JPS6355965B2 - - Google Patents

Info

Publication number
JPS6355965B2
JPS6355965B2 JP10848080A JP10848080A JPS6355965B2 JP S6355965 B2 JPS6355965 B2 JP S6355965B2 JP 10848080 A JP10848080 A JP 10848080A JP 10848080 A JP10848080 A JP 10848080A JP S6355965 B2 JPS6355965 B2 JP S6355965B2
Authority
JP
Japan
Prior art keywords
solute
solvent
cell
transport carrier
permeation
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
Application number
JP10848080A
Other languages
Japanese (ja)
Other versions
JPS5732701A (en
Inventor
Kazuhisa Hiratani
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.)
National Institute of Advanced Industrial Science and Technology AIST
Original Assignee
Agency of Industrial Science and Technology
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 Agency of Industrial Science and Technology filed Critical Agency of Industrial Science and Technology
Priority to JP10848080A priority Critical patent/JPS5732701A/en
Publication of JPS5732701A publication Critical patent/JPS5732701A/en
Publication of JPS6355965B2 publication Critical patent/JPS6355965B2/ja
Granted legal-status Critical Current

Links

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は、液膜法によつて溶質の透過を行う溶
質透過装置の改良に関するものであり、さらに詳
しくは、一方のセルの溶媒から他方のセルの溶媒
中へ特定の溶質のみを輸送担体と錯形成させて移
動させ、各種溶質存在下で特定物質の濃縮、抽
出、または除去等を行うために用いる透過装置に
関するものである。 従来、溶質透過装置としてH字管型及びU字管
型のものがあり、H字管型のものは、H字管の下
部立管部内に溶質を含む溶媒と含まない溶媒、そ
の上部に溶質の輸送担体を含む溶媒がそれぞれ位
置するように注入されることから、溶質を含む溶
媒の比重がその溶質の輸送担体を含む溶媒の比重
より大きい場合に用いられ、U字管型のものは、
U字管の底部に溶質の輸送担体を含む溶媒、その
両側立管部内に溶質を含む溶媒及び含まない溶媒
が位置するようにそれぞれ注入されることから、
溶質の輸送担体を含む溶媒と溶質を含む溶媒(以
下、二つの溶媒又は両溶媒という)の比重の大小
が上記と逆の場合に用いられる。このように、従
来のH字管型及びU字管型の溶質透過装置は、二
つの溶媒のどちらの比重が大きいかによつて使い
分けなければならないという煩雑さがあり、両溶
媒の比重差がほとんどない場合にはその溶質の透
過を行うことができないという難点があつた。さ
らに、これらの溶質透過装置においては、難溶の
二つの溶媒をその比重の違いによつて分割するた
め、それらが直接混合しないように撹拌に注意を
払う必要があるだけでなく、透過経路が長くなる
という難点もあつた。 また、従来の他の溶質透過装置として、ミクロ
ポーラスな高分子膜やセルロースに輸送担体のみ
あるいはそれを溶媒と共に含浸させて使用するも
のもあるが、含浸させた物質が溶出しやすかつた
り、含浸できる輸送担体の絶対量が少ないという
難点があつた。 本発明は、上記に鑑みてなされたもので、二つ
の溶媒の比重の大小に拘わりなく、且つそれらの
比重差がほとんどない場合にも使用でき、また溶
質の透過を能率的に行い得ると共に取扱いも容易
な溶質透過装置を提供しようとするものである。 以下、本発明の実施例を図面に基づいて詳細に
説明するに、第1図において、1,1は相対向さ
せた同一構成の略L字状の管体で、これらの管体
1は、上端に液体の注入口1dを備えた垂直管部
1aと、相互の対向端の開口1eを備えた水平管
部1bとによつて構成され、上記開口1eの周囲
には挾着用のフランジ部1cが形成されている。
これらの管体1,1は、ガラス、ステンレス、プ
ラスチツク等によつて構成することができるが、
それに収容する溶媒等に対する化学的安定性、加
工の難易性を考慮すれば、ガラス製とするのが最
適である。 なお、上記注入口1d,1dには、内部に収容
した液体の蒸発を防ぐための蓋を被設することが
でき、さらにこれらの注入口1d,1dから液体
中にPH電極や温度計等の各種測定器を挿入可能と
することができる。 上記管体1,1の間に配設される環状体2は、
周壁の上部に外部へ開口した液体注入用通孔(直
径約1mm程度)2aを穿設して、該通孔2aから
環状体2の内部へシリンダ等により液体を注入可
能とし、該通孔2aには、内部の液体の流出や蒸
発を防ぐ栓3を挿着している。これらの環状体2
及び栓3は、収容すべき液体に対して不溶性のフ
ツ素樹脂その他の合成樹脂、ガラス等によつて構
成されるものである。また、上記環状体2は、使
用条件に合わせて数mm〜数cmの間で各種の厚さの
ものを用意し、使用条件に応じてそれらを交換し
て使用できるものである。 上記環状体2の両側に配設される隔膜体4,4
は、それに接触する液体に対して不溶性をもつと
共にその液体中の溶質についての透過性を備えた
合成高分子膜、セルロース膜(濾紙)等によつて
構成される。なお、透過速度を高めるには適度の
径の多数の微細孔を備えたミクロポーラス膜を使
用することもできる。また、これら隔膜体4,4
のさらに外側には、環状体2と同様にフツ素樹脂
等の材料で構成したシール用の環状パツキン5が
配設されており、これらのパツキン5はその複数
枚を重ねることにより液密性を高めることができ
る。 管体1,1、環状体2及び隔膜体4,4等を一
体化する固定手段は、管体1,1におけるフラン
ジ部1c,1cを挾んで対向する一対の挾着板
7,7と、それらを締結するボルト8,8及びナ
ツト9,9により構成され、その締結によつて管
体1,1及び環状体2の内部にはそれぞれ隔膜体
4,4によつて区画された三つのセル1A,1
A,2Aが構成される。 上記管体1,1におけるセル1A,1A内に配
設された撹拌子10,10は、その下部に設置し
た撹拌駆動装置11,11で駆動されて液体を撹
拌するものであるが、管体1,1の上端注入口1
d,1dから挿入した撹拌棒をモータで駆動して
撹拌することもできる。 このように構成した溶質透過装置においては、
セル1A,1Aの一方に、透過すべき溶質を含ん
だ溶媒を上端注入口1dから注入すると共に、他
方にその溶質を受入れるべき溶媒を注入し、且つ
