JPH0363561A - Device and method for filter type electrophoresis - Google Patents
Device and method for filter type electrophoresisInfo
- Publication number
- JPH0363561A JPH0363561A JP1199648A JP19964889A JPH0363561A JP H0363561 A JPH0363561 A JP H0363561A JP 1199648 A JP1199648 A JP 1199648A JP 19964889 A JP19964889 A JP 19964889A JP H0363561 A JPH0363561 A JP H0363561A
- Authority
- JP
- Japan
- Prior art keywords
- electrophoresis
- separation
- carrier
- buffer solution
- supply port
- 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
Links
- 238000001962 electrophoresis Methods 0.000 title claims abstract description 30
- 238000000034 method Methods 0.000 title claims description 18
- 238000000926 separation method Methods 0.000 claims abstract description 37
- 239000007788 liquid Substances 0.000 claims abstract description 22
- 239000007853 buffer solution Substances 0.000 claims description 27
- 239000011550 stock solution Substances 0.000 claims description 19
- 239000003792 electrolyte Substances 0.000 claims description 9
- 238000001914 filtration Methods 0.000 claims description 9
- 230000005684 electric field Effects 0.000 claims description 5
- 230000004907 flux Effects 0.000 claims description 3
- 239000000872 buffer Substances 0.000 abstract description 11
- 239000000126 substance Substances 0.000 abstract description 8
- 239000011148 porous material Substances 0.000 abstract description 4
- 229920002301 cellulose acetate Polymers 0.000 abstract description 3
- 238000010030 laminating Methods 0.000 abstract 1
- 238000001997 free-flow electrophoresis Methods 0.000 description 8
- 102000004169 proteins and genes Human genes 0.000 description 7
- 108090000623 proteins and genes Proteins 0.000 description 7
- 239000012528 membrane Substances 0.000 description 5
- FTOAOBMCPZCFFF-UHFFFAOYSA-N 5,5-diethylbarbituric acid Chemical compound CCC1(CC)C(=O)NC(=O)NC1=O FTOAOBMCPZCFFF-UHFFFAOYSA-N 0.000 description 4
- 239000000243 solution Substances 0.000 description 4
- 150000001413 amino acids Chemical class 0.000 description 3
- 238000005370 electroosmosis Methods 0.000 description 3
- 239000000017 hydrogel Substances 0.000 description 3
- 238000013508 migration Methods 0.000 description 3
- 230000005012 migration Effects 0.000 description 3
- 229960002319 barbital Drugs 0.000 description 2
- 238000011094 buffer selection Methods 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 239000000499 gel Substances 0.000 description 2
- 230000020169 heat generation Effects 0.000 description 2
- 238000004811 liquid chromatography Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 102000039446 nucleic acids Human genes 0.000 description 2
- 108020004707 nucleic acids Proteins 0.000 description 2
- 150000007523 nucleic acids Chemical class 0.000 description 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- HRPVXLWXLXDGHG-UHFFFAOYSA-N Acrylamide Chemical compound NC(=O)C=C HRPVXLWXLXDGHG-UHFFFAOYSA-N 0.000 description 1
- 235000000722 Celosia argentea Nutrition 0.000 description 1
- 240000008365 Celosia argentea Species 0.000 description 1
- 102000006395 Globulins Human genes 0.000 description 1
- 108010044091 Globulins Proteins 0.000 description 1
- 239000004372 Polyvinyl alcohol Substances 0.000 description 1
- 229920002472 Starch Polymers 0.000 description 1
- 241000727732 Tokoyo Species 0.000 description 1
- 239000000969 carrier Substances 0.000 description 1
- GTKRFUAGOKINCA-UHFFFAOYSA-M chlorosilver;silver Chemical compound [Ag].[Ag]Cl GTKRFUAGOKINCA-UHFFFAOYSA-M 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000004925 denaturation Methods 0.000 description 1
- 230000036425 denaturation Effects 0.000 description 1
- 238000005194 fractionation Methods 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 229920002451 polyvinyl alcohol Polymers 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 210000002966 serum Anatomy 0.000 description 1
- 239000008107 starch Substances 0.000 description 1
- 235000019698 starch Nutrition 0.000 description 1
- 239000010409 thin film Substances 0.000 description 1
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Description
【発明の詳細な説明】
「産業上の分野」
本発明は蛋白質・核酸・アミノ酸の如き両性電解質を電
気泳動法を利用して分離する連続電気泳動法及びその装
置に関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial Field] The present invention relates to a continuous electrophoresis method and apparatus for separating ampholytes such as proteins, nucleic acids, and amino acids using electrophoresis.
