の冷媒入口端(96)に接続さ
れ、この凍結防止部(9)の冷媒出口端(97)は減圧
弁又はキャピラリーチューブからなる減圧部(C4)を
介して上記過冷却解消部(8)の冷媒入口端(86)に
接続されるとともに、その冷媒出口端(87)が圧縮機
(11),(21)の吸入側となる低圧部(25)に接
続されている。すなわち、過冷却解消部(8)において
、減圧部(C4)で減圧され温度の下がった冷媒との熱
交換により、主熱交換器(22)で過冷却された水又は
水溶液を再冷却し、その過冷却状態を解消させてスラリ
ー状に氷化させ、復管路(51B)を介してスラリー状
の氷化物を蓄氷槽(5)まで循環させる一方、凍結防止
部(9)に凝縮された冷媒液をバイパスさせることによ
り、管壁を加熱して、過冷却状態の解消により生じた氷
化物の管壁への付着を解離させるようになされている。Furthermore, a return pipe (
51B), on the downstream side of the main heat exchanger (22),
A recooler is provided as a supercooling elimination section (8) that cools the water or aqueous solution in the return pipe (51B) to eliminate the supercooled state of the water or aqueous solution that has been supercooled in the main heat exchanger (22). A freeze prevention section (9) having a heating heat transfer surface (91) for preventing freezing of the pipe line is provided around the supercooling elimination section (8), and a freeze prevention section (9) is provided around the supercooling elimination section (8). (8) and the main heat exchanger (22), there is heat insulation as a freeze progress prevention part to prevent the freezing of the return pipe (51B) from progressing to the main heat exchanger (22). An exchanger (7) is provided. In addition, the liquid pipe section (35) of the refrigerant circuit (1)
While the liquid refrigerant is passed from the liquid refrigerant to the thermal insulation heat exchanger (7), the liquid refrigerant is branched from the liquid pipe section (35) to form an elimination bypass path (85).
As shown in FIG. 24, this relief bypass path (85) is connected to the refrigerant inlet end (96) of the antifreeze section (9), and the refrigerant outlet end (97) of the antifreeze section (9) is connected to the It is connected to the refrigerant inlet end (86) of the supercooling elimination section (8) via a pressure reducing section (C4) consisting of a pressure reducing valve or a capillary tube, and its refrigerant outlet end (87) is connected to the compressor (11), (21) is connected to the low pressure part (25) on the suction side. That is, in the supercooling elimination section (8), the water or aqueous solution that has been supercooled in the main heat exchanger (22) is recooled by heat exchange with the refrigerant whose pressure has been reduced and the temperature has decreased in the pressure reduction section (C4), The supercooled state is eliminated and the slurry is frozen, and the frozen slurry is circulated to the ice storage tank (5) via the return pipe (51B), while condensed in the antifreeze section (9). By bypassing the refrigerant liquid, the tube wall is heated, and the ice formed by the removal of the supercooled state from adhesion to the tube wall is dissociated.
【0019】さらに、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加熱して、上記過冷却
解消部(8)や復管路(51B)で水又は水溶液の過冷
却解消により生じた氷化物が復管路(51B)の管壁に
付着して凍結が主熱交換器(22)まで進展するのを防
止するようになされている。空気調和装置の運転時室内
で冷房を行うときには、四路切換弁(10)が図中実線
側に切り換えられる。そして、水側切換弁(26)が図
中実線側に切り換えられているときには、各圧縮機(1
1),(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)が図中破線側に切り換えられている
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
媒は主熱交換器(22)に流れ、それぞれ凝縮された後
、各室内熱交換器(32),(32)で蒸発するよう循
環するまた、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(10)及び水側切換弁(26)を図中実線
側に切り換え、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)で減圧して主熱交換器(
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蓄氷槽(5)の水又は水溶液を氷化
し、冷熱を蓄えるようになされている。Furthermore, in the heat retention heat exchanger (7), the water or aqueous solution is heated by heat exchange with the liquid refrigerant in the liquid line, and the water or aqueous solution is supercooled in the supercooling elimination section (8) and return pipe (51B). The ice formed by melting adheres to the pipe wall of the return pipe (51B) to prevent freezing from progressing to the main heat exchanger (22). When the air conditioner is operated to cool the room, the four-way switching valve (10) is switched to the solid line side in the figure. When the water side switching valve (26) is switched to the solid line side in the figure, each compressor (1
After the refrigerant discharged from 1) and (21) is condensed in the outdoor heat exchanger (12), the refrigerant is transferred to each indoor heat exchanger (32), (
32), the room is cooled by evaporation. Furthermore, when the water side switching valve (26) is switched to the side shown by the broken line in the figure, the refrigerant discharged from the first compressor (11) flows to the outdoor heat exchanger (12), while the refrigerant discharged from the second compressor (21) flows to the outdoor heat exchanger (12). The discharged refrigerant flows to the main heat exchanger (22), where it is condensed and then circulated to be evaporated in each indoor heat exchanger (32). Tank (
5) A cold storage heat operation is performed to store cold heat. That is,
Switch the four-way switching valve (10) and water side switching valve (26) to the solid line side in the figure, close each indoor electric expansion valve (33), (33), and turn on each compressor (11), (21). After condensing the discharged refrigerant in the outdoor heat exchanger (12), the water side electric expansion valve (23)
) or the main heat exchanger (
By evaporating in step 22), the water or aqueous solution in the ice storage tank (5) is supercooled and the water or aqueous solution in the ice storage tank (5) is turned into ice, thereby storing cold heat.
