JP2002257441A - System for taking out ice slurry, low temperature ice, and artificial snow in steam compression freezer utilizing anti-freezing solution - Google Patents

System for taking out ice slurry, low temperature ice, and artificial snow in steam compression freezer utilizing anti-freezing solution

Info

Publication number
JP2002257441A
JP2002257441A JP2001056398A JP2001056398A JP2002257441A JP 2002257441 A JP2002257441 A JP 2002257441A JP 2001056398 A JP2001056398 A JP 2001056398A JP 2001056398 A JP2001056398 A JP 2001056398A JP 2002257441 A JP2002257441 A JP 2002257441A
Authority
JP
Japan
Prior art keywords
ice
low
temperature
antifreeze
steam compression
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
JP2001056398A
Other languages
Japanese (ja)
Other versions
JP4545332B2 (en
Inventor
Masaru Hongo
賢 本郷
Ryosuke Yuki
了介 結城
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.)
Sanken Setsubi Kogyo Co Ltd
Original Assignee
Sanken Setsubi Kogyo Co 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 Sanken Setsubi Kogyo Co Ltd filed Critical Sanken Setsubi Kogyo Co Ltd
Priority to JP2001056398A priority Critical patent/JP4545332B2/en
Publication of JP2002257441A publication Critical patent/JP2002257441A/en
Application granted granted Critical
Publication of JP4545332B2 publication Critical patent/JP4545332B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Other Air-Conditioning Systems (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a system for generating and taking out low temperature ice slurry from a vaporizer in a steam compression freezer, low temperature ice from an ice concentrator, and low temperature artificial snow from a snow making machine by adding the anti-freezing solution having predetermined concentration to circulated water as an impurity, in a steam compression freezer utilizing the anti-freezing solution. SOLUTION: A title system for taking out ice slurry, low temperature ice, and artificial snow in a steam compression freezer utilizing an anti-freezing solution is adapted such that a steam compression freezer 6 includes a vaporizer 6a, a compressor 6b, and a condenser 6c, the vaporizer 6a leads circulation water 7 from an ice storage tank 8 and adds an anti-freezing solution 14 such as ethylene glycol having the predetermined concentration to the circulation water 7, and low temperature ice slurry 6d is taken out from the vaporizer 6a and simultaneously an ice concentrator 21 is assembled in the foregoing construction, from which ice concentrator 21 low temperature condensed ice (low temperature ice) is taken out from the ice concentrator 21, and further low temperature artificial ice 25a is generated and taken out with the aid of an ice making machine 25 coupled to the ice concentrator 21.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、水蒸気圧縮冷凍機
に備えている蒸発器から低温の氷スラリーを取出すと共
に当該水蒸気圧縮機に別置された氷濃縮器又は雪製造機
から低温氷や人工雪を取出すことができる技術に関す
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for extracting low-temperature ice slurry from an evaporator provided in a steam compression refrigerator and a method for extracting low-temperature ice or artificial ice from an ice concentrator or a snow making machine separately provided in the steam compressor. Related to technology that can extract snow.

【0002】[0002]

【従来の技術】従来、この種の水蒸気圧縮冷凍機による
製氷技術は、例えば、図5に示すような基本構成であっ
た。これについて説明すれば、水蒸気圧縮冷凍機1で補
給水2aを導く循環水2から水を含んだ氷スラリー5を
製氷し、この氷スラリー5から氷濃縮器3により生成さ
れた濃縮氷4を取り出す構成であった。
2. Description of the Related Art Conventionally, an ice making technique using a steam compression refrigerator of this kind has a basic configuration as shown in FIG. To explain this, an ice slurry 5 containing water is made from the circulating water 2 for guiding the makeup water 2a by the steam compression refrigerator 1, and the concentrated ice 4 generated by the ice concentrator 3 is taken out from the ice slurry 5. Configuration.

【0003】[0003]

【発明が解決しようとする課題】従来の技術は叙上のよ
うな構成であるので次の課題が存在した。 前記水蒸気圧縮冷凍機1の蒸発部から前記氷濃縮器3
に流入する氷スラリー5は、例えば氷が体積比率におい
て、約15%を含有している。ところで、当該氷スラリ
ー5の凝固点つまり、凍結温度は0℃程度であり、前記
蒸発部や前記氷濃縮器3から低温度の氷スラリーや低温
氷を取出すことができなかった。 前記従来の技術に於いては、前記水蒸気圧縮冷凍機1
や氷濃縮器3に雪製造機を備えたものがあるが、当該雪
製造機によって低温の人工雪を生成かつ取出すことがで
きなかった。また、雪の温度を降下させるために塩化カ
ルシウムなどの寒剤を散布する方法もあるが、環境の点
から望ましくなかった。
Since the prior art has the above-described configuration, the following problems exist. From the evaporator of the steam compression refrigerator 1 to the ice concentrator 3
Contains about 15% by volume of ice, for example. By the way, the freezing point of the ice slurry 5, that is, the freezing temperature is about 0 ° C., so that the low temperature ice slurry or the low temperature ice could not be taken out from the evaporator or the ice concentrator 3. In the prior art, the steam compression refrigerator 1
Some of the ice concentrators 3 include a snow making machine, but the snow making machine could not generate and extract low-temperature artificial snow. There is also a method of spraying a cryogen such as calcium chloride in order to lower the temperature of snow, but this is not desirable from an environmental point of view.

【0004】[0004]

【課題を解決するための手段】本発明は、前記氷蓄熱槽
から蒸発器に流過する循環水に所定濃度を有するエチレ
ングリコール等の不凍液を添加し、該循環水の凝固点を
降下させて前記蒸発器や前記氷濃縮器で製造された氷ス
ラリー又は氷の温度低下を図り、これらを取出すと共に
雪製造機でもって、低温の人工雪を取出すシステムであ
って、叙上した課題を解決することを目的とするもので
あり、次の構成、手段から成立するものである。
According to the present invention, an antifreeze such as ethylene glycol having a predetermined concentration is added to circulating water flowing from the ice heat storage tank to the evaporator, and the freezing point of the circulating water is lowered to reduce the freezing point. A system for reducing the temperature of an ice slurry or ice produced by an evaporator or the above-mentioned ice concentrator, and taking out the same and using a snow making machine to remove low-temperature artificial snow. It is intended to be realized by the following configuration and means.

【0005】請求項1記載の発明によれば、氷蓄熱槽か
ら循環水を導く蒸発器、圧縮機、熱交換器を介して冷却
水閉回路を形成した凝縮器及び該凝縮器で生成した凝縮
水を循環水に戻す回路で構成された水蒸気圧縮冷凍機に
於いて、前記循環水に所定濃度を有する不凍液を添加
し、前記蒸発器から低温の氷スラリーを取出すことを特
徴とする不凍液を利用した水蒸気圧縮冷凍機の氷スラリ
ー取り出しシステムである。
According to the first aspect of the present invention, a condenser having a cooling water closed circuit formed through an evaporator, a compressor, and a heat exchanger for guiding circulating water from an ice heat storage tank, and a condenser formed by the condenser. In a steam compression refrigerator comprising a circuit for returning water to circulating water, an antifreeze having a predetermined concentration is added to the circulating water, and a low-temperature ice slurry is taken out from the evaporator. 1 is an ice slurry removal system for a steam compression refrigerator.

