JPH065226B2 - Method for producing gradient gel membrane for electrophoresis - Google Patents

Method for producing gradient gel membrane for electrophoresis

Info

Publication number
JPH065226B2
JPH065226B2 JP62147827A JP14782787A JPH065226B2 JP H065226 B2 JPH065226 B2 JP H065226B2 JP 62147827 A JP62147827 A JP 62147827A JP 14782787 A JP14782787 A JP 14782787A JP H065226 B2 JPH065226 B2 JP H065226B2
Authority
JP
Japan
Prior art keywords
electrophoresis
liquid
liquids
gradient gel
gel
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 - Fee Related
Application number
JP62147827A
Other languages
Japanese (ja)
Other versions
JPS63313053A (en
Inventor
文隆 寺井
公夫 湯川
峰夫 末藤
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.)
Fujifilm Holdings Corp
Original Assignee
Fuji Photo Film 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 Fuji Photo Film Co Ltd filed Critical Fuji Photo Film Co Ltd
Priority to JP62147827A priority Critical patent/JPH065226B2/en
Publication of JPS63313053A publication Critical patent/JPS63313053A/en
Publication of JPH065226B2 publication Critical patent/JPH065226B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Polymerisation Methods In General (AREA)
  • Application Of Or Painting With Fluid Materials (AREA)
  • Peptides Or Proteins (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、蛋白質特に尿中蛋白質などのように分子量分
布範囲の広い蛋白質を分離分析する為の電気泳動用グラ
ジエントゲル膜の製造方法に関するものである。
TECHNICAL FIELD The present invention relates to a method for producing a gradient gel membrane for electrophoresis for separating and analyzing a protein, particularly a protein having a wide molecular weight distribution range such as a protein in urine. Is.

〔従来の技術〕[Conventional technology]

従来、平板型電気泳動法において、自己支持性のないア
クリルアミドの高分子濃度グラジエントゲルは、一枚の
支持体の上または二枚の支持体の間の濃度の異なるゲル
を電気泳動方向に層状に形成させ、膜状物として用いら
れて来た。
Conventionally, in flat-plate electrophoresis, a high-concentration acrylamide gel with no self-supporting property is formed by layering gels with different concentrations on one support or between two supports in the electrophoresis direction. Formed and used as a film.

しかしながら支持体上にゲルを形成して用いる方法は、
支持体上にゲルを形成する時、泳動槽にセツトする時、
ゲルの保存中、あるいは分析試料を添加するときなどに
誤つてゲルをこわしたり、試料以外のものをゲルの上に
落してゲルを損なつたりすること等があり、操作上細心
と注意と熟練が必要であつた。
However, the method of forming a gel on a support and using it is
When forming a gel on the support, when setting in the electrophoresis tank,
During storage of the gel or when adding an analytical sample, the gel may be broken by mistake, or something other than the sample may be dropped on the gel to damage the gel. Was necessary.

一方二枚のガラス板などでモールドをつくり、この中で
ゲルを形成させて、そのモールドを垂直に保つたまま電
気泳動分析を行う垂直式電気泳動法においては、モール
ドの厚さを均一にすることが困難であつたり、ゲル形成
液がゲル化しないうちに狭いモールド中にゲル液を注入
しなければならないことなど操作上高度の熟練を要して
いた。
On the other hand, in a vertical electrophoresis method in which a mold is made with two glass plates, a gel is formed in the mold, and electrophoretic analysis is performed while the mold is held vertically, the mold thickness is made uniform. However, it requires a high degree of skill in operation such that the gel solution must be injected into a narrow mold before the gel-forming solution gels.

また、ガラス板を用いるために破損しやすいという欠点
があつた。
In addition, since the glass plate is used, there is a drawback that it is easily damaged.

近年工業的に電気泳動用グラジエントゲル物質を製造す
る方法として、アクリルアミドモノマー及び架橋剤の混
合物の水溶液または水分散液を作り、光の照射を吸収
し、モノマーの重合を開始する遊離ラジカル発生物質を
添加した後、該溶液を所望のゲル生成物の形に形成し、
形成した溶液に光照射してモノマー溶液または、分散液
を重合させる架橋させる際、ゲルの多孔度を変えるため
にモノマー溶液に印加する光照射時間を調整する工程を
含む電気泳動グラジエントゲルの製法(特開昭61−2
8512号公報参照)が開示されている。さらに又単量
体、架橋剤および重合開始剤を含有し、濃度の相互に異
る二種類の水溶液を混合比率を漸次変化させながら混合
しつつ成形器に導入し、該成形器中で単量体と架橋剤と
の重合を完了させ、電気泳動方向に重合体の濃度勾配を
有する電気泳動用グラジエントゲルの製造方法(特公昭
61−22903号公報,特公昭61−39617号公
報参照)等が開示されている。
In recent years, as a method for industrially producing a gradient gel substance for electrophoresis, an aqueous solution or an aqueous dispersion of a mixture of an acrylamide monomer and a cross-linking agent is prepared, and a free radical generating substance that absorbs light irradiation and starts polymerization of the monomer is prepared. After addition, the solution is formed into the desired gel product form,
A method for producing an electrophoretic gradient gel including a step of adjusting the light irradiation time applied to the monomer solution in order to change the porosity of the gel when the formed solution is subjected to crosslinking by polymerizing the monomer solution or the dispersion by irradiating the solution ( JP-A-61-2
Japanese Patent No. 8512) is disclosed. Furthermore, two kinds of aqueous solutions containing a monomer, a cross-linking agent and a polymerization initiator and having different concentrations are introduced into a molding machine while mixing while gradually changing the mixing ratio, and a single amount is charged in the molding machine. A method for producing a gradient gel for electrophoresis having a concentration gradient of the polymer in the electrophoretic direction by completing the polymerization between the body and the cross-linking agent (see JP-B-61-22903, JP-B-61-39617) and the like. It is disclosed.