その中央におけるセル2Aに環状体2の通孔2a
から上記溶質と錯形成する輸送担体を必要な溶媒
と共に注入する。この場合、一方のセル1Aに入
れた溶媒中の特定の溶質が隔膜体4を透過し、セ
ル2Aに入つて輸送担体と錯形成し、その溶質は
さらに他方の隔膜体4を透過して他方のセル1A
に移送される。従つて、各種溶質が存在する一方
のセル1Aから特定の溶質のみを他方のセルに移
動させ、特定物質の濃縮、抽出、または除去を行
うことができる。 なお、各セル1A,2A,1A間における溶媒
の溶出、混合は、上記セル1A,1Aに収容する
液体試料の量を調節して、一対の隔膜体4,4に
かかる圧力を調節することにより、最小限に抑え
ることができる。 このように本発明によれば、特定の溶質を含ん
だ溶媒と、その溶質を受入れる他の溶媒と、その
溶質の輸送担体とを、それぞれ透過性隔膜体によ
つて隔離して収容するようにしたので、輸送担体
の濃度を高めることが容易で、それによつて溶質
の透過による効率的な抽出、濃縮、除去が期待で
き、しかも輸送担体の収納容積を小さくすること
ができるので、従来の装置に比して輸送経路が短
くなつて装置を小型化することができる。また、
従来の溶質透過装置においては、溶媒の比重によ
りH字管型やU字管型の装置を使い分ける必要が
あり、比重の近接した溶媒間では使用不可能であ
つたが、本発明の溶質透過装置は溶媒の比重とは
無関係に使用することができ、さらにその取扱い
も極めて簡単であるなどのすぐれた特長がある。 実施例 図面に示した装置を用いて、溶液Aに含まれる
溶質を溶液Bへ移送させる透過実験を行つた。こ
の場合の実験条件は次の通りである。 (1) 隔膜体4,4 細孔0.2ミクロンを有する多孔性ポリプロピレ
ンフイルム、膜厚25μm。 (2) 溶液A(一方の管体1のセル1Aに注入) 0.1M LiOH、0.1M NaCl及び0.1M Kclを含む
PH約12の混合水溶液40ml。 (3) 溶液B(他方の管体1のセル1Aに注入) 0.1M H3PO4を含むPH1.30の水溶液40ml。 (4) 溶質輸送担体溶液(環状体2のセル2Aに注
入) 溶質輸送担体として下記式で表わされる化合物
1.5×10-4モルをクロロホルム3mlに溶かした溶
液 〔溶質輸送担体〕 化合物名:1―〔3―(o―カルボキシフエニル
オキシ)プロポキシ〕―2―〔3―
(8―キノリルオキシ)プロポキシ〕
―4(又は5)―t―ブチルベンゼン 構造式: 前記実験の結果を次表に示す。
The present invention relates to an improvement in a solute permeation device that permeates a solute by a liquid film method, and more specifically, the present invention relates to an improvement in a solute permeation device that permeates a solute using a liquid film method. The present invention relates to a permeation device used to concentrate, extract, or remove specific substances in the presence of various solutes by forming complexes and transporting them. Conventionally, there are two types of solute permeation devices: an H-tube type and a U-tube type. The U-tube type is used when the specific gravity of the solvent containing the solute is greater than the specific gravity of the solvent containing the solute transport carrier.
Since the solvent containing the solute transport carrier is placed at the bottom of the U-shaped tube, and the solvent containing and not containing the solute are placed in the vertical tubes on both sides,
It is used when the specific gravities of the solvent containing the solute transport carrier and the solvent containing the solute (hereinafter referred to as two solvents or both solvents) are opposite to the above. As described above, the conventional H-tube type and U-tube type solute permeation devices are complicated in that they must be used depending on which of the two solvents has a higher specific gravity, and the difference in specific gravity between the two solvents is There was a problem that if there was almost no solute, it was impossible to permeate the solute. Furthermore, in these solute permeation devices, two poorly soluble solvents are separated based on the difference in their specific gravity, so not only must careful stirring be done to prevent them from directly mixing, but the permeation path is There was also the problem that it was long. In addition, other conventional solute permeation devices use a microporous polymer membrane or cellulose impregnated with a transport carrier alone or with a solvent; The problem was that the absolute amount of transport carrier that could be produced was small. The present invention has been made in view of the above, and can be used regardless of the specific gravity of two solvents, even when there is almost no difference in