【0020】ここで、本発明では、主熱交換器(22)
下流側の復管路(51B)において、主熱交換器(22
)で過冷却された水又は水溶液が過冷却解消部(8)で
再冷却され、その過冷却状態が解消し、スラリー状で蓄
氷槽(5)に強制循環され、蓄氷槽(5)にスラリー状
の氷化物が貯溜されて昼間の冷房運転に必要な冷熱が蓄
えられる。その際、復管路(51B)での水又は水溶液
の全体の流速が速いと、過冷却解消部(8)で水又は水
溶液の温度が十分に下がる前に流れ去る。また、復管路
(51B)での水又は水溶液の全体の流速を遅くすると
、氷化物のスラリーの管路内への氷の付着や管路の閉塞
を生じる。Here, in the present invention, the main heat exchanger (22)
In the return pipeline (51B) on the downstream side, the main heat exchanger (22
) The supercooled water or aqueous solution is recooled in the supercooling elimination section (8), the supercooled state is eliminated, and the water or aqueous solution is forcibly circulated in the form of slurry to the ice storage tank (5). Slurry-like frozen material is stored in the tank, storing the cold energy necessary for daytime cooling operation. At this time, if the overall flow rate of the water or aqueous solution in the return pipe (51B) is high, the water or aqueous solution will flow away before the temperature of the water or aqueous solution is sufficiently lowered in the supercooling elimination section (8). Furthermore, if the overall flow rate of water or aqueous solution in the return pipe (51B) is slowed down, ice may adhere to the pipe of the frozen product slurry or the pipe may be blocked.
【0021】そこで、請求項1の発明に係わる実施例は
、復管路(51B)における管内表面に対し外方に膨出
する窪み部(83)を形成して、この窪み部(83)内
面を、過冷却解消部(8)の冷却伝熱面(81)とした
ことにより、この過冷却解消部(8)の冷却伝熱面(8
1)で水又は水溶液の流速を局所的に遅くすることがで
きるので、この冷却伝熱面(81)での水又は水溶液の
滞留時間は長くなり、水又は水溶液の温度を十分に下げ
ることができ、冷却能力が向上する。よって、この冷却
伝熱面(81)の伝熱面積を大きくすることなく、また
過冷却解消部(8)のために特に低温の冷熱源を用意す
ることなく、効率よく過冷却の解消が行える。図3,図
4は請求項1の発明の実施例に係わる過冷却解消部(8
)の冷却伝熱面(81)の形状を示したものである。図
3はその縦断面図、図4はその横断面図である。
円柱形状の窪み部(83)内面がこの冷却伝熱面(81
)になっており、この円柱形状の窪み部(83)で水又
は水溶液の滞留時間が長くなり、温度が十分に下がるの
で、過冷却解消部(8)の冷却能力が高く、過冷却の解
消が効率よく行われる。Therefore, the embodiment according to the invention of claim 1 forms a recessed portion (83) that bulges outward with respect to the inner surface of the pipe in the return pipe (51B), and the inner surface of this recessed portion (83) is the cooling heat transfer surface (81) of the supercooling elimination section (8), so that the cooling heat transfer surface (81) of the supercooling elimination section (8) is
Since the flow rate of water or aqueous solution can be locally slowed down in step 1), the residence time of water or aqueous solution on this cooling heat transfer surface (81) becomes longer, and the temperature of water or aqueous solution cannot be lowered sufficiently. cooling capacity is improved. Therefore, supercooling can be efficiently eliminated without increasing the heat transfer area of the cooling heat transfer surface (81) and without preparing a particularly low-temperature cold source for the supercooling elimination section (8). . 3 and 4 show the supercooling eliminating section (8) according to the embodiment of the invention of claim 1.
) shows the shape of the cooling heat transfer surface (81). FIG. 3 is a longitudinal cross-sectional view thereof, and FIG. 4 is a cross-sectional view thereof. The inner surface of the cylindrical recess (83) is the cooling heat transfer surface (81).
), the residence time of water or aqueous solution becomes longer in this cylindrical depression (83) and the temperature is sufficiently lowered, so the cooling capacity of the supercooling elimination section (8) is high and supercooling is eliminated. is carried out efficiently.
【0022】ここで冷却伝熱面(81)を冷却する手段
として、過冷却解消部(8)の冷媒入口端(86)から
導入した冷媒により冷却伝熱面(81)を冷却し、その
冷媒を過冷却解消部(8)の冷媒出口端(87)から出
すようにする。この冷媒として請求項4の発明のように
冷却装置(1)の冷媒回路(2)のものを用いるのが望
ましいが、請求項1の発明は別途冷却装置を設けてその
冷媒を用いてもよく、この冷却装置(1)の冷媒回路(
2)の冷媒を用いるものに限定されるものではない。
なお、請求項1の発明において、過冷却解消部(8)の
窪み部(83)の形状は図3,図4に限定されるもので
はない。図5〜図12は上記実施例1の変形例を示し、
各奇数番号の図は縦断面図、各偶数番号の図は前の番号
の図に対応する横断面図である。ここで、図5,図6は
窪み部(83)の形状を円錐とした場合、図7,図8は
窪み部(83)の形状を半球とした場合、図9,図10
は円柱形状の窪み部(83)が3個ある場合、図11,
図12は窪み部(83)が配管の横断面を一周してつな
がっている場合である。これらの変形例においても、水
又は水溶液の流速が局所的に遅くなり、温度が十分に下
がるので、過冷却解消部(8)の冷却能力が高く、過冷
却の解消が効率よく行われる。他に三角柱、直方体など
の形状の窪み部(83)も同様の効果を示す。Here, as a means for cooling the cooling heat transfer surface (81), the cooling heat transfer surface (81) is cooled by a refrigerant introduced from the refrigerant inlet end (86) of the supercooling elimination section (8), and the refrigerant is The refrigerant is discharged from the refrigerant outlet end (87) of the supercooling elimination section (8). As this refrigerant, it is preferable to use the refrigerant circuit (2) of the cooling device (1) as in the invention of claim 4, but in the invention of claim 1, a separate cooling device may be provided and the refrigerant may be used. , the refrigerant circuit (
It is not limited to those using the refrigerant of 2). In addition, in the invention of claim 1, the shape of the recessed part (83) of the supercooling eliminating part (8) is not limited to that shown in FIGS. 3 and 4. 5 to 12 show modified examples of the above-mentioned embodiment 1,
Each odd-numbered figure is a longitudinal cross-sectional view, and each even-numbered figure is a cross-sectional view corresponding to the previous numbered figure. Here, FIGS. 5 and 6 show a case where the shape of the recess (83) is a cone, and FIGS. 7 and 8 show a case where the shape of the recess (83) is a hemisphere, and FIGS. 9 and 10
In the case where there are three cylindrical depressions (83), Fig. 11,
FIG. 12 shows a case where the recesses (83) extend around the cross section of the pipe and are connected. In these modifications as well, the flow rate of water or aqueous solution is locally slowed down and the temperature is sufficiently lowered, so that the cooling capacity of the supercooling eliminating section (8) is high and supercooling is efficiently eliminated. Other recesses (83) shaped like triangular prisms or rectangular parallelepipeds also exhibit similar effects.