【0006】請求項2記載の発明によれば、氷蓄熱槽
と、該氷蓄熱槽に氷を導く氷濃縮器と、該氷濃縮器から
循環水を導く蒸発器、圧縮機、熱交換器を介して冷却水
閉回路を形成した凝縮器及び該凝縮器で生成した凝縮水
を循環水に戻す回路で構成された水蒸気圧縮冷凍機に於
いて、前記循環水に所定濃度を有する不凍液を添加し、前
記蒸発部から低温の氷スラリーを取出すと共に、前記氷
濃縮器において低温氷を生成することを特徴とする不凍
液を利用した水蒸気圧縮冷凍機の氷スラリー及び低温氷
取出しシステムである。
According to the second aspect of the present invention, an ice heat storage tank, an ice concentrator for guiding ice to the ice heat storage tank, an evaporator, a compressor, and a heat exchanger for guiding circulating water from the ice concentrator are provided. An antifreeze having a predetermined concentration is added to the circulating water in a steam compression refrigerator including a condenser having a cooling water closed circuit formed therein and a circuit for returning the condensed water generated by the condenser to the circulating water. An ice slurry and a low-temperature ice removal system for a steam compression refrigerator using an antifreeze liquid, wherein a low-temperature ice slurry is removed from the evaporator and low-temperature ice is generated in the ice concentrator.

【0007】請求項3記載の発明によれば、氷濃縮器
と、該氷濃縮器から低温氷を導く雪製造機と、該氷濃縮
器から循環水を導く蒸発器、圧縮機、熱交換器を介して
冷却水閉回路を形成した凝縮器及び該凝縮器で生成した
凝縮水を循環水に戻す回路で構成された水蒸気圧縮冷凍
機に於いて、前記循環水に所定濃度を有する不凍液を添
加し、前記蒸発器から低温の氷スラリーを取出しかつ前
記氷濃縮器において低温氷を生成すると共に、前記雪製
造機で人工雪を生成することを特徴とする不凍液を利用
した水蒸気圧縮冷凍機の氷スラリー及び低温氷並びに人
工雪取出しシステムである。
According to the third aspect of the present invention, an ice concentrator, a snow making machine that guides low-temperature ice from the ice concentrator, an evaporator, a compressor, and a heat exchanger that guides circulating water from the ice concentrator An antifreeze having a predetermined concentration is added to the circulating water in the condenser having a cooling water closed circuit formed therein and a circuit for returning the condensed water generated in the condenser to the circulating water. Removing a low-temperature ice slurry from the evaporator, generating low-temperature ice in the ice concentrator, and generating artificial snow in the snow making machine. Slurry and low-temperature ice and artificial snow removal system.

【0008】請求項4記載の発明によれば、前記雪製造
機がロータリーフィーダー等でなることを特徴とする請
求項3記載の不凍液を利用した水蒸気圧縮冷凍機の氷ス
ラリー及び低温氷並びに人工雪取出しシステムである。
According to a fourth aspect of the present invention, the snow making machine comprises a rotary feeder or the like. It is an extraction system.

【0009】請求項5記載の発明によれば、前記所定濃
度を有する不凍液が塩化ナトリウム溶液又はグリコール
類溶液であって、プロピレングリコール、エチレングリ
コール、二価アルコール又はプロパンジオールでなるこ
とを特徴とする請求項1、2又は3記載の不凍液を利用
した水蒸気圧縮冷凍機の氷スラリー及び低温氷並びに人
工雪取出しシステムである。
According to a fifth aspect of the present invention, the antifreeze having the predetermined concentration is a sodium chloride solution or a glycol solution, and is made of propylene glycol, ethylene glycol, dihydric alcohol or propanediol. An ice slurry, a low-temperature ice, and an artificial snow removal system for a steam compression refrigerator using the antifreeze according to claim 1, 2, or 3.

【0010】請求項6記載の発明によれば、前記蒸発器
が攪拌機を備えたことを特徴とする請求項1、2又は3
記載の不凍液を利用した水蒸気圧縮冷凍機の氷スラリー
及び低温氷並びに人工雪取出しシステムである。
According to a sixth aspect of the present invention, the evaporator is provided with a stirrer.
An ice slurry, a low-temperature ice, and an artificial snow removal system for a steam compression refrigerator using the antifreeze described above.

【0011】請求項7記載の発明によれば、前記熱交換
器が冷却水用熱交換器又は密閉冷却塔でなることを特徴
とする請求項1、2又は3記載の不凍液を利用した水蒸
気圧縮冷凍機の氷スラリー及び低温氷並びに人工雪取出
しシステムである。
According to a seventh aspect of the present invention, the heat exchanger is a heat exchanger for cooling water or a closed cooling tower, and the steam compression using an antifreeze solution according to the first, second or third aspect of the present invention. The ice slurry and the low-temperature ice of the refrigerator and the artificial snow removal system.

【0012】[0012]

【発明の実施の形態】以下、添付図面に基づき、本発明
に係る不凍液を利用した水蒸気圧縮冷凍機の氷スラリー
及び低温氷並びに人工雪取出しシステムの各実施の形態
について、詳細に説明する。
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is an exploded perspective view showing an ice slurry and a low-temperature ice for a steam compression refrigerator using an antifreeze according to the present invention;

【0013】[0013]

【発明の実施の形態1】図1は本発明に係る実施の形態
1を示すのもであって、不凍液を利用した水蒸気圧縮冷
凍機の氷スラリー取出しシステムの構成配置図である。
Embodiment 1 FIG. 1 shows Embodiment 1 according to the present invention, and is an arrangement diagram of an ice slurry extraction system of a steam compression refrigerator using an antifreeze.

【0014】6は水蒸気圧縮冷凍機であって、蒸発器6
a、圧縮機6b及び凝縮器6cを備えている。該蒸発器
6aは氷蓄熱槽8から循環水7を導くと共に前記圧縮機
6bの運転によって、低圧に保持しつつ当該循環水7の
一部を蒸発させる。該圧縮機6bは当該蒸発器6aから
導入された水蒸気を所定の条件で加圧する。前記凝縮器
6cは、前記圧縮機6bで加圧されかつ高温になった水
蒸気を導入し、これを外部に設置した冷却水用熱交換器
15等から導いた冷却水10で冷却し、凝縮する。
Reference numeral 6 denotes a steam compression refrigerator, which is an evaporator 6
a, a compressor 6b and a condenser 6c. The evaporator 6a guides the circulating water 7 from the ice heat storage tank 8 and evaporates a part of the circulating water 7 by operating the compressor 6b while maintaining a low pressure. The compressor 6b pressurizes the steam introduced from the evaporator 6a under predetermined conditions. The condenser 6c introduces steam which has been pressurized and has a high temperature in the compressor 6b, and cools and condenses the steam with cooling water 10 introduced from a cooling water heat exchanger 15 or the like installed outside. .