「従来の技術」
従来の、蛋白質・核酸・アミノ酸等の両性電解質の分離
精製法は、電気泳動法・膜分離法及び液体クロマト法で
どかある。膜分離法は、膜の孔の大きさによって物質を
分離する方法で、連続的に大量処理できる点で有利であ
るが、分子量の似ている蛋白質同士やアミノ酸同士の分
離には不適当である。液体、クロマト法は、物質を担体
充填カラム中を通して分離する方法で、分離性能は優れ
ているがバッチ操作のため工業規模の大量処理には適し
ていない、一方電気泳動法は、両性電解質の荷電差を利
用して電場の中で分離精製する方法である。この電気泳
動には、ゲルや濾紙等の担体を用いる担体電気泳動と、
担体を用いず自由溶液中で行う無担体電気泳動がある。"Prior Art" Conventional methods for separating and purifying ampholytes such as proteins, nucleic acids, and amino acids include electrophoresis, membrane separation, and liquid chromatography. Membrane separation is a method of separating substances based on the size of the membrane's pores, and has the advantage of being able to process large quantities continuously, but is unsuitable for separating proteins with similar molecular weights or amino acids. . The liquid chromatography method is a method in which substances are separated through a carrier-packed column, and although it has excellent separation performance, it is a batch operation and is not suitable for large-scale processing on an industrial scale.On the other hand, the electrophoresis method separates substances by passing them through a carrier-packed column. This is a method of separating and purifying in an electric field using the difference. This electrophoresis includes carrier electrophoresis using carriers such as gel and filter paper;
There is carrier-free electrophoresis, which is performed in a free solution without using a carrier.
「発明が解決しようとする課題」
担体電気泳動は分離性能が非常に優れているので、分析
用途に盛んに利用されているが、分離された物質を回収
するのが困難であるため、分取用途にはほとんど利用さ
れていない。大量に連続的に分離した物質を回収する用
途には、従来無担体電気泳動が専ら注目され研究されて
きた。無担体電気泳動については、松尾雄志が底置「最
新電気泳動法J (1986年 第3版発行、床用書
店)に詳しく述べているように、分離緩衝液に電流を流
すためジュール熱が必ず発生し、その熱により緩衝液に
対流が起こり、緩衝液の流れが乱れ電流を流し、緩衝液
および物質の分離が低下する。``Problem to be solved by the invention'' Carrier electrophoresis has excellent separation performance and is widely used for analytical purposes, but it is difficult to recover the separated substances, so preparative It is hardly used for any purpose. In the past, carrier-free electrophoresis has been the focus of attention and research for applications in which large amounts of continuously separated substances are recovered. Regarding carrier-free electrophoresis, as Yuji Matsuo describes in detail in Soko's ``Latest Electrophoresis Methods J'' (3rd edition, 1986, published by Tokoyo Shoten), Joule heat is always generated because electric current is passed through the separation buffer. The heat generated causes convection in the buffer, which disrupts the flow of the buffer and conducts an electric current, reducing the separation of the buffer and the substance.
無担体電気泳動のこのような欠点を改善するために、分
#緩衝液の温度や流速を極めて精度よく制御する必要が
あり、そのために分離室を薄い平板型で極力小さくさゼ
るをえず、処理量が少なく、工業規模に大型化する際に
問題であった。特開昭61−83952号では、分離を
行う原液の注入口と分離された物質の回収口を発熱によ
っておこる対流液流れの上に設置することで、分離室の
大型化を行っている。しかしこの方法では、分離室内へ
の原液の注入を液の流れの途中で行うため、分離時間を
充分に確保できず、大型化した割には少流量の処理しか
できない。In order to improve these drawbacks of carrier-free electrophoresis, it is necessary to control the temperature and flow rate of the separation buffer solution with extreme precision, and for this purpose it is necessary to make the separation chamber as thin and flat as possible. However, the throughput was small, which was a problem when scaling up to an industrial scale. In JP-A No. 61-83952, the size of the separation chamber is increased by installing an injection port for the stock solution to be separated and a recovery port for the separated substance above the convective liquid flow caused by heat generation. However, in this method, the stock solution is injected into the separation chamber midway through the flow of the solution, so sufficient separation time cannot be secured, and only a small flow rate can be processed despite the increased size.
