JP2002071247A - Method and system for producing ice containing salt - Google Patents

Method and system for producing ice containing salt

Info

Publication number
JP2002071247A
JP2002071247A JP2000254120A JP2000254120A JP2002071247A JP 2002071247 A JP2002071247 A JP 2002071247A JP 2000254120 A JP2000254120 A JP 2000254120A JP 2000254120 A JP2000254120 A JP 2000254120A JP 2002071247 A JP2002071247 A JP 2002071247A
Authority
JP
Japan
Prior art keywords
air
ice
low
salt
producing
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
JP2000254120A
Other languages
Japanese (ja)
Other versions
JP3410068B2 (en
Inventor
Masaaki Shimizu
雅彰 清水
Motohisa Uda
素久 宇田
Hideo Tanaka
秀男 田中
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Kajima Corp
Original Assignee
Kajima Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Kajima Corp filed Critical Kajima Corp
Priority to JP2000254120A priority Critical patent/JP3410068B2/en
Publication of JP2002071247A publication Critical patent/JP2002071247A/en
Application granted granted Critical
Publication of JP3410068B2 publication Critical patent/JP3410068B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

PROBLEM TO BE SOLVED: To produce healthy ice containing salt uniformly with high efficiency without using a refrigerating machine utilizing condensation/evaporation of refrigerant, e.g. CFC. SOLUTION: Ice containing salt is produced by spraying saline water into low temperature air flow to generate nuclei of ice in the low temperature air flow, floating the nuclei of ice in the low temperature air flow until they grow up or join to produce ice particles containing salt and then separating the ice particles containing salt from the air flow and collecting them.

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,海産魚介類保存用
に適した含塩氷の製造法および装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method and an apparatus for producing salted ice suitable for storing marine fish and shellfish.

【0002】[0002]

【従来の技術】海産魚介類の輸送中または貯留時におい
て氷を共存させて鮮度を維持することが行われている。
そのさい海産魚介類に対して淡水氷を使用するとエラや
表皮から淡水が侵入して鮮度が低下するので,海水と同
様な塩分を含む含塩氷を使用することが望ましい。
2. Description of the Related Art During transportation or storage of marine fish and shellfish, freshness is maintained by coexisting ice.
When freshwater ice is used for marine fish and shellfish, freshwater penetrates from gills and epidermis and freshness is reduced. Therefore, it is desirable to use salted ice containing salt similar to seawater.

【0003】含塩氷を得るために海水そのものを氷結さ
せても固液間で塩の溶解度が相違するので通常は海水と
同じ成分の氷にならない。すなわち,淡水と同様の処理
で海水を原料として製氷しても,水の分子が徐々に結合
して凝固するさいに,粒子間に析出する塩分は外部に押
し出される結果,塩分濃度の薄い氷となる。また海水を
原料とするのでは衛生上も問題がある。そこで,淡水を
使用していったん淡水氷を製造し,これに適度の塩分を
添加し,さらに氷結させることが提案されている。例え
ば,特開平1−184375号公報および特公平6−6
3678号公報には,淡水からフレーク状または粉・粒
状の淡水氷を製造し,この淡水氷に,濃度を調節した塩
水を添加または噴霧したうえ,冷却条件下で攪拌・混合
し,加圧成形する塩水氷の製造装置を開示している。
[0003] Even if seawater itself is frozen in order to obtain salt-containing ice, the solubility of salts differs between solid and liquid, so that the ice does not usually have the same composition as seawater. In other words, even if ice is produced using seawater as a raw material in the same manner as freshwater, the salt that precipitates between the particles is pushed out to the outside when the water molecules gradually bind and solidify. Become. There is also a problem in terms of hygiene when using seawater as a raw material. Therefore, it has been proposed to produce fresh water ice once using fresh water, add an appropriate amount of salt to the ice, and freeze the ice. For example, JP-A-1-184375 and JP-B-6-6-6
Japanese Patent No. 3678 discloses a method of producing flaked or powdered / granular freshwater ice from freshwater, adding or spraying saltwater having an adjusted concentration to the freshwater ice, stirring and mixing under cooling conditions, and press forming. An apparatus for producing salt water ice is disclosed.

【0004】なお,海水から直接的に塩水氷を製造しよ
うとする試みについては例えば特開平5−256547
号公報に提案されたように,真空(減圧)容器内に,冷
却した海水を噴霧し,水滴が蒸発するさいの潜熱によっ
て水滴を急冷して製氷化するものが知られている。
An attempt to produce salt water ice directly from seawater is disclosed in, for example, Japanese Patent Application Laid-Open No. 5-25647.
As disclosed in Japanese Patent Application Laid-Open Publication No. H10-209, there is known an apparatus in which cooled seawater is sprayed into a vacuum (decompression) vessel, and the waterdrop is rapidly cooled by latent heat when the waterdrop evaporates to produce ice.