【0015】ここに於いて、前記氷蓄熱槽8、前記水蒸
気圧縮冷凍機6の蒸発器6a、氷スラリーポンプ11、
解氷水ポンプ12及び冷熱用熱交換器13、及びこれら
を結ぶ連絡管には補給水19として水道水が満されてい
る。前記循環水7へは、所定濃度を有する不凍液14を
添加する。当該不凍液14は塩化ナトリウム又はグリコ
ール類溶液であって、エチレングリコール等でなる。前
記不凍液14としては、エチレングリコールの他にプロ
ピレングリコール、二価アルコール、プロパンジオール
等を適用してもよい。
Here, the ice heat storage tank 8, the evaporator 6a of the steam compression refrigerator 6, an ice slurry pump 11,
The de-icing water pump 12 and the heat exchanger 13 for cooling and cooling, and the connecting pipe connecting them are filled with tap water as makeup water 19. An antifreeze 14 having a predetermined concentration is added to the circulating water 7. The antifreeze 14 is a solution of sodium chloride or glycols, and is made of ethylene glycol or the like. As the antifreeze 14, propylene glycol, dihydric alcohol, propanediol, or the like may be applied in addition to ethylene glycol.

【0016】8は氷蓄熱槽であり、前記蒸発器6aから
氷スラリーポンプ11を介して取出された低温氷スラリ
ー6dを貯留する。該氷蓄熱槽8では冷熱用熱交換器1
3から氷融解水8aを導き、低温の氷スラリーの氷融解
作用が行なわれ、氷と融解水すなわち冷水が混在するこ
とになる。当該冷水は解氷水ポンプ12で冷熱用熱交換
器13に圧送される。該冷熱用熱交換器13はいわゆる
熱取出しサイクルとして冷房負荷(開示せず)等に冷水
ポンプ18で冷水を循環流送する。
Reference numeral 8 denotes an ice heat storage tank for storing the low-temperature ice slurry 6d taken out from the evaporator 6a via the ice slurry pump 11. The ice heat storage tank 8 includes a heat exchanger 1 for cooling and heating.
The ice melting water 8a is derived from 3 and the ice melting action of the low-temperature ice slurry is performed, so that ice and melting water, that is, cold water are mixed. The cold water is pumped to the heat exchanger 13 for cooling by the deicing water pump 12. The cooling heat exchanger 13 circulates cold water by a cold water pump 18 to a cooling load (not disclosed) or the like as a so-called heat extraction cycle.

【0017】次に、本発明に係る実施の形態1の不凍液
を利用した水蒸気圧縮冷凍機の氷スラリー取出しシステ
ムの動作について説明する。図2に示すように一般的に
水溶液中の不凍液、例えば、エチレングリコールの場合、
濃度(g/L)を高めれば当該水溶液の凍結温度、つまり
凝固点(℃)が降下することが判明している。先ず、前
記蒸発器6aから低温の氷スラリー6dを取出す前に於
いて、前記循環水7にエチレングリコール等の不凍液1
4を添加し、当該不凍液の濃度を約50(g/L)に保
有する。ここに於いて、前記水蒸気圧縮冷凍機6の蒸発
器6aに於ける製氷温度は上記エチレングリコールが水
溶液や前記循環水7中に溶解しているので、約−1.0
(℃)となり、前記蒸発器6a内の攪拌機6eの攪拌作
用によって、氷同士の結氷を防止し結氷のない氷スラリ
ー6dとして前記蒸発器6aから取出すことができる。
一方、前記蒸発器6aで蒸発した水蒸気は冷却水10の
冷却作用によって凝縮器6cで凝縮し、その量に相当す
る水が補給水すなわち凝縮水9として循環水7に戻され
る。そこで、戻される凝縮氷9の水質はほぼ蒸溜水に近
く、そして、不純物である前記エチレングリコール等の
不凍液14は前記循環水7に滞留したままであることか
ら前記循環水7の水量や不凍液の濃度(g/L)には変
化がない。そして、以上説明したように、本実施の形態
1のシステムによれば、前記循環水7に於ける不凍液の
濃度を50(g/L)とすることにより、蒸発器6aか
ら−1.0(℃)の低温度の氷スラリー6dを取出しで
きる。尚、図1に於いて、15は冷却水用熱交換器又は
密閉冷却塔であって、前記凝縮機6cで得られた冷却水
(凝縮水)10を密閉回路として冷却水ポンプ16で循環
させる。また、17は下水、海水、河川水、工業用水又
は上水等であり、前記冷却水用熱交換器又は密閉冷却塔
15に供給している。
Next, the operation of the ice slurry extracting system of the steam compression refrigerator using the antifreeze according to the first embodiment of the present invention will be described. As shown in FIG. 2, generally, in the case of an antifreeze in an aqueous solution, for example, ethylene glycol,
It has been found that increasing the concentration (g / L) lowers the freezing temperature of the aqueous solution, that is, the freezing point (° C.). First, before taking out the low-temperature ice slurry 6d from the evaporator 6a, the circulating water 7 contains an antifreeze solution 1 such as ethylene glycol.
4 to maintain the concentration of the antifreeze at about 50 (g / L). Here, the ice making temperature in the evaporator 6a of the steam compression refrigerator 6 is about -1.0 because the ethylene glycol is dissolved in the aqueous solution or the circulating water 7.
(° C.), and the stirring action of the stirrer 6e in the evaporator 6a prevents ice from forming between the ices, and the ice can be taken out from the evaporator 6a as an ice slurry 6d free of ice.
On the other hand, the water vapor evaporated in the evaporator 6a is condensed in the condenser 6c by the cooling action of the cooling water 10, and water corresponding to the amount is returned to the circulating water 7 as makeup water, that is, condensed water 9. Therefore, the quality of the returned condensed ice 9 is substantially close to that of distilled water, and the antifreeze 14 such as ethylene glycol, which is an impurity, remains in the circulating water 7. There is no change in the concentration (g / L). Then, as described above, according to the system of the first embodiment, by setting the concentration of the antifreeze in the circulating water 7 to 50 (g / L), the evaporator 6a receives -1.0 ( C), and the low temperature ice slurry 6d can be taken out. In FIG. 1, reference numeral 15 denotes a cooling water heat exchanger or a closed cooling tower, and the cooling water obtained by the condenser 6c.
(Condensed water) 10 is circulated by a cooling water pump 16 as a closed circuit. Reference numeral 17 denotes sewage, seawater, river water, industrial water, clean water, or the like, which is supplied to the heat exchanger for cooling water or the closed cooling tower 15.

【0018】また、前記蒸発器6aから更に低い温度の
氷スラリー6dを取出すためには当該不凍液濃度(g/
L)を高め、製氷温度つまり凝固点を降下させればよ
い。
Further, in order to remove the ice slurry 6d at a lower temperature from the evaporator 6a, the concentration of the antifreeze solution (g / g) is required.
L) may be increased to lower the ice making temperature, that is, the freezing point.

【0019】[0019]

【発明の実施の形態2】図3は本発明に係る実施の形態
2を示すものであって、不凍液を利用した水蒸気圧縮冷
凍機の氷スラリー及び低温氷取出しシステムの構成配置
図である。
Second Embodiment FIG. 3 shows a second embodiment according to the present invention, and is a configuration layout diagram of an ice slurry and a low-temperature ice removal system of a steam compression refrigerator using an antifreeze.