分離室内を電場に対して並行に複数分画し、各分画室ご
とに原液を供給できるようにする工夫が、特開昭63−
26392号で行われている。この方法は液流れの乱れ
を小さくすることに対しては非常に効果がある。しかし
あまり分離室を多数に分割したり細かく分割すると、各
分割室内の液流量を一定にすることが困難となり、この
方法も満足できる解決策とはなっていない。A device was developed in 1983 to allow multiple fractions to be fractionated in parallel to the electric field in the separation chamber, and to supply the stock solution to each fractionation chamber.
This is done in No. 26392. This method is very effective in reducing turbulence in liquid flow. However, if the separation chamber is divided into too many parts or divided too finely, it becomes difficult to keep the liquid flow rate in each division chamber constant, and this method is not a satisfactory solution either.
「発明の目的」
本発明の目的は、無担体電気泳動が有する前記のような
欠点を解消し、分離性能が優れ且つ大量連続処理の可能
な濾過型電気泳動及びその装置を提供することである。"Objective of the Invention" The object of the present invention is to eliminate the above-mentioned drawbacks of carrier-free electrophoresis, and to provide a filtration-type electrophoresis device that has excellent separation performance and is capable of continuous large-scale processing. .
「課題を解決するための手段」
前記発明の目的は、電気泳動による分離を多孔室担体中
で行う以下の方法にて達成されたので、その概要を述べ
る。"Means for Solving the Problems" The object of the invention was achieved by the following method of performing electrophoretic separation in a porous chamber carrier, and an overview thereof will be described below.
容器内に多孔室担体直方体を収容し、直方体の一つの面
に対して平行に陽電極をその面の外に配置し、その反対
面の外に陰電極を面に平行に配置し、両電極間に電流を
流して電場を形成するようにし電流を流し、緩衝液およ
びこの電流の方向に対して平行な多孔質担体直方体の一
方の面に、緩衝液供給口および分離原液供給口を備え、
その反対面は電流方向とは直角に少なくとも二つ以上に
区分されそれぞれに集液口を備えた、濾過型電気泳動装
置を用い、その両電極間に電流を流し、緩衝液および分
離原液をそれぞれ緩衝液供給口および分離原液供給口に
同一流束で供給し、多孔質担体直方体中に電流を流し、
緩衝液および分離原液中に溶解している両性電解質を電
気泳動させて分離し、各集液口でそれぞれ透過して出て
くる液を集液する。A porous chamber carrier rectangular parallelepiped is housed in a container, a positive electrode is arranged parallel to one surface of the rectangular parallelepiped outside that surface, a negative electrode is arranged outside the opposite surface parallel to the surface, and both electrodes A current is passed between them to form an electric field, and a buffer solution supply port and a separation stock solution supply port are provided on one surface of the porous carrier rectangular parallelepiped parallel to the direction of the buffer solution and the current,
On the other side, a filtration type electrophoresis device is used, which is divided into at least two parts perpendicular to the current direction and each has a liquid collection port, and a current is passed between the two electrodes to separate the buffer solution and separation stock solution respectively. The same flux is supplied to the buffer solution supply port and separation stock solution supply port, and a current is passed through the porous carrier rectangular parallelepiped.
The amphoteric electrolyte dissolved in the buffer solution and separation stock solution is separated by electrophoresis, and the permeated liquid is collected at each liquid collection port.
この方法を用いると、ジュール熱が発生しても緩衝液の
対流の多孔質担体に邪魔されておこりおくいため、分離
精度が従来の無担体電気泳動に較べて飛躍的に向上する
。When this method is used, even if Joule heat is generated, it is disturbed by the porous carrier due to the convection of the buffer solution, so separation accuracy is dramatically improved compared to conventional carrier-free electrophoresis.
以下発明の詳細な説明する。The invention will be explained in detail below.
ここで使用する電極は、電極が対面する多孔質担体直方
体の平面に平行な平板電極が主に使用されるが、基本的
に従来の無担体電気泳動装置で用いられているものと同
じでよい。従ってその材質も白金が最も普通に使用され
、そのほかには銀塩化銀電極か使用される。The electrodes used here are mainly flat plate electrodes that are parallel to the plane of the porous carrier rectangular parallelepiped that the electrodes face, but they can basically be the same as those used in conventional carrier-free electrophoresis devices. . Therefore, platinum is the most commonly used material, and silver-silver chloride electrodes are also used.