specific gravity between them, and allows for efficient permeation of solutes and ease of handling. The present invention also aims to provide a simple solute permeation device. Hereinafter, embodiments of the present invention will be described in detail based on the drawings. In FIG. 1, reference numerals 1, 1 are substantially L-shaped tubes having the same configuration and facing each other, and these tubes 1 are as follows: It is composed of a vertical tube section 1a having a liquid inlet 1d at its upper end, and a horizontal tube section 1b having an opening 1e at opposite ends thereof, and a flange section 1c for clamping around the opening 1e. is formed.
These tube bodies 1, 1 can be made of glass, stainless steel, plastic, etc.
Considering the chemical stability against the solvent contained therein and the difficulty of processing, it is best to use glass. Note that the injection ports 1d and 1d can be covered with lids to prevent the liquid contained therein from evaporating, and furthermore, a PH electrode, a thermometer, etc. can be inserted into the liquid from these injection ports 1d and 1d. Various measuring instruments can be inserted. The annular body 2 disposed between the tube bodies 1, 1 is
A liquid injection hole (approximately 1 mm in diameter) opened to the outside is formed in the upper part of the peripheral wall to enable liquid to be injected into the annular body 2 from the hole 2a with a cylinder or the like. A plug 3 is inserted into the housing to prevent the liquid inside from flowing out or evaporating. These annular bodies 2
The stopper 3 is made of fluororesin or other synthetic resin, glass, or the like which is insoluble in the liquid to be contained. Further, the annular body 2 is available in various thicknesses ranging from several mm to several centimeters depending on the conditions of use, and can be used by changing them according to the conditions of use. Diaphragms 4, 4 disposed on both sides of the annular body 2
is composed of a synthetic polymer membrane, cellulose membrane (filter paper), etc., which is insoluble in the liquid that comes into contact with it and is permeable to solutes in the liquid. Note that in order to increase the permeation rate, a microporous membrane having a large number of fine pores of an appropriate diameter can also be used. In addition, these diaphragms 4, 4
A sealing annular gasket 5 made of a material such as fluororesin, similar to the annular body 2, is disposed on the outer side of the annular body 2, and a plurality of these gaskets 5 are layered to achieve liquid tightness. can be increased. The fixing means for integrating the tubes 1, 1, the annular body 2, the diaphragms 4, 4, etc. includes a pair of clamping plates 7, 7 facing each other with the flange portions 1c, 1c of the tubes 1, 1 interposed therebetween; It is constituted by bolts 8, 8 and nuts 9, 9 that fasten them, and by the fastening, three cells are formed inside the tube bodies 1, 1 and the annular body 2, respectively partitioned by diaphragms 4, 4. 1A, 1
A and 2A are configured. The stirring bars 10, 10 disposed in the cells 1A, 1A in the tube bodies 1, 1 are driven by stirring drive devices 11, 11 installed at the bottom thereof to stir the liquid. 1,1 upper end inlet 1
