JPH02265624A - Dehydrating process and device - Google Patents

Dehydrating process and device

Info

Publication number
JPH02265624A
JPH02265624A JP1085332A JP8533289A JPH02265624A JP H02265624 A JPH02265624 A JP H02265624A JP 1085332 A JP1085332 A JP 1085332A JP 8533289 A JP8533289 A JP 8533289A JP H02265624 A JPH02265624 A JP H02265624A
Authority
JP
Japan
Prior art keywords
solution
water
dehydrated
membrane
osmotic pressure
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.)
Pending
Application number
JP1085332A
Other languages
Japanese (ja)
Inventor
Yoshihisa Ito
伊東 良久
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP1085332A priority Critical patent/JPH02265624A/en
Publication of JPH02265624A publication Critical patent/JPH02265624A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To dehydrate efficiently by bringing a material to be dehydrated into contact with concentrated solution of salt water, sugared water or the like through a film and dehydrating by means of osmotic pressure. CONSTITUTION:When a material 1 to be dehydrated is brought into contact with concentrated solution 3 of salt water, sugared water or the like through a film 2, the water content of the material 1 to be dehydrated is transferred into solution 3 by means of osmotic pressure. The pressure of solution 3 is risen by a pressurizing pump 4 and water content 6 is so prepared and concentrated by a reverse osmosis film 5 as to control the solution 3 so as to retain almost constant high concentration. Dehydration of high efficiency can be carried out effectively by said process, not by mechanical compression.

Description

【発明の詳細な説明】 この発明は1例えば鮮魚や生野菜などの含水固形物や、
汚泥などの含水スラッジ等を、高能率で効果的に脱水す
る。方法と装置とに係わるものである。
[Detailed Description of the Invention] This invention provides 1. water-containing solids such as fresh fish and raw vegetables;
Water-containing sludge such as sludge is effectively dehydrated with high efficiency. The present invention relates to a method and an apparatus.

鮮魚などの含水固形物や汚泥などの含水スラジを、天日
乾燥や加熱や冷凍などの方法によらず常温下で脱水する
際に1機械的な圧縮による方法では不都合な場合が多い
。即ち、前者(鮮魚など)の場合には商品価値の点で圧
縮加工が不適なことは言うまでもないが、いずれの場合
も、圧縮によって粒子が圧密化されて水分の流路が狭め
られるので、一般的には加圧力を高めてもその割には脱
水効果が上がらない。
When dehydrating water-containing solids such as fresh fish or water-containing sludge such as sludge at room temperature without using methods such as solar drying, heating, or freezing, mechanical compression is often inconvenient. In other words, in the case of the former (fresh fish, etc.), it goes without saying that compression processing is inappropriate in terms of commercial value, but in both cases, compression densifies the particles and narrows the water flow path, so it is generally Specifically, even if the pressure is increased, the dehydration effect does not increase accordingly.

以上に鑑み本発明は、上記のような対象物を常温下で脱
水する場合に9機械的な圧縮によらず。
In view of the above, the present invention does not rely on mechanical compression when dehydrating the above objects at room temperature.

被脱水物を高濃度に維持した溶液と膜を介して接触せし
め、この際に生ずる浸透圧を利用して効果的に脱水する
方法と装置とを提供するもので、以下図面によりさらに
詳細に説明する。
The present invention provides a method and apparatus for effectively dehydrating a material to be dehydrated by bringing it into contact with a solution maintained at a high concentration through a membrane and utilizing the osmotic pressure generated at this time, which will be explained in more detail with reference to the drawings below. do.

第1図は本発明の詳細な説明する原理図、第2図及び第
3図は鮮魚等の含水固形物を脱水する場合の実施例の説
明図、第4図第5図第6図は汚泥などの含水スラジを脱
水する場合の実施例の説明図、をそれぞれ示す。
Figure 1 is a diagram explaining the principle of the present invention in detail, Figures 2 and 3 are explanatory diagrams of an embodiment for dehydrating water-containing solids such as fresh fish, Figure 4, Figure 5, and Figure 6 are sludge. An explanatory view of an example in which water-containing sludge such as the following is dehydrated is shown, respectively.