【0020】本実施の形態2は前記実施の形態1の構成
に氷濃縮器を組込み、前記蒸発器から低温の氷スラリー
及び前記氷濃縮器から低温氷を取出すことを特徴とした
ものである。21は氷濃縮器であり、前記水蒸気圧縮冷
凍機6内の蒸発器6aで生成された例えば、体積比率で
約15%の氷を含有する氷スラリー6dを氷スラリーポ
ンプ11で導入している。該氷濃縮器21は前記氷スラ
リー6dを氷の浮力により氷と水に分離、すなわち固液
分離し、例えば、重量比率で約80%の氷を含有する濃
縮氷22を生成する。また、当該濃縮氷22を取出し
て、前記氷蓄熱槽8に供給し、氷解された水は補給水ポ
ンプ23によって循環水7に導かれ、前記蒸発器6aに
流送される。また、前記氷濃縮器21、前記水蒸気圧縮
冷凍機6の蒸発器6a、氷スラリーポンプ11、解氷水
ポンプ12、冷熱用熱交換器13、前記氷蓄熱槽8及び
これらを結ぶ連結管には前記循環水7及び補給水19と
して水道水が満たされている。前記循環水7へは所定濃
度を有するエチレングリコール等の不凍液14を添加
し、前記循環水7に必要な不凍液濃度を確保する。そし
て、前記循環水7へは前記氷蓄熱槽8から補給水ポンプ
23で氷解された水を補給水として流送している。
The second embodiment is characterized in that an ice concentrator is incorporated in the configuration of the first embodiment, and low-temperature ice slurry is extracted from the evaporator and low-temperature ice is extracted from the ice concentrator. Reference numeral 21 denotes an ice concentrator. An ice slurry 6d containing, for example, about 15% by volume of ice and generated by an evaporator 6a in the steam compression refrigerator 6 is introduced by an ice slurry pump 11. The ice concentrator 21 separates the ice slurry 6d into ice and water by the buoyancy of the ice, that is, separates it into solid and liquid, thereby producing, for example, concentrated ice 22 containing about 80% by weight of ice. Further, the concentrated ice 22 is taken out and supplied to the ice heat storage tank 8, and the thawed water is guided to the circulating water 7 by the makeup water pump 23 and sent to the evaporator 6a. In addition, the ice concentrator 21, the evaporator 6a of the steam compression refrigerator 6, the ice slurry pump 11, the ice melting water pump 12, the heat exchanger 13 for cooling and cooling, the ice heat storage tank 8, and the connecting pipe connecting these Tap water is filled as the circulating water 7 and the makeup water 19. An antifreeze 14 having a predetermined concentration, such as ethylene glycol, is added to the circulating water 7 to ensure a necessary concentration of the antifreeze in the circulating water 7. The water that has been thawed by the make-up water pump 23 from the ice heat storage tank 8 is supplied to the circulating water 7 as make-up water.

【0021】上述した本発明の実施の形態2の他の構成
は、上記実施の形態1と略同一でありその説明を省略す
る。
The other configuration of the second embodiment of the present invention is substantially the same as that of the first embodiment, and the description thereof is omitted.

【0022】次に、本発明に係る発明の実施の形態2の
不凍液を利用した水蒸気圧縮冷凍機の氷スラリー及び低
温氷取出しシステムの動作について説明する。前記水蒸
気圧縮冷凍機6の蒸発部6aから低温の氷スラリー6d
を取出す動作については、前記実施の形態1の動作と略
同一であるのでその説明を省略する。そこで、前記循環
水7にエチレングリコール等の不凍液14を添加する。
本実施の形態2のシステムによれば、不凍液の濃度を5
0(g/L)とすることにより、蒸発器6aから−1.
0(℃)の低温の氷スラリーを取出し、前記蒸発器6a
で生成された低温の氷スラリー6dは一旦前記氷濃縮器
21に流送され、該濃縮器21で氷と水の固液分離が行
なわれる。而して、前記氷濃縮器21に低温度の約−
1.0(℃)の濃縮氷22を貯留する。そして、当該氷
濃縮器21から従来にない低温氷を取出すことができ
る。そして、前記氷濃縮器21から、さらに低い温度の
濃縮氷22を取出すためには、当該不凍液濃度(g/
L)を高め、製氷温度つまり、循環水7の凝固点を降下
させればよい。
Next, the operation of the ice slurry and low-temperature ice removal system of the steam compression refrigerator using the antifreeze according to the second embodiment of the present invention will be described. Low-temperature ice slurry 6d from the evaporator 6a of the steam compression refrigerator 6
The operation of taking out is substantially the same as the operation of the first embodiment, and the description thereof is omitted. Therefore, an antifreeze 14 such as ethylene glycol is added to the circulating water 7.
According to the system of the second embodiment, the concentration of the antifreeze is set to 5
0 (g / L), from the evaporator 6a to -1.
0 (° C.) low temperature ice slurry is taken out and the evaporator 6a
The low-temperature ice slurry 6d generated in the above is once sent to the ice concentrator 21, where the solid and liquid separation of ice and water is performed. Thus, the ice concentrator 21 has a low temperature of about-
The concentrated ice 22 of 1.0 (° C.) is stored. Then, unprecedented low-temperature ice can be taken out from the ice concentrator 21. Then, in order to take out the concentrated ice 22 at a lower temperature from the ice concentrator 21, the concentration of the antifreeze liquid (g /
L) may be increased to lower the ice making temperature, that is, the freezing point of the circulating water 7.

【0023】[0023]

【発明の実施の形態3】図4は本発明に係る実施の形態
3を示すものであって、不凍液を利用した水蒸気圧縮冷
凍機の氷スラリー及び低温氷並びに人工雪取出しシステ
ムの構成配置図である。
Third Embodiment FIG. 4 shows a third embodiment according to the present invention, and is a configuration layout diagram of an ice slurry, a low-temperature ice, and an artificial snow removal system of a steam compression refrigerator using an antifreeze. is there.

【0024】本実施の形態3は前記実施の形態2の構成
に雪製造機を組み込み、前記蒸発器から低温の氷スラリ
ー及び前記氷濃縮器から低温氷並びに前記雪製造機で人
工雪を生成しかつ取出すことを特徴としたものである。
25は雪製造機であり、例えば、ロータリーフィーダー
等で構成されている。前記氷濃縮器21で生成された低
温の濃縮氷22を取り出し該氷濃縮器21に連結された
雪製造機25によって、当該濃縮氷22をもとに噴霧状
の人工雪25aを生成する。
In the third embodiment, a snow making machine is incorporated in the structure of the second embodiment, and low-temperature ice slurry is produced from the evaporator, low-temperature ice is produced from the ice concentrator, and artificial snow is produced by the snow making machine. And it is characterized by taking out.
Reference numeral 25 denotes a snow making machine, which is constituted by, for example, a rotary feeder. The low-temperature concentrated ice 22 generated by the ice concentrator 21 is taken out, and the artificial snow 25a in the form of spray is generated based on the concentrated ice 22 by the snow making machine 25 connected to the ice concentrator 21.