It is also possible to stir by driving the stirring rod inserted from d and 1d with a motor. In the solute permeation device configured in this way,
A solvent containing the solute to be permeated is injected into one of the cells 1A, 1A from the upper injection port 1d, a solvent to receive the solute is injected into the other, and the annular body 2 is passed through the cell 2A in the center. Hole 2a
A transport carrier complexed with the solute is injected together with the necessary solvent. In this case, a specific solute in the solvent placed in one cell 1A passes through the diaphragm 4, enters the cell 2A, and forms a complex with the transport carrier, and the solute further passes through the other diaphragm 4 to form a complex with the transport carrier. Cell 1A of
will be transferred to. Therefore, only a specific solute can be transferred from one cell 1A where various solutes are present to the other cell, and the specific substance can be concentrated, extracted, or removed. Note that elution and mixing of the solvent between the cells 1A, 2A, 1A can be carried out by adjusting the amount of liquid sample contained in the cells 1A, 1A and adjusting the pressure applied to the pair of diaphragms 4, 4. , can be minimized. According to the present invention, a solvent containing a specific solute, another solvent that accepts the solute, and a carrier for transporting the solute are separated and accommodated by the permeable diaphragm. Therefore, it is easy to increase the concentration of the transport carrier, and thereby efficient extraction, concentration, and removal can be expected through permeation of the solute.Moreover, the storage volume of the transport carrier can be reduced, making it possible to increase the concentration of the transport carrier using conventional equipment. Since the transport route is shorter than that in the conventional method, the device can be made smaller. Also,
In conventional solute permeation devices, it was necessary to use either an H-tube type or a U-tube type device depending on the specific gravity of the solvent, and it was impossible to use it for solvents with similar specific gravities, but the solute permeation device of the present invention It has excellent features such as being able to be used regardless of the specific gravity of the solvent and being extremely easy to handle. Example A permeation experiment was conducted in which a solute contained in solution A was transferred to solution B using the apparatus shown in the drawings. The experimental conditions in this case are as follows. (1) Diaphragm 4, 4 Porous polypropylene film with pores of 0.2 microns, film thickness 25 μm. (2) Solution A (injected into cell 1A of one tube body 1) Contains 0.1M LiOH, 0.1M NaCl and 0.1M Kcl
40ml of a mixed aqueous solution with a pH of approximately 12. (3) Solution B (injected into cell 1A of the other tube 1) 40 ml of an aqueous solution containing 0.1 MH 3 PO 4 at pH 1.30. (4) Solute transport carrier solution (injected into cell 2A of annular body 2) A compound represented by the following formula as a solute transport carrier
Solution of 1.5×10 -4 mol dissolved in 3 ml of chloroform [Solute transport carrier] Compound name: 1-[3-(o-carboxyphenyloxy)propoxy]-2-[3-
(8-quinolyloxy)propoxy]
-4 (or 5)-t-butylbenzene Structural formula: The results of the above experiment are shown in the following table.

