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JPH0636841B2 - Pressurized freeze concentrator - Google Patents
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JPH0636841B2 - Pressurized freeze concentrator - Google Patents

Pressurized freeze concentrator

Info

Publication number
JPH0636841B2
JPH0636841B2 JP7950090A JP7950090A JPH0636841B2 JP H0636841 B2 JPH0636841 B2 JP H0636841B2 JP 7950090 A JP7950090 A JP 7950090A JP 7950090 A JP7950090 A JP 7950090A JP H0636841 B2 JPH0636841 B2 JP H0636841B2
Authority
JP
Japan
Prior art keywords
cylinder
ice crystals
cooling
mother liquor
solute
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP7950090A
Other languages
Japanese (ja)
Other versions
JPH03278801A (en
Inventor
隆 太田
順 一岡
靖之 鈴木
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.)
TOYO. SS. CO., LTD.
Original Assignee
TOYO. SS. 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 TOYO. SS. CO., LTD. filed Critical TOYO. SS. CO., LTD.
Priority to JP7950090A priority Critical patent/JPH0636841B2/en
Publication of JPH03278801A publication Critical patent/JPH03278801A/en
Publication of JPH0636841B2 publication Critical patent/JPH0636841B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は各種の飲料液や薬液等の水を溶媒とする水溶液
から溶質濃度の高い濃縮液を製造するための加圧式凍結
濃縮装置に関する。
TECHNICAL FIELD The present invention relates to a pressurization type freeze concentration apparatus for producing a concentrated solution having a high solute concentration from an aqueous solution containing water such as various beverages and chemicals as a solvent.

[従来技術] 溶質と溶媒(水)とからなる溶液を一旦凍結せしめて氷
晶となし、さらにこの氷晶を加圧、加温することにより
氷晶中から溶質濃度の高い溶液を分離して濃縮液を製造
するいわゆる加圧式凍結濃縮装置は従前より知られてい
る。
[Prior Art] A solution consisting of a solute and a solvent (water) is once frozen to form an ice crystal, and the ice crystal is pressurized and heated to separate a solution having a high solute concentration from the ice crystal. So-called pressure-type freeze concentrators for producing concentrated liquids have been known for some time.

こうした装置では、溶液の凝固点が溶媒(水)に対する
溶質濃度及び溶液に加わる圧力によって変化する物理現
象を利用している。
Such a device utilizes a physical phenomenon in which the freezing point of a solution changes depending on the concentration of a solute with respect to a solvent (water) and the pressure applied to the solution.

すなわち、水溶液では加わる圧力が高いほど、また水溶
液中に含まれる溶質の濃度が高いほど凝固点が降下する
物性を利用している。
That is, the physical properties are used in which the freezing point is lowered as the pressure applied to the aqueous solution is higher and the concentration of the solute contained in the aqueous solution is higher.

こうした原理を利用した従前の装置の概系統図を第2図
に示す。
FIG. 2 shows a schematic system diagram of a conventional device using such a principle.

同図において、ポンプ3により母液用容器2に注入され
た原料液1は冷却用シリンダ4に自然落下する。
In the figure, the raw material liquid 1 injected into the mother liquor container 2 by the pump 3 naturally drops into the cooling cylinder 4.

この冷却用シリンダ4内の原料液は、シリンダ外周のジ
ャケット6へ流入口7から入り、流出口8から排出され
る冷却用媒体9により冷却され、凍結して氷晶26とな
る。
The raw material liquid in the cooling cylinder 4 enters the jacket 6 on the outer periphery of the cylinder from the inflow port 7 and is cooled by the cooling medium 9 discharged from the outflow port 8 to be frozen and become ice crystals 26.

この氷晶26が牽引体23によりシリンダ内を下方へ牽引さ
れ、下部が狭窄したテーパー孔を有する加圧筒13に圧入
される。
The ice crystals 26 are pulled downward in the cylinder by the pulling body 23, and are pressed into the pressure cylinder 13 having a tapered hole with a narrowed lower portion.

この加圧筒13に設けたジャケット15へ流入口16から入
り、流出口17から排出される冷却用媒体18(前記冷却媒
体9より温度の高い)により氷晶26の表面が加温され、
氷晶26の表面硬は若干軟化し、また氷晶26はより加圧さ
れる。
The surface of the ice crystals 26 is heated by the cooling medium 18 (having a higher temperature than the cooling medium 9) that enters the jacket 15 provided in the pressurizing cylinder 13 through the inflow port 16 and is discharged through the outflow port 17.
The surface hardness of the ice crystals 26 is slightly softened, and the ice crystals 26 are pressed more.