ここで言う多孔質担体には、ジュール熱による対流を抑
えるとともに蛋白質の如き電解質の電気泳動を妨げない
という性質が求められる。従ってその孔の直径はO,1
μmから5μmであることが好ましい、さらに蛋白質を
吸着しないことが必要である。また担体は電解¥[緩衝
液中ではその表面に電解を持つため、電場がかけられた
時緩衝液が一方の電極方向に移動をおこす電気浸透とい
う現象が起こる。電気浸透が強く起こると、分離したい
電解質が緩衝液と一緒に移動し電流を流し、緩衝液およ
び充分に分離できなくなる。蛋白質の吸着がなく、電気
浸透が少なく、且つ適当な孔径を有する多孔質担体とし
ては、酢酸セルローズ多孔質膜を積層したものやアクリ
ルアミドゲル・デンプンゲン・濾紙を積層したものか使
用される。The porous carrier mentioned here is required to have properties that suppress convection due to Joule heat and do not interfere with electrophoresis of electrolytes such as proteins. Therefore, the diameter of the hole is O,1
It is preferable that the diameter is from μm to 5 μm, and it is also necessary that no protein be adsorbed. In addition, the carrier has an electrolyte on its surface in a buffer solution, so a phenomenon called electroosmosis occurs in which the buffer solution moves toward one electrode when an electric field is applied. When electroosmosis occurs strongly, the electrolyte to be separated moves together with the buffer solution and current flows, making it impossible to separate the electrolyte from the buffer solution sufficiently. As a porous carrier that does not adsorb proteins, has little electroosmosis, and has an appropriate pore size, a layer of cellulose acetate porous membranes or a layer of acrylamide gel, starch, and filter paper may be used.
多孔質担体の形状は直方体が好ましいが、実質的に電気
泳動操作・給液・集液ができる形状であればよい、直方
体の大きさは分離する電解質の性質、分離精度や処理量
によって違ってくる。電極間の長さ(泳動距離)は通常
は10cm以下、2〜5C1で充分である。液の供給・
排出方向の担体厚さは、分離原液と緩衝液の供給速度が
決まれば、あとは分離に必要な泳動時間(液体の平均滞
留時間)によって必然的に決まる。泳動時間は分離した
電解質の性質によって大きく異なるので、−船釣には言
えない、しかし担体の厚さがあまり厚いと、ジュール熱
が溜まって担体が発熱するので好ましくない0通常はl
0CI以下であることが好ましい、直方体の残るもう一
方の方向(奥行き)は、専ら処理する液体の量によって
決まる。The shape of the porous carrier is preferably a rectangular parallelepiped, but any shape that allows electrophoretic operation, liquid supply, and liquid collection is sufficient.The size of the rectangular parallelepiped varies depending on the properties of the electrolyte to be separated, separation accuracy, and throughput. come. The length between the electrodes (migration distance) is usually 10 cm or less, and 2 to 5 C1 is sufficient. Liquid supply/
The thickness of the carrier in the discharge direction is determined by the electrophoresis time (average residence time of the liquid) required for separation once the supply rates of the separation stock solution and buffer solution are determined. The electrophoresis time varies greatly depending on the properties of the separated electrolyte, so this cannot be said for boat fishing.However, if the thickness of the carrier is too thick, Joule heat will accumulate and the carrier will generate heat, which is undesirable.
The remaining direction (depth) of the rectangular parallelepiped, which is preferably less than or equal to 0 CI, is determined solely by the amount of liquid to be treated.
緩衝液の選択は電気泳動にとっては担体の選択の次に重
要な要素である。これについては前述の底置に詳しく述
べられている。緩衝液選択の最も重要な観点は、分離し
たい二つの両性電解質の等電点の中間pHを有する緩衝
液を選ぶことである。Buffer selection is the second most important factor for electrophoresis, next to carrier selection. This is detailed in the bottom section above. The most important aspect of buffer selection is to select a buffer having a pH intermediate between the isoelectric points of the two ampholytes to be separated.
もうひとつの観点はイオン強度である。イオン強度が強
いと分離はシャープになか、泳動時間が永くなるので、
あとで述べる電圧電流条件の設定と併せ電流を流し、緩
衝液および試行実験を行って決めることになる。Another aspect is ionic strength. If the ionic strength is strong, the separation will be sharp, but the electrophoresis time will be longer.