【0005】[0005]

【発明が解決しようとする課題】前者のようにフレーク
状または粉・粒状の淡水氷を製造してから,冷却条件下
で塩水と攪拌混合して再度氷結する方式では,製氷を2
回に分けて行うことになるので工数が多くなって管理が
煩雑化すると共に,淡水氷と塩水の攪拌混合の仕方によ
っては含塩氷中の塩濃度が均一にならず,濃度差が生ず
るおそれがある。また,製氷のための冷凍機を必要と
し,設備が大掛かりにならざるを得ない。またフロン等
の冷媒の凝縮・蒸発を利用した冷凍機は環境上の問題も
ある。
According to the former method, flake-like or powdery / granular fresh water ice is produced and then mixed with salt water under cooling conditions to re-freeze the ice.
Since the steps are performed separately, the man-hours increase and the management becomes complicated, and depending on the method of stirring and mixing the fresh water ice and the salt water, the salt concentration in the salt-containing ice may not be uniform, and a concentration difference may occur. There is. In addition, a refrigerator for ice making is required, and the equipment must be large-scale. Refrigerators utilizing condensation and evaporation of refrigerants such as chlorofluorocarbon also have environmental problems.

【0006】他方,塩水を真空中に噴霧する方式では,
水が蒸発除去されるので,生成した氷中の塩濃度が高く
なり,また水の氷への固化率が低下するので製氷効率が
悪く設備的にも操業的にも実用的ではない。
On the other hand, in the method of spraying salt water in a vacuum,
Since the water is removed by evaporation, the salt concentration in the produced ice increases, and the solidification rate of the water decreases, so that the ice making efficiency is poor and the equipment and operation are not practical.

【0007】したがって,本発明は,このような問題を
解決し,含塩氷を効率良く且つ安価に製造する方法およ
び装置を提供しようとするものである。
Accordingly, an object of the present invention is to solve such a problem and to provide a method and an apparatus for producing salted ice efficiently and at low cost.

【0008】[0008]

【課題を解決するための手段】本発明によれば,低温空
気流中に,好ましくは低温空気の上昇気流中に塩水を噴
霧して該低温空気流中で氷核を生成させ,該氷核が含塩
氷粒子にまで成長または接合するまで該低温気流中に浮
遊させ,ついで該含塩氷粒子を空気流から分離捕集す
る,好ましくは自重により自然落下させて分離捕集す
る,含塩氷の製造法を提供する。
According to the present invention, ice nuclei are formed in a low temperature air stream, preferably in a rising air stream of low temperature air, by spraying salt water. Suspended in the low-temperature air flow until the particles grow or bond to salt-containing ice particles, and then separate and collect the salt-containing ice particles from the air flow, preferably, separate and collect them by gravity by gravity. A method for producing ice is provided.

【0009】また,本発明によれば,下方に空気吹出口
を上方に空気排出口をもち,塔内上部にスプレーノズル
を備えたスプレー塔と,低温空気流を製造するための低
温空気製造装置と,該スプレー塔の空気吹出口に該低温
空気製造装置で製造された低温空気を導く空気管路と,
からなる含塩氷の製造装置であって,該低温空気製造装
置が,空気の流れの順に,一次圧縮機,一次冷却器,二
次圧縮機,二次冷却器,空気対空気熱交換器および膨張
機を連結したものである,含塩氷の製造装置を提供す
る。
Further, according to the present invention, a spray tower having an air outlet below and an air outlet above and having a spray nozzle in the upper part of the tower, and a low-temperature air producing apparatus for producing a low-temperature air flow An air conduit for guiding the low-temperature air produced by the low-temperature air producing device to an air outlet of the spray tower;
The apparatus for producing salted ice, comprising: a primary compressor, a primary cooler, a secondary compressor, a secondary cooler, an air-to-air heat exchanger, and an air-to-air heat exchanger in the order of air flow. Provided is an apparatus for producing salt ice, which is connected to an expander.

【0010】この含塩氷の製造装置は,スプレー塔の底
部に氷粒子の受け部を有し,この氷粒子の受け部内に一
端が連結し,他端が塔外の容器(氷貯蔵庫)内に連結す
る氷粒子の移送手段例えばスクリューコンベアを備える
ことができ,そして,塔外の容器内に氷プレス機を設置
し,この氷プレス機に該移送手段のの吐出端を連結する
ように構成される。また,前記の低温空気製造装置は,
機内への空気採取口と,機内からの空気出口を備え,そ
の空気採取口はHEPAフイルタを介して外気取入口に
接続されると共にスプレー塔の空気排出口にも接続さ
れ,その空気出口はスプレー塔の空気吹出口に連結され
る。
This apparatus for producing salted ice has an ice particle receiving portion at the bottom of the spray tower, one end of which is connected to the ice particle receiving portion, and the other end of which is inside a container (ice storage) outside the tower. A means for transferring ice particles, such as a screw conveyor, connected to the ice press, and an ice press installed in a container outside the tower, and a discharge end of the transfer means connected to the ice press. Is done. In addition, the low-temperature air producing device is
It has an air sampling port to the inside of the machine and an air outlet from the inside of the machine. The air sampling port is connected to the outside air inlet through a HEPA filter and is also connected to the air outlet of the spray tower. It is connected to the air outlet of the tower.