しかしながら、前者の方法は光照射の設備と生産性の悪
さによるコスト高と、ゲルの厚いが厚いための解像性が
悪い点,反応開始剤が製造終了後も光の存在下で重合・
架橋反応をおこし、安定性,再現性のあるグラジエント
ゲルが得られない等の問題点を有し、後者はやはりバツ
チ式製造方式であるため生産性が悪く、又電気泳動分離
用媒体液を成形器に分岐流入する際に均一に分岐するこ
とが難しく、再現性のあるグラジエントゲルが得られな
い等の問題点を有していた。
However, the former method is costly due to light irradiation equipment and poor productivity, and the resolution is poor due to the thick and thick gel, and the reaction initiator polymerizes in the presence of light even after the production is completed.
There is a problem that a gradient gel with stability and reproducibility cannot be obtained due to a crosslinking reaction. The latter is also a batch type manufacturing method, so productivity is poor, and a medium solution for electrophoretic separation is molded. It has a problem that it is difficult to uniformly branch when flowing into the vessel and a reproducible gradient gel cannot be obtained.

上記問題点を解消し、生産性が高く、再現性の高い電気
泳動用グラジエントゲル膜の製造方法として本出願人に
は先に連続的に流量比を変えた濃・淡二種のモノマー液
と一定量の重合反応開始剤液とをスタテイツクミクサー
で混合し電気泳動分離用媒体液を調液し、連続的に走行
するウエブ上に該電気泳動分離用媒体液を塗布する電気
泳動用グラジエントゲル膜の製造方法を提案した。
As a method for producing a gradient gel film for electrophoresis, which solves the above problems and has high productivity and high reproducibility, the applicant of the present invention has previously used two types of concentrated and light monomer liquids in which the flow ratio was continuously changed. An electrophoretic gradient gel in which a certain amount of a polymerization reaction initiator liquid is mixed with a static mixer to prepare an electrophoretic separation medium liquid, and the electrophoretic separation medium liquid is applied onto a continuously running web. A method of manufacturing the membrane was proposed.

〔発明が解決しようとする問題点〕[Problems to be solved by the invention]

前記塗布による方法は優れた方法であり、濃・淡2液の
液量比の切換え及び濃度勾配が多段階で、高級な電気泳
動用グラジエント膜としての生産には適しているが、一
方単純な数段階の濃度勾配の電気泳動用グラジエントゲ
ル膜を再現性高く生産性も高く製造する方法が望まれて
いた。
The coating method is an excellent method and is suitable for production as a high-grade electrophoretic gradient film because of the switching of the liquid volume ratio of the dark and light two liquids and the multi-stage concentration gradient. A method for producing a reproducible and highly productive gradient gel membrane for electrophoresis having a concentration gradient of several steps has been desired.

本発明の目的は上記問題点に対処し、単純な数段階の濃
度勾配をもつた蛋白質分離分析電気泳動用グラジエント
膜を再現性高く、又生産性良く製造する方法を提供する
ことにある。
An object of the present invention is to address the above problems and to provide a method for producing a gradient membrane for protein separation analysis electrophoresis having a simple concentration gradient of several steps with high reproducibility and high productivity.

