JPH01138454A - Production of gradient gel film for electrophoresis - Google Patents
Production of gradient gel film for electrophoresisInfo
- Publication number
- JPH01138454A JPH01138454A JP62295141A JP29514187A JPH01138454A JP H01138454 A JPH01138454 A JP H01138454A JP 62295141 A JP62295141 A JP 62295141A JP 29514187 A JP29514187 A JP 29514187A JP H01138454 A JPH01138454 A JP H01138454A
- Authority
- JP
- Japan
- Prior art keywords
- liquids
- liquid
- electrophoresis
- monomer
- coating
- 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 25
- 239000011544 gradient gel Substances 0.000 title claims description 21
- 238000004519 manufacturing process Methods 0.000 title claims description 21
- 108010025899 gelatin film Proteins 0.000 title claims description 3
- 239000007788 liquid Substances 0.000 claims abstract description 83
- 238000000576 coating method Methods 0.000 claims abstract description 29
- 239000011248 coating agent Substances 0.000 claims abstract description 28
- 239000000178 monomer Substances 0.000 claims abstract description 21
- 239000003999 initiator Substances 0.000 claims abstract description 10
- 239000012528 membrane Substances 0.000 claims description 27
- 238000000926 separation method Methods 0.000 claims description 21
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 claims description 8
- 239000004202 carbamide Substances 0.000 claims description 8
- 238000006116 polymerization reaction Methods 0.000 claims description 7
- 239000003795 chemical substances by application Substances 0.000 claims description 4
- 239000003505 polymerization initiator Substances 0.000 claims description 3
- 230000003068 static effect Effects 0.000 abstract description 9
- 238000002156 mixing Methods 0.000 abstract description 5
- 239000000203 mixture Substances 0.000 abstract description 3
- 238000003756 stirring Methods 0.000 abstract description 3
- 230000000379 polymerizing effect Effects 0.000 abstract 1
- 238000000034 method Methods 0.000 description 18
- 239000000499 gel Substances 0.000 description 14
- 239000000243 solution Substances 0.000 description 11
- MUBZPKHOEPUJKR-UHFFFAOYSA-N Oxalic acid Chemical compound OC(=O)C(O)=O MUBZPKHOEPUJKR-UHFFFAOYSA-N 0.000 description 3
- 239000007864 aqueous solution Substances 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 239000011521 glass Substances 0.000 description 3
- -1 polyethylene terephthalate Polymers 0.000 description 3
- HRPVXLWXLXDGHG-UHFFFAOYSA-N Acrylamide Chemical compound NC(=O)C=C HRPVXLWXLXDGHG-UHFFFAOYSA-N 0.000 description 2
- ZHNUHDYFZUAESO-UHFFFAOYSA-N Formamide Chemical compound NC=O ZHNUHDYFZUAESO-UHFFFAOYSA-N 0.000 description 2
- 239000011324 bead Substances 0.000 description 2
- 229920001577 copolymer Polymers 0.000 description 2
- 238000005520 cutting process Methods 0.000 description 2
- 239000008367 deionised water Substances 0.000 description 2
- 229910021641 deionized water Inorganic materials 0.000 description 2
- 238000004090 dissolution Methods 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000011259 mixed solution Substances 0.000 description 2
- 239000003607 modifier Substances 0.000 description 2
- 229920002401 polyacrylamide Polymers 0.000 description 2
- 229920006395 saturated elastomer Polymers 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- YAHTUJLFNVSDAI-UHFFFAOYSA-N 1-ethoxy-4-hexoxy-1,4-dioxobutane-2-sulfonic acid Chemical compound CCCCCCOC(=O)CC(S(O)(=O)=O)C(=O)OCC YAHTUJLFNVSDAI-UHFFFAOYSA-N 0.000 description 1
- OEPOKWHJYJXUGD-UHFFFAOYSA-N 2-(3-phenylmethoxyphenyl)-1,3-thiazole-4-carbaldehyde Chemical compound O=CC1=CSC(C=2C=C(OCC=3C=CC=CC=3)C=CC=2)=N1 OEPOKWHJYJXUGD-UHFFFAOYSA-N 0.000 description 1