【0023】次に、請求項2の発明に係わる実施例につ
いて説明する。図13,図14は過冷却解消部(8)の
冷却伝熱面(81)の縦断面と横断面をそれぞれ示す。
本発明では、過冷却解消部(8)の冷却伝熱面(81)
の周りを中空の円柱形状の障壁部(82)で囲み、この
障壁部(82)の一方端は過冷却解消部(8)と接して
閉じており、他端の開口部からのみ水又は水溶液は出入
りするので、水又は水溶液の流れが妨げられ、流速がこ
の冷却伝熱面(81)で局所的に遅くなる。よって、こ
の冷却伝熱面(81)での水又は水溶液の滞留時間が長
くなり、温度が十分に下がるので、過冷却解消部(8)
の冷却能力が高く、過冷却の解消が効率よく行われる。
過冷却解消部(8)の構成は異なるが、請求項1の発明
と同様の効果を発揮する。ここで冷却伝熱面(81)の
冷却手段は請求項1と同様である。Next, an embodiment according to the second aspect of the invention will be described. 13 and 14 show a longitudinal section and a transverse section, respectively, of the cooling heat transfer surface (81) of the supercooling elimination section (8). In the present invention, the cooling heat transfer surface (81) of the supercooling elimination section (8)
is surrounded by a hollow cylindrical barrier part (82), one end of which is closed in contact with the supercooling elimination part (8), and water or aqueous solution is only allowed to enter through the opening at the other end. enters and exits, the flow of water or aqueous solution is obstructed and the flow rate is locally slowed down on this cooling heat transfer surface (81). Therefore, the residence time of water or aqueous solution on this cooling heat transfer surface (81) becomes longer and the temperature is sufficiently lowered, so that the supercooling elimination section (8)
has a high cooling capacity and eliminates supercooling efficiently. Although the structure of the supercooling eliminating section (8) is different, it exhibits the same effect as the invention of claim 1. Here, the cooling means for the cooling heat transfer surface (81) is the same as in claim 1.
【0024】なお、この実施例として図13,図14で
示した障壁部(82)は円柱形状としたが、過冷却解消
部(8)の冷却伝熱面(81)を囲む形状であれば、直
方体又は三角柱の形状を有するものでもよく、請求項2
の発明において、過冷却解消部(8)の冷却伝熱面(8
1)及び障壁部(82)の形状は図13,図14に限定
されるものではない。図15〜図18は上記実施例の各
変形例を示し、各奇数番号の図は縦断面図、各偶数番号
の図は前の番号の図に対応する横断面図である。図15
,図16は過冷却解消部(8)の冷却伝熱面(81)が
円柱形状を有して、管路内に突き出ており、その周りを
過冷却解消部(8)より大きい中空の円柱形状の障壁部
(82)で囲っていて、障壁部(82)の一方端は過冷
却解消部(8)と接して閉じており、他端の開口してい
る場合である。図17,図18は過冷却解消部(8)の
冷却伝熱面(81)が円柱形状を有して、復管路(51
B)を横断しており、この冷却伝熱面(81)の水又は
水溶液の上流と下流とに板状の障壁部(82)を設けて
いる場合である。これら変形例においても、水又は水溶
液の流速が遅くなり、温度が十分に下がるので、過冷却
解消部(8)の冷却能力が高く、過冷却の解消が効率よ
く行われる。また、水又は水溶液全部の流速を遅くする
ものではないので、生成した氷化物の流れが悪くなるこ
とによる復管路(51)内の閉塞も生じない。なお、水
又は水溶液全部を冷却することなく、水又は水溶液全部
の過冷却状態を解消できるのは、窪み部(83)におい
て氷化物ができ、この氷化物が核となるからである。
なお、これら請求項1及び請求項2の発明に係わる実施
例において、水又は水溶液全部を再冷却することなく、
水又は水溶液全部の過冷却状態を解消できるのは、発明
の窪み部(83)又は障壁部(82)の内側において氷
化物ができ、この氷化物が核となるからである。In this embodiment, the barrier part (82) shown in FIGS. 13 and 14 is cylindrical, but it may have a shape that surrounds the cooling heat transfer surface (81) of the supercooling eliminating part (8). , may have the shape of a rectangular parallelepiped or a triangular prism, as claimed in claim 2.
In the invention, the cooling heat transfer surface (8) of the supercooling eliminating section (8)
1) and the shapes of the barrier portion (82) are not limited to those shown in FIGS. 13 and 14. 15 to 18 show variations of the above embodiment, each odd numbered figure being a longitudinal sectional view, and each even numbered figure being a transverse sectional view corresponding to the previous numbered figure. Figure 15
, FIG. 16 shows that the cooling heat transfer surface (81) of the supercooling elimination section (8) has a cylindrical shape and protrudes into the pipe, and is surrounded by a hollow cylinder larger than the supercooling elimination section (8). This is a case where the barrier part (82) is surrounded by a shaped barrier part (82), one end of which is closed in contact with the supercooling elimination part (8), and the other end is open. 17 and 18 show that the cooling heat transfer surface (81) of the supercooling elimination section (8) has a cylindrical shape, and the return pipe (51) has a cylindrical shape.