〔問題点を解決するための手段〕[Means for solving problems]

本発明の前記目的は連続的に走行するウエブ上に電気泳
動分離用媒体液を塗布する蛋白質分析電気泳動用グラジ
エントゲル膜の製造方法において、複数段階の濃度の異
なるモノマー液とそれぞれの重合開始剤液とを各々、混
合・調液し、その各々の混合液を塗布ヘッドの複数個の
給液口に濃度順に並べて別々に供給し、各々スロツト幅
に液を拡げ、複数種の混合液を横一列の塗布膜としてス
ロツト開口よりウエブ上に塗布することを特徴とする、
変性剤として陰イオン界面活性剤を含む電気泳動用グラ
ジエントゲル膜の製造方法によつて達成される。
The above-mentioned object of the present invention is a method for producing a gradient gel membrane for protein analysis electrophoresis in which a medium solution for electrophoretic separation is applied onto a continuously running web, and a monomer solution having different concentrations at a plurality of stages and respective polymerization initiators. Mix and prepare the liquid and the liquid, respectively, and supply the mixed liquids to the plurality of liquid supply ports of the coating head in the order of concentration and separately, and spread the liquid in each slot width to horizontally mix multiple liquids. Characterized in that it is applied on the web from the slot opening as a single-row coating film,
This is achieved by a method for producing a gradient gel membrane for electrophoresis containing an anionic surfactant as a denaturant.

本発明において連続的に走行するウエブとは、平面性の
よいシート状のもので非導電性かつ実質的に水不透過性
であれば、どのような材質のものでもよく、ポリエチレ
ンテレフタレート,ビスフエノールAのポリカルボネー
トのようなポリエステル,ポリメチルメタクリレート,
ポリエチレン,ポリスチレン,ポリ塩化ビニルなどのビ
ニル系重合体,ナイロンなどのポリアミド、およびそれ
らの共重合体(例、塩化ビニリデン・塩化ビニルコポリ
マー)が好ましく用いられる。
In the present invention, the continuously running web may be made of any material as long as it is a sheet having good flatness, non-conductive and substantially impermeable to water, such as polyethylene terephthalate and bisphenol. Polyesters such as A's polycarbonate, polymethylmethacrylate,
Vinyl-based polymers such as polyethylene, polystyrene and polyvinyl chloride, polyamides such as nylon, and copolymers thereof (eg, vinylidene chloride / vinyl chloride copolymer) are preferably used.

本発明における電気泳動分離用媒体液とは、電気泳動分
離用媒体膜を作れるものであれば何でもよく、その代表
的なものとしては、アクリルアミドゲル,アガロースゲ
ル,澱粉ゲル,寒天ゲル等の原料液となる液をいう。
The medium solution for electrophoretic separation in the present invention may be anything as long as it can form a medium film for electrophoretic separation, and typical examples thereof include a raw material solution such as acrylamide gel, agarose gel, starch gel, agar gel and the like. It means the liquid that becomes.

本発明の電気泳動用媒体材料は、主として蛋白質または
複合蛋白質(たとえば、リポプロテイン,糖プロテイン
など)の分析に有利に用いられるものであり、電気泳動
用媒体層には、変性剤として陰イオン界面活性剤を含有
させることができる。この他に、DNAの塩基配列を決
定する目的で電気泳動用グラジェント膜を用いる場合に
は、変性剤として尿素が使われるが、本発明のように蛋
白質の分析が目的の場合には、蛋白質の等電点が多価で
あるため尿素を用いると電荷が一定しないので、分子当
たり一定の電荷を与える陰イオン界面活性剤を用いるの
が有効である。このように、分析試料が蛋白質または複
合蛋白質(例えばリポ蛋白質,糖蛋白質など)の場合に
は陰イオン界面活性剤を含ませることは好ましいか、ま
たは必須であることが多い。陰イオン界面活性剤をゲル
媒体層に含有させないことがあることは勿論である。た
とえば陰イオン界面活性剤を含有しないゲル媒体層は、
DNAフラグメント分析に基づく遺伝病診断あるいは制
限酵素分解を利用したDNA構造解析などの目的に用い
ることができる。
The electrophoretic medium material of the present invention is advantageously used mainly for the analysis of proteins or complex proteins (for example, lipoproteins, glycoproteins, etc.), and the electrophoretic medium layer contains an anionic interface as a denaturant. An activator can be included. In addition to this, when a gradient membrane for electrophoresis is used for the purpose of determining the nucleotide sequence of DNA, urea is used as a denaturing agent. Since the isoelectric point is polyvalent and the charge is not constant when urea is used, it is effective to use an anionic surfactant that gives a constant charge per molecule. Thus, when the analysis sample is a protein or complex protein (eg lipoprotein, glycoprotein, etc.), it is often preferable or essential to include an anionic surfactant. Of course, the anionic surfactant may not be contained in the gel medium layer. For example, a gel medium layer containing no anionic surfactant is
It can be used for the purpose of genetic disease diagnosis based on DNA fragment analysis or DNA structure analysis utilizing restriction enzyme decomposition.

陰イオン界面活性剤を電気泳動用媒体層に含有させるこ
とにより、蛋白質または複合蛋白質の効率的な分離およ
びそれらの分子量測定が可能となる。
By including an anionic surfactant in the medium layer for electrophoresis, it becomes possible to efficiently separate proteins or complex proteins and measure their molecular weights.