- PKZCRWFNSBIBEW-UHFFFAOYSA-N 2-n,2-n,2-trimethylpropane-1,2-diamine Chemical compound CN(C)C(C)(C)CN PKZCRWFNSBIBEW-UHFFFAOYSA-N 0.000 description 1
- 229920001817 Agar Polymers 0.000 description 1
- 229920000936 Agarose Polymers 0.000 description 1
- 239000004971 Cross linker Substances 0.000 description 1
- 238000001712 DNA sequencing Methods 0.000 description 1
- ZGTMUACCHSMWAC-UHFFFAOYSA-L EDTA disodium salt (anhydrous) Chemical compound [Na+].[Na+].OC(=O)CN(CC([O-])=O)CCN(CC(O)=O)CC([O-])=O ZGTMUACCHSMWAC-UHFFFAOYSA-L 0.000 description 1
- 239000004677 Nylon Substances 0.000 description 1
- 239000004952 Polyamide Substances 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 239000011543 agarose gel Substances 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- IISBACLAFKSPIT-UHFFFAOYSA-N bisphenol A Chemical compound C=1C=C(O)C=CC=1C(C)(C)C1=CC=C(O)C=C1 IISBACLAFKSPIT-UHFFFAOYSA-N 0.000 description 1
- 239000000872 buffer Substances 0.000 description 1
- 239000007853 buffer solution Substances 0.000 description 1
- 125000003917 carbamoyl group Chemical group [H]N([H])C(*)=O 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000003431 cross linking reagent Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000007765 extrusion coating Methods 0.000 description 1
- 230000000977 initiatory effect Effects 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 229920001778 nylon Polymers 0.000 description 1
- 235000006408 oxalic acid Nutrition 0.000 description 1
- 125000005385 peroxodisulfate group Chemical group 0.000 description 1
- 229920003229 poly(methyl methacrylate) Polymers 0.000 description 1
- 229920002647 polyamide Polymers 0.000 description 1
- 229920000515 polycarbonate Polymers 0.000 description 1
- 239000004417 polycarbonate Substances 0.000 description 1
- 229920000728 polyester Polymers 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 229920000139 polyethylene terephthalate Polymers 0.000 description 1
- 239000005020 polyethylene terephthalate Substances 0.000 description 1
- 239000004926 polymethyl methacrylate Substances 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 239000004800 polyvinyl chloride Substances 0.000 description 1
- 229920000915 polyvinyl chloride Polymers 0.000 description 1
- 229920000036 polyvinylpyrrolidone Polymers 0.000 description 1
- 239000001267 polyvinylpyrrolidone Substances 0.000 description 1
- 235000013855 polyvinylpyrrolidone Nutrition 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000004080 punching Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 229950001574 riboflavin phosphate Drugs 0.000 description 1
- 125000006850 spacer group Chemical group 0.000 description 1
- 238000003892 spreading Methods 0.000 description 1
- 229920002554 vinyl polymer Polymers 0.000 description 1
Landscapes
- Application Of Or Painting With Fluid Materials (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、DNAもしくは、DNA部分分解物の塩基配
列を決定する為の電気泳動用グラジェントゲル膜の製造
方法に関する、特に電気泳動分離用媒体液の塗布方法に
関するものである。Detailed Description of the Invention [Field of Industrial Application] The present invention relates to a method for producing a gradient gel membrane for electrophoresis for determining the base sequence of DNA or a partially degraded DNA product, particularly for electrophoretic separation. The present invention relates to a method for applying a medium liquid.
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ェントゲルは、−枚の
支持体の上または二枚の支持体の間にテーパー状スペー
サーを用いてゲルを電気泳動方向にテーパー状に形成さ
せ、膜状物として用いられて来た。Conventionally, in plate electrophoresis, a non-self-supporting acrylamide polymer concentration gradient gel is electrophoresed using a tapered spacer on two supports or between two supports. It has been formed into a tapered shape in the direction and used as a film-like material.