【0011】[0011]

【発明の実施の形態】本発明者らは,前記の課題を解決
すべく種々の試作を重ねたが,マイナス10℃以下,好
ましくはマイナス20℃以下の極低温空気の流れの中に
塩水を噴霧すると,その塩水ミストはただちに塩分を含
んだままの氷核となって浮遊し,この氷核を該低温空気
中に適切に浮遊させると,これらが互いに接合するから
であろうと推察されるが,径大の塩を含む含塩氷粒子,
代表的には平均径が5mm前後の含塩氷粒子にまで成長
することを知った。この氷粒子中には,塩水と実質的に
同じ濃度で塩が含まれている。すなわち,真空蒸発させ
る場合のように,塩だけが固体となって析出した塩粒子
が発生するようなことは実質的に防止される。
BEST MODE FOR CARRYING OUT THE INVENTION The inventors of the present invention have made various prototypes in order to solve the above-mentioned problems. It is presumed that when sprayed, the salt water mist immediately floats as salt-containing ice nuclei, and if these ice nuclei are properly floated in the low-temperature air, they will bond to each other. , Salt-containing ice particles containing large salt,
Typically, it has been found that the particles grow to salt-containing ice particles having an average diameter of about 5 mm. The ice particles contain salt at substantially the same concentration as the salt water. That is, it is substantially prevented that only the salt becomes solid and precipitated salt particles are generated as in the case of vacuum evaporation.

【0012】このように,塩水噴霧で含塩氷粒子を生成
させるには,含塩ミストが低温空気中に適切に浮遊する
ことが必要であり,このミストの浮遊のためには低温空
気の「気流」が必要である。この気流を形成するには,
少なくとも90KPaの圧をもつ空気の流れを形成させ
るのがよい。最も好ましくは,スプレー塔内で90KP
a以上でマイナス10℃以下の空気の連続流れの上昇流
を形成し,この上昇流に塩水を噴霧するのがよい。すな
わち,この低温空気の上昇流中に含塩ミストを流動状態
で浮遊させると,それらが互いに接合して塩を含んだま
まの含塩氷粒子に成長し,その粒径が大きくなったもの
から自然落下するようになる。この場合の風速は6m/
sec 以上, 実際には10〜15m/sec 程度であるのが
よい。なお,特開平5−256547号公報に提案され
たように,空気の気流が存在しない真空または減圧雰囲
気中に塩水を噴霧したのでは,塩水中の水が雰囲気中に
直ちに蒸発し,また気流中にミストが浮遊するという現
象は起きないので,氷粒子の成長は殆んど起こらないと
考えられる。
As described above, in order to generate salt-containing ice particles by spraying with salt water, it is necessary that the salt-containing mist floats properly in the low-temperature air. Airflow is required. To create this airflow,
Preferably, a flow of air having a pressure of at least 90 KPa is formed. Most preferably, 90 KP in the spray tower
It is preferable to form an upward flow of a continuous flow of air having a temperature equal to or higher than a and equal to or lower than -10 ° C, and spraying the upward flow with brine. That is, when the salt-containing mist is suspended in a flowing state in the rising flow of low-temperature air, they are joined to each other and grow into salt-containing ice particles containing salt, and the particle size increases. Fall naturally. The wind speed in this case is 6m /
More than sec, in practice, it is preferably about 10 to 15 m / sec. If salt water is sprayed in a vacuum or reduced-pressure atmosphere where no air flow exists as proposed in Japanese Patent Application Laid-Open No. 5-25647, water in the salt water evaporates immediately into the atmosphere, and Since the phenomenon of mist floating does not occur, it is considered that ice particles hardly grow.

【0013】このような90KPa以上でマイナス10
℃以下,好ましくはマイナス20℃以下の低温空気流れ
を形成するには,連続的に取入れられる空気を順次圧縮
・冷却・膨張してこのような低温空気の流れに変えるの
がよい。フロン等の冷媒の凝縮・蒸発サイクルを利用し
た通常の冷凍機を用いて間接的に低温空気を製造する方
法では,マイナス10℃以下,さらには20℃以下の空
気流れを効率よく作ることは難しく,熱および動力消費
の点でも無駄が生ずることになる。
[0013] At 90 KPa or more, minus 10
In order to form a low-temperature air flow of not more than 0 ° C., preferably not more than −20 ° C., it is preferable that the continuously taken air is sequentially compressed, cooled and expanded to change into such a low-temperature air flow. In a method of indirectly producing low-temperature air using a normal refrigerator using a condensation / evaporation cycle of a refrigerant such as chlorofluorocarbon, it is difficult to efficiently create an air flow of -10 ° C or less, and even 20 ° C or less. , Heat and power consumption are also wasted.

【0014】以下,図面に示した本発明の実施の形態に
ついて説明する。
Hereinafter, embodiments of the present invention shown in the drawings will be described.