【0025】上述した本発明の実施の形態3の他の構成
は上記実施の形態2と略同一であり、その説明は省略す
る。
The other configuration of the third embodiment of the present invention is substantially the same as that of the second embodiment, and a description thereof will be omitted.

【0026】次に、本発明に係る実施の形態3の不凍液
を利用した水蒸気圧縮冷凍機の氷スラリー及び低温氷並
びに人工雪取出しシステムの動作について説明する。前
記水蒸気圧縮冷凍機6の蒸発器6aから低温の氷スラリ
ー6dを取出すことや、前記氷濃縮器21から低温氷を
取出すことの動作は前記本発明の実施の形態1及び2の
動作と略同一であるのでその説明を省略する。
Next, the operation of the ice slurry and low-temperature ice and the artificial snow removal system of the steam compression refrigerator using the antifreeze according to the third embodiment of the present invention will be described. The operation of extracting the low-temperature ice slurry 6d from the evaporator 6a of the steam compression refrigerator 6 and the operation of extracting the low-temperature ice from the ice concentrator 21 are substantially the same as the operations of the first and second embodiments of the present invention. Therefore, the description is omitted.

【0027】そこで、前記循環水7にエチレングリコー
ル等の不凍液14を添加して、その不凍液濃度(g/
L)を相当に高くし、例えば、約150(g/L)とす
れば、前記氷濃縮器21に極めて低温の約−5(℃)の
濃縮氷22を得ることができる。当該−5(℃)の低温
度の濃縮氷(低温氷)22を該氷濃縮器21の上部から
取出し、前記雪製造機25に運送し、該雪製造機25を
駆動動作させてこれを噴霧状であって−5(℃)の低温
の人工雪25aを生成し取出しを行なう。当該人工雪2
5aは取出されてスキー場等に搬送され、当該スキー場
に利用される。また、前記氷濃縮器21から、更に低い
温度の濃縮氷22を取出しかつ低い温度の人工雪25a
を生成するためには、当該不凍液濃度(g/L)を高
め、製氷温度つまり循環水7の凝固点を降下させればよ
い。
Therefore, an antifreeze 14 such as ethylene glycol is added to the circulating water 7, and the concentration of the antifreeze (g / g) is added.
If L) is considerably increased, for example, to about 150 (g / L), very low-temperature concentrated ice 22 of about -5 (° C.) can be obtained in the ice concentrator 21. The concentrated ice (low-temperature ice) 22 having a low temperature of -5 (° C.) is taken out from the upper part of the ice concentrator 21 and transported to the snow making machine 25, and the snow making machine 25 is driven and sprayed. An artificial snow 25a having a low temperature of -5 (° C.) is generated and taken out. The artificial snow 2
5a is taken out, transported to a ski resort or the like, and used at the ski resort. Further, the ice concentrate 22 of lower temperature is taken out from the ice concentrator 21 and the artificial snow 25a of lower temperature is taken out.
Is generated by increasing the antifreeze concentration (g / L) and lowering the ice-making temperature, that is, the freezing point of the circulating water 7.

【0028】上記説明に於いて、前記実施の形態3に係
る発明では低温の氷スラリー6d、低温度氷22、更に
は、人工雪25aを一緒に蒸発器6aや氷濃縮器21及
び雪製造機25で取出す技術を説明したが、これに限定
されず、必要に応じて低温の氷スラリー6d、低温氷
(濃縮水)22又は人工雪25aのいずれか1つを取出す
技術であってもよく、その場合、当該取出す低温の氷ス
ラリー6d等を温度条件によって、前記不凍液の濃度を
適宜変更すればよく又必要に応じて配置構成要素を削
減、変更して対応することもできる。
In the above description, in the invention according to the third embodiment, the low-temperature ice slurry 6d, the low-temperature ice 22, and the artificial snow 25a are combined together with the evaporator 6a, the ice concentrator 21, and the snow making machine. 25, the extraction technique has been described. However, the present invention is not limited thereto.
(Concentrated water) 22 or a technique for removing one of the artificial snow 25a may be used. In this case, the concentration of the antifreeze may be appropriately changed depending on the temperature condition of the low-temperature ice slurry 6d or the like. It is also possible to reduce or change the arrangement components as needed.

【0029】[0029]

【発明の効果】本発明に係る不凍液を利用した水蒸気圧
縮冷凍機の氷スラリー及び低温氷並びに人工雪取出しシ
ステムは叙上の構成、動作を有するので次の効果があ
る。
The ice slurry, low-temperature ice, and artificial snow removal system of the steam compression refrigerator using an antifreeze according to the present invention have the above-described configuration and operation, and therefore have the following effects.

【0030】請求項1記載の発明によれば、氷蓄熱槽か
ら循環水を導く蒸発器、圧縮機、熱交換器を介して冷却
水閉回路を形成した凝縮器及び該凝縮器で生成した凝縮
水を循環水に戻す回路で構成された水蒸気圧縮冷凍機に
於いて、前記循環水に所定濃度を有する不凍液を添加
し、前記蒸発器から低温の氷スラリーを取出すことを特
徴とする不凍液を利用した水蒸気圧縮冷凍機の氷スラリ
ー取り出しシステムを提供する。このような構成とした
ので、前記循環水の凝固点を降下させ、蒸発器から所望
の例えば、−0.1(℃)〜−10(℃)の低温の氷の
体積比率が0.5%〜50%程度の氷スラリーを取出す
ことができると共に循環水に不純物として添加する汎用
のエチレングリコール等の不凍液であって、実施化が極
めて容易である。
According to the first aspect of the present invention, a condenser having a cooling water closed circuit formed through an evaporator, a compressor, and a heat exchanger for guiding circulating water from an ice heat storage tank, and a condenser formed by the condenser. In a steam compression refrigerator comprising a circuit for returning water to circulating water, an antifreeze having a predetermined concentration is added to the circulating water, and a low-temperature ice slurry is taken out from the evaporator. Provided is an ice slurry removal system for a steam compression refrigerator. With such a configuration, the freezing point of the circulating water is lowered, and the volume ratio of the desired low-temperature ice of -0.1 (° C) to -10 (° C) from the evaporator is 0.5% to It is a general-purpose antifreeze such as ethylene glycol that can take out about 50% of an ice slurry and is added to the circulating water as an impurity, and is very easy to implement.