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、泳動槽にセットする時、
ゲルの保存中、あるいは分析試料を添加するときなどに
誤ってゲルをこわしたり、試料以外のものをゲルの上に
落してゲルを損なったりすること等があり、操作上細心
の注意と熟練が必要であった。However, the method of forming and using a gel on a support is
When forming a gel on a support, when setting it in an electrophoresis tank,
When storing the gel or adding an analysis sample, it is possible to accidentally break the gel or drop something other than the sample onto the gel, damaging the gel. It 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ったまま電
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ったり、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 the vertical electrophoresis method, in which a mold is made from two glass plates, etc., gel is formed in the mold, and electrophoretic analysis is performed while the mold is held vertically, the thickness of the mold is made uniform. In addition, the gel forming solution has to be injected into a narrow mold before it becomes a gel, which requires a high degree of operational skill.
また、ガラスいた用いるために、そのガラス板が破損し
やすいという欠点があった。また、膜厚勾配は、テーパ
ー上に限られ、任意の膜厚勾配の実現は不可能であった
。In addition, since glass was used, there was a drawback that the glass plate was easily damaged. Further, the film thickness gradient is limited to the taper, and it has been impossible to realize an arbitrary film thickness gradient.
上記問題点を解消し、生産性が高く、再現性の高い電気
泳動用グラジェントゲル膜の製造方法として本出願人は
先に連続的に流量を変えた一定濃度のモノマー液と該モ
ノマー液に対応する重合反応開始剤液とをスタティック
ミクサーで混合し電気泳動分離用媒体液を調液し、連続
的に走行するウェ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ェントゲル膜の製造方法を提案し
た。In order to solve the above problems and produce a gradient gel membrane for electrophoresis that has high productivity and high reproducibility, the applicant has developed a method for producing a gradient gel membrane for electrophoresis that has high productivity and high reproducibility. A gradient gel membrane for electrophoresis, in which a medium solution for electrophoretic separation is prepared by mixing a corresponding polymerization reaction initiator solution with a static mixer, and the medium solution for electrophoretic separation is applied onto a continuously running web. proposed a manufacturing method.
前記塗布による方法は優れた方法であり、膜厚勾配が多
段階で、高級な電気泳動用グラジェ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膜厚勾配の電気
泳動用グラジェ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 described above is an excellent method and is suitable for production as a high-grade gradient membrane for electrophoresis with a multi-step film thickness gradient. A method for manufacturing gradient gel membranes with high reproducibility and high productivity 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
の濃度勾配をもったDNAシーケンス用電気泳動用グラ
ジェ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-mentioned problems and provide a method for manufacturing a gradient membrane for electrophoresis for DNA sequencing with a simple several-step concentration gradient with high reproducibility and high productivity. .
本発明の前記目的は連続的に走行するウェブ上に電気泳
動分離用媒体液を塗布する電気泳動用グラジェントゲル
膜の製造方法において、複数段階の流量の異なる一定濃
度の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
液口に別々に流量層に並べて供給し、各々スロット幅に
液を拡げ、複数種の流量の異なる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、変性剤として尿素を含む電気泳動用グラジェ
ントゲル膜の製造方法によって達成される。The object of the present invention is to provide a method for producing a gradient gel membrane for electrophoresis in which a medium liquid for electrophoretic separation is applied onto a continuously running web, in which a monomer liquid of a constant concentration and a monomer liquid of a constant concentration at different flow rates are polymerized in multiple stages. The initiator liquid and the initiator liquid are mixed and prepared, and each of the mixed liquids is separately supplied to multiple liquid supply ports of the coating head in a flow rate layer, and the liquid is spread over the width of each slot, allowing multiple types of flow rates to be applied. This is achieved by a method for producing a gradient gel membrane for electrophoresis containing urea as a denaturing agent, which is characterized in that different mixed solutions are applied as a horizontally aligned coating film onto a web through slot openings.
本発明において連続的に走行するウェブとは平面性のよ
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、ビスフェノール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。In the present invention, the continuously running web may be made of any material as long as it is in the form of a sheet with good flatness, is non-conductive, and is substantially water-impermeable, such as polyethylene terephthalate or bisphenol A. Polyesters like polycarbonate, polymethyl methacrylate, polyethylene.