【0015】図1は,本発明法を実施する装置例を示し
たものであり,図示の含塩氷の製造装置は,スプレー塔
1と,低温空気製造装置2と,含塩氷のプレス機3とか
ら構成されており,低温空気製造装置2で製造された低
温空気は空気管路4を経てスプレー塔1に送り込まれ,
スプレー塔で生成した含塩氷粒子はスクリューコンベア
5でプレス機3に送り込まれる。
FIG. 1 shows an example of an apparatus for carrying out the method of the present invention. The apparatus for producing salted ice shown in the figure comprises a spray tower 1, a low-temperature air producing apparatus 2, and a press machine for salted ice. The low-temperature air produced by the low-temperature air producing device 2 is sent to the spray tower 1 through the air line 4 and
The salt-containing ice particles generated in the spray tower are sent to the press 3 by the screw conveyor 5.

【0016】スプレー塔1は,塔内の下方に空気吹出口
6を,上方に空気排出口7を有しており,塔内上部にス
プレーノズル8が設置してある。塔内底部の含塩氷粒子
受部9には,スクリューコンベア5の一端が気密に挿入
されている。
The spray tower 1 has an air outlet 6 in the lower part of the tower and an air outlet 7 in the upper part, and a spray nozzle 8 is installed in the upper part of the tower. One end of the screw conveyor 5 is hermetically inserted into the salt ice particle receiving portion 9 at the bottom of the tower.

【0017】スプレーノズル8には塩水が供給される
が,この塩水は,水槽10において淡水(水道水)に塩を
必要量添加することによって製造される。海水を使用す
ることもできるが,この場合には濾過・殺菌(滅菌)処
理をした上で,さらには脱臭処理した上で,水槽10に貯
える。図例の装置ではスプレーノズル8における塩水噴
霧を助成するために,超音波振動装置11を用いて塩水
に超音波を付与して噴霧するようにしてある。12は塩水
ポンプを表している。
Salt water is supplied to the spray nozzle 8. The salt water is produced by adding a required amount of salt to fresh water (tap water) in a water tank 10. Seawater can be used, but in this case, it is filtered, sterilized (sterilized), deodorized, and stored in the water tank 10. In the apparatus shown in the figure, in order to assist the spraying of salt water in the spray nozzle 8, an ultrasonic wave is applied to the salt water by using an ultrasonic vibration device 11 to spray the salt water. Reference numeral 12 denotes a salt water pump.

【0018】空気吹出口6は,ここから吹き出される低
温空気が一様に塔内を上昇するように,吐出口を上に向
けて且つスプレーノズル8から所定の距離をあけて,塔
内下方に設置されており,この空気の上昇流に向けて塩
水が噴霧されることにより,噴霧された塩水ミストはこ
の上昇流に乗って浮遊流動し,この低温空気中での浮遊
の間に径大の氷粒子に成長し,その成長の大きいものほ
ど上昇流に抗して下降し,塔底部の含塩氷粒子受部9に
落下する。図示しないが,スプレーノズル8と空気排出
口7との間には,ミストを捕集するためのエリミネータ
を取付けておくことができる。
The air outlet 6 is provided at a predetermined distance from the spray nozzle 8 with the discharge port facing upward so that the low-temperature air blown from the air outlet rises uniformly in the tower. When the salt water is sprayed toward this upward flow of air, the sprayed salt water mist floats on this upward flow, and has a large diameter during floating in the low-temperature air. Ice particles, and the larger the particles grow, the lower the particles against the upward flow and fall into the salt-containing ice particle receiving portion 9 at the bottom of the tower. Although not shown, an eliminator for collecting mist can be provided between the spray nozzle 8 and the air outlet 7.

【0019】このようにして,スプレー塔1内には90
KPa以上でマイナス10℃以下の低温空気の上昇流を
連続的に形成させるのであるが,この低温空気の連続流
れは低温空気製造装置2から管路4を経て空気吹出口6
に供給される。
In this manner, 90
An ascending flow of low-temperature air of not less than KPa and not more than -10 ° C. is continuously formed, and the continuous flow of the low-temperature air is supplied from the low-temperature air producing device 2 through the pipe 4 to the air outlet 6.
Supplied to

【0020】低温空気製造装置2は,動力源(図示の例
ではモーター)13に接続された一次圧縮機14を備えてお
り,この一次圧縮機14で得られた圧縮空気を,一次冷却
器15,二次圧縮機16,二次冷却器17,空気対空気熱交換
器18および膨張機19を順に経て低温空気を連続生産する
ものである。一次圧縮機14はモーター駆動のブースター
を使用できる。一次冷却器15と二次冷却器17は冷却水と
熱交換する空気対水熱交換器を使用できる。二次圧縮機
16と膨張機19は同軸回転する一体型の空気圧縮膨張装置
を利用できる。空気対空気熱交換器18は樹脂素材を熱伝
達板とした直交流型のものを使用できる。
The low-temperature air producing apparatus 2 includes a primary compressor 14 connected to a power source (motor in the illustrated example) 13. The compressed air obtained by the primary compressor 14 is converted into a primary cooler 15. , A secondary compressor 16, a secondary cooler 17, an air-to-air heat exchanger 18, and an expander 19 in order to continuously produce low-temperature air. The primary compressor 14 can use a motor-driven booster. The primary cooler 15 and the secondary cooler 17 can use an air-water heat exchanger that exchanges heat with the cooling water. Secondary compressor
16 and the expander 19 can utilize an integrated air compression and expansion device that rotates coaxially. As the air-to-air heat exchanger 18, a cross-flow type using a resin material as a heat transfer plate can be used.