【0031】請求項2記載の発明によれば、氷蓄熱槽
と、該氷蓄熱に氷を導く氷濃縮器と、該氷濃縮器から循
環水を導く蒸発器、圧縮機、熱交換器を介して冷却水閉
回路を形成した凝縮器及び該凝縮器で生成した凝縮水を
循環水に戻す回路で構成された水蒸気圧縮冷凍機に於い
て、前記循環水に所定濃度を有する不凍液を添加し、前記
蒸発部から低温の氷スラリーを取出すと共に、前記氷濃
縮器において低温氷を生成することを特徴とする不凍液
を利用した水蒸気圧縮冷凍機の氷スラリー及び低温氷取
出しシステムを提供する。このような構成としたので、
前記循環水の凝固点を降下させ、蒸発器から低温の氷ス
ラリー及び前記氷濃縮器から所望の例えば、−0.1
(℃)〜−10(℃)の低温氷を取出すことができると
共に、循環水に不純物として添加する汎用のエチレング
リコール等の不凍液であって、実施化が極めて容易とな
るシステムを提供できるものである。
According to the second aspect of the present invention, an ice heat storage tank, an ice concentrator for guiding ice to the ice heat storage, an evaporator for guiding circulating water from the ice concentrator, a compressor, and a heat exchanger. In a steam compression refrigerator having a condenser that forms a cooling water closed circuit and a circuit that returns condensed water generated by the condenser to circulating water, an antifreeze having a predetermined concentration is added to the circulating water, An ice slurry and a low-temperature ice removal system for a steam compression refrigerator using an antifreeze, wherein low-temperature ice is removed from the evaporator and low-temperature ice is generated in the ice concentrator. With such a configuration,
The freezing point of the circulating water is lowered and the cold ice slurry from the evaporator and the desired ice e.g.
It is a general-purpose antifreeze such as ethylene glycol added as impurities to circulating water, and can provide a system that can take out low-temperature ice of (° C) to −10 (° C) and is extremely easy to implement. is there.

【0032】請求項3記載の発明によれば、氷濃縮器
と、該氷濃縮器から低温氷を導く雪製造機と、該氷濃縮
器から循環水を導く蒸発器、圧縮機、熱交換器を介して
冷却水閉回路を形成した凝縮器及び該凝縮器で生成した
凝縮水を循環水に戻す回路で構成された水蒸気圧縮冷凍
機に於いて、前記循環水に所定濃度を有する不凍液を添
加し、前記蒸発器から低温の氷スラリーを取出しかつ前
記氷濃縮器において低温氷を生成すると共に、前記雪製
造機で人工雪を生成することを特徴とする不凍液を利用
した水蒸気圧縮冷凍機の氷スラリー及び低温氷並びに人
工雪取出しシステムを提供する。このような構成とした
ので、前記循環水の凝固点を降下させ、蒸発器から例え
ば、−0.1(℃)〜−10(℃)の低温の氷スラリー
及び氷濃縮器から−0.1(℃)〜−10(℃)の低温
氷を、更には雪製造機から極めて低温であって純水の人
工雪を取出し外気温度の高い季節でも有効なスキー場を
設営することができる効果がある。また、これら低温氷
スラリー、低温氷又は人工雪のいずれか1つをも取出す
システムを提供すると共に、塩化カルシウムなどの寒剤
を散布することなく、環境悪弊害を防止する効果があ
る。
According to the third aspect of the present invention, an ice concentrator, a snow making machine that guides low-temperature ice from the ice concentrator, an evaporator, a compressor, and a heat exchanger that guides circulating water from the ice concentrator An antifreeze having a predetermined concentration is added to the circulating water in the condenser having a cooling water closed circuit formed therein and a circuit for returning the condensed water generated in the condenser to the circulating water. Removing a low-temperature ice slurry from the evaporator, generating low-temperature ice in the ice concentrator, and generating artificial snow in the snow making machine; A slurry and cold ice and artificial snow removal system is provided. With such a configuration, the freezing point of the circulating water is lowered, and for example, a low-temperature ice slurry of -0.1 (° C) to -10 (° C) and -0.1 ( C) to -10 (C), and extremely low temperature and pure water artificial snow from a snow making machine to take out an effective ski area even in a season with a high outside air temperature. . In addition to providing a system for removing any one of these low-temperature ice slurries, low-temperature ice and artificial snow, there is an effect of preventing environmental harmful effects without spraying a cryogen such as calcium chloride.

【0033】請求項4記載の発明によれば、前記雪製造
機がロータリーフィーダー等でなることを特徴とする請
求項3記載の不凍液を利用した水蒸気圧縮冷凍機の氷ス
ラリー及び低温氷並びに人工雪取出しシステムを提供す
る。このような構成としたので、ロータリーフィーダー
等の雪製造機で容易に人工雪を生成することができる効
果がある。
According to a fourth aspect of the present invention, the snow making machine comprises a rotary feeder or the like. Provide a retrieval system. With such a configuration, there is an effect that artificial snow can be easily generated by a snow making machine such as a rotary feeder.

【0034】請求項5記載の発明によれば、前記所定濃
度を有する不凍液が塩化ナトリウム溶液又はグリコール
類溶液であって、プロピレングリコール、エチレングリ
コール、二価アルコール又はプロパンジオールでなるこ
とを特徴とする請求項1、2又は3記載の不凍液を利用
した水蒸気圧縮冷凍機の氷スラリー及び低温氷並びに人
工雪取出しシステムを提供する。このような構成とした
ので、不凍液として汎用の塩化ナトリウムやプロピレン
グリコール、エチレングリコール、二価アルコール、プ
ロパンジオール等を適用しており、本発明の実施化が容
易となる効果がある。
According to the fifth aspect of the present invention, the antifreeze having the predetermined concentration is a sodium chloride solution or a glycol solution, and is made of propylene glycol, ethylene glycol, dihydric alcohol or propanediol. An ice slurry, a low-temperature ice, and an artificial snow removal system for a steam compression refrigerator using the antifreeze according to claim 1, 2 or 3. With such a configuration, general-purpose sodium chloride, propylene glycol, ethylene glycol, dihydric alcohol, propanediol, or the like is used as the antifreeze, and the present invention has an effect of easily implementing the present invention.

【0035】請求項6記載の発明によれば、前記蒸発器
が攪拌機を備えたことを特徴とする請求項1、2又は3
記載の不凍液を利用した水蒸気圧縮冷凍機の氷スラリー
及び低温氷並びに人工雪取出しシステムを提供する。こ
のような構成としたので、蒸発器内を攪拌機によって攪
拌でき、氷同士の結氷を防止し、低温の氷スラリーを該
蒸発器から容易に取出すことができる効果がある。
According to the sixth aspect of the present invention, the evaporator is provided with a stirrer.
An ice slurry, a low-temperature ice, and an artificial snow removal system for a steam compression refrigerator using the antifreeze described above. With such a configuration, the inside of the evaporator can be agitated by the stirrer, ice formation between the ices can be prevented, and low-temperature ice slurry can be easily taken out from the evaporator.

【0036】請求項7記載の発明によれば、前記熱交換
器が冷却水用熱交換器又は密閉冷却塔でなることを特徴
とする請求項1、2又は3記載の不凍液を利用した水蒸
気圧縮冷凍機の氷スラリー及び低温氷並びに人工雪取出
しシステムを提供する。このような構成としたので、凝
縮器で得られた冷却水を密閉回路として循環させ補給水
として利用できる効果がある。
According to a seventh aspect of the present invention, the heat exchanger is a heat exchanger for cooling water or a closed cooling tower, and the steam compression using an antifreeze solution according to the first, second or third aspect of the present invention. An ice slurry and low-temperature ice for a refrigerator and an artificial snow removal system are provided. With such a configuration, there is an effect that the cooling water obtained by the condenser can be circulated as a closed circuit and used as makeup water.