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。Vinyl polymers such as polystyrene and polyvinyl chloride,
Polyamides such as nylon, and their copolymers (
Examples, 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、R粉ゲル、寒天ゲル等の原料液となる液をいう。The medium liquid for electrophoretic separation in the present invention may be anything as long as it can produce a medium membrane for electrophoretic separation, and representative examples thereof include raw materials such as acrylamide gel, agarose gel, R powder gel, and agar gel. A liquid that becomes liquid.
ポリアクリルアミドゲル膜に含有させる変性剤としては
、少なくとも1個のカルバモイル基を持つ化合物を挙げ
ることができ、その具体例としては、尿素、ホルムアミ
ド等が挙げられる。これらのうちで尿素が特に好ましく
用いられる。変性剤の量は単量体と架橋剤とを含む水性
ゲルの容積に対し、約40 w t / v%から約6
0 w t / v%の範囲で用いられる。尿素を用い
る場合には、単量体と架橋剤とを含む水性ゲル1Nに対
し約6モル(約300 g)から飽和溶解量まで、好ま
しくは約7モル(約420g)から飽和溶解量までの範
囲で用いることができる。Examples of the modifier to be included in the polyacrylamide gel membrane include compounds having at least one carbamoyl group, specific examples of which include urea, formamide, and the like. Among these, urea is particularly preferably used. The amount of modifier is from about 40 wt/v% to about 6%, based on the volume of the aqueous gel containing the monomer and crosslinker.
It is used in the range of 0 wt/v%. When using urea, the amount is from about 6 mol (about 300 g) to a saturated dissolution amount, preferably from about 7 mol (about 420 g) to a saturated dissolution amount, per 1N of an aqueous gel containing a monomer and a crosslinking agent. Can be used within a 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
。ホッパーコート、カーテンコート等が用いられる。塗
布する媒体膜の厚みは分離の目的に応じて選ばれるが通
常50 Ilmから約1、0mm、好ましくは約100
ttmから約0.5画の範囲とされる。In the present invention, methods for applying the electrophoretic separation medium include slide bead coating and extrusion coating. Hopper coat, curtain coat, etc. are used. The thickness of the media film to be applied is selected depending on the purpose of separation, but is usually from 50 mm to about 1.0 mm, preferably about 100 mm.
The range is approximately 0.5 strokes from ttm.
本発明における電気泳動用グラジェントゲル膜とは、一
つの製品単位長内に特に段階的膜厚勾配をもったものを
いう。又本発明において複数段階の流量の異なるモノマ
ー液とは、使用目的に応じて膜厚が50μIm〜1mm
になるように複数段階に流量を変えたものを言う。The gradient gel membrane for electrophoresis in the present invention refers to one having a stepwise film thickness gradient within one product unit length. In addition, in the present invention, the monomer liquid with different flow rates in multiple stages refers to a monomer liquid having a film thickness of 50 μIm to 1 mm depending on the purpose of use.
The flow rate is changed in multiple stages so that
各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、タンク混合であっても、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ィックミクサー
を用いることが出来る。スタティックミクサーとは、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
攪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。As a mixing device for each monomer liquid and each polymerization initiator liquid, tank mixing or any other method may be used, but a static mixer can be used as a preferable method. A static mixer is a mixer that stirs the fluid by its own movement when the fluid is passed through the mixer. Examples of tubular types include a spiral tube, an alternating left and right spiral, or a propeller with baffles. be.
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 using figures.
第1図は本発明の電気泳動用グラジェントゲル膜の製造
方法の1実施例の工程図である。本実施例としては流量
を5段階に分けた例で説明する。FIG. 1 is a process diagram of one embodiment of the method for producing a gradient gel membrane for electrophoresis according to the present invention. This embodiment will be explained using an example in which the flow rate is divided into five stages.
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)によって圧
送し、スタティックミクサー5(a−e)内で攪拌・混
合することによって各混合液である電気泳動分離用媒体
液6(a−e)を調液する。The electrophoretic separation medium liquid 6 (a-e) is the monomer liquid 1 (
a-e), polymerization reaction initiator liquids 2 (a-e) corresponding to the monomer liquids were adjusted in each tank, and each was pumped by constant flow pumps 3 (a-e) and 4 (a-e). By stirring and mixing in static mixers 5 (ae), electrophoretic separation medium liquids 6 (ae), which are mixed liquids, are prepared.