This will be determined by applying a current, using a buffer solution, and conducting trial experiments in conjunction with setting voltage and current conditions, which will be described later.
両電極間にかける電圧は電極間距離や緩衝液のイオン強
度により最適条件を探さなければならない、!圧をあま
り高く設定すると電流が増加して泳動速度が速くなるが
、ジュール熱の発生が大きくなり担体が高温になってし
まう。The voltage applied between the two electrodes must be found to find the optimal conditions depending on the distance between the electrodes and the ionic strength of the buffer solution! If the pressure is set too high, the current will increase and the migration speed will become faster, but the generation of Joule heat will increase and the carrier will become hot.
こうした電気泳動条件の設定は、使用する担体と同じ材
質の薄膜を使った分析手法の電気泳動実験を行うことに
よっ電流を流し、緩衝液および比較的容易に行うことが
可能である。These electrophoresis conditions can be set relatively easily by conducting an electrophoresis experiment using a thin film made of the same material as the carrier, applying a current, and using a buffer solution.
最後にジュール熱による発熱の防止の必要性について述
べる。ii解質液中に電流を流すと、必然的にジュール
熱が発生する。無担体電気泳動では液体の対流が起こる
事によって生じた熱が外へ逃げる0本濾過型電気泳動法
では積極的に熱を放出しないと、熱が蓄積されて担体や
電解質液が高温になり、溶解している蛋白質が熱変成を
おこす。Finally, we will discuss the necessity of preventing heat generation due to Joule heat. ii When an electric current is passed through the solute, Joule heat is inevitably generated. In carrier-free electrophoresis, heat generated by convection of the liquid escapes to the outside.In zero-filtration electrophoresis, if heat is not actively released, heat will accumulate and the carrier and electrolyte will become hot. Dissolved proteins undergo thermal denaturation.
冷却に効果のある方法としては、電極と含水ゲル層との
間に空間を設けここにも緩衝液を通じる方法がある。ま
た装置の外から装置全体を冷却する方法もよく使われる
。また分離条件の設定におい電流を流し、緩衝液および
緩衝液のイオン強度を可能な限り小さくし、小さな電流
で速く泳動するのもよい方法である。An effective method for cooling is to provide a space between the electrode and the hydrogel layer and pass a buffer solution there as well. A method of cooling the entire device from outside the device is also often used. Another good method is to set the separation conditions by applying a current, reducing the ionic strength of the buffer solution and the buffer solution as much as possible, and performing fast migration with a small current.
また緩衝液や分離原液の供給流束をできるだけ大きくす
ることも、温度の上昇を少なくするに効果がある。Furthermore, increasing the supply flux of the buffer solution or separation stock solution as much as possible is also effective in reducing the temperature rise.
以下実施例に従って更に詳しく説明する。A more detailed explanation will be given below according to examples.
実施例
第1図は本発明の濾過型電気泳動装置の全体を表してい
る。第2図は第1図のA−A’断面を表している。3は
多孔質担体直方体で、本実施例では平均孔径0.5μm
の酢酸セルローズ電気泳動膜を約100枚重に積層した
ものを使っている。Embodiment FIG. 1 shows the entire filtration type electrophoresis apparatus of the present invention. FIG. 2 shows a cross section taken along the line AA' in FIG. 3 is a porous carrier rectangular parallelepiped, and in this example, the average pore diameter is 0.5 μm.
It uses approximately 100 layers of cellulose acetate electrophoresis membranes.
1と2はそれぞれ陰極と陽極である。4aおよび4bは
半透性の含水ゲル層で、ポリビニルアルコールを部分的
にホルマール化したものを使用した。1 and 2 are a cathode and an anode, respectively. 4a and 4b are semipermeable hydrogel layers made of partially formalized polyvinyl alcohol.
5a、5bは緩衝液供給口、6は分離原液供給口、7a
、7bは集液口をそれぞれしめしている。電極間距離は
25III11.担体の厚さ(濾過距離)は14am、
担体の幅は100++mである。5a, 5b are buffer solution supply ports, 6 is separation stock solution supply port, 7a
, 7b respectively indicate liquid collection ports. The distance between the electrodes is 25III11. The thickness of the carrier (filtration distance) is 14 am,
The width of the carrier is 100++ m.