【0021】いま,一次圧縮機14に100KPaで30
℃の空気を取入れて,100KPa・マイナス55℃の
低温空気流を製造する場合の各機器での空気処理状態を
説明すると,このほぼ常温常圧の空気を一次圧縮機14に
おいて140KPa・65℃の高圧高温空気とする。こ
の空気を一次冷却器15において冷却水と熱交換して14
0KPa・40℃としたうえ,二次圧縮機16において1
80KPa・70℃の高圧高温空気とする。この高圧高
温空気を二次冷却器17において冷却水で冷却して18
0KPa・40℃としたうえ,さらに空気対空気熱交換
器18において,スプレー塔1から戻ってくるマイナス3
0℃の戻り空気と熱交換することによって,180KP
a・マイナス20℃の高圧低温空気とし,これを膨張機
19に送り出して断熱膨張させることにより100KPa
・マイナス55℃の低温空気流を得る。
Now, the primary compressor 14 is set to 30 at 100 KPa.
A description will be given of the state of air treatment in each device when a low-temperature air flow of 100 KPa minus 55 ° C. is produced by taking in air at a temperature of 140 KPa · 65 ° C. in the primary compressor 14. Use high pressure and high temperature air. This air is heat-exchanged with cooling water in a primary cooler 15 to
0KPa ・ 40 ℃, and the secondary compressor 16
High pressure and high temperature air of 80 KPa and 70 ° C. This high-pressure high-temperature air is cooled by cooling water in the secondary
0 KPa · 40 ° C., and in the air-to-air heat exchanger 18, minus 3 returning from the spray tower 1
180 KP by heat exchange with return air at 0 ° C
a. High-pressure low-temperature air of minus 20 ° C, which is an expander
100 KPa by sending to 19 and adiabatic expansion
Obtain a low temperature air flow of minus 55 ° C.

【0022】この100KPa・マイナス55℃の低温
空気流は管路4を経てスプレー塔1内に供給され,スプ
レーノズル8から噴霧される塩水から含塩氷粒子を製造
するのに使用されたあと,空気排出口7および排気管路
20を経て100KPa・マイナス30℃の空気となって
低温空気製造装置2の空気対空気熱交換器18に入り,こ
こで,二次冷却器17を出た空気(180KPa・40
℃)と熱交換し,100KPaで30℃の空気となって
一次圧縮器14に戻る。図中の「In」は低温空気製造装
置への空気採取口を示しており,この空気採取口(I
n)はスプレー塔からの排気管路20に接続されている。
また図中の「Out」は低温空気製造装置から低温空気
を取り出す空気出口であり,この空気出口(Out)が
空気管路4を介してスプレー塔の空気吹出口6に連結さ
れている。
This low-temperature air flow of 100 KPa minus 55 ° C. is supplied through line 4 into the spray tower 1 and used to produce salted ice particles from the salt water sprayed from the spray nozzle 8. Air outlet 7 and exhaust pipe
After passing through 20, the air becomes 100 KPa · −30 ° C. and enters the air-to-air heat exchanger 18 of the low-temperature air producing apparatus 2, where the air (180 KPa · 40
C), and returns to the primary compressor 14 as air at 30 ° C. at 100 KPa. "In" in the figure indicates an air sampling port for the low-temperature air producing apparatus, and this air sampling port (I
n) is connected to an exhaust line 20 from the spray tower.
Further, “Out” in the figure is an air outlet for taking out low-temperature air from the low-temperature air producing device, and this air outlet (Out) is connected to the air outlet 6 of the spray tower via the air line 4.

【0023】この例では,低温空気製造装置2とスプレ
ー塔1とを空気の閉回路で連結してクローズド系に構成
し,スプレー塔1には100KPa・マイナス55℃の
低温空気流が連続供給され,スプレー塔1からは100
KPa・マイナス30℃の空気となって低温空気製造装
置2に戻るようにしたものであるが,運転中における系
内から外部に流出する空気を補うために,或いは装置始
動時の空気の装填のために,外気を系内に導入するさい
には,空気採取口(In)に通ずる管路に外気管路を接
続し,その外気取入口21にHEPAフイルタ22を取付け
ておき,大気中の塵埃や細菌類が系内に混入するのを防
止するのが望ましい。
In this example, the low-temperature air producing device 2 and the spray tower 1 are connected in a closed air system to form a closed system, and a low-temperature air flow of 100 KPa minus 55 ° C. is continuously supplied to the spray tower 1. , 100 from spray tower 1
Although it returns to the low-temperature air producing device 2 as KPa · −30 ° C. air, it is used to supplement the air flowing out of the system during operation or to charge the air when starting the device. Therefore, when introducing the outside air into the system, the outside air line is connected to the line leading to the air sampling port (In), and the HEPA filter 22 is attached to the outside air inlet 21, and the dust in the atmosphere is installed. It is desirable to prevent bacteria and bacteria from entering the system.