陰イオン界面活性剤の例としてはアルキル硫酸塩を挙げ
ることができ、特に炭素原子数10以上の長鎖アルキル
基を有するアルキル硫酸塩が好ましく用いられる。塩を
形成する陽イオンとしては、ナトリウムイオン,カリウ
ムイオン,リチウムイオン等のアルカリ金属イオンが一
般的であり、これらのうちではナトリウムイオンが用い
やすい。アルキル硫酸塩のうちではドデシル硫酸塩(ナ
トリウム塩,カルウム塩,リチウム塩等)が好ましく、
なかでもドデシル硫酸ナトリウム(SDS)が最も好ま
しい。SDSを本発明のゲル媒体層に含有させることに
より蛋白質または複合蛋白質の効率的な分離およびそれ
らの分子量測定が可能となる。
Examples of the anionic surfactant include alkylsulfates, and alkylsulfates having a long-chain alkyl group having 10 or more carbon atoms are particularly preferably used. Alkali metal ions such as sodium ions, potassium ions and lithium ions are generally used as the cations that form salts, and of these, sodium ions are easy to use. Among the alkyl sulfates, dodecyl sulfate (sodium salt, calcium salt, lithium salt, etc.) is preferable,
Of these, sodium dodecyl sulfate (SDS) is most preferable. The inclusion of SDS in the gel medium layer of the present invention enables efficient separation of proteins or complex proteins and measurement of their molecular weight.

変性剤としての陰イオン界面活性剤の含有量はゲル形成
液に対して約0.05W/V%から約2.0W/V%、好
ましくは約0.1W/V%から約1.5W/V%の範囲
である。
The content of the anionic surfactant as a modifier is about 0.05 W / V% to about 2.0 W / V%, preferably about 0.1 W / V% to about 1.5 W / V with respect to the gel forming solution. % Range.

本発明における電気泳動分離用媒体液の塗布方法として
は、スライドビードコート,エクストルージョンコー
ト,ホツパーコート,カーテンコート等が用いられる。
塗布する媒体液の厚みは分離の目的に応じて選ばれるが
通常50μmから約2.0mm、好ましく約100μmから
約1.0mmの範囲とされる。
As a method for applying the medium liquid for electrophoretic separation in the present invention, slide bead coating, extrusion coating, hopper coating, curtain coating and the like are used.
The thickness of the medium liquid to be applied is selected depending on the purpose of separation, but is usually in the range of 50 μm to about 2.0 mm, preferably about 100 μm to about 1.0 mm.

本発明における電気泳動用グラジエントゲル膜とは、一
つの製品単位長内に特に段階的濃度勾配をもつたものを
いう。又本発明において複数段階の濃度の異なるモノマ
ー液とは、使用目的に応じて3〜35W/V%内に複数
段階に濃度を変えたものを言う。
The gradient gel film for electrophoresis in the present invention refers to one having a stepwise concentration gradient within one product unit length. In the present invention, the term "monomer liquid having different concentrations in multiple stages" refers to a liquid in which the concentration is changed in multiple stages within 3 to 35 W / V% depending on the purpose of use.

各濃度モノマー液とそれぞれの重合開始剤液との混合装
置としては、タンク混合であつても、その他の如何なる
方法でもよいが、好ましい方法としてスタテイツクミク
サーを用いることが出来る。スタテイツクミクサーと
は、流体がミクサーの中に通される時、流体自身の運動
により撹拌作用を行うものをいい、管状のものとしては
スパイラルチューブ、左右交互らせん状、又は邪魔板入
りプロペラ状等がある。
A mixing device for mixing each concentration of the monomer liquid and each of the polymerization initiator liquids may be tank mixing or any other method, but a preferred method is a static mixer. A static mixer is a mixer that agitates by the motion of the fluid itself when the fluid is passed through the mixer, and as a tubular one, a spiral tube, alternating left and right spirals, or a propeller with baffles, etc. There is.

本発明の実施態様を図を用いて説明する。Embodiments of the present invention will be described with reference to the drawings.

第1図は本発明の電気泳動用グラジエントゲル膜の製造
方法の1実施例の工程図である。本実施例としては液濃
度を5段階に分けた例で説明する。
FIG. 1 is a process chart of one embodiment of the method for producing a gradient gel film for electrophoresis of the present invention. In this embodiment, an example in which the liquid concentration is divided into 5 stages will be described.

電気泳動分離用媒体液6(a〜e)は、モノマー液1
(a〜e),そのモノマー液に対応する重合反応開始剤
液2(a〜e)を各タンクで調整し、それぞれを定流量
ポンプ3(a〜e),4(a〜e)によつて圧送し、ス
タテイツクミクサー5(a〜e)内で撹拌・混合するこ
とによつて各混合液である電気泳動用分離用媒体液6
(a〜e)を調液する。
The electrophoretic separation medium liquid 6 (a to e) is the monomer liquid 1
(A to e), the polymerization reaction initiator liquid 2 (a to e) corresponding to the monomer liquid is adjusted in each tank, and each is adjusted by the constant flow rate pumps 3 (a to e) and 4 (a to e). Then, the mixture medium 6 for electrophoresis, which is each mixed solution, is sent by pressure and is stirred and mixed in the static mixer 5 (a to e).
Prepare (a to e).

