JPH06226054A - Electrophoresis device for continuous treatment - Google Patents

Electrophoresis device for continuous treatment

Info

Publication number
JPH06226054A
JPH06226054A JP5019985A JP1998593A JPH06226054A JP H06226054 A JPH06226054 A JP H06226054A JP 5019985 A JP5019985 A JP 5019985A JP 1998593 A JP1998593 A JP 1998593A JP H06226054 A JPH06226054 A JP H06226054A
Authority
JP
Japan
Prior art keywords
electrolyte solution
tank
sample
electrolyte soln
electrolyte
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.)
Withdrawn
Application number
JP5019985A
Other languages
Japanese (ja)
Inventor
Jiro Kobayashi
次郎 小林
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries 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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP5019985A priority Critical patent/JPH06226054A/en
Priority to CN 94100800 priority patent/CN1100479A/en
Publication of JPH06226054A publication Critical patent/JPH06226054A/en
Withdrawn legal-status Critical Current

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  • Spinning Methods And Devices For Manufacturing Artificial Fibers (AREA)
  • Peptides Or Proteins (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

PURPOSE:To realize the device which can be continuously operated and prevents the inclusion of air bubbles into a migration cell, etc., by decreasing the amt. of the electrolyte soln. to be used and eliminating the need for an electrolyte soln. tank of a large capacity. CONSTITUTION:This electrophoresis device has an electrolyte soln. regeneration treating device 6 which is provided between the migration cell 3 to be injected with a sample from a sample injector 2 and to be supplied with the electrolyte soln. from the electrolyte soln. tank 1 and the electrolyte soln. tank 1 via an electrolyte soln. feed pump 4 and has a separating membrane 7. As a result, the separating membrane 7 removes a slight amt. of the sample and, therefore, the reutilization of the electrolyte soln. after the use is possible and the need for prepn. of a large amt. of the electrolyte soln. and the electrolyte soln. tank 1 of the large capacity is eliminated. Since an electrolyte soln. piping is formed as a closed loop, a continuous automatic operation is possible. The possibility of the intrusion of the air bubbles is eliminated and, therefore, the electrophoresis maintaining sepn. accuracy is possible.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、試料を連続的に処理す
る連続処理用電気泳動装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an electrophoretic device for continuous processing for continuously processing a sample.

【0002】[0002]

【従来の技術】タンパク質、細胞など電解質溶液中で電
荷を持つ試料に電界を作用させると、これらの試料は電
気泳動を行う。溶液中を電気泳動する速度は、各試料の
もつ電荷量により異なるため、これらの試料の分離、精
製、同定等に電気泳動が利用されている。
2. Description of the Related Art When an electric field is applied to a sample having a charge in an electrolyte solution such as protein or cell, these samples perform electrophoresis. Since the speed of electrophoresis in a solution varies depending on the amount of electric charge of each sample, electrophoresis is used for separation, purification, identification, etc. of these samples.

【0003】従来の電気泳動装置において、使用されて
いる電解質溶液は、図3に示すように電解質溶液タンク
1に貯蔵されており、電気泳動に供された後、試料を多
く含む少量の溶液は分取容器5に保管されるが、試料を
ほとんど含まない大部分の電解質溶液はそのまま廃液容
器8へ集められ廃棄される。
In the conventional electrophoresis apparatus, the electrolyte solution used is stored in the electrolyte solution tank 1 as shown in FIG. 3, and after being subjected to the electrophoresis, a small amount of the solution containing a large amount of the sample is stored. Although stored in the sorting container 5, most of the electrolyte solution containing almost no sample is directly collected in the waste liquid container 8 and discarded.

【0004】したがって、電解質溶液タンク1の電解質
溶液を全て使用してしまうと、電解質溶液タンク1の交
換、電解質溶液の補充、または電解質溶液配管の繋ぎ換
えなどの作業が必要となり、電気泳動装置を停止しなけ
ればならない。
Therefore, if all the electrolyte solution in the electrolyte solution tank 1 is used up, it is necessary to replace the electrolyte solution tank 1, replenish the electrolyte solution, or change the connection of the electrolyte solution pipes. I have to stop.