【0024】このようなほぼ常圧で極低温の空気流中に
塩水が噴霧されることにより瞬間的に塩水ミストは氷核
に相変化し,この氷核(1〜2mm以下の微細な氷粉・
スターダストに似ている)が所定の時間だけこの空気の
上昇流中に浮遊することによって互いに凝集または接合
しあって塩を含んだ含塩氷粒子に成長し,成長したもの
は受部9に落下して貯留する。次にこの捕集された含塩
氷粒子の処理について説明する。
When the salt water is sprayed into the cryogenic air stream at substantially normal pressure, the salt water mist instantaneously changes into an ice nucleus, and this ice nucleus (fine ice powder having a size of 1 to 2 mm or less) is formed.・
(Similar to stardust) floats in this upward flow of air for a predetermined period of time, and aggregates or joins with each other to grow into salt-containing ice particles containing salt. And store. Next, the treatment of the collected salted ice particles will be described.

【0025】スプレー塔1の塔外近傍には気密容器とし
ての氷貯蔵庫23が設けられており,この氷貯蔵庫23の内
部中段に氷プレス機3が設置されている。氷プレス機3
は,シリンダー24とピストン25とからなり,ピストン25
とは反対側のシリンダー壁に開閉扉26を設けた往復動式
プレス機である。この氷プレス機3と,スプレー塔底部
の受部9との間に,スクリューコンベア5が気密に懸け
渡されており,このスクリューコンベア5の駆動によっ
て受部9に溜まる含塩氷粒子を氷プレス機3内のシリン
ダー24内に送り込むようにしてある。すなわち,スプレ
ー塔1と氷プレス機のシリンダー24との間をスクリュー
コンベアの外筒で気密空間とし,この外筒内にスクリュ
ーを配置することによって,受部9の含塩氷粒子を受け
取り,これをスクリューコンベアの吐出端からシリンダ
ー24内に送り込めるようにしてある。含塩氷粒子をシリ
ンダー24内に送り込むときは開閉扉26を開けておき,シ
リンダー24内に含塩氷粒子が充填されたら開閉扉26を閉
じてピストン25で含塩氷粒子をプレスする。そのプレス
品は,シリンダー24の底部に設けた開閉弁27を開くこと
によって,シリンダー24内から氷貯蔵庫23の底部の貯留
部に落下させる。
An ice storage 23 as an airtight container is provided near the outside of the spray tower 1, and an ice press machine 3 is installed in the middle of the ice storage 23. Ice press 3
Consists of a cylinder 24 and a piston 25,
This is a reciprocating press in which an opening / closing door 26 is provided on the cylinder wall on the opposite side. A screw conveyor 5 is air-tightly suspended between the ice press machine 3 and a receiving portion 9 at the bottom of the spray tower, and the salt-contained ice particles accumulated in the receiving portion 9 by driving the screw conveyor 5 are ice-pressed. It is fed into a cylinder 24 in the machine 3. That is, an airtight space is formed between the spray tower 1 and the cylinder 24 of the ice press by an outer cylinder of a screw conveyor, and a screw is arranged in the outer cylinder to receive the salt-containing ice particles in the receiving portion 9 and to receive the ice-containing particles. Can be fed into the cylinder 24 from the discharge end of the screw conveyor. When the salt-containing ice particles are fed into the cylinder 24, the opening / closing door 26 is opened. When the salt-containing ice particles are filled in the cylinder 24, the door 26 is closed and the piston 25 presses the salt-containing ice particles. The pressed product is dropped from the inside of the cylinder 24 to the storage portion at the bottom of the ice storage 23 by opening the on-off valve 27 provided at the bottom of the cylinder 24.

【0026】この氷貯蔵庫23内はもとより,プレス機3
の内部およびスクリューコンベア5の内部も含塩氷の融
点以下の十分な低温に維持されねばならないが,この低
温の維持は,スプレー塔1の上部に設けた開口28と氷貯
蔵庫23の上部に設けた開口29とをブロア30を介装したダ
クト31で連結し,ブロア30の駆動によって,スプレー塔
1内を通過した低温空気の一部を氷貯蔵庫23内に送り込
むようにすればよい。氷プレス機3が氷貯蔵庫23に設置
され,且つ氷プレス機3とスプレー塔底部の受部9との
間がスクリューコンベア5で気密に連結されているの
で,その内部は低温空気が循環することになり,十分な
低温に維持される。
The ice storage 23 as well as the press 3
The inside of the screw conveyor 5 and the inside of the screw conveyor 5 must also be maintained at a sufficiently low temperature not higher than the melting point of salted ice, but this low temperature is maintained by the opening 28 provided at the upper part of the spray tower 1 and the upper part of the ice storage 23. The opening 29 may be connected to a duct 31 interposed with a blower 30, and a part of the low-temperature air that has passed through the spray tower 1 may be sent into the ice storage 23 by driving the blower 30. Since the ice press 3 is installed in the ice storage 23 and the screw press 5 is hermetically connected between the ice press 3 and the receiving portion 9 at the bottom of the spray tower, low-temperature air circulates inside. And maintained at a sufficiently low temperature.