5種類の液6(a〜e)は、ポンプ3(a〜e)4(a
〜e)の圧力によつて塗布ヘツド7の夫々の給液口14
(a〜e)に供給され、スロツト開口16よりコーテイ
ングローラ8上のウエブ9上に横一列に並べて塗布され
る。塗布の安定性のため塗布液ビードの後側を背圧にす
るため差圧チヤンバー10が設けられている。
The five types of liquids 6 (a to e) are pumps 3 (a to e) 4 (a
~ E) pressure applied to each of the liquid supply ports 14 of the coating head 7
(A) to (e), and are applied side by side on the web 9 on the coating roller 8 through the slot opening 16. A differential pressure chamber 10 is provided to apply back pressure to the rear side of the coating liquid bead for stability of coating.

第2図はウエブ9上に5種の濃度の異なる電気泳動分離
用媒体液6(a〜e)が塗布された状態を説明する平面
図(a),側面図(b),断面図(c)である。
FIG. 2 is a plan view (a), a side view (b), and a cross-sectional view (c) illustrating a state in which five kinds of electrophoretic separation medium liquids 6 (a to e) having different concentrations are applied on the web 9. ).

塗布ヘツド7の供給口14(a〜e)にそれぞれ混合液
6(a〜e)が供給され、スロツト開口16より横一例
となつてウエブ9上に塗布される。即ち電気泳動用グラ
ジエントゲル膜としてはウエブの幅方向に製品単位が作
られ、ウエブは切断機によつて加工されることになる。
The mixed liquids 6 (a to e) are respectively supplied to the supply ports 14 (a to e) of the coating head 7 and are applied on the web 9 through the slot openings 16 as a horizontal example. That is, as the gradient gel film for electrophoresis, product units are formed in the width direction of the web, and the web is processed by a cutting machine.

第3図は本発明に用いる塗布ヘツドの側面断面図,第4
図は第3図の正面断面図を示す。
FIG. 3 is a side sectional view of the coating head used in the present invention,
The figure shows a front sectional view of FIG.

第3図,第4図において,5種類の液は夫々ポンプ17
(a〜e)によつて塗布ヘツド7の給液口14(a〜
e)に液を送液する。各液は塗布ヘツド7内でギヤビテ
イなしでスロツト15(a〜e)によりそれぞれ幅方向
に拡げられる。この場合各スロツト幅は狭くスロツト内
の液の拡がり角度θ≦40°ですますことが出来るので
液は自然に拡がり、液の滞留及びそれによつて生じる異
物の発生をおこすことがない。スロツト開口16前では
各隣接する液は相接しスロツト開口16では各液が横一
列の塗布膜となり、ウエブ9上に塗布されることにな
る。
In FIG. 3 and FIG. 4, the five kinds of liquids are pump 17 respectively.
(A to e), the liquid supply port 14 (a to
Liquid is sent to e). The respective liquids are spread in the width direction in the coating head 7 by the slots 15 (a to e) without a gear bit. In this case, the width of each slot is narrow and the spread angle of the liquid in the slot can be set to θ ≦ 40 °, so that the liquid spreads naturally and the accumulation of liquid and the generation of foreign matter caused by it do not occur. The adjacent liquids are in contact with each other in front of the slot opening 16, and the liquids form a coating film in a horizontal row in the slot opening 16 and are applied onto the web 9.

〔作 用〕[Work]