B), and plate-shaped barrier portions (82) are provided upstream and downstream of the water or aqueous solution of this cooling heat transfer surface (81). In these modified examples as well, the flow rate of water or aqueous solution is slowed down and the temperature is sufficiently lowered, so the cooling capacity of the supercooling eliminating section (8) is high and supercooling is efficiently eliminated. In addition, since the flow rate of the entire water or aqueous solution is not slowed down, there will be no blockage in the return pipe (51) due to a slow flow of generated frozen substances. The reason why the supercooled state of the entire water or aqueous solution can be eliminated without cooling the entire water or aqueous solution is that a frozen product is formed in the recess (83) and this frozen product becomes a core. In addition, in the embodiments according to the invention of claims 1 and 2, without recooling the entire water or aqueous solution,
The reason why the supercooled state of the entire water or aqueous solution can be eliminated is because a frozen product is formed inside the recessed portion (83) or barrier portion (82) of the invention, and this frozen product becomes a core.
【0025】請求項3の発明に係わる実施例は、上記請
求項1又は請求項2の発明に係わる実施例において、過
冷却解消部(8)の冷却伝熱面(81)に近接して凍結
防止部(9)の加熱伝熱面(91)を設けるのであり、
図19,図20は請求項1の発明に係わる実施例におい
て凍結防止部(9)を設けた実施例である。過冷却解消
部(8)に近接した凍結防止部(9)により、過冷却解
消部(8)で生じた氷化物の管壁への付着を解離させる
ことができるので、氷化物の管壁への付着と成長による
閉塞を防止できる。とくに、請求項1又は請求項2の発
明に係わる実施例による過冷却解消部(8)は、冷却能
力が高いので、冷却伝熱面(81)が小さくできる。よ
って、近接した凍結防止部(9)の加熱伝熱面(91)
も小さくできる。ここで加熱伝熱面(91)を加熱する
手段として、凍結防止部(9)の冷媒入口端(96)か
ら導入した熱媒により加熱伝熱面(81)を加熱し、そ
の熱媒を凍結防止部(9)の冷媒出口端(97)から出
すようにする。この実施例の凍結防止部(9)と過冷却
解消部(8)は二重円管になっており、上記熱媒は過冷
却解消部(8)の外側にある凍結防止部(9)の空間を
通って、凍結防止部(9)の冷媒入口端(96)から凍
結防止部(9)の冷媒出口端(97)に抜ける。また、
冷却伝熱面(81)を冷却する手段として、過冷却解消
部(8)の冷媒入口端(86)から導入した冷媒により
冷却伝熱面(81)を冷却し、その冷媒を過冷却解消部
(8)の冷媒出口端(87)から出すようにする。この
熱媒及び冷媒として請求項5の発明のように冷却装置(
1)の冷媒回路(2)のものを用いるのが望ましいが、
請求項3の発明は別途加熱冷却装置を設けてその熱冷媒
を用いてもよく、この冷却装置(1)の冷媒回路(2)
の冷媒を用いるものに限定されるものではない。
なお、図21,図22は請求項3の発明に係わる実施例
の変形例を示し、請求項2の発明に係わる実施例におい
て凍結防止部(9)を設けた実施例である。[0025] The embodiment according to the invention of claim 3 is the embodiment according to the invention of claim 1 or claim 2, in which the supercooling eliminating section (8) is frozen in the vicinity of the cooling heat transfer surface (81). A heating heat transfer surface (91) of the prevention part (9) is provided,
19 and 20 show an embodiment in which a freeze prevention section (9) is provided in the embodiment according to the invention of claim 1. The anti-freezing section (9) close to the supercooling eliminating section (8) can dissociate the frozen matter that has adhered to the tube wall caused by the supercooling eliminating section (8), so that the frozen matter can be removed from the tube wall. can prevent blockage due to adhesion and growth. In particular, since the supercooling eliminating section (8) according to the embodiment of the invention of claim 1 or claim 2 has a high cooling capacity, the cooling heat transfer surface (81) can be made small. Therefore, the heating heat transfer surface (91) of the adjacent anti-freeze section (9)
can also be made smaller. Here, as a means of heating the heating heat transfer surface (91), the heating heat transfer surface (81) is heated by a heat medium introduced from the refrigerant inlet end (96) of the anti-freeze section (9), and the heat transfer surface (81) is frozen. The refrigerant is made to come out from the refrigerant outlet end (97) of the prevention part (9). The antifreeze section (9) and supercooling elimination section (8) in this embodiment are double circular tubes, and the heat medium is transferred to the antifreeze section (9) located outside the supercooling elimination section (8). Through the space, the refrigerant exits from the refrigerant inlet end (96) of the antifreeze section (9) to the refrigerant outlet end (97) of the antifreeze section (9). Also,
As a means for cooling the cooling heat transfer surface (81), the cooling heat transfer surface (81) is cooled by a refrigerant introduced from the refrigerant inlet end (86) of the supercooling elimination section (8), and the refrigerant is transferred to the supercooling elimination section. The refrigerant is discharged from the refrigerant outlet end (87) of (8). As the heating medium and the refrigerant, a cooling device (
It is preferable to use the refrigerant circuit (2) in 1).
In the invention of claim 3, a heating/cooling device may be provided separately and the thermal refrigerant may be used in the refrigerant circuit (2) of this cooling device (1).
The invention is not limited to those using refrigerants. 21 and 22 show a modification of the embodiment according to the third aspect of the invention, which is an embodiment in which a freeze prevention part (9) is provided in the embodiment according to the second aspect of the invention.