第1図に於て、被脱水物1を膜2を介して塩水や砂糖水
などの)n原溶液3と接触せしめると、被脱水物1の水
分は浸透圧により溶wI3に移動するが、この際、被脱
水物1においては機械的圧密がほとんど生じないので、
優れた脱水効果が得られる。この脱水により溶[3は希
釈されるが、これを加圧ポンプ4で昇圧させ逆浸透膜5
により水分6を分離濃縮して、溶液3が常にほぼ一定の
高濃度を保つように制御する。被脱水物1を脱水する4
(B進方は浸透圧によって生ずるのであるが、該浸透圧
は溶液の濃度差に比例するので1以上のように常に濃厚
な溶液濃度を保つことによって効果的な脱水が行えるの
である。
In FIG. 1, when the dehydrated material 1 is brought into contact with the raw solution 3 (such as salt water or sugar water) through the membrane 2, the water in the dehydrated material 1 moves to the solution wI3 due to osmotic pressure. At this time, since almost no mechanical compaction occurs in the material to be dehydrated 1,
Excellent dehydration effect can be obtained. This dehydration dilutes the solution [3], which is then pressurized by a pressure pump 4 and transferred to a reverse osmosis membrane 5.
The water 6 is separated and concentrated, and the solution 3 is controlled to always maintain a substantially constant high concentration. Dehydrating the object to be dehydrated 1 4
(The progress of B is caused by osmotic pressure, and since osmotic pressure is proportional to the difference in concentration of the solution, effective dehydration can be achieved by always maintaining a concentrated solution concentration of 1 or more.

次に鮮魚などの脱水例に就いて第2図及び第3図で説明
する。洗浄した魚1°を包装機7により膜2゛で密封包
装した後、液槽8に供給する。該液槽8には、内部にコ
ンベア9を備え且つ塩水や砂糖水などの溶液3°を満た
しておき、またコンベア速度は所期の脱水率が得られる
滞留時間に見合って設定しておく。なお、浸透作用を鮮
魚1゜の全表面で有効に作用させる為に、鮮魚l° と
膜2°との間に空気が入らぬよう、包装機7は真空包装
にするとよい。以上により、浸透圧の作用で鮮魚1゛は
脱水されるが、浸出水で希釈された溶液3°は、常時加
圧ポンプ4°で昇圧させて逆浸透膜5゛によって水分6
°を分離濃縮し、液槽8に戻す。図中10は流量調整弁
を示す。以上の構成によって、溶液3′を常に一定の濃
厚な濃度に保つことにより、高く安定した浸透圧が維持
されるから、鮮魚などの効果的な脱水が連続的に行われ
る。
Next, an example of dehydration of fresh fish will be explained with reference to FIGS. 2 and 3. The cleaned fish 1° is sealed and packaged with a membrane 2° by a packaging machine 7 and then supplied to a liquid tank 8. The liquid tank 8 is equipped with a conveyor 9 and filled with 3° of a solution such as salt water or sugar water, and the conveyor speed is set in accordance with the residence time to obtain the desired dehydration rate. In order to effectively effect the osmotic action on the entire surface of the fresh fish 1°, the packaging machine 7 is preferably vacuum packed so that air does not enter between the fresh fish 1° and the membrane 2°. As described above, 1゜ fresh fish is dehydrated by the action of osmotic pressure, but the solution 3゜ diluted with leachate is constantly pressurized with a pressure pump 4゜ and water is 6゜ through a reverse osmosis membrane 5゜.
The liquid is separated and concentrated and returned to the liquid tank 8. In the figure, 10 indicates a flow rate regulating valve. With the above configuration, by always keeping the solution 3' at a constant concentration, a high and stable osmotic pressure is maintained, so that effective dehydration of fresh fish etc. is continuously performed.

次に汚泥などの含水スラジの脱水例に就い゛CC第4図
竿第5(第4図のX−x断面図)、及び第6図(第5図
のY部詳細図)で説明する。本脱水機は、内部に塩水や
砂糖水などの溶液3”を満たし且つ外周を多孔体11で
構成した回転円筒8”と、該円筒8”の外周と圧接して
移動するベルト状の膜2”及び多孔体ベルト12.並び
に加圧ポンプ4”逆浸透膜5”流量調整弁10”などか
らなる逆浸透膜装置9等で構成されている。図中。
Next, an example of dehydration of water-containing sludge such as sludge will be explained with reference to Fig. 4, Pole No. 5 (X-x sectional view in Fig. 4) and Fig. 6 (detailed view of section Y in Fig. 5). . This dehydrator consists of a rotating cylinder 8'' whose interior is filled with a solution 3'' such as salt water or sugar water and whose outer periphery is made of a porous material 11, and a belt-shaped membrane 2 that moves in pressure contact with the outer periphery of the cylinder 8''. ” and porous belt 12. It also includes a reverse osmosis membrane device 9, which includes a pressure pump 4, a reverse osmosis membrane 5, a flow rate adjustment valve 10, etc. In the figure.