【0005】[0005]

【発明が解決しようとする課題】従来の装置において、
連続的に電気泳動を実施しようとした場合には以下の課
題があった。 (1)大量の電解質溶液を用意しなければならず、大き
な電解質溶液タンクが必要となり、装置が大型となる。 (2)電解質溶液タンク内の電解質溶液の残量がわずか
になった場合、電解質溶液タンクの交換、電解質溶液の
補充、または電解質溶液配管の繋ぎ換えなどの作業が必
要となり、電気泳動を停止しなければならない。 (3)上記の配管の繋ぎ換えなどの作業時には、気泡が
配管中や泳動槽内に入る可能性があり、分離精度の低下
を招く可能性がある。 本発明は上記の課題を解決しようとするものである。
In the conventional device,
The following problems were encountered when trying to carry out electrophoresis continuously. (1) A large amount of electrolyte solution must be prepared, a large electrolyte solution tank is required, and the device becomes large. (2) When the remaining amount of the electrolyte solution in the electrolyte solution tank becomes very small, it is necessary to replace the electrolyte solution tank, replenish the electrolyte solution, or reconnect the electrolyte solution pipes, and stop the electrophoresis. There must be. (3) At the time of work such as reconnection of the above-mentioned pipes, bubbles may enter the pipes or the migration tank, which may lead to a decrease in separation accuracy. The present invention is intended to solve the above problems.

【0006】[0006]

【課題を解決するための手段】本発明の連続処理用電気
泳動装置は、内部に陽極電極と陰極電極が設けられた泳
動槽、同泳動槽に電解質溶液を供給する電解質溶液タン
クと試料を注入する試料注入器、および上記泳動槽より
分取液が排出される分取容器を備えた電気泳動装置にお
いて、上記泳動槽と電解質溶液の間に電解質溶液送液ポ
ンプを介して接続され内部に分離膜が設けられた電解質
溶液再生処理装置を備えたことを特徴としている。
An electrophoretic device for continuous processing according to the present invention is provided with an electrophoretic tank having an anode electrode and a cathode electrode therein, an electrolyte solution tank for supplying an electrolytic solution to the electrophoretic tank, and a sample. In an electrophoretic device equipped with a sample injector and a preparative container from which the preparative liquid is discharged from the electrophoretic tank, the electrophoretic solution feed pump is connected between the electrophoretic tank and the electrolytic solution to separate the electrophoretic solution into the inside. It is characterized in that it is provided with an electrolyte solution regeneration treatment device provided with a membrane.

【0007】[0007]

【作用】上記において、電解質溶液が電解質溶液タンク
より供給された泳動槽内に試料注入器より注入された試
料は、電気泳動を行い、分離、精製、同定等が行われた
後、試料を多く含んだ電解質溶液が分取容器に分取され
る。
In the above, the sample injected from the sample injector into the electrophoretic solution tank supplied with the electrolyte solution is subjected to electrophoresis, separation, purification, identification, etc., and then many samples are added. The contained electrolyte solution is dispensed in a dispensing container.

【0008】分取されなかった電解質溶液は、電解質溶
液送液ポンプにより電解質溶液再生処理装置に送られ、
同装置内に設けられた分離膜がほとんどの試料を分離
し、小さな電解質溶液イオンを素通りさせるため、上記
再生処理装置は電解質溶液のPHや電導度等の電気泳動
に大きく影響する基本的性状が変化しない電解質溶液を
回収し、電解質溶液タンクへ供給する。
The uncollected electrolyte solution is sent to the electrolyte solution regeneration treatment device by the electrolyte solution sending pump,
Since the separation membrane provided in the device separates most of the sample and allows small electrolyte solution ions to pass through, the above regeneration treatment device has basic properties that greatly affect the electrophoresis such as the pH and conductivity of the electrolyte solution. Collect the unchanged electrolyte solution and supply it to the electrolyte solution tank.