この加圧により氷晶26中の濃度のより高い溶質部分が氷
晶26より分離して、氷晶中の圧力の低い部分、すなわち
上部へと移動し、ポケット19を経て排出パイプ20から濃
縮液27として流出する。
By this pressurization, the solute portion having a higher concentration in the ice crystal 26 is separated from the ice crystal 26 and moved to the portion having a lower pressure in the ice crystal, that is, to the upper portion, and the concentrated liquid is discharged from the discharge pipe 20 via the pocket 19. Spill as 27.

しかし上記の装置では、原料液1を凍結させながら通過
させる冷却シリンダ4の内筒5は内径が均一な縦長構造
であり、しかも冷却用ジャケット6がその内筒5周囲を
取り巻くように設けられていることにより、原料液中の
内筒壁面近傍部分にあり、しかも溶質濃度のより低い部
分が早く凍結することになる。
However, in the above apparatus, the inner cylinder 5 of the cooling cylinder 4 that allows the raw material liquid 1 to pass while being frozen has a vertically long structure with a uniform inner diameter, and the cooling jacket 6 is provided so as to surround the inner cylinder 5. As a result, the portion in the vicinity of the wall surface of the inner cylinder in the raw material liquid, which has a lower solute concentration, freezes faster.

この結果、氷晶26全体の結氷硬度にむらが発生し、牽引
体23近傍ほどその結氷硬度が低いうえに溶質濃度も周辺
部より高い氷結晶ができる。
As a result, the ice hardness of the entire ice crystal 26 becomes uneven, and the ice hardness is lower near the traction body 23 and the solute concentration is higher than that of the peripheral portion.

こうして生成された氷晶26を牽引体23で牽引して加圧筒
13に圧入し、加圧すると、溶質濃度が高く、しかも結氷
硬度の低い牽引体23近傍の氷晶がより早く融解し、融解
した溶質濃度の高い液が槽22に漏出してしまうことにな
る。
The ice crystals 26 generated in this way are towed by the tow body 23 and pressed.
When pressed into 13 and pressurized, the ice crystals near the traction body 23, which has a high solute concentration and low freezing hardness, will melt more quickly, and the melted liquid with a high solute concentration will leak into the tank 22. .

[本発明の目的] 以上に鑑み、本発明では溶質を含む原料液を冷却用シリ
ンダにて凍結せしめて氷晶を生成させる際に、その氷晶
全体の結氷硬度分布を均一ならしめるとともに氷晶内の
溶質濃度分布をも均一にならしめるようにし、加圧筒に
圧入させられる氷晶の融解が氷晶全体で等しく進行する
ようにし、溶質濃度が均一にして高い濃縮液が得られる
加圧式凍結濃縮装置を提供できるようにした。
[Object of the Present Invention] In view of the above, in the present invention, when a raw material solution containing a solute is frozen in a cooling cylinder to generate ice crystals, the ice crystals are made uniform in ice hardness distribution and the ice crystals are made uniform. In order to evenly distribute the solute concentration in the inside of the pressurizing cylinder, the melting of the ice crystals that are pressed into the pressurizing cylinder proceeds equally throughout the ice crystals, and the solute concentration is made uniform so that a high concentrated solution can be obtained. A freeze concentration device can be provided.

[課題を解決するための手段] 上記の課題を解決するために、本発明の加圧式凍結濃縮
装置は、上部に母液容器を有する垂直な冷却用シリンダ
の下部に、下細りのテーパー孔を有する加圧筒を断熱筒
体を介して接続し、前記テーパー孔上部に濃縮液回収用
の排出パイプを接続し、前記冷却用シリンダ内で結氷し
た氷晶を牽引するエンドレスな抗張線材を前記母液容
器、シリンダ内、断熱筒体内、加圧筒内を上部から下方
に向かって回送されるように設け、しかも前記冷却用シ
リンダ内の母液中に圧搾空気送出管の先端を開口せしめ
た構造のものとしてある。
[Means for Solving the Problems] In order to solve the above problems, a pressurization type freeze concentration apparatus of the present invention has a tapered taper hole in a lower portion of a vertical cooling cylinder having a mother liquor container in an upper portion. A pressurizing cylinder is connected through a heat insulating cylinder, a discharge pipe for collecting a concentrated liquid is connected to the upper part of the tapered hole, and an endless tensile wire that pulls ice crystals frozen in the cooling cylinder is connected to the mother liquor. A structure in which a container, a cylinder, a heat insulating cylinder, and a pressurizing cylinder are provided so as to be circulated downward from the upper portion, and the compressed air delivery pipe has an open end in the mother liquor in the cooling cylinder. There is.