5種類の液6(a−e)は、ポンプ3(a−e)。Five types of liquids 6 (ae) are supplied to pumps 3 (ae).
4(a−e)の圧力によって塗布ヘッド7の夫々゛の給
液口14(a−e)に供給され、スロット開口16より
コーティングローラ8上のウェブ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ャンバー10が設けられている。The liquid is supplied to the liquid supply ports 14 (a-e) of each of the coating heads 7 by a pressure of 4 (a-e), and is applied from the slot openings 16 onto the web 9 on the coating roller 8 in a horizontal line. 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図はウェブ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0))、断面図(C)である。FIG. 2 shows a plan view (a), a side view 0)), and a cross-sectional view (C ).
塗布ヘッド7の供給口14(a−e)に−それぞ −れ
混合液6(a−e)が供給され、スロット開口16より
横1列となってウェブ9上に塗布される。The mixed liquid 6 (ae) is supplied to the supply ports 14 (ae) of the coating head 7, respectively, and is applied onto the web 9 in one horizontal row from the slot opening 16.
即ち電気泳動用グラジェントゲル膜としてはウェブの幅
方向に製品単位が作られ、ウェブは切断機′ によっ
て加工されることになる。That is, as a gradient gel membrane for electrophoresis, product units are made 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ッドの側面断面図、第4
図は第3図の正面断面図を示す。Figure 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)によって塗布ヘッド7の供給口14(a−e
)に液を送液する。各法は塗布ヘッド7内でキャビティ
なしでスロット15(a−e)によりそれぞれ幅方向に
拡げられる。この場合各スロット幅は狭くスロット内の
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って生じる異物
の発生をおこすことがない。スロット開口16前では各
隣接する液は相接しスロット開口16では各法が横一列
の塗布膜となり、ウェブ9上に塗布されることになる。In FIGS. 3 and 4, the five types of liquids are pumped 17, respectively.
The supply port 14 (a-e) of the coating head 7 is indicated by (a-e).
). Each method is expanded widthwise within the application head 7 by slots 15 (a-e) without cavities. In this case, the width of each slot is narrow and the spreading angle of the liquid in the slot can be kept at θ≦40'', so the liquid spreads naturally, and there is no accumulation of liquid and the generation of foreign matter due to it. In front of the slot opening 16 Then, the adjacent liquids come into contact with each other, and in the slot opening 16, each layer forms a horizontal line of coating film, which is applied onto the web 9.
連続的に走行するウェブ上に電気泳動分離用媒体液を塗
布する電気泳動用グラジェントゲル膜の製造方法におい
て、複数段階の流量の異なる一定濃度ノモノマー液とそ
れぞれの重合開始剤液とを各々混合・調液し、その各々
の混合液を塗布ヘンドの複数個の給液口に別々に流量順
に並べて供給し、各々スロント幅に液を拡げ、複数種の
流量の異なる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
として尿素を含む電気泳動用グラジェントゲル膜の製造
方法により、電気泳動用グラジェントゲル膜の製造方法
により、電気泳動用グラジェント膜としてはウェブ幅方
向に製品単位長を形成する。各段階流量の混合液は、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
ッドにおいては塗布液(混合液のこと)は自然に拡がっ
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 electrophoresis in which a medium solution for electrophoretic separation is applied onto a continuously running web, monomer solutions at a constant concentration and each polymerization initiator solution are mixed at different flow rates in multiple stages.・Prepare liquids, supply each mixed liquid to multiple liquid supply ports of the coating hand separately in order of flow rate, spread the liquid across the front width, and apply multiple mixed liquids with different flow rates in a horizontal line. A method for producing a gradient gel membrane for electrophoresis containing urea as a denaturing agent, characterized in that the membrane is applied onto a web through a slot opening; As a gradient film for use, a unit length of the product is formed in the width direction of the web. The mixed liquid at each stage of flow rate is prepared under certain conditions, so the quality is stable, and in the coating head, the coating liquid (mixed liquid) naturally spreads and is applied as a coating film, so it does not stagnate. A coating film of good quality is obtained without the generation of foreign matter, and due to stable manufacturing conditions, the quality and reproducibility of the product are good, and the productivity is also high.