【0026】請求項4の発明に係わる実施例は、上記請
求項1又は請求項2の発明に係わる実施例において、過
冷却解消部(8)の冷却用の冷熱源として、冷却装置(
2)の冷媒回路(1)から分岐した液冷媒を用いるので
あり、図2の実施例では、解消バイパス路(85)を凍
結防止部(9)に接続したのち、過冷却解消部(8)に
接続しているが、この実施例はこの凍結防止部(9)を
除いて直接に解消バイパス路(85)を過冷却解消部(
8)と接続するのである。具体的には、凝縮器としての
室外熱交換器(12)の出口側の液管部(35)から分
岐した解消バイパス路(85)を、図23に要部を示す
ように、減圧部(C4)を介して、過冷却解消部(8)
に接続し、過冷却解消部(8)の出口端は圧縮機(11
),(21)の吸入側の低圧部(25)に接続するので
ある。すなわち、減圧部(C4)により温度が下がった
冷媒液を過冷却解消部(8)に流して、水又は水溶液を
冷却する。よって、別途冷却装置を設ける必要がないの
である。The embodiment according to the invention of claim 4 is the embodiment according to the invention of claim 1 or claim 2, in which a cooling device (
2), the liquid refrigerant branched from the refrigerant circuit (1) is used, and in the embodiment shown in FIG. However, in this embodiment, excluding this antifreeze section (9), the elimination bypass passage (85) is directly connected to the supercooling elimination section (
8). Specifically, as shown in FIG. 23, the elimination bypass path (85) branched from the liquid pipe section (35) on the outlet side of the outdoor heat exchanger (12) as a condenser is connected to the pressure reducing section ( C4), the supercooling elimination section (8)
The outlet end of the supercooling elimination section (8) is connected to the compressor (11
), (21) are connected to the low pressure part (25) on the suction side. That is, the refrigerant liquid whose temperature has been lowered by the pressure reduction section (C4) is flowed into the supercooling elimination section (8) to cool the water or aqueous solution. Therefore, there is no need to provide a separate cooling device.
【0027】請求項5の発明に係わる実施例は、上記請
求項3の発明に係わる実施例において、過冷却解消部(
8)の冷却及び凍結防止部(9)の加熱の熱源として、
冷却装置(2)の冷媒回路(1)から分岐した液冷媒を
用いるのであり、図2及び図24に要部を示したように
、凝縮器としての室外熱交換器(12)の出口側の液管
部(35)から分岐した解消バイパス路(85)を凍結
防止部(9)の冷媒入口端(96)に接続し、さらに凍
結防止部(9)の冷媒出口端(97)を減圧部(C4)
を介して、過冷却解消部(8)の冷媒入口端(86)に
接続し、そして過冷却解消部(8)の冷媒出口端(87
)は圧縮機(11),(21)の吸入側の低圧部(25
)に接続するのである。すなわち、凝縮後の液冷媒を、
凍結防止部(9)による過冷却解消部(8)に近接する
管壁の加熱に用い、さらにこの液冷媒を減圧部(C4)
により温度を下げて、過冷却解消部(8)に流して、水
又は水溶液を冷却する。よって、別途加熱冷却装置を設
ける必要がないのである。なお、図25と図26は請求
項5の発明に係わる実施例の各変形例の要部を示す。図
25の実施例は減圧部(C4)としてキャピラリーチュ
ブを用い、冷熱損失を少なくするために、過冷却解消部
(8)の冷媒入口端(86)としてのキャピラリーチュ
ーブ(C4)の出口端を冷却伝熱面(81)の近傍に設
けるものである。図26の実施例は減圧部(C4)とし
て、過冷却解消部(8)と凍結防止部(9)の間の壁面
に設けたオリフィスを用いたものである。この実施例で
は凍結防止部(9)の冷媒出口端(97)、減圧部(C
4)と過冷却解消部(8)の冷媒入口端(86)が近接
し、事実上一体となっているので、構造が簡単になる。
なお、これらの発明に係わる実施例において、水又は水
溶液全部を再冷却することなく、水又は水溶液全部の過
冷却状態を解消できるのは、窪み部(83)又は障壁部
(82)の内側において氷化物ができ、この氷化物が核
となるからである。The embodiment according to the invention of claim 5 is the embodiment according to the invention of claim 3, in which the supercooling eliminating section (
8) as a heat source for cooling and heating the antifreeze section (9);
A liquid refrigerant branched from the refrigerant circuit (1) of the cooling device (2) is used, and as shown in FIGS. 2 and 24, the liquid refrigerant is The decompression bypass path (85) branched from the liquid pipe section (35) is connected to the refrigerant inlet end (96) of the antifreeze section (9), and the refrigerant outlet end (97) of the antifreeze section (9) is connected to the decompression section. (C4)
is connected to the refrigerant inlet end (86) of the supercooling elimination section (8) through the refrigerant outlet end (87) of the supercooling elimination section (8).
) is the low pressure part (25) on the suction side of the compressor (11), (21).
). In other words, the liquid refrigerant after condensation is
This liquid refrigerant is used to heat the pipe wall adjacent to the supercooling elimination section (8) by the anti-freeze section (9), and the liquid refrigerant is then transferred to the decompression section (C4).
The water or aqueous solution is cooled by lowering its temperature and passing it through the supercooling elimination section (8). Therefore, there is no need to provide a separate heating and cooling device. Note that FIGS. 25 and 26 show essential parts of each modification of the embodiment according to the fifth aspect of the invention. In the embodiment shown in FIG. 25, a capillary tube is used as the pressure reducing section (C4), and in order to reduce cooling loss, the outlet end of the capillary tube (C4) is used as the refrigerant inlet end (86) of the supercooling elimination section (8). It is provided near the cooling heat transfer surface (81). The embodiment shown in FIG. 26 uses an orifice provided on the wall between the supercooling eliminating section (8) and the antifreezing section (9) as the pressure reducing section (C4). In this embodiment, the refrigerant outlet end (97) of the antifreeze section (9), the pressure reducing section (C
4) and the refrigerant inlet end (86) of the supercooling elimination section (8) are close to each other and are virtually integrated, which simplifies the structure. In addition, in the embodiments related to these inventions, the supercooled state of the entire water or aqueous solution can be eliminated without recooling the entire water or aqueous solution when the inside of the recessed portion (83) or the barrier portion (82) This is because frozen matter is formed and this frozen matter becomes the nucleus.