[作用] 冷却用シリンダ内で母液容器から供給される原料液が冷
却により凍結させられる際に、その凍結しつつある原料
液中に圧搾空気送出管で圧搾空気が供給される。この圧
搾空気が供給されることにより母液中には無数の気泡が
発生し、この気泡によって母液は撹拌させられ、凍結前
のシリンダ内の母液は濃度分布が均一なものになる。
[Operation] When the raw material liquid supplied from the mother liquor container is frozen in the cooling cylinder by cooling, compressed air is supplied to the frozen raw material liquid by the compressed air delivery pipe. By supplying this compressed air, innumerable bubbles are generated in the mother liquor, the mother liquor is agitated by the bubbles, and the mother liquor in the cylinder before freezing has a uniform concentration distribution.

したがってシリンダ内で凍結させられた氷晶は濃度分布
が均一なものになっており、加圧筒により加圧されるこ
とによって氷晶中から分離する溶質分は均一なものとな
り、均一な濃度の濃縮液が得られる。
Therefore, the ice crystals frozen in the cylinder have a uniform concentration distribution, and the solute separated from the ice crystals by pressing with the pressurizing cylinder becomes uniform, and the concentration of the solute is uniform. A concentrate is obtained.

[実施例] 以下本発明の実施例を第1図を用いて詳細に説明する。
なお従来例と同一物には同一符号を付してある。
[Embodiment] An embodiment of the present invention will be described in detail below with reference to FIG.
The same components as those in the conventional example are designated by the same reference numerals.

第1図は本実施例の縦断面系統図であり、同図において
果汁等の溶質を溶かし込んだ溶液である原料液1を一時
的に蓄える母液用容器2があり、この容器2上には前記
原料液1がポンプ3から供給される。また、容器2の下
部には垂直な冷却用シリンダ4を接続してあり、このシ
リンダ4の内筒5を取り巻くようにジャケット6を設け
てある。しかしてこのジャケット6には図示しないポン
プにより冷却用媒体9が注入させられ、このジャケット
6内を通過した冷却用媒体9は流出口8より排出するよ
うになっている。
FIG. 1 is a longitudinal cross-sectional system diagram of the present embodiment. In FIG. 1, there is a mother liquor container 2 for temporarily storing a raw material liquid 1 which is a solution in which a solute such as fruit juice is dissolved. The raw material liquid 1 is supplied from a pump 3. Further, a vertical cooling cylinder 4 is connected to the lower portion of the container 2, and a jacket 6 is provided so as to surround the inner cylinder 5 of the cylinder 4. The cooling medium 9 is injected into the jacket 6 by a pump (not shown), and the cooling medium 9 passing through the jacket 6 is discharged from the outflow port 8.

前記冷却用シリンダ4下部に形成したフランジ10には内
径がシリンダ4の内筒5と同径な輪状の断熱体11を接続
してあり、さらにこの断熱体11下部には加圧筒13の上部
に設けたフランジ12を接続せしめてある。
A ring-shaped heat insulator 11 having an inner diameter equal to that of the inner cylinder 5 of the cylinder 4 is connected to the flange 10 formed in the lower portion of the cooling cylinder 4. Further, below the heat insulator 11 is an upper portion of the pressure cylinder 13. The flange 12 provided in the is connected.

この加圧筒13の内筒14は下細りのテーパー孔を有してお
り、しかもこの内筒14を取り巻くようにジャケット15を
内設してある。このジャケット15には下部に流入口16
が、上部に流出口17がそれぞれ設けてあり、この流入口
16より第2冷却用媒体18が図示しないポンプで注入させ
られ、さらにジャケット15内を通った媒体18は流出口17
より排出させられるようになっている。
The inner cylinder 14 of the pressure cylinder 13 has a tapered taper hole, and a jacket 15 is provided so as to surround the inner cylinder 14. This jacket 15 has an inlet 16 at the bottom.
However, there are outlets 17 at the top, and this inlet
The second cooling medium 18 is injected from a 16 by a pump (not shown), and the medium 18 passing through the jacket 15 is discharged from the outlet 17
It is designed to be discharged more.

また、加圧内筒14の上端部には液溜め用の凹みポケット
19を設けてあり、このポケット19には液排出用パイプ20
を接続せしめてある。
In addition, the upper end of the pressurizing inner cylinder 14 has a recess pocket for storing liquid.
19 is provided, and a liquid discharge pipe 20 is provided in this pocket 19.
Is connected.