【0009】上記のように、電解質溶液再生処理装置が
電気泳動後の電解質溶液に含まれる微量の試料を除去し
た後、再び電解質溶液タンクに戻すため、電気泳動に再
利用することができ、大量の電解質溶液を準備する必要
がなくなり、大きな電解質溶液タンクを必要としなくな
る。また、電解質溶液配管を閉ループとしているため、
自動運転で連続的に試料を処理することができ、かつ、
気泡が配管中や泳動槽内に混入するおそれもないため、
分離精度を維持した状態で連続的な電気泳動が可能とな
る。
As described above, after the electrolyte solution regeneration treatment device removes a small amount of sample contained in the electrolyte solution after electrophoresis, it is returned to the electrolyte solution tank and can be reused for electrophoresis. There is no need to prepare the above electrolyte solution, and a large electrolyte solution tank is not required. Also, because the electrolyte solution piping is a closed loop,
Samples can be processed continuously by automatic operation, and
Since there is no risk of air bubbles entering the piping or the migration tank,
Continuous electrophoresis is possible while maintaining the separation accuracy.

【0010】[0010]

【実施例】本発明の一実施例を図1に示す。図1に示す
本実施例は、内部に陽極電極3aと陰極電極3bが設け
られた泳動槽3、同泳動槽3に試料を注入する試料注入
器2、上記泳動槽3に電解質溶液を供給する電解質溶液
タンク1、同タンク1に接続された電解質溶液送液ポン
プ4、および上記泳動槽3より分取液5aが送られる分
取容器5を備えた電気泳動装置において、上記電解質溶
液タンク1と電解質溶液送液ポンプ4の間に接続され内
部に分離膜7を有する電解質溶液再生処理装置6を備え
ている。
FIG. 1 shows an embodiment of the present invention. In this embodiment shown in FIG. 1, an electrophoretic bath 3 having an anode electrode 3a and a cathode electrode 3b therein, a sample injector 2 for injecting a sample into the electrophoretic bath 3, and an electrolyte solution are supplied to the electrophoretic bath 3. An electrophoretic device comprising an electrolyte solution tank 1, an electrolyte solution feed pump 4 connected to the tank 1, and a sorting container 5 to which a fractionation liquid 5a is fed from the migration tank 3, wherein: An electrolyte solution regeneration treatment device 6 that is connected between the electrolyte solution feed pumps 4 and has a separation membrane 7 inside is provided.

【0011】上記において、電解質溶液が電解質溶液タ
ンク1より供給され、試料が試料注入器2により注入さ
れた泳動槽3内では、電極3a,3b間で試料の電解泳
動が行われ、試料の分離、精製、同定等が行われた後、
試料を多く含む電解質溶液は分取容器5に分取される。
In the above, in the migration tank 3 in which the electrolyte solution is supplied from the electrolyte solution tank 1 and the sample is injected by the sample injector 2, the sample is electrophoresed between the electrodes 3a and 3b to separate the sample. After purification, identification, etc.,
The electrolyte solution containing a large amount of the sample is collected in the collecting container 5.

【0012】分取されなかった電解質溶液は、電解質溶
液再生処理装置6に電解質溶液送液ポンプ4により回送
される。電解質溶液再生処理装置6内には分離膜7があ
り、ここで試料成分と電解質溶液が分離され、電解質溶
液は再生される。その再生処理された電解質溶液は電解
質溶液タンク1に戻され、再び泳動槽3に導かれ再利用
される。
The uncollected electrolyte solution is sent to the electrolyte solution regeneration treatment device 6 by the electrolyte solution feed pump 4. There is a separation membrane 7 in the electrolytic solution regeneration processing device 6, in which the sample component and the electrolytic solution are separated, and the electrolytic solution is regenerated. The regenerated electrolyte solution is returned to the electrolyte solution tank 1 and again guided to the migration tank 3 for reuse.