【0027】以上説明したように,図1の設備によれば
含塩氷粒子が効率よく連続的に製造できるものである
が,図1のスプレー塔1と低温空気製造装置2とからな
る設備はさらなる応用として,食品や医薬品などの瞬間
冷凍にも適用可能である。すなわち,液状の食品や医薬
品を瞬間冷凍して粒子状とする場合,この設備によると
液中のミネラルや必要栄養素等を粒子中に歩留り良く残
留させることができる。この場合には,その処理品の種
類や量に応じてスプレー塔に供給する低温空気の温度や
風速を適切に制御すればよく,得られる固形粒子もプレ
ス以外の方法で必要な製品に区分けすることも可能であ
る。
As described above, according to the equipment of FIG. 1, salt-containing ice particles can be efficiently and continuously produced. However, the equipment comprising the spray tower 1 and the low-temperature air production apparatus 2 of FIG. As a further application, it can be applied to flash freezing of foods and pharmaceuticals. That is, when liquid foods and pharmaceuticals are flash-frozen into particles, this equipment allows minerals, necessary nutrients, and the like in the liquid to remain in the particles at a high yield. In this case, the temperature and wind speed of the low-temperature air supplied to the spray tower may be appropriately controlled according to the type and amount of the processed product, and the obtained solid particles are also classified into necessary products by a method other than pressing. It is also possible.

【0028】[0028]

【発明の効果】本発明によると,極低温空気の流れの中
に塩水を霧状で放出することにより微細な含塩氷核を生
成させ,これらを互いに集合して塩がその中に閉じ込め
られた粒径の大きな含塩氷粒子を得るものであるから,
均一に塩を含有した含塩氷を製造できる。そして,この
含塩氷粒子をプレス成形することによって,やはり塩を
均一に含有した含塩氷のプレス品が得られる。そして,
空気を圧縮・冷却・断熱膨張させて前記の低温空気を製
造することによって,連続的で且つ無菌の低温空気流を
得ることができるので,衛生的な含塩氷を効率良く且つ
安価に製造することができる。このため,陸上における
含塩氷の製造はもとより,船上での含塩氷の製造も行う
ことができ,保存中や搬送中での魚介類の鮮度維持はも
とより,遠洋漁業での鮮度維持に対しても大きく貢献で
きる。
According to the present invention, fine salt-containing ice nuclei are generated by discharging salt water in a cryogenic air stream in a mist state, and these are aggregated together to confine salt therein. To obtain salty ice particles with a large particle size.
Salt-containing ice containing salt uniformly can be produced. Then, by pressing the salt-containing ice particles, a pressed product of salt-containing ice, which also contains salt uniformly, is obtained. And
By producing the low-temperature air by compressing, cooling and adiabatic expansion of the air, a continuous and sterile low-temperature air flow can be obtained, so that sanitary salt-containing ice can be produced efficiently and at low cost. be able to. For this reason, salt ice can be produced not only on land but also on ships as well as on sea, and it can be used not only to maintain the freshness of seafood during storage and transportation, but also to maintain the freshness in pelagic fisheries. Can greatly contribute.

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

【図1】本発明に従う含塩氷の製造装置の例を示す略断
面図である。
FIG. 1 is a schematic sectional view showing an example of an apparatus for producing salted ice according to the present invention.

【符号の説明】[Explanation of symbols]

1 スプレー塔 2 低温空気製造装置 3 プレス機 4 空気管路 5 スクリューコンベア 6 空気吹出口 7 空気排出口 8 スプレーノズル 9 受部 14 一次圧縮機 15 一次冷却器 16 二次圧縮機 17 二次冷却器 18 空気対空気熱交換器 19 膨張機 23 氷貯蔵庫 In 低温空気製造装置への空気採取口 Out 低温空気製造装置からの空気出口 DESCRIPTION OF SYMBOLS 1 Spray tower 2 Low-temperature air production apparatus 3 Press machine 4 Air line 5 Screw conveyor 6 Air outlet 7 Air outlet 8 Spray nozzle 9 Receiving part 14 Primary compressor 15 Primary cooler 16 Secondary compressor 17 Secondary cooler 18 Air-to-air heat exchanger 19 Expander 23 Ice storage In Air inlet to cryogenic air generator Out Air outlet from cryogenic air generator

Claims (7)