緩衝液にベロナール緩衝液を、分離原液としては人血清
をベロナール緩衝液でl0倍希釈した液を用いた。ポン
プを使って18m1/sinの流量で緩衝液を供給し、
21d/winの流量で分離原液を供給し、電極間に1
5Vの直流電圧をかける。Veronal buffer was used as the buffer solution, and human serum diluted 10 times with veronal buffer was used as the separation stock solution. Supply the buffer solution at a flow rate of 18 ml/sin using a pump,
The separation stock solution is supplied at a flow rate of 21 d/win, and 1 d/win is applied between the electrodes.
Apply 5V DC voltage.
集液ロ7aからはアルダごンが、集液ロ7bからはTグ
ロブリンが得られた。Aldagon was obtained from the liquid collector 7a, and T globulin was obtained from the liquid collector 7b.
第1図は本発明の濾過型電気泳動装置の全体図を表わし
、第2図は第1図のA−A断面を表わす。
図中の番号は下記を表わす。
1:陰電極 2;陽電極
3:多孔質担体 4a、4b:含水ゲル層5a、
5b:緩衝液供給口
6:分離原液供給口
7a、7b、7c、7d:集液口
8:濾過型電気泳動装置
11 : w!A縁体 12:枠体13a
、 13b : II衝液室
14:分離原液室FIG. 1 shows an overall view of the filtration type electrophoresis apparatus of the present invention, and FIG. 2 shows a cross section taken along line AA in FIG. The numbers in the figure represent the following. 1: negative electrode 2; positive electrode 3: porous carrier 4a, 4b: hydrogel layer 5a,
5b: Buffer solution supply port 6: Separation stock solution supply port 7a, 7b, 7c, 7d: Liquid collection port 8: Filtration type electrophoresis device 11: w! A edge body 12: frame body 13a
, 13b: II solution chamber 14: Separation stock solution chamber
Claims (2)
つの面に対して平行に陽電極をその面の外に配置し、そ
の反対面の外に陰電極を面に平行に配置し、両電極間に
電流を流して電場を形成するようにし、この電流の方向
に対して平行な多孔質担体直方体の一方の面に、緩衝液
供給口および分離原液供給口を備え、その反対面は電流
方向とは直角に少なくとも二つ以上に区別されそれぞれ
に集液口を備えていることを特徴とする、濾過型電気泳
動装置。(1) A porous carrier rectangular parallelepiped is housed in a container, a positive electrode is arranged parallel to one surface of the rectangular parallelepiped outside that surface, and a negative electrode is arranged outside the opposite surface parallel to the surface. , a current is passed between both electrodes to form an electric field, and a buffer solution supply port and a separation stock solution supply port are provided on one side of the porous carrier rectangular parallelepiped parallel to the direction of this current, and the opposite side is provided with a buffer solution supply port and a separation stock solution supply port. A filtration type electrophoresis device, characterized in that it is divided into at least two parts perpendicular to the current direction, each of which is provided with a liquid collection port.
間に電流を流し、緩衝液および分離原液をそれぞれ緩衝
液供給口および分離原液供給口に同一流束で供給し、多
孔質担体直方体中にて、分離原液中に溶解している両性
電解質を電気泳動させて分離し、各集液口でそれぞれ透
過して出てくる液を集液する、濾過型電気泳動方法。(2) A current is passed between both electrodes of the filtration type electrophoresis device according to claim (1), and the buffer solution and the separation stock solution are supplied at the same flux to the buffer solution supply port and the separation stock solution supply port, respectively, and the porous A filtration type electrophoresis method in which amphoteric electrolytes dissolved in a separation stock solution are electrophoresed and separated in a rectangular carrier, and the liquid that passes through each liquid collection port is collected.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1199648A JPH0363561A (en) | 1989-08-01 | 1989-08-01 | Device and method for filter type electrophoresis |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1199648A JPH0363561A (en) | 1989-08-01 | 1989-08-01 | Device and method for filter type electrophoresis |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0363561A true JPH0363561A (en) | 1991-03-19 |
Family
ID=16411341
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1199648A Pending JPH0363561A (en) | 1989-08-01 | 1989-08-01 | Device and method for filter type electrophoresis |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0363561A (en) |
-
1989
- 1989-08-01 JP JP1199648A patent/JPH0363561A/en active Pending
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