連続的に走行するウエブ上に電気泳動分離用媒体液を塗
布する蛋白質分析電気泳動用グラジエントゲル膜の製造
方法において、複数段階の濃度の異なるモノマー液とそ
れぞれの重合開始剤液とを各々混合・調液し、その各々
の混合液を塗布ヘツドの複数個の給液口に濃度順に並べ
て別々に供給し、各々スロツト幅に液を拡げ、複数種の
混合液が一線の塗布膜としてスロツト開口よりウエブ上
に塗布されることを特徴とする蛋白質分析電気泳動用グ
ラジエントゲル膜の製造方法により、電気泳動用グラジ
エント膜としてはウエブ幅方向に製品単位長を形成す
る。各段階濃度の混合液は、工程において濃度変化なく
一定条件で調液されるので品質は安定しており、又塗布
ヘツドにおいては塗布液(混合液のこと)は自然に拡が
つて塗布膜として塗布されるので滞留による異物の発生
もなく良品質の塗布膜が得られ、安定した製造条件によ
り製品の品質及び再現性は良く、且つ生産性も高い。
In a method for producing a gradient gel membrane for protein analysis electrophoresis, in which a medium solution for electrophoretic separation is applied on a continuously running web, a monomer solution having different concentrations in a plurality of stages and respective polymerization initiator solutions are mixed and mixed. Liquid is prepared, and each of the mixed liquids is arranged separately in the order of concentration to a plurality of liquid supply ports of the coating head, and the liquids are spread over each slot width, and a plurality of mixed liquids form a straight line coating film from the slot opening. A product unit length is formed in the web width direction as the electrophoresis gradient film by the method for producing a gradient gel film for protein analysis electrophoresis, which is characterized by being applied onto a web. Since the mixed solution of each step concentration is prepared under constant conditions without any change in the concentration in the process, the quality is stable, and in the coating head, the coating solution (mixed solution) naturally spreads to form a coating film. Since it is applied, a good quality coating film can be obtained without the generation of foreign matter due to stagnation, and the quality and reproducibility of the product are good and the productivity is high due to stable manufacturing conditions.

〔実施例〕〔Example〕

本発明は1実施例について第1,2,3,又は4図を用
いて説明する。
The present invention will be described with reference to one embodiment with reference to FIGS.

電気泳動分離用媒体液 低濃度モノマー液1aとして アクリルアミド …102.6g N,N′−メチレンビスアクリルアミド…5.4g ドデシル硫酸ナトリウム …1.8g 〔pH緩衝剤〕 1.5M−Tris−塩酸(pH8.9) …450ml 脱イオン水を加えて出来上がり1800mlにする。Medium liquid for electrophoretic separation As low-concentration monomer liquid 1a Acrylamide 102.6 g N, N'-methylenebisacrylamide 5.4 g Sodium dodecyl sulfate 1.8 g [pH buffer] 1.5 M-Tris-hydrochloric acid (pH 8.9) Add 450ml deionized water to make 1800ml.

高濃度モノマー液1eとして アクリルアミド…342g N,N′−メチレンビスアクリルアミド…18g ドデシル硫酸ナトリウム …1.8g 〔pH緩衝剤〕 1.5M−Tris−塩酸(pH8.9) …450ml 脱イオン水を加えて出来上がり1800mlにする。更に
その間の濃度の液として、低中濃度モノマー液1b,中
濃度モノマー液1c,高中濃度モノマー液1dを作る。
1b,1c,1dの各モノマー液は、アクリルアミド及
びN,N′−メチレンビスアクリルアミドのそれぞれの
量を1a及び1eの間の値で等間隔にとる他は、1a及
び1eと同じとする。
High-concentration monomer liquid 1e Acrylamide 342g N, N'-methylenebisacrylamide 18g Sodium dodecyl sulfate 1.8g [pH buffer] 1.5M-Tris-hydrochloric acid (pH 8.9) 450ml Deionized water is added Bring to 1800 ml. Further, as a liquid having a concentration between them, a low-medium concentration monomer liquid 1b, a medium-concentration monomer liquid 1c, and a high-medium concentration monomer liquid 1d are prepared.
Each of the monomer liquids 1b, 1c and 1d is the same as 1a and 1e except that the respective amounts of acrylamide and N, N'-methylenebisacrylamide are equally spaced with a value between 1a and 1e.

(註)Tris:トリス(ヒドロキシメチル)アミノメタン
次に重合反応開始剤液2(a〜e)として 2.5%ペルオキソニ硫酸アンモニウム水溶液 …43.2ml 25%N,N,N′,N′-テトラメチルエチレンジアミン液 …0.45ml 0.375%リボフラビンリン酸エステルナトリウム塩水溶液…30ml の混合液を作り、 次に定流量送液ポンプ3(a〜e)で各モノマー液1
(a〜e)を7.6ml/min,それに加えるに重合反応開始
剤液2(a〜e)を定流量送液ポンプ4で流量0.311ml
/minずつ、共にスタイツクミクサー5(a〜e)内に
送液する。
(Note) Tris: Tris (hydroxymethyl) aminomethane Next, 2.5% ammonium peroxodisulfate aqueous solution as polymerization reaction initiator liquid 2 (a to e) ... 43.2 ml 25% N, N, N ', N'-tetramethylethylenediamine liquid ... 0.45 ml 0.375% riboflavin phosphate sodium salt aqueous solution ... Make a mixed solution of 30 ml, and then use the constant flow rate feed pumps 3 (a to e) to remove each monomer solution 1
(A to e) is 7.6 ml / min, and in addition, polymerization reaction initiator liquid 2 (a to e) is added by a constant flow rate liquid feed pump 4 to a flow rate of 0.311 ml.
/ Min each, and liquid is fed into the Stykix mixer 5 (a to e) together.