13.34は、それぞれベルト状の膜2″及び多孔体ベ
ルト12を支持するローラー、15は回転継ぎ手、矢印
Rは回転円筒8″の回転方法、矢印Sは膜2”及びベル
ト12の移動方向、をそれぞれ示す。なお2回転円筒及
びベルトの駆動装置や洗浄装置などは図示していない。
13.34 are rollers that support the belt-shaped membrane 2'' and the porous belt 12, 15 is a rotating joint, arrow R is the rotation method of the rotating cylinder 8'', and arrow S is the moving direction of the membrane 2'' and the belt 12. , respectively. Note that the drive device for the two-rotation cylinder and the belt, the cleaning device, etc. are not shown.

以上の構成により、含水スラジ1”を、矢印Aの方向か
らベルト状の膜2″と多孔体ベルト12の間ζこ供給す
ると、含水スラジ1″は、膜2″を介して多孔体11の
外周に流出した溶8!3”と接触するので浸透圧の作用
で脱水され、膜2”とベルト12に挟まれて移動し排出
される。この際スラジl”には、ベルト12の張力に基
ずく圧力しか加わらないので脱水に支障を来す程の粒子
の圧密化が起こらず、ベルト12の張力を適宜設定する
ことにより効果的に脱水できる。而して前記例同様**
脱した水で希釈された溶液3”は、加圧ポンプ4”逆浸
透膜5”流量調整弁10”などからなる逆浸透膜装置に
よって水分6″を分離濃縮され、常に高濃度に維持し得
るので効果的な脱水が連続的に行われる。
With the above configuration, when the water-containing sludge 1'' is supplied between the belt-shaped membrane 2'' and the porous belt 12 from the direction of arrow A, the water-containing sludge 1'' passes through the membrane 2'' to the porous body 11. Since it comes into contact with the melt 8!3'' that has flowed out to the outer periphery, it is dehydrated by the action of osmotic pressure, moves between the membrane 2'' and the belt 12, and is discharged. At this time, only the pressure based on the tension of the belt 12 is applied to the sludge l'', so the particles are not compacted to the extent that it interferes with dewatering, and by setting the tension of the belt 12 appropriately, dewatering can be effectively achieved. Yes, same as above example**
The solution 3'' diluted with the dehydrated water is separated and concentrated by a reverse osmosis membrane device consisting of a pressure pump 4, a reverse osmosis membrane 5, a flow rate adjustment valve 10, etc., and can be maintained at a high concentration at all times. Therefore, effective dehydration is carried out continuously.

以上の説明で明らかなように本発明によれば。According to the present invention, as is clear from the above description.

鮮魚や生野菜などの含水固形物や汚泥などの含水スラジ
等を常温下で脱水する場合に9機械的な圧縮によらず、
高能率で効果的に脱水でき、産業上大変有益である。
9 When dehydrating water-containing solids such as fresh fish and raw vegetables, water-containing sludge such as sludge, etc. at room temperature, without using mechanical compression,
It can be dehydrated effectively with high efficiency and is very useful industrially.