【0013】上記電解質溶液再生処理装置6における電
解質溶液の再生については、分離膜7により試料を分離
することにより行っているが、電気泳動の代表的な試料
であるタンパク質の大きさは数十オングストローム、細
胞では数万オングストロームあるのに対し、電解質溶液
を構成するイオンは数オングストロームと小さく、分離
膜7は電解質溶液からほとんどの試料を分離することが
でき、かつ、小さな電解質溶液イオンは素通りさせるこ
とができるため、電解質溶液のpHや電導度等の電気泳動
に大きく影響する基本的性状は変化しない。
Regeneration of the electrolyte solution in the electrolyte solution regeneration treatment device 6 is carried out by separating the sample with the separation membrane 7. However, the size of the protein, which is a typical sample for electrophoresis, is several tens of angstroms. , Cells have tens of thousands of angstroms, whereas the ions that make up the electrolyte solution are as small as a few angstroms, the separation membrane 7 can separate most of the sample from the electrolyte solution, and small electrolyte solution ions can pass through. Therefore, the basic properties such as pH and conductivity of the electrolyte solution, which greatly affect electrophoresis, do not change.

【0014】上記電解質溶液の基本的性状の変化を確認
するため、試料としてヒト血清アルブミン、電解質溶液
として7mMトリエタノールアミン/酢酸(pH7.5at2
0℃)、分離膜としてUF膜(分画分子量:10,00
0)を用い、実験を行った。
In order to confirm changes in the basic properties of the electrolyte solution, human serum albumin was used as a sample, and 7 mM triethanolamine / acetic acid (pH 7.5 at 2) was used as the electrolyte solution.
0 ° C), UF membrane as a separation membrane (molecular weight cut-off: 10,000)
0) was used to perform the experiment.

【0015】この実験結果から、図2に示すように少な
くとも4回以上電気泳動と再生処理を繰り返して使用し
ても、電気泳動上重要な基本的性状であるpH、電導度は
変化しないことを確認した。
From the results of this experiment, it can be seen that, as shown in FIG. 2, even if the electrophoresis and the regeneration treatment are repeated at least four times or more, the basic properties important for electrophoresis, pH and conductivity, do not change. confirmed.

【0016】上記により、電解質溶液タンクを大きくす
ることなしに4倍以上の時間、連続的に電気泳動を実施
することが可能となった。また、同じ量の試料を処理す
るのであれば、電解質溶液は必要量の4分の1以下で処
理できることから、電解質溶液タンクの容量を4分の1
以下にすることができ、装置を小型化することも可能と
なった。
From the above, it has become possible to continuously perform electrophoresis for four times or more without increasing the size of the electrolyte solution tank. In addition, if the same amount of sample is processed, the electrolyte solution can be processed with a quarter or less of the required amount, so that the capacity of the electrolyte solution tank can be reduced to a quarter.
The following can be achieved, and the device can be downsized.

【0017】一方、電解質溶液配管を閉ループにするこ
とができ、ほぼ自動運転で連続的に試料を処理すること
が可能なため、気泡が配管中や泳動槽内に入るおそれが
なく分離精度を維持した状態で連続的に試料を処理する
ことが可能となった。
On the other hand, since the electrolyte solution pipe can be closed loop and the sample can be continuously processed by almost automatic operation, there is no possibility that bubbles enter the pipe or the migration tank, and the separation accuracy is maintained. It became possible to process the sample continuously in the state.

【0018】[0018]

【発明の効果】本発明の連続処理用電気泳動装置は、試
料が試料注入器より注入され電解質溶液が電解質溶液タ
ンクより供給される泳動槽と上記電解質溶液タンクの間
に電解質溶液送液ポンプを介して設けられ、分離膜を有
する電解質溶液再生処理装置を備えたことによって、上
記分離膜が微量の試料を除去するため、使用後の電解質
溶液の再利用が可能となり、大量の電解質溶液の準備と
大容量の電解質溶液タンクが不要となり、また、電解質
溶液配管が閉ループとなるため、連続自動運転が可能と
なり、気泡の混入のおそれがなくなるため、分離精度を
維持した電気泳動が可能となる。
The electrophoretic device for continuous processing of the present invention includes an electrolyte solution feed pump between the electrophoresis tank in which the sample is injected from the sample injector and the electrolyte solution is supplied from the electrolyte solution tank, and the electrolyte solution tank. Since the separation membrane removes a trace amount of the sample, it is possible to reuse the electrolyte solution after use by preparing an electrolyte solution regeneration treatment device having a separation membrane provided through A large-capacity electrolyte solution tank is no longer required, and the electrolyte solution piping forms a closed loop, which allows continuous automatic operation and eliminates the possibility of air bubbles being mixed in, enabling electrophoresis that maintains separation accuracy.