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

【図1】本発明に係る実施の形態1のシステムの配置構
成図である。
FIG. 1 is an arrangement configuration diagram of a system according to a first embodiment of the present invention.

【図2】本発明に係るシステムに於いて、水溶液中の不
凍液(g/L)に対する凝固点降下(℃)を示す特性チ
ャートである。
FIG. 2 is a characteristic chart showing a freezing point drop (° C.) with respect to an antifreeze solution (g / L) in an aqueous solution in the system according to the present invention.

【図3】本発明に係る実施の形態2ののシステムの配置
構成図である。
FIG. 3 is an arrangement configuration diagram of a system according to a second embodiment of the present invention.

【図4】本発明に係る実施の形態3ののシステムの配置
構成図である。
FIG. 4 is an arrangement configuration diagram of a system according to a third embodiment of the present invention.

【図5】従来の技術に於ける水蒸気圧縮冷凍機による製
氷技術の例を示す基本構成図である。
FIG. 5 is a basic configuration diagram showing an example of an ice making technique using a steam compression refrigerator in a conventional technique.

【符号の説明】[Explanation of symbols]

1、6 水蒸気圧縮冷凍機 2 循環水 2a 補給水 3 氷濃縮器 4 濃縮氷 5 氷スラリー 6a 蒸発器 6b 圧縮機 6c 凝縮器 6d 低温の氷スラリー 6e 攪拌機 7 循環水 8 氷蓄熱槽 8a 氷融解水 9 凝縮水 10 冷却水 11 氷スラリーポンプ 12 解氷水ポンプ 13 冷熱用熱交換器 14 不凍液 15 冷却水用熱交換器又は密閉冷却塔 16 冷却水ポンプ 17 下水、海水、河川水、工業用水又は上水 18 冷水ポンプ 19 補給水 21 氷濃縮器 22 低温氷(濃縮氷) 23 補給水ポンプ 25 雪製造機 25a 人工雪 1, 6 steam compression refrigerator 2 circulating water 2a makeup water 3 ice concentrator 4 concentrated ice 5 ice slurry 6a evaporator 6b compressor 6c condenser 6d low temperature ice slurry 6e stirrer 7 circulating water 8 ice storage tank 8a ice melting water 9 Condensed water 10 Cooling water 11 Ice slurry pump 12 Defrosting water pump 13 Heat exchanger for cooling and heating 14 Antifreeze 15 Heat exchanger for cooling water or closed cooling tower 16 Cooling water pump 17 Sewage, seawater, river water, industrial water or clean water 18 Cold water pump 19 Makeup water 21 Ice concentrator 22 Low temperature ice (concentrated ice) 23 Makeup water pump 25 Snow making machine 25a Artificial snow

Claims (7)

【特許請求の範囲】[The claims] 【請求項1】氷蓄熱槽から循環水を導く蒸発器、圧縮
機、熱交換器を介して冷却水閉回路を形成した凝縮器及
び該凝縮器で生成した凝縮水を循環水に戻す回路で構成
された水蒸気圧縮冷凍機に於いて、前記循環水に所定濃
度を有する不凍液を添加し、前記蒸発器から低温の氷ス
ラリーを取出すことを特徴とする不凍液を利用した水蒸
気圧縮冷凍機の氷スラリー取り出しシステム。
1. A condenser having a cooling water closed circuit formed through an evaporator, a compressor, and a heat exchanger for guiding circulating water from an ice heat storage tank, and a circuit for returning condensed water generated by the condenser to the circulating water. An ice slurry for a steam compression refrigerator using an antifreeze, wherein an antifreeze having a predetermined concentration is added to the circulating water, and a low-temperature ice slurry is removed from the evaporator. Retrieval system.
【請求項2】氷蓄熱槽と、該氷蓄熱槽に氷を導く氷濃縮
器と、該氷濃縮器から循環水を導く蒸発器、圧縮機、熱
交換器を介して冷却水閉回路を形成した凝縮器及び該凝
縮器で生成した凝縮水を循環水に戻す回路で構成された
水蒸気圧縮冷凍機に於いて、前記循環水に所定濃度を有
する不凍液を添加し、前記蒸発部から低温の氷スラリー
を取出すと共に、前記氷濃縮器において低温氷を生成す
ることを特徴とする不凍液を利用した水蒸気圧縮冷凍機
の氷スラリー及び低温氷取出しシステム。
2. An ice heat storage tank, an ice concentrator for guiding ice to the ice heat storage tank, and a cooling water closed circuit formed through an evaporator, a compressor, and a heat exchanger for guiding circulating water from the ice concentrator. In the steam compression refrigerating machine constituted by the condenser and the circuit for returning the condensed water generated by the condenser to the circulating water, an antifreeze having a predetermined concentration is added to the circulating water, and low-temperature ice An ice slurry and a low-temperature ice removing system for a steam compression refrigerator using an antifreeze, wherein the slurry is removed and low-temperature ice is generated in the ice concentrator.
【請求項3】氷濃縮器と、該氷濃縮器から低温氷を導く
雪製造機と、該氷濃縮器から循環水を導く蒸発器、圧縮
機、熱交換器を介して冷却水閉回路を形成した凝縮器及
び該凝縮器で生成した凝縮水を循環水に戻す回路で構成
された水蒸気圧縮冷凍機に於いて、前記循環水に所定濃
度を有する不凍液を添加し、前記蒸発器から低温の氷ス
ラリーを取出しかつ前記氷濃縮器において低温氷を生成
すると共に、前記雪製造機で人工雪を生成することを特
徴とする不凍液を利用した水蒸気圧縮冷凍機の氷スラリ
ー及び低温氷並びに人工雪取出しシステム。
3. An ice concentrator, a snow making machine for introducing low-temperature ice from the ice concentrator, and a cooling water closing circuit via an evaporator, a compressor and a heat exchanger for introducing circulating water from the ice concentrator. In a steam compression refrigerator including a formed condenser and a circuit for returning condensed water generated by the condenser to circulating water, an antifreeze having a predetermined concentration is added to the circulating water, and a low-temperature Removing an ice slurry, generating low-temperature ice in the ice concentrator, and generating artificial snow in the snow making machine; removing an ice slurry, low-temperature ice, and artificial snow from a steam compression refrigerator using antifreeze system.
【請求項4】前記雪製造機がロータリーフィーダー等で
なることを特徴とする請求項3記載の不凍液を利用した
水蒸気圧縮冷凍機の氷スラリー及び低温氷並びに人工雪
取出しシステム。
4. The system according to claim 3, wherein said snow making machine comprises a rotary feeder or the like.
【請求項5】前記所定濃度を有する不凍液が塩化ナトリ
ウム溶液又はグリコール類溶液であって、プロピレング
リコール、エチレングリコール、二価アルコール又はプロ
パンジオールでなることを特徴とする請求項1、2又は
3記載の不凍液を利用した水蒸気圧縮冷凍機の氷スラリ
ー及び低温氷並びに人工雪取出しシステム。
5. The antifreeze having the predetermined concentration is a sodium chloride solution or a glycol solution, and is made of propylene glycol, ethylene glycol, dihydric alcohol or propanediol. Of ice slurry, low-temperature ice and artificial snow for a steam compression refrigerator using the antifreeze of the present invention.
【請求項6】前記蒸発器が攪拌機を備えたことを特徴と
する請求項1、2又は3記載の不凍液を利用した水蒸気
圧縮冷凍機の氷スラリー及び低温氷並びに人工雪取出し
システム。
6. The system according to claim 1, wherein the evaporator includes a stirrer, and wherein the ice slurry, the low-temperature ice and the artificial snow are removed from the steam compression refrigerator using the antifreeze.
【請求項7】前記熱交換器が冷却水用熱交換器又は密閉
冷却塔でなることを特徴とする請求項1、2又は3記載
の不凍液を利用した水蒸気圧縮冷凍機の氷スラリー及び
低温氷並びに人工雪取出しシステム。
7. The ice slurry and low-temperature ice for a steam compression refrigerator using an antifreeze according to claim 1, wherein the heat exchanger is a heat exchanger for cooling water or a closed cooling tower. And artificial snow removal system.
JP2001056398A 2001-03-01 2001-03-01 Steam compression refrigerator using antifreeze Expired - Fee Related JP4545332B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001056398A JP4545332B2 (en) 2001-03-01 2001-03-01 Steam compression refrigerator using antifreeze