スタテイツクミクサー5(a〜e)内では上記2液が自
力により混合撹拌し、混合液である電気泳動分離用媒体
液6(a〜e)が出来る。
In the static mixer 5 (a-e), the above-mentioned two liquids are mixed and stirred by their own force to form a mixed liquid for electrophoretic separation 6 (a-e).

塗布ヘツド7の各給液口14(a〜e)より混合液であ
る電気泳動分離用媒体液6(a〜e)が供給され、スロ
ツト開口16よりウエブ9上に塗布される。
The electrophoretic separation medium liquid 6 (a to e), which is a mixed liquid, is supplied from the liquid supply ports 14 (a to e) of the coating head 7, and is applied onto the web 9 through the slot openings 16.

その時の各濃度の電気泳動分離用媒体液6(a〜e)の
塗布状況は第2図(a)に示したとおりであり、塗布され
たゲル膜の濃度は5段階に分けられて連続的に塗布され
る状態になる。
The state of application of the electrophoretic separation medium liquids 6 (a to e) at each concentration at that time is as shown in FIG. 2 (a), and the concentration of the applied gel film is divided into 5 stages and is continuously. Is ready to be applied to.

尚、電気泳動分離用媒体膜としての製品は、塗布後硬化
処理をする行程,試料注入口としてコーム(櫛)を打抜
く行程,カバーシートを貼付ける行程,製品長さに切断
する行程,等を経て初めて製品となる。
In addition, the product as a medium film for electrophoretic separation is a process of curing after coating, a process of punching a comb (comb) as a sample injection port, a process of applying a cover sheet, a process of cutting to a product length, etc. It becomes a product only after going through.

しかしこれらの工程は如何なる方法,手段を用いても本
発明とは関係がない。
However, these methods are not related to the present invention by using any method or means.

〔発明の効果〕〔The invention's effect〕

本発明は連続的に走行するウエブ上に電気泳動分離用媒
体液を塗布する蛋白質分析電気泳動用グラジエントゲル
膜の製造方法において、複数段階の濃度の異なるモノマ
ー液とそれぞれの重合反応開始剤液とを各々混合・調液
し、その各々の混合液を塗布ヘツドの複数個の給液口に
濃度順に並べて別々に供給し、各々スロツト幅に液を拡
げ、複数種の混合液が横一列の塗布膜としてスロツト開
口よりウエブ上に塗布されることを特徴とする変性剤と
して陰イオン界面活性剤を含む電気泳動用グラジエント
ゲル膜の製造方法により単純な数段階の濃度勾配の電気
泳動用グラジエントゲル膜を生産性良く、製品品質の安
定性、再現性よく製造することが出来た。
The present invention is a method for producing a gradient gel membrane for protein analysis electrophoresis in which a medium solution for electrophoretic separation is applied on a continuously running web, and a monomer solution having different concentrations in a plurality of stages and respective polymerization reaction initiator solutions Are mixed and prepared, and the mixed liquids are lined up in multiple supply ports of the coating head in the order of concentration and supplied separately, and the liquids are spread in each slot width, and multiple types of mixed liquids are applied in a horizontal row. A gradient gel membrane for electrophoresis having a simple concentration gradient of several steps by a method for producing a gradient gel membrane for electrophoresis containing an anionic surfactant as a denaturant characterized by being applied onto a web through a slot opening as a membrane Was manufactured with good productivity, stable product quality, and good reproducibility.