〔実 施 例]
本発明の1実施例について第1.2,3.又は4図を用
いて説明する。[Example] Regarding one example of the present invention, Sections 1.2, 3. Or, explain using Figure 4.
電気泳動分離用媒体液
モノマー液I Ca−e)として−一−−■アガロース
・・・・・・・・・ 12.1g尿素 ・・・・・・・
・・840g
アクリルアミド ・・・・・・153g1.3.5−)
リアクリ
ロイル−へキサヒドロ−
3−トリアジン・・・・・・・・1.62g脱イオン水
up to 1,800mJ!を作り緩衝液として
□■
トリスヒドロキシメチル
アミン ・・・・・・・121.14gはう酸
・・・・・・・65.4gエチレンジアミンテト
ラ
酢酸2ナトリウム塩・・・・・・7.45g脱イオン水
up to 1.000a+1を作り緩衝液■・・
・・・・・・・・・・15(1m ii2.9χポリビ
ニルピロリドン水溶液・160@425χN、 N、
N’、 N’−テトラメチルエチレンジアミン液・・・
・・ 1.34m lの混合液−■を
モノマー■1 、800に加え、モノマー液1(a−e
)とする。As electrophoretic separation medium liquid monomer liquid I Ca-e) -1-■ Agarose...... 12.1g Urea...
...840g Acrylamide ...153g1.3.5-)
Liacryloyl-hexahydro-3-triazine...1.62g deionized water up to 1,800mJ! Make and use as a buffer □■ Trishydroxymethylamine ・・・・・・121.14g oxalic acid
・・・・・・・・・65.4g Ethylenediaminetetraacetic acid disodium salt・・・・・・7.45g Deionized water up to 1.000a+1 and make buffer solution■・・
・・・・・・・・・・・・15(1m ii2.9χ polyvinylpyrrolidone aqueous solution・160@425χN, N,
N', N'-tetramethylethylenediamine liquid...
...Add 1.34 ml of mixed liquid -■ to monomer ■1, 800, and add monomer liquid 1 (a-e
).
次に重合反応開始剤2(a−e)として2Xdi−2エ
チルへキシルスル
ホサクシネート液・・・・・・ 20m10.375χ
リボフラビンリン酸
エステルナトリウム塩水溶液・ 30m j!3.75
χペルオキソニ硫酸アン
モニウム水溶液・・・・・・・ 32m j!の混合溶
液を作る。Next, as the polymerization reaction initiator 2 (a-e), 2Xdi-2 ethylhexyl sulfosuccinate solution...20m10.375χ
Riboflavin phosphate ester sodium salt aqueous solution・30m j! 3.75
χAmmonium peroxodisulfate aqueous solution...32m j! Make a mixed solution of
次に定流量送液3 (a−e)で各モノマー液1 (a
−e)を各々47.5 mj!/min、 9.5mj
!/min+19 mf/+in、 28.5 mj!
/l1lin、 38 +a2/minの流量で、それ
に加えるに重合反応開始液2(a−e)を定流量送液ポ
ンプ4で各々1.85 ml!、/win、 0.37
ml。Next, each monomer solution 1 (a
-e) each 47.5 mj! /min, 9.5mj
! /min+19 mf/+in, 28.5 mj!
/l1lin, 38 +a2/min, and in addition to that, 1.85 ml of each of polymerization reaction initiating solutions 2 (a-e) were added using a constant flow pump 4! ,/win, 0.37
ml.
/ akin、 0.71/!/sin、 1.11
mj!/win、 1.48 tan/1111n+の
fi!で、共にスタティックミクサー5(a−e)内で
は上記2液が自刃により混合攪拌し、混合液である電気
泳動分離用媒体液6(a−e)が出来る。/ akin, 0.71/! /sin, 1.11
mj! /win, 1.48 tan/1111n+ fi! Then, in the static mixer 5 (ae), the above two liquids are mixed and stirred by self-blading blades, and a mixed liquid, ie, a medium liquid for electrophoretic separation 6 (ae), is produced.
スタティックミクサー5 (a−e)内では上記2Mが
自刃により混合攪拌し、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 2M is mixed and stirred by a self-blading blade, and a mixed liquid, ie, a medium liquid for electrophoretic separation 6 (a-e), is produced.