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001056398A JP4545332B2 (en) 2001-03-01 2001-03-01 Steam compression refrigerator using antifreeze

Publications (2)

Publication Number Publication Date
JP2002257441A true JP2002257441A (en) 2002-09-11
JP4545332B2 JP4545332B2 (en) 2010-09-15

Family

ID=18916430

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2001056398A Expired - Fee Related JP4545332B2 (en) 2001-03-01 2001-03-01 Steam compression refrigerator using antifreeze

Country Status (1)

Country Link
JP (1) JP4545332B2 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007530896A (en) * 2003-07-07 2007-11-01 デユポン・テイト・アンド・ライル・バイオ・プロダクツ・カンパニー・エルエルシー Heat transfer system
JP2008531965A (en) * 2005-02-23 2008-08-14 アイ・ディ・イー・テクノロジーズ・リミテッド Small heat pump using water as refrigerant
CN102494447A (en) * 2011-12-09 2012-06-13 浙江海洋学院普陀科学技术学院 Impurity-free binary ice system
CN110657613A (en) * 2019-11-14 2020-01-07 广州科勒尔制冷设备有限公司 Low-temperature-40-below-50 ℃ chemical fluid ice making machine

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH06147564A (en) * 1992-11-10 1994-05-27 Suga Kogyo Kk Ice heat storage system
JPH07280401A (en) * 1994-04-07 1995-10-27 Nkk Corp Vacuum ice-making apparatus
JPH07318208A (en) * 1994-05-25 1995-12-08 Nkk Corp Method and device for vacuum ice making
JP2000018779A (en) * 1998-06-29 2000-01-18 Tokyo Gas Co Ltd Ice machine
JP2001033134A (en) * 1999-07-22 2001-02-09 Nkk Corp Method and apparatus for transporting ice and snow

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH06147564A (en) * 1992-11-10 1994-05-27 Suga Kogyo Kk Ice heat storage system
JPH07280401A (en) * 1994-04-07 1995-10-27 Nkk Corp Vacuum ice-making apparatus
JPH07318208A (en) * 1994-05-25 1995-12-08 Nkk Corp Method and device for vacuum ice making
JP2000018779A (en) * 1998-06-29 2000-01-18 Tokyo Gas Co Ltd Ice machine
JP2001033134A (en) * 1999-07-22 2001-02-09 Nkk Corp Method and apparatus for transporting ice and snow

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007530896A (en) * 2003-07-07 2007-11-01 デユポン・テイト・アンド・ライル・バイオ・プロダクツ・カンパニー・エルエルシー Heat transfer system
JP2008531965A (en) * 2005-02-23 2008-08-14 アイ・ディ・イー・テクノロジーズ・リミテッド Small heat pump using water as refrigerant
CN102494447A (en) * 2011-12-09 2012-06-13 浙江海洋学院普陀科学技术学院 Impurity-free binary ice system
CN110657613A (en) * 2019-11-14 2020-01-07 广州科勒尔制冷设备有限公司 Low-temperature-40-below-50 ℃ chemical fluid ice making machine

Also Published As

Publication number Publication date
JP4545332B2 (en) 2010-09-15

Similar Documents

Publication Publication Date Title
JPH01500215A (en) High Performance Vapor Compression Heat Pump Cycle Utilizing Nonazeotropic Working Fluid Mixtures
JP2007509303A (en) High performance heat storage and cooling system using refrigerant
US20120247149A1 (en) Process cooling system and method using seawater
JP2002257441A (en) System for taking out ice slurry, low temperature ice, and artificial snow in steam compression freezer utilizing anti-freezing solution
KR100881328B1 (en) Heat Pump apparatus
EA039194B1 (en) Refrigeration plant
BR8100634A (en) REFRIGERATION METHOD AND SYSTEM FOR COOLING A LIQUID
JP2002257385A (en) Ice slurry and low temperature ice and artificial snow taking out system of steam compression freezer utilizing sodium chloride
JP3490691B2 (en) Water quality management system in combination of steam compression refrigerator and heat storage tank
CN101935078B (en) Sea water desalination device and method
US5307641A (en) Method and apparatus for producing ice by direct contact of a non-hydrate producing refrigerant with water
JP2002071237A (en) Stirling cooling system and cooling compartment
EP0076294A1 (en) A method and a system for production of loose ice at large capacity
JP4601190B2 (en) Cold liquid extraction system for steam compression refrigerators used for freezing or ice making
JP3126424B2 (en) Heat source equipment using a heating tower
JP2534002B2 (en) Vegetable vacuum cooling device with cold storage tank
TWI303995B (en) Absorption freezing method to separate pure water from sea water
JP3852801B2 (en) Internal / external melting double flow type ice heat storage system
JP3729393B2 (en) Cold heat and pure water or clean water take-off system of steam compression refrigerator
JP2834722B2 (en) Vacuum cooling device with regenerator
JP2928835B2 (en) Open type heating tower circulating liquid concentration adjustment device
JP2000035272A (en) Cooling facility for food
JPH05137499A (en) Vacuum cooler provided with coldness-storing tank
JP2902448B2 (en) Vacuum cooling device with regenerator
CN201834782U (en) Seawater desalination device

Legal Events

Date Code Title Description
A711 Notification of change in applicant

Free format text: JAPANESE INTERMEDIATE CODE: A711

Effective date: 20050630

RD02 Notification of acceptance of power of attorney

Free format text: JAPANESE INTERMEDIATE CODE: A7422

Effective date: 20050630

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A821

Effective date: 20050630

A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20070508

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20090910

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20090924

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20091208

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20100629

A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20100630

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130709

Year of fee payment: 3

R150 Certificate of patent or registration of utility model

Free format text: JAPANESE INTERMEDIATE CODE: R150

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

S531 Written request for registration of change of domicile

Free format text: JAPANESE INTERMEDIATE CODE: R313531

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

LAPS Cancellation because of no payment of annual fees