【0028】[0028]
【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、過冷却状態を解消する過冷却解消部(8)の冷
却伝熱面(81)として、復管路(51B)における管
内表面に対して外方に膨出する窪み部(83)を形成し
て、この窪み部(83)内面を用いたことにより、水又
は水溶液の流速が窪み部(83)で遅くなり、十分に温
度が下がってから流れ去るので、冷却能力の向上が図れ
る。さらに、水又は水溶液の流速はこの窪み部(83)
でのみ遅くなり、全体としては速く保つことができるの
で、過冷却解消部(8)で生じた氷化物の流れが悪くな
り、復管路(51B)内で閉塞するようなことはない。
また、この窪み部(83)で効率よく過冷却が解消でき
るので、過冷却解消部(8)の冷却伝熱面(81)を小
さくできる、あるいは特に低温の冷熱源を用意しなくて
もよい。As explained above, according to the invention of claim 1, the cooling heat transfer surface (81) of the supercooling eliminating section (8) that eliminates the supercooling state is used as the cooling heat transfer surface (81) in the return pipe (51B). By forming a recess (83) that bulges outward with respect to the inner surface of the tube and using the inner surface of the recess (83), the flow rate of water or aqueous solution is slowed down in the recess (83) and Since it flows away after the temperature has fallen, the cooling capacity can be improved. Furthermore, the flow rate of water or aqueous solution is controlled by this depression (83).
Since it is possible to maintain a high speed as a whole, the flow of frozen substances generated in the supercooling elimination section (8) will not deteriorate and the return pipe (51B) will not be clogged. In addition, since supercooling can be efficiently eliminated in this depression (83), the cooling heat transfer surface (81) of the supercooling elimination section (8) can be made smaller, or there is no need to prepare a particularly low-temperature cold source. .
【0029】請求項2の発明によれば、過冷却解消部(
8)の冷却伝熱面(81)の周りに障壁部(82)を設
けることにより、水又は水溶液の流れが妨げられ、冷却
伝熱面(81)に接する所で遅くなり、十分に温度が下
がってから流れ去るので、冷却能力の向上が図れる。
さらに、水又は水溶液の流速はこの冷却伝熱面(81)
に接する所でのみ遅くなり、全体としては速く保つこと
ができるので、過冷却解消部(8)で生じた氷化物の流
れが悪くなり、復管路(51B)内で閉塞するようなこ
とはない。また、この障壁部(82)を有する過冷却解
消部(8)で効率よく過冷却を解消できるので、過冷却
解消部(8)の冷却伝熱面(81)を小さくできる、あ
るいは特に低温の冷熱源を用意しなくてもよい。According to the invention of claim 2, the supercooling eliminating section (
By providing a barrier part (82) around the cooling heat transfer surface (81) in 8), the flow of water or aqueous solution is obstructed and slows down at the point in contact with the cooling heat transfer surface (81), so that the temperature is sufficiently low. Since it flows away after falling, the cooling capacity can be improved. Furthermore, the flow rate of water or aqueous solution is determined by the cooling heat transfer surface (81).
It slows down only at the point where it comes into contact with , and can be kept fast as a whole, so there is no possibility that the flow of ice generated in the supercooling elimination section (8) will deteriorate and blockage in the return pipe (51B). do not have. In addition, since supercooling can be efficiently eliminated in the supercooling eliminating section (8) having this barrier section (82), the cooling heat transfer surface (81) of the supercooling eliminating section (8) can be made small, or especially at low temperatures. There is no need to prepare a cold source.
【0030】請求項3の発明によると、上記請求項1又
は請求項2の発明に加えて、過冷却解消部(8)に近接
して設けられ、過冷却解消部(8)で生じた氷化物の管
壁への付着を解離させるよう復管路(51B)を加熱す
る凍結防止部(9)を備えたことにより、過冷却解消部
(8)及びこの付近の管壁の凍結を防止し、過冷却解消
部(8)の製氷効率を向上させる。特に請求項1又は請
求項2の発明の過冷却解消部(8)の冷却伝熱面(81
)は小さくできるので、この凍結防止部(9)の加熱伝
熱面(91)も小さくできる。According to the invention of claim 3, in addition to the invention of claim 1 or claim 2, the ice generated in the supercooling elimination section (8) is disposed close to the supercooling elimination section (8). By providing the antifreeze section (9) that heats the return pipe line (51B) to dissociate the adhesion of chemical substances to the pipe wall, freezing of the supercooling release section (8) and the pipe wall in the vicinity thereof is prevented. , improves the ice making efficiency of the supercooling elimination section (8). In particular, the cooling heat transfer surface (81
) can be made small, so the heating heat transfer surface (91) of this antifreeze section (9) can also be made small.
【0031】請求項4の発明によると、上記請求項1又
は請求項2の発明に加えて、主熱交換器(22)が冷却
装置(2)の冷媒回路(1)に接続されていて、過冷却
解消部(8)には、上記冷媒回路(1)の液冷媒を減圧
部(C4)で減圧し低温として流通するので、別途冷却
装置を設ける必要がなく、よって装置の小型化及びコス
トの低減を図ることができる。According to the invention of claim 4, in addition to the invention of claim 1 or claim 2, the main heat exchanger (22) is connected to the refrigerant circuit (1) of the cooling device (2), Since the liquid refrigerant in the refrigerant circuit (1) is depressurized in the depressurization part (C4) and distributed as a low temperature in the supercooling elimination part (8), there is no need to provide a separate cooling device, which reduces the size and cost of the device. It is possible to reduce the
【0032】請求項5の発明によると、上記請求項3の
発明に加えて、主熱交換器(22)が冷却装置(2)の
冷媒回路(1)に接続されていて、凍結防止部(9)に
は、上記冷媒回路(1)の液冷媒を流通する一方、過冷
却解消部(8)には、凍結防止部(9)で冷媒との熱交
換により冷却され、さらに減圧部(C4)で減圧され低
温となった冷媒が流通するので、別途加熱冷却装置を設
ける必要がなく、よって装置の小型化及びコストの低減
を図ることができる。According to the invention of claim 5, in addition to the invention of claim 3, the main heat exchanger (22) is connected to the refrigerant circuit (1) of the cooling device (2), and the antifreeze section ( 9), the liquid refrigerant of the refrigerant circuit (1) flows through it, while the supercooling eliminating section (8) is cooled by heat exchange with the refrigerant in the anti-freezing section (9), and further passes through the decompression section (C4). ), the refrigerant whose pressure has been reduced to a low temperature flows through the refrigerant, so there is no need to provide a separate heating/cooling device, and it is therefore possible to downsize the device and reduce costs.