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

第1図は本発明の電気泳動用グラジエントゲル間の製造
方法の工程図、第2図は本発明の濃・淡5種の電気泳動
分離用媒体液の塗布状況説明図。第3図は本発明に係わ
る塗布ヘツドの側面断面図、第4図は第3図の正面断面
図である。 1(a〜e)…モノマー液、2…2(a−e)…重合反
応開始剤液、3(a〜e),4(ae)…定流量送液ポ
ンプ、5(a〜e)…スタテイツクミクサー、6(a〜
e)…電気泳動分離用媒体液、7…塗布ヘツド、8…コ
ーテイングローラ、9…ウエブ、10…差圧チヤンバ
ー、11…コントローラ、12…コンピユータリンケー
ジアダプタ、13…ウエブ、14(a〜e)…給液口、
15(a〜e)…スロツト、16…スロツト開口、17
(a〜e)…定量ポンプ。
FIG. 1 is a process diagram of a method for producing an electrophoretic gradient gel according to the present invention, and FIG. 2 is an explanatory diagram of a coating state of 5 kinds of medium liquids for electrophoresis separation of dark and light according to the present invention. FIG. 3 is a side sectional view of the coating head according to the present invention, and FIG. 4 is a front sectional view of FIG. 1 (a to e) ... Monomer liquid, 2 ... 2 (a to e) ... Polymerization reaction initiator liquid, 3 (a to e), 4 (ae) ... Constant flow rate liquid feed pump, 5 (a to e) ... Status Mixer, 6 (a-
e) ... Electrophoretic separation medium solution, 7 ... Coating head, 8 ... Coating roller, 9 ... Web, 10 ... Differential pressure chamber, 11 ... Controller, 12 ... Computer linkage cage adapter, 13 ... Web, 14 (a to e) … Filling port,
15 (a to e) ... Slot, 16 ... Slot opening, 17
(A to e) ... Metering pump.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】連続的に走行するウエブ上に電気泳動分離
用媒体液を塗布する蛋白質分析電気泳動用グラジェント
ゲル膜の製造方法において、複数段階の濃度の異なるモ
ノマー液とそれぞれの重合開始剤液とを各々混合・調液
し、その各々の混合液を塗布ベッドの複数個の給液口に
別々に濃度順に並べて供給し、各々スロット幅に液を拡
げ、複数種の混合液を横一列の塗布膜としてスロット開
口よりウェブ上に塗布することを特徴とする、変性剤と
して陰イオン界面活性剤を含む電気泳動用グラジェント
ゲル膜の製造方法。
1. A method for producing a gradient gel membrane for protein analysis electrophoresis, wherein a medium solution for electrophoretic separation is applied onto a continuously running web, and a monomer solution having different concentrations in a plurality of stages and respective polymerization initiators. Mix and prepare liquids, and supply the mixed liquids to the multiple liquid supply ports of the coating bed separately in the order of concentration, and spread the liquid into each slot width. The method for producing a gradient gel film for electrophoresis containing an anionic surfactant as a modifier, characterized in that the coating film is applied onto the web through a slot opening.
【請求項2】前記複数種の濃度の異なるモノマー液の濃
度の変化が3〜35W/V%であることを特徴とする特
許請求の範囲第1項記載の蛋白質分析電気泳動用グラジ
ェントゲル膜の製造方法。
2. The gradient gel membrane for protein analysis electrophoresis according to claim 1, wherein the change in concentration of the monomer liquids having different concentrations is 3 to 35 W / V%. Manufacturing method.
JP62147827A 1987-06-16 1987-06-16 Method for producing gradient gel membrane for electrophoresis Expired - Fee Related JPH065226B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62147827A JPH065226B2 (en) 1987-06-16 1987-06-16 Method for producing gradient gel membrane for electrophoresis

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62147827A JPH065226B2 (en) 1987-06-16 1987-06-16 Method for producing gradient gel membrane for electrophoresis

Publications (2)

Publication Number Publication Date
JPS63313053A JPS63313053A (en) 1988-12-21
JPH065226B2 true JPH065226B2 (en) 1994-01-19

Family

ID=15439131

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62147827A Expired - Fee Related JPH065226B2 (en) 1987-06-16 1987-06-16 Method for producing gradient gel membrane for electrophoresis

Country Status (1)

Country Link
JP (1) JPH065226B2 (en)

Also Published As

Publication number Publication date
JPS63313053A (en) 1988-12-21

Similar Documents

Publication Publication Date Title
US4968535A (en) Method of producing gradient gel medium membrane for electrophoresis
US6719840B2 (en) In situ crystal growth and crystallization
US3384564A (en) Electrophoretic process for simultaneously spearating and concentrating particles
Kleparnik et al. DNA diagnostics by capillary electrophoresis
EP2906330B1 (en) Coated ion exchange membranes
US4966792A (en) Method of producing gradient gel medium membrane for electrophoresis
JP2003519359A (en) Continuous gel casting method and apparatus
CN103237600A (en) Anion exchange membranes and process for making same
EP0042157B1 (en) Electrode for measurement of ion activity
JP3071927B2 (en) Method for producing gel plate for electrophoresis
JPH065226B2 (en) Method for producing gradient gel membrane for electrophoresis
JPH05203621A (en) Manufacture of polyacrylamide gel plate for electrophoresis
US3655541A (en) CONTINUOUS ELECTROPHORESIS CELL WITH LATERAL pH GRADIENT
JPH01138454A (en) Production of gradient gel film for electrophoresis
JPH063435B2 (en) Method for producing gradient gel membrane for electrophoresis
JPH0553227B2 (en)
JPS63313056A (en) Production of gradient gel film for electrophoresis
JPS63313054A (en) Production of gradient gel film for electrophoresis
DE3855429T2 (en) Electrophoresis method
JPH01132951A (en) Manufacture of gradient gel for electrophoresis
JPS63313055A (en) Production of gradient gel film for electrophoresis
JPS63298045A (en) Production of gradient gel film for electrophoresis
JPS63313050A (en) Production of gradient gel film for electrophoresis
McCann et al. Separation of Latex Particles According to Size by Continuous Electrophoresis
JPS63298049A (en) Production of gradient gel film for electrophoresis

Legal Events

Date Code Title Description
R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

LAPS Cancellation because of no payment of annual fees