【特許請求の範囲】[Claims] 【請求項1】 低温空気流中に塩水を噴霧して該低温空
気流中で氷核を生成させ,該氷核が含塩氷粒子にまで成
長または接合するまで該低温気流中に浮遊させ,ついで
該含塩氷粒子を空気流から分離捕集する含塩氷の製造
法。
1. A method of spraying salt water into a stream of cold air to generate ice nuclei in the stream of cold air, suspending the ice nuclei in the stream of cold ice until the ice nuclei grow or join to salt-containing ice particles, Then, a method for producing salted ice, wherein the salted ice particles are separated and collected from an air stream.
【請求項2】 低温空気流は圧力が90KPa以上で温
度がマイナス10℃以下であり,平均粒径が1mm以上
の含塩氷粒子を自重により自然落下させて該空気流から
分離捕集する請求項1に記載の含塩氷の製造法。
2. The low-temperature air stream has a pressure of 90 KPa or more and a temperature of -10 ° C. or less, and the salt-containing ice particles having an average particle diameter of 1 mm or more are naturally dropped by their own weight and separated and collected from the air stream. Item 10. The method for producing salted ice according to Item 1.
【請求項3】 下方に空気吹出口を上方に空気排出口を
もち,塔内上部に塩水を噴霧するためのスプレーノズル
を備えたスプレー塔と,氷点下の低温空気流を製造する
ための低温空気製造装置と,該スプレー塔の空気吹出口
に該低温空気製造装置で製造された低温空気を導く空気
管路と,からなる含塩氷の製造装置。
3. A spray tower having an air outlet below and an air outlet above and having a spray nozzle for spraying salt water in the upper part of the tower, and a low-temperature air for producing a low-temperature low-temperature air stream. An apparatus for producing salt ice, comprising: a production apparatus; and an air conduit for guiding the low-temperature air produced by the low-temperature air production apparatus to an air outlet of the spray tower.
【請求項4】 該低温空気製造装置が,空気の流れの順
に,一次圧縮機,一次冷却器,二次圧縮機,二次冷却
器,空気対空気熱交換器および膨張機を連結したもので
ある請求項3に記載の含塩氷の製造装置。
4. The low-temperature air producing apparatus is constructed by connecting a primary compressor, a primary cooler, a secondary compressor, a secondary cooler, an air-to-air heat exchanger, and an expander in the order of air flow. The apparatus for producing salted ice according to claim 3.
【請求項5】 該スプレー塔はその底部に氷粒子の受部
を有し,この氷粒子の受部内に一端が連結し,他端が塔
外の容器内に連結する氷粒子の移送手段を備えた請求項
3または4に記載の含塩氷の製造装置。
5. The spray tower has an ice particle receiving portion at the bottom thereof, one end of which is connected to the ice particle receiving portion and the other end of which is connected to a container outside the tower. The apparatus for producing salted ice according to claim 3 or 4, further comprising:
【請求項6】 塔外の容器内には氷プレス機が設置さ
れ,この氷プレス機に該移送手段の吐出端が連結されて
いる請求項5に記載の含塩氷の製造装置。
6. The apparatus for producing salted ice according to claim 5, wherein an ice press is installed in a container outside the tower, and the discharge end of the transfer means is connected to the ice press.
【請求項7】 低温空気製造装置は,空気採取口と空気
出口を備え,その空気採取口はHEPAフイルタを介し
て外気取入口に接続されると共にスプレー塔の空気排出
口にも接続され,その空気出口は空気管路を介してスプ
レー塔の空気吹出口に接続されている請求項4に記載の
含塩氷の製造装置。
7. The low-temperature air producing apparatus has an air sampling port and an air outlet, and the air sampling port is connected to an outside air inlet via a HEPA filter and to an air outlet of a spray tower. The apparatus for producing salted ice according to claim 4, wherein the air outlet is connected to an air outlet of the spray tower via an air pipe.
JP2000254120A 2000-08-24 2000-08-24 Salt ice production equipment Expired - Fee Related JP3410068B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000254120A JP3410068B2 (en) 2000-08-24 2000-08-24 Salt ice production equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000254120A JP3410068B2 (en) 2000-08-24 2000-08-24 Salt ice production equipment

Publications (2)

Publication Number Publication Date
JP2002071247A true JP2002071247A (en) 2002-03-08
JP3410068B2 JP3410068B2 (en) 2003-05-26

Family

ID=18743121

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP3410068B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009544928A (en) * 2006-07-24 2009-12-17 エム. エニス,ベン Desalination system and desalination system using continuous spiral slush recovery system
JP6482691B1 (en) * 2017-11-09 2019-03-13 チュン コー ジェームズ Production equipment for fine ice containing salt
JP2020016427A (en) * 2018-07-25 2020-01-30 チュン コー ジェームズ Apparatus for making fine ice with salinity

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009544928A (en) * 2006-07-24 2009-12-17 エム. エニス,ベン Desalination system and desalination system using continuous spiral slush recovery system
JP6482691B1 (en) * 2017-11-09 2019-03-13 チュン コー ジェームズ Production equipment for fine ice containing salt
EP3483532A1 (en) * 2017-11-09 2019-05-15 James Chun Koh Apparatus for manufacturing powdered ice with salinity
KR20190053065A (en) * 2017-11-09 2019-05-17 제임스 천 고 Apparatus for manufacturing powdered ice with salinity
CN109764587A (en) * 2017-11-09 2019-05-17 J·C·高 Equipment for manufacturing the powdered ice with salinity
KR102115350B1 (en) * 2017-11-09 2020-05-26 제임스 천 고 Apparatus for manufacturing powdered ice with salinity
CN109764587B (en) * 2017-11-09 2022-03-01 J·C·高 Apparatus for manufacturing powdery ice having salinity
JP2020016427A (en) * 2018-07-25 2020-01-30 チュン コー ジェームズ Apparatus for making fine ice with salinity

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