塗布へラド7の各供給口14(a−e)より混合液であ
る電気泳動分離用媒体液&(a−e)が供給され、スロ
ット開口16よりウェブ9上に塗布される。The electrophoretic separation medium liquid &(ae), which is a mixed liquid, is supplied from each supply port 14 (ae) of the coating pad 7 and applied onto the web 9 through the slot opening 16 .
その時の各流量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
れたゲル膜の膜厚は5段階に分けられて連続的に塗布さ
れる状態になる。The application status of the electrophoretic separation medium liquid 6 (a-e) at each flow rate at that time is as shown in Figure 2 (a), and the film thickness of the applied gel film is divided into five stages and is continuous. It will be in a state where it will be coated.
尚、電気泳動分離用媒体膜としての製品は、塗布後硬化
処理をする工程、試料注入口としてコーム(櫛)を打抜
く工程、カバーシートを貼付ける工程、製品長さに切断
する工程1等を経て初めて製品となる。In addition, the product as a media membrane for electrophoretic separation requires a process of curing after coating, a process of punching out a comb as a sample injection port, a process of pasting a cover sheet, a process of cutting the product to length, etc. Only after this process does it become a product.
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 steps have no relation to the present invention no matter what method or means is used.
本発明は連続的に走行するウェブ上に電気泳動分離用媒
体液を塗布する電気泳動用グラジェントゲル膜の製造方
法において、複数段階の流量の異なる一定濃度のモノマ
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ッドの複数個の給液口に
別々に流量順に並べて供給し、各々スロット幅に液を拡
げ、複数種の流量の異なる混合液を横1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、変性剤として尿素を含む電気泳動用グラジェントゲ
ル膜の製造方法により、単純な数段階の膜厚勾配の電気
泳動用グラジェ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 relates to a method for producing a gradient gel membrane for electrophoresis in which a medium liquid for electrophoretic separation is applied onto a continuously running web, and a monomer liquid with a constant concentration and a polymerization reaction initiator at different flow rates in multiple stages. Mix and prepare each liquid, supply each mixed liquid to multiple liquid supply ports of the coating head separately in order of flow rate, spread the liquid to each slot width, and mix multiple types of mixed liquids with different flow rates. The method for producing a gradient gel membrane for electrophoresis containing urea as a denaturing agent is characterized in that it is applied as a horizontally lined coating film onto a web through a slot opening. We were able to manufacture a gradient gel membrane for electrophoresis with good productivity, stable product quality, and good reproducibility.
第1図は本発明の電気泳動用グラジェントゲル膜の製造
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ッドの側面断面図、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 (a−e) ・・・重合反応開始剤液3(a−e
)。
4(a−e) ・・・定流量送液ポンプ5(a−e)
・・・スタティックミクサー6(a−e) ・・
・電気泳動分離用媒体液7・・・塗布ヘッド
8・・・コーティングローラ
9・・・ウェブ 10・・・差圧チャンバー11 ・・
・コントローラ
12・・・コンピュータリンケージアダプタ13・・・
ウェブ
14(a−e) ・・・給液口
15(a−e) ・・・スロット
16・・・スロット開口
17(a−e) ・・・定量ポンプFIG. 1 is a process diagram of the method for producing a gradient gel membrane for electrophoresis of the present invention, and FIG. 2 is an explanatory diagram of the application state of the five types of dark and light electrophoretic separation medium solutions of the present invention. FIG. 3 is a side sectional view of the coating head according to the present invention;
The figure is a front sectional view of FIG. 3. 1 (a-e) ... Monomer liquid 2 (a-e) ... Polymerization reaction initiator liquid 3 (a-e
). 4 (a-e) ... constant flow liquid sending pump 5 (a-e)
... Static mixer 6 (a-e) ...
- Electrophoretic separation medium liquid 7... Coating head 8... Coating roller 9... Web 10... Differential pressure chamber 11...
- Controller 12... Computer linkage adapter 13...