【表】【table】

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

第1図は本発明の実施例の断面図である。 1A,2A……セル、1……管体、1b……水
平管部、1e……開口、2……環状体、4……隔
膜体。
FIG. 1 is a sectional view of an embodiment of the invention. 1A, 2A...Cell, 1...Tube body, 1b...Horizontal tube part, 1e...Opening, 2...Annular body, 4...Diaphragm body.

Claims (1)

【特許請求の範囲】[Claims] 1 特定の溶質を含んだ溶媒と上記溶質を受入れ
る溶媒とを収容するためのセルを形成する略L字
状の一対の管体を備え、それらの管体の水平管部
の開口間に、上記溶質と錯形成する輸送担体を収
容するためのセルを形成する環状体を、その両側
に上記溶質に対する透過性を備えた隔膜体を配設
して挾着締結したことを特徴とする溶質透過装
置。
1 A pair of substantially L-shaped tubes forming a cell for accommodating a solvent containing a specific solute and a solvent that receives the solute, and between the openings of the horizontal tube portions of the tubes, the above-mentioned A solute permeation device characterized in that a ring-shaped body forming a cell for accommodating a transport carrier that forms a complex with a solute is fastened with a diaphragm body having permeability to the solute arranged on both sides of the ring-shaped body. .
JP10848080A 1980-08-07 1980-08-07 Solute permeating device Granted JPS5732701A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10848080A JPS5732701A (en) 1980-08-07 1980-08-07 Solute permeating device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10848080A JPS5732701A (en) 1980-08-07 1980-08-07 Solute permeating device

Publications (2)

Publication Number Publication Date
JPS5732701A JPS5732701A (en) 1982-02-22
JPS6355965B2 true JPS6355965B2 (en) 1988-11-07

Family

ID=14485814

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10848080A Granted JPS5732701A (en) 1980-08-07 1980-08-07 Solute permeating device

Country Status (1)

Country Link
JP (1) JPS5732701A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NO311464B1 (en) * 1998-12-01 2001-11-26 Pedersen Bjergaard Stig Process and disposable micro-extraction device

Also Published As

Publication number Publication date
JPS5732701A (en) 1982-02-22

Similar Documents

Publication Publication Date Title
US5326533A (en) Multiwell test apparatus
JP3436312B2 (en) Apparatus and method for sample dialysis
US6506346B1 (en) Diagnostic test container and method of sampling
US6837995B1 (en) Device for concentrating and purifying macromolecules
US7056440B2 (en) Dialysis device with air chamber
US7468281B2 (en) Hollow fiber membrane sample preparation devices
US20150360183A1 (en) Biomimetic membranes and uses thereof
Eljaddi et al. Review on mechanism of facilitated transport on liquid membranes
EP1285257B1 (en) Processing chamber with apertures for pipette access
Anderson Concentration of dilute industrial wastes by direct osmosis
AU2001262612A1 (en) Processing Chamber
CA1290701C (en) Dialysis cell
JPS6355965B2 (en)
US5045207A (en) Multi-concentration disposable liquid concentrating device
US8007668B2 (en) Dialysis device with access port
JPH034345Y2 (en)
US7799282B2 (en) Sample chamber for a liquid
JPH0233869Y2 (en)
NL8801183A (en) Immobilised liq. membrane - has liq. fixed in pores of inert support by gelation with polymer used for sepn. of gases or liq(s).
US20040124142A1 (en) Multi-sided immersion formation of composite structures and method
JPS6034702A (en) Liquid separator
JPH01139108A (en) Filtration system
JP2513894Y2 (en) Water treatment mechanism in automatic analyzer
JPH0618964U (en) Liquid sample concentration and desalting method
JPS6059962U (en) liquid chromatograph