さらに加圧筒13の下部フランジ21には処理済氷晶受け用
の槽22を接続してある。
Further, a tank 22 for receiving treated ice crystals is connected to the lower flange 21 of the pressure cylinder 13.

上記した冷却用シリンダ4、断熱体11及び加圧筒13内に
は、その中心軸線を通るように氷晶牽引用の抗張線材で
あるエンドレスな鎖23を上下方向に貫通せしめて設けて
あり、鎖23は図示を省略した駆動装置により下降回送さ
せられるようにしてある。
An endless chain 23, which is a tensile wire for pulling ice crystals, is provided in the cooling cylinder 4, the heat insulating body 11 and the pressurizing cylinder 13 so as to pass through the central axis of the cooling cylinder 4 in the vertical direction. The chain 23 is designed to be lowered and fed by a driving device (not shown).

また、前記冷却用シリンダ4の内筒5上部内には圧搾空
気供給管24を母液用容器2上方より挿入してあり、この
空気供給管24は図示しないコンプレッサに接続してあっ
て、圧搾空気25が内筒5内に噴出させられるようにして
ある。
Further, a compressed air supply pipe 24 is inserted into the upper part of the inner cylinder 5 of the cooling cylinder 4 from above the mother liquor container 2, and the air supply pipe 24 is connected to a compressor (not shown) to provide compressed air. 25 is ejected into the inner cylinder 5.

次ぎに各機能について以下詳述する。Next, each function will be described in detail below.

ポンプ3で容器2に注ぎ込まれた原料液1は、この容器
2に一時的に蓄えられ、冷却用シリンダ4の内筒5内に
落下する。この冷却用シリンダ4内のジャケット6を循
環している冷却用媒体9は−20℃前後の冷却温度であ
り、原料液1はこの冷却用媒体にて冷却され、凍結して
氷晶26となる。
The raw material liquid 1 poured into the container 2 by the pump 3 is temporarily stored in the container 2 and drops into the inner cylinder 5 of the cooling cylinder 4. The cooling medium 9 circulating in the jacket 6 in the cooling cylinder 4 has a cooling temperature of about -20 ° C., and the raw material liquid 1 is cooled by this cooling medium and frozen to form ice crystals 26. .

また、この氷晶26と原料液1の液体が混在する内筒5上
部に挿入された空気送出管24より噴出する圧搾空気によ
り原料液1が撹拌され、ために溶質濃度分布にむらの無
い氷晶26ができる。
Further, the raw material liquid 1 is agitated by the compressed air ejected from the air delivery pipe 24 inserted in the upper portion of the inner cylinder 5 in which the ice crystals 26 and the liquid of the raw material liquid 1 are mixed, so that the solute concentration distribution is uniform in ice. Crystal 26 is formed.

氷晶26は鎖23に凍結しているため、鎖23に引かれて加圧
筒13に圧入される。
Since the ice crystals 26 are frozen in the chain 23, they are attracted by the chain 23 and pressed into the pressure cylinder 13.

この加圧筒13のジャケット15を循環している第2冷却溶
媒体18は2〜3℃であるため氷晶26の外周面は若干軟化
され、また内筒14のテーパー孔により加圧されることに
より氷点が低下し、ために氷晶中の溶質分が分離され
て、濃縮液27として加圧力の小なるテーパー孔の上部へ
移動する。
Since the temperature of the second cooling solvent body 18 circulating in the jacket 15 of the pressurizing cylinder 13 is 2 to 3 ° C., the outer peripheral surface of the ice crystal 26 is slightly softened and is pressurized by the taper hole of the inner cylinder 14. This lowers the freezing point, so that the solute in the ice crystals is separated and moves as the concentrated liquid 27 to the upper part of the tapered hole where the pressing force is small.

この濃縮液27は排出用パイプ20で図示しない製品貯蔵タ
ンクに排出され、濃縮液27が分離された残存氷晶26は加
圧筒13下の槽22に落下する。
The concentrated liquid 27 is discharged to a product storage tank (not shown) through the discharge pipe 20, and the residual ice crystals 26 from which the concentrated liquid 27 is separated fall into the tank 22 below the pressurizing cylinder 13.

このように原料液1には氷晶26となる前に圧搾空気が噴
出せしめられることによって母液が撹拌され、凍結する
ため氷晶26中の溶質濃度分布が均一になるとともに、氷
晶26の結氷硬度分布も均一なものとなる。したがって加
圧筒13内で加圧される氷晶は良好に半融解し溶質を多く
含む濃縮液27が効率よく分離せしめることとなる。
In this way, the compressed air is blown into the raw material liquid 1 before it becomes ice crystals 26, whereby the mother liquor is agitated and freezes, so that the solute concentration distribution in the ice crystals 26 becomes uniform and the ice crystals 26 become frozen. The hardness distribution is also uniform. Therefore, the ice crystals pressurized in the pressurizing cylinder 13 satisfactorily semi-melt and the concentrated liquid 27 containing a large amount of solute can be efficiently separated.