Web 14 (a-e) ... Liquid supply port 15 (a-e) ... Slot 16 ... Slot opening 17 (a-e) ... Metering pump
Claims (2)
液を塗布する電気泳動用グラジェントゲル膜の製造方法
において、複数段階の流量の異なる一定濃度のモノマー
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別々に
流量順に並べて供給し、各々スロット幅に液を拡げ、複
数種の流量の異なる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
性剤として尿素を含む電気泳動用グラジェントゲル膜の
製造方法。(1) In a method for producing an electrophoretic gradient gel membrane in which a medium solution for electrophoretic separation is applied onto a continuously running web, a monomer solution with a constant concentration and a polymerization initiator solution with different flow rates in multiple stages are used. The mixed liquids are mixed and prepared respectively, and each of the mixed liquids is supplied to multiple liquid supply ports of the coating head separately in order of flow rate, and the liquid is spread across the width of each slot, and multiple types of mixed liquids with different flow rates are supplied. A method for producing a gradient gel membrane for electrophoresis containing urea as a denaturing agent, characterized in that the membrane is coated onto a web from slot openings in a horizontal row.
応開始剤液より作られるゲル膜の膜厚変化が50μm〜
1mmであることを特徴とする特許請求の範囲第1項記
載の電気泳動用グラジェントゲル膜の製造方法。(2) The thickness change of the gel film made from the plurality of monomer liquids and polymerization reaction initiator liquids with different flow rates is 50 μm or more.
The method for producing a gradient gel membrane for electrophoresis according to claim 1, wherein the membrane has a thickness of 1 mm.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP62295141A JPH01138454A (en) | 1987-11-25 | 1987-11-25 | Production of gradient gel film for electrophoresis |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP62295141A JPH01138454A (en) | 1987-11-25 | 1987-11-25 | Production of gradient gel film for electrophoresis |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH01138454A true JPH01138454A (en) | 1989-05-31 |
Family
ID=17816808
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP62295141A Pending JPH01138454A (en) | 1987-11-25 | 1987-11-25 | Production of gradient gel film for electrophoresis |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH01138454A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6090081A (en) * | 1997-05-22 | 2000-07-18 | Daikyo Seiko, Ltd. | Sealing stopper for a syringe and a prefilled syringe |
CN100412540C (en) * | 2005-12-15 | 2008-08-20 | 西安工业学院 | Apparatus and method for making gradient gel film for full-automatic electrophoresis |
US9597458B2 (en) | 2009-10-29 | 2017-03-21 | W. L. Gore & Associates, Inc. | Fluoropolymer barrier materials for containers |
US10471212B2 (en) | 2009-10-29 | 2019-11-12 | W. L. Gore & Associates, Inc. | Silicone free drug delivery devices |
US11612697B2 (en) | 2010-10-29 | 2023-03-28 | W. L. Gore & Associates, Inc. | Non-fluoropolymer tie layer and fluoropolymer barrier layer |
-
1987
- 1987-11-25 JP JP62295141A patent/JPH01138454A/en active Pending
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6090081A (en) * | 1997-05-22 | 2000-07-18 | Daikyo Seiko, Ltd. | Sealing stopper for a syringe and a prefilled syringe |
CN100412540C (en) * | 2005-12-15 | 2008-08-20 | 西安工业学院 | Apparatus and method for making gradient gel film for full-automatic electrophoresis |
US9597458B2 (en) | 2009-10-29 | 2017-03-21 | W. L. Gore & Associates, Inc. | Fluoropolymer barrier materials for containers |
US10471212B2 (en) | 2009-10-29 | 2019-11-12 | W. L. Gore & Associates, Inc. | Silicone free drug delivery devices |
US10478563B2 (en) | 2009-10-29 | 2019-11-19 | W. L. Gore & Associates, Inc. | Fluoropolymer barrier materials for containers |
US11020531B2 (en) | 2009-10-29 | 2021-06-01 | W. L. Gore & Associates, Inc. | Silicone free drug delivery devices |
US11654241B2 (en) | 2009-10-29 | 2023-05-23 | W. L. Gore & Associates, Inc. | Fluoropolymer barrier material for containers |
US11612697B2 (en) | 2010-10-29 | 2023-03-28 | W. L. Gore & Associates, Inc. | Non-fluoropolymer tie layer and fluoropolymer barrier layer |
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