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

【図1】本発明の一実施例に係る連続電気泳動装置の説
明図である。
FIG. 1 is an explanatory diagram of a continuous electrophoresis device according to an embodiment of the present invention.

【図2】上記一実施例に係る電解質溶液の再生処理後の
基本的性状変化についての説明図で、(a)はpHの変
化、(b)は電導度の変化の説明図である。
FIG. 2 is an explanatory diagram of a change in basic properties of the electrolyte solution according to the above embodiment after the regeneration treatment, in which (a) is a change in pH and (b) is an explanatory view of a change in conductivity.

【図3】従来の電気泳動装置の説明図である。FIG. 3 is an explanatory diagram of a conventional electrophoresis device.

【符号の説明】[Explanation of symbols]

1 電解質溶液タンク 2 試料注入器 3 泳動槽 3a,3b 電極 4 電解質液送液ポンプ 5 分取容器 5a 分取液 6 電解質溶液再生処理装置 7 分離膜 1 Electrolyte Solution Tank 2 Sample Injector 3 Migration Tank 3a, 3b Electrode 4 Electrolyte Liquid Delivery Pump 5 Preparative Container 5a Preparative Liquid 6 Electrolyte Solution Regeneration Device 7 Separation Membrane

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.5 識別記号 庁内整理番号 FI 技術表示箇所 G01N 27/447 ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 5 Identification code Internal reference number FI technical display location G01N 27/447

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 内部に陽極電極と陰極電極が設けられた
泳動槽、同泳動槽に電解質溶液を供給する電解質溶液タ
ンクと試料を注入する試料注入器、および上記泳動槽よ
り分取液が排出される分取容器を備えた電気泳動装置に
おいて、上記泳動槽と電解質溶液の間に電解質溶液送液
ポンプを介して接続され内部に分離膜が設けられた電解
質溶液再生処理装置を備えたことを特徴とする連続処理
用電気泳動装置。
1. A migration tank in which an anode electrode and a cathode electrode are provided, an electrolyte solution tank for supplying an electrolyte solution to the migration tank, a sample injector for injecting a sample, and a preparative liquid discharged from the migration tank. In an electrophoretic device having a preparative separation container, an electrolytic solution regeneration treatment device is provided which is connected between the electrophoretic bath and the electrolytic solution via an electrolytic solution feed pump and has a separation membrane provided therein. Characteristic electrophoretic device for continuous processing.
JP5019985A 1993-02-08 1993-02-08 Electrophoresis device for continuous treatment Withdrawn JPH06226054A (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
JP5019985A JPH06226054A (en) 1993-02-08 1993-02-08 Electrophoresis device for continuous treatment
CN 94100800 CN1100479A (en) 1993-02-08 1994-02-08 A ceramic fiber yarn, and a method of making the same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5019985A JPH06226054A (en) 1993-02-08 1993-02-08 Electrophoresis device for continuous treatment

Publications (1)

Publication Number Publication Date
JPH06226054A true JPH06226054A (en) 1994-08-16

Family

ID=12014480

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5019985A Withdrawn JPH06226054A (en) 1993-02-08 1993-02-08 Electrophoresis device for continuous treatment

Country Status (2)

Country Link
JP (1) JPH06226054A (en)
CN (1) CN1100479A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2246537A3 (en) * 2001-05-25 2012-10-10 Ibiden Co., Ltd. Alumina-silica based fiber, ceramic fiber, ceramic fiber aggregation, holding seal material and manufacturing methods thereof, as well as manufacturing method of alumina fiber aggregation
JP4730495B2 (en) * 2001-05-25 2011-07-20 イビデン株式会社 Holding seal material for catalytic converter and method for manufacturing the same, catalytic converter

Also Published As

Publication number Publication date
CN1100479A (en) 1995-03-22

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