【図1】本発明の製氷装置の基本構成を示すブロック図
である。FIG. 1 is a block diagram showing the basic configuration of an ice making apparatus of the present invention.
【図2】本発明の実施例を示す冷媒配管系統図である。FIG. 2 is a refrigerant piping system diagram showing an embodiment of the present invention.
【図3】請求項1の発明の実施例を示す要部縦断面図で
ある。FIG. 3 is a vertical sectional view of a main part showing an embodiment of the invention of claim 1.
【図4】請求項1の発明の実施例を示す要部横断面図で
ある。FIG. 4 is a cross-sectional view of a main part showing an embodiment of the invention according to claim 1.
【図5】請求項1の発明の実施例を示す要部縦断面図で
ある。FIG. 5 is a vertical sectional view of a main part showing an embodiment of the invention of claim 1.
【図6】請求項1の発明の実施例を示す要部横断面図で
ある。FIG. 6 is a cross-sectional view of a main part showing an embodiment of the invention of claim 1.
【図7】請求項1の発明の実施例を示す要部縦断面図で
ある。FIG. 7 is a longitudinal sectional view of a main part showing an embodiment of the invention of claim 1.
【図8】請求項1の発明の実施例を示す要部横断面図で
ある。FIG. 8 is a cross-sectional view of a main part showing an embodiment of the invention of claim 1.
【図9】請求項1の発明の実施例を示す要部縦断面図で
ある。FIG. 9 is a longitudinal sectional view of a main part showing an embodiment of the invention of claim 1.
【図10】請求項1の発明の実施例を示す要部横断面図
である。FIG. 10 is a cross-sectional view of a main part showing an embodiment of the invention of claim 1.
【図11】請求項1の発明の実施例を示す要部縦断面図
である。FIG. 11 is a longitudinal sectional view of a main part showing an embodiment of the invention of claim 1.
【図12】請求項1の発明の実施例を示す要部横断面図
である。FIG. 12 is a cross-sectional view of a main part showing an embodiment of the invention according to claim 1.
【図13】請求項2の発明の実施例を示す要部縦断面図
である。FIG. 13 is a vertical sectional view of a main part showing an embodiment of the invention of claim 2.
【図14】請求項2の発明の実施例を示す要部横断面図
である。FIG. 14 is a cross-sectional view of a main part showing an embodiment of the invention according to claim 2.
【図15】請求項2の発明の実施例を示す要部縦断面図
である。FIG. 15 is a vertical sectional view of a main part showing an embodiment of the invention of claim 2.
【図16】請求項2の発明の実施例を示す要部横断面図
である。FIG. 16 is a cross-sectional view of a main part showing an embodiment of the invention according to claim 2.
【図17】請求項2の発明の実施例を示す要部縦断面図
である。FIG. 17 is a vertical sectional view of a main part showing an embodiment of the invention of claim 2.
【図18】請求項2の発明の実施例を示す要部横断面図
である。FIG. 18 is a cross-sectional view of a main part showing an embodiment of the invention according to claim 2.
【図19】請求項3の発明の実施例を示す要部縦断面図
である。FIG. 19 is a vertical sectional view of a main part showing an embodiment of the invention according to claim 3.
【図20】請求項3の発明の実施例を示す要部横断面図
である。FIG. 20 is a cross-sectional view of a main part showing an embodiment of the invention according to claim 3.
【図21】請求項3の発明の実施例を示す要部縦断面図
である。FIG. 21 is a longitudinal sectional view of a main part showing an embodiment of the invention according to claim 3.
【図22】請求項3の発明の実施例を示す要部横断面図
である。FIG. 22 is a cross-sectional view of a main part showing an embodiment of the invention according to claim 3.
【図23】請求項4の発明の実施例を示す要部縦断面図
である。FIG. 23 is a vertical sectional view of a main part showing an embodiment of the invention according to claim 4.
【図24】請求項5の発明の実施例を示す要部縦断面図
である。FIG. 24 is a vertical sectional view of a main part showing an embodiment of the invention of claim 5.
【図25】請求項5の発明の実施例を示す要部縦断面図
である。FIG. 25 is a longitudinal sectional view of a main part showing an embodiment of the invention of claim 5.
【図26】請求項5の発明の実施例を示す要部縦断面図
である。FIG. 26 is a vertical sectional view of a main part showing an embodiment of the invention of claim 5.
1 冷媒回路
2 冷却装置
5 蓄氷槽
8 過冷却解消部
9 凍結防止部
22 主熱交換器
25 低圧部
35 液管部
51B 復管路
81 過冷却解消部の冷却伝熱面82
過冷却解消部の障壁部83 過冷却解
消部の窪み部85 解消バイパス路
86 過冷却解消部の冷媒入口端87
過冷却解消部の冷媒出口端96 凍結
防止部の冷媒入口端97 凍結防止部の冷媒
出口端C4 減圧部1 Refrigerant circuit 2 Cooling device 5 Ice storage tank 8 Supercooling elimination section 9 Freezing prevention section 22 Main heat exchanger 25 Low pressure section 35 Liquid pipe section 51B Return pipe line 81 Cooling heat transfer surface 82 of supercooling elimination section
Barrier section 83 of supercooling elimination section Recessed section 85 of supercooling elimination section Elimination bypass path 86 Refrigerant inlet end 87 of supercooling elimination section
Refrigerant outlet end 96 of supercooling elimination section Refrigerant inlet end 97 of antifreeze section Refrigerant outlet end C4 of antifreeze section Pressure reduction section
Claims (5)
貯溜するための蓄氷槽(5)と、冷却装置(2)に接続
され、水又は水溶液を過冷却するための主熱交換器(2
2)と、上記主熱交換器(22)と蓄氷槽(5)とを接
続する復管路(51B)内の流路中に介設され、水又は
水溶液の過冷却状態を解消させてスラリー状の氷化物に
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、上記復管路(51B)における管内表面に対し外
方に膨出する窪み部(83)を形成して、この窪み部(
83)内面を、上記過冷却解消部(8)の冷却伝熱面(
81)としたことを特徴とする製氷装置。Claim 1: An ice storage tank (5) for storing frozen slurry of water or an aqueous solution, and a main heat exchanger (2) connected to a cooling device (2) for supercooling the water or an aqueous solution. 2
2) and a flow path in the return pipe (51B) connecting the main heat exchanger (22) and the ice storage tank (5) to eliminate the supercooled state of water or aqueous solution. In an ice making apparatus equipped with a supercooling eliminating section (8) for producing frozen material in the form of slurry, a recess (83) is formed that bulges outward with respect to the inner surface of the pipe in the return pipe (51B). This hollow part (
83) The inner surface is the cooling heat transfer surface (
81).