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

第1図は本発明の詳細な説明する原理図、第2図及び第
3図は鮮魚等の含水固形物を脱水する場合の実施例の説
明図、第4図第5図第6図は汚泥などの含水スラジを脱
水する場合の実施例の説明図、をそれぞれ示す。 図中の記号は次のものを表す。 l −一 被脱水物 1゛ −一 鮮魚 1”−一 含水スラジ 2 2’ 2”−一膜 3 3°  3”−一 溶液 4  4’   4” −一 加圧ポンプ5 5°  
5”−一 逆浸透膜 6 6゛  6”−一 水分 7−一 包装機 8−一 液槽 8”−一 回転円筒 ]1 −一 多孔体 12−一 多孔体ベルト
Figure 1 is a diagram explaining the principle of the present invention in detail, Figures 2 and 3 are explanatory diagrams of an embodiment for dehydrating water-containing solids such as fresh fish, Figure 4, Figure 5, and Figure 6 are sludge. An explanatory view of an example in which water-containing sludge such as the following is dehydrated is shown, respectively. The symbols in the figure represent the following: l -1 Material to be dehydrated 1゛ -1 Fresh fish 1"-1 Water-containing sludge 2 2'2"-1 membrane 3 3° 3"-1 Solution 4 4'4" -1 Pressure pump 5 5°
5"-1 Reverse osmosis membrane 6 6"6"-1 Water 7-1 Packaging machine 8-1 Liquid tank 8"-1 Rotating cylinder] 1-1 Porous body 12-1 Porous body belt

Claims (3)

【特許請求の範囲】[Claims] (1)被脱水物を、膜を介して塩水や砂糖水などの濃厚
溶液と接触せしめて浸透圧で脱水すると共に、該溶液を
逆浸透法により濃縮して常にほぼ一定の高濃度に保つこ
とを特徴とする、脱水方法。
(1) The material to be dehydrated is brought into contact with a concentrated solution such as salt water or sugar water through a membrane to dehydrate it by osmotic pressure, and the solution is concentrated by reverse osmosis to maintain a nearly constant high concentration at all times. A dehydration method characterized by:
(2)被脱水物を膜で密封包装して供給する設備と、塩
水や砂糖水などの溶液を満たしかつ内部にコンベア装置
を設けた液槽と、前記溶液を濃縮する逆浸透膜装置とで
構成され、溶液濃度をほぼ一定の高濃度に保ちながら連
続的に被脱水物を浸透圧で脱水することを特徴とする、
例えば鮮魚などの脱水装置。
(2) Equipment for supplying the material to be dehydrated in sealed packaging with a membrane, a liquid tank filled with a solution such as salt water or sugar water and equipped with a conveyor device inside, and a reverse osmosis membrane device for concentrating the solution. It is characterized by continuously dehydrating the dehydrated material using osmotic pressure while maintaining the solution concentration at a nearly constant high concentration.
For example, a dehydrator for fresh fish.
(3)内部に塩水や砂糖水などの溶液を満たし且つ外周
を多孔体で構成した回転円筒と、該回転円筒の外周と圧
接して移動する膜ベルト及び多孔体ベルトと、前記溶液
を濃縮する逆浸透膜装置とで構成され、溶液濃度をほぼ
一定の高濃度に保ちながらベルト間に供給した被脱水物
を連続的に浸透圧で脱水することを特徴とする、例えば
汚泥等含水スラジの脱水装置。
(3) A rotating cylinder whose interior is filled with a solution such as salt water or sugar water and whose outer periphery is made of a porous material, a membrane belt and a porous material belt that move in pressure contact with the outer periphery of the rotating cylinder, and which concentrate the solution. Dewatering of water-containing sludge such as sludge, for example, consists of a reverse osmosis membrane device, and is characterized by continuously dewatering the material to be dehydrated supplied between the belts using osmotic pressure while keeping the solution concentration at a nearly constant high concentration. Device.
JP1085332A 1989-04-04 1989-04-04 Dehydrating process and device Pending JPH02265624A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1085332A JPH02265624A (en) 1989-04-04 1989-04-04 Dehydrating process and device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1085332A JPH02265624A (en) 1989-04-04 1989-04-04 Dehydrating process and device

Publications (1)

Publication Number Publication Date
JPH02265624A true JPH02265624A (en) 1990-10-30

Family

ID=13855683

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1085332A Pending JPH02265624A (en) 1989-04-04 1989-04-04 Dehydrating process and device

Country Status (1)

Country Link
JP (1) JPH02265624A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005118491A1 (en) * 2004-06-02 2005-12-15 Kerttu Eriksson Arrangement to increase the concentration of solids in solutions
JP2014061486A (en) * 2012-09-21 2014-04-10 Kubota Corp Water treatment method and water treatment system

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005118491A1 (en) * 2004-06-02 2005-12-15 Kerttu Eriksson Arrangement to increase the concentration of solids in solutions
JP2014061486A (en) * 2012-09-21 2014-04-10 Kubota Corp Water treatment method and water treatment system

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