[発明の効果] 上述したごとく、本発明によれば凍結前の原料液は圧搾
空気によって撹拌されて濃度分布が均一になり、ムラの
ない濃度の氷晶が生成される。
[Effects of the Invention] As described above, according to the present invention, the raw material liquid before freezing is agitated by compressed air to have a uniform concentration distribution, and ice crystals having a uniform concentration are generated.

したがって、加圧により分離される溶質分も濃度ムラが
なく、均一な濃度の濃縮液を得ることができる。
Therefore, the concentration of the solute separated by the pressurization is not uneven, and a concentrated liquid having a uniform concentration can be obtained.

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

第1図は本発明の実施例を示す系統断面図、第2図は従
来例の系統断面図である。 図中 1……原料液、2……母液用容器 3……ポンプ、4……冷却用シリンダ 5……内筒、6……ジャケット 7……流入口、8……流出口 9……冷却用媒体、10……フランジ 11……断熱筒体、12……フランジ 13……加圧筒、14……加圧内筒 15……ジャケット、16……流入口 17……流出口、18……第2冷却用媒体 19……凹みポケット、20……排出用パイプ 21……下部シリンダ、22……槽 23……鎖、24……圧搾空気送出管 25……圧搾空気、26……氷晶 27……濃縮液
FIG. 1 is a system sectional view showing an embodiment of the present invention, and FIG. 2 is a system sectional view of a conventional example. In the figure 1 ... Raw material liquid, 2 ... Mother liquor container 3 ... Pump, 4 ... Cooling cylinder 5 ... Inner cylinder, 6 ... Jacket 7 ... Inlet, 8 ... Outlet 9 ... Cooling Medium, 10 …… Flange 11 …… Insulation cylinder, 12 …… Flange 13 …… Pressure cylinder, 14 …… Pressure inner cylinder 15 …… Jacket, 16 …… Inflow port 17 …… Outflow port, 18… … Second cooling medium 19 …… Recessed pocket, 20 …… Discharge pipe 21 …… Lower cylinder, 22 …… Bath 23 …… Chain, 24 …… Compressed air delivery pipe 25 …… Compressed air, 26 …… Ice Crystal 27 ... Concentrated liquid

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】上部に母液容器を有する垂直な冷却用シリ
ンダの下部に、下細りのテーパー孔を有する加圧筒を断
熱筒体を介して接続し、前記テーパー孔上部に濃縮液回
収用の排出パイプを接続し、前記冷却用シリンダ内で結
氷した氷晶を牽引するエンドレスな抗張線材を前記母液
容器、シリンダ内、断熱筒体内、加圧筒内を上部から下
方に向かって回送されるように設け、しかも圧縮機に接
続した圧搾空気送出管の先端を前記冷却用シリンダの上
部内へ開口せしめてなる加圧式凍結濃縮装置。
1. A vertical cooling cylinder having a mother liquor container on an upper part thereof is connected to a lower part of a pressurizing cylinder having a tapered taper hole through a heat insulating cylinder, and an upper part of the tapered hole for collecting a concentrated liquid is collected. An endless tensile wire that connects an exhaust pipe and draws ice crystals frozen in the cooling cylinder is circulated downward from the upper part through the mother liquor container, the cylinder, the heat insulating cylinder, and the pressurizing cylinder. Pressurized freezing and concentrating device in which the tip of the compressed air delivery pipe connected to the compressor is opened into the upper part of the cooling cylinder.
JP7950090A 1990-03-27 1990-03-27 Pressurized freeze concentrator Expired - Lifetime JPH0636841B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7950090A JPH0636841B2 (en) 1990-03-27 1990-03-27 Pressurized freeze concentrator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7950090A JPH0636841B2 (en) 1990-03-27 1990-03-27 Pressurized freeze concentrator

Publications (2)

Publication Number Publication Date
JPH03278801A JPH03278801A (en) 1991-12-10
JPH0636841B2 true JPH0636841B2 (en) 1994-05-18

Family

ID=13691649

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7950090A Expired - Lifetime JPH0636841B2 (en) 1990-03-27 1990-03-27 Pressurized freeze concentrator

Country Status (1)

Country Link
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