貯溜するための蓄氷槽(5)と、冷却装置(2)に接続
され、水又は水溶液を過冷却するための主熱交換器(2
2)と、上記主熱交換器(22)と蓄氷槽(5)とを接
続する復管路(51B)内の流路中に介設され、水又は
水溶液の過冷却状態を解消させてスラリー状の氷化物に
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、上記過冷却解消部(8)の冷却伝熱面(81)の
周りに設けられ、水又は水溶液の流速を冷却伝熱面(8
1)で局所的に遅くするための障壁部(82)を備えた
ことを特徴とする製氷装置。Claim 2: An ice storage tank (5) for storing frozen slurry of water or an aqueous solution, and a main heat exchanger (2) connected to the cooling device (2) for supercooling the water or the aqueous solution. 2
2) and a flow path in the return pipe (51B) connecting the main heat exchanger (22) and the ice storage tank (5) to eliminate the supercooled state of water or aqueous solution. In an ice-making apparatus equipped with a supercooling eliminating section (8) for producing a slurry-like frozen product, the ice making device is provided around the cooling heat transfer surface (81) of the supercooling eliminating section (8), Heat transfer surface (8
1) An ice-making device characterized by comprising a barrier section (82) for locally slowing down the speed.
れ、過冷却解消部(8)で生じた氷化物の管壁への付着
を解離させるよう復管路(51B)を加熱する凍結防止
部(9)を備えたことを特徴とする請求項1又は請求項
2記載の製氷装置。3. A return pipe (51B) is provided close to the supercooling eliminating section (8) and heats the return pipe line (51B) so as to dissociate iced matter generated in the supercooling eliminating section (8) from adhering to the tube wall. The ice-making device according to claim 1 or 2, further comprising a freeze prevention section (9).
(21)、凝縮器(12)、減圧機構(23)及び蒸発
器として作用する主熱交換器(22)を順次接続してな
る冷媒回路(1)を備え、過冷却解消部(8)は上記冷
媒回路(1)の冷媒との熱交換により過冷却状態の水又
は水溶液を冷却するものであり、冷媒回路(1)の液管
部(35)と過冷却解消部(8)の冷媒入口端(86)
との間は減圧部(C4)を介して接続され、過冷却解消
部(8)の冷媒出口端(87)は冷媒回路(1)の低圧
部(25)に接続されていることを特徴とする請求項1
又は請求項2記載の製氷装置。Claim 4: The cooling device (2) includes a compressor (11),
(21), a condenser (12), a pressure reducing mechanism (23), and a main heat exchanger (22) functioning as an evaporator are sequentially connected to each other. It cools supercooled water or aqueous solution by heat exchange with the refrigerant of the refrigerant circuit (1), and the refrigerant inlet of the liquid pipe section (35) and supercooling elimination section (8) of the refrigerant circuit (1). Edge (86)
The refrigerant outlet end (87) of the supercooling elimination section (8) is connected to the low pressure section (25) of the refrigerant circuit (1). Claim 1
Or the ice making device according to claim 2.
(21)、凝縮器(12)、減圧機構(23)及び蒸発
器として作用する主熱交換器(22)を順次接続してな
る冷媒回路(1)を備え、過冷却解消部(8)は上記冷
媒回路(1)の冷媒との熱交換により過冷却状態の水又
は水溶液を冷却するものであり、凍結防止部(9)は上
記冷媒回路(1)の冷媒との熱交換により過冷却解消部
(8)に近接する管壁を加熱するものであり、凍結防止
部(9)の冷媒入口端(96)は冷媒回路(1)の液管
部(35)に接続され、過冷却解消部(8)の冷媒出口
端(87)は冷媒回路の低圧部(25)に接続され、凍
結防止部(9)の冷媒出口端(97)と過冷却解消部(
8)の冷媒入口端(86)との間は減圧部(C4)を介
して接続されていることを特徴とする請求項3記載の製
氷装置。Claim 5: The cooling device (2) includes a compressor (11),
(21), a condenser (12), a pressure reducing mechanism (23), and a main heat exchanger (22) functioning as an evaporator are sequentially connected to each other. It cools supercooled water or aqueous solution by heat exchange with the refrigerant in the refrigerant circuit (1), and the antifreeze section (9) eliminates supercooling by heat exchange with the refrigerant in the refrigerant circuit (1). The refrigerant inlet end (96) of the antifreeze section (9) is connected to the liquid pipe section (35) of the refrigerant circuit (1), and the subcooling elimination section The refrigerant outlet end (87) of (8) is connected to the low pressure part (25) of the refrigerant circuit, and the refrigerant outlet end (97) of the antifreeze part (9) and the supercooling elimination part (
4. The ice making apparatus according to claim 3, wherein the ice making apparatus is connected to the refrigerant inlet end (86) of the ice making apparatus (8) via a pressure reducing part (C4).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP03021584A JP3102042B2 (en) | 1991-01-22 | 1991-01-22 | Ice making equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP03021584A JP3102042B2 (en) | 1991-01-22 | 1991-01-22 | Ice making equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH04240367A true JPH04240367A (en) | 1992-08-27 |
| JP3102042B2 JP3102042B2 (en) | 2000-10-23 |
Family
ID=12059088
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP03021584A Expired - Fee Related JP3102042B2 (en) | 1991-01-22 | 1991-01-22 | Ice making equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3102042B2 (en) |
-
1991
- 1991-01-22 JP JP03021584A patent/JP3102042B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JP3102042B2 (en) | 2000-10-23 |
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