JPH0713124B2 - Radiation graft polymerization equipment - Google Patents
Radiation graft polymerization equipmentInfo
- Publication number
- JPH0713124B2 JPH0713124B2 JP63043566A JP4356688A JPH0713124B2 JP H0713124 B2 JPH0713124 B2 JP H0713124B2 JP 63043566 A JP63043566 A JP 63043566A JP 4356688 A JP4356688 A JP 4356688A JP H0713124 B2 JPH0713124 B2 JP H0713124B2
- Authority
- JP
- Japan
- Prior art keywords
- graft polymerization
- inner cylinder
- monomer
- base material
- cylinder
- 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
Links
- 238000010559 graft polymerization reaction Methods 0.000 title claims description 33
- 230000005855 radiation Effects 0.000 title claims description 19
- 239000000463 material Substances 0.000 claims description 40
- 239000000178 monomer Substances 0.000 claims description 37
- 239000000758 substrate Substances 0.000 claims description 13
- 238000000034 method Methods 0.000 description 23
- 239000007791 liquid phase Substances 0.000 description 14
- 239000007789 gas Substances 0.000 description 13
- 239000012071 phase Substances 0.000 description 13
- 239000000835 fiber Substances 0.000 description 11
- 239000007788 liquid Substances 0.000 description 11
- 239000012528 membrane Substances 0.000 description 9
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 8
- 238000006243 chemical reaction Methods 0.000 description 5
- 238000001704 evaporation Methods 0.000 description 5
- 230000008020 evaporation Effects 0.000 description 5
- 239000012510 hollow fiber Substances 0.000 description 5
- 238000003756 stirring Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
- 239000004745 nonwoven fabric Substances 0.000 description 4
- 238000006116 polymerization reaction Methods 0.000 description 4
- 239000000843 powder Substances 0.000 description 4
- 238000000926 separation method Methods 0.000 description 4
- 239000000470 constituent Substances 0.000 description 3
- 238000010894 electron beam technology Methods 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- -1 polyethylene Polymers 0.000 description 3
- 239000004698 Polyethylene Substances 0.000 description 2
- 239000003708 ampul Substances 0.000 description 2
- LFYJSSARVMHQJB-QIXNEVBVSA-N bakuchiol Chemical compound CC(C)=CCC[C@@](C)(C=C)\C=C\C1=CC=C(O)C=C1 LFYJSSARVMHQJB-QIXNEVBVSA-N 0.000 description 2
- 238000005119 centrifugation Methods 0.000 description 2
- 230000005865 ionizing radiation Effects 0.000 description 2
- 229920000573 polyethylene Polymers 0.000 description 2
- 125000006850 spacer group Chemical group 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000012808 vapor phase Substances 0.000 description 2
- 238000004804 winding Methods 0.000 description 2
- 239000002759 woven fabric Substances 0.000 description 2
- 239000004743 Polypropylene Substances 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000007306 functionalization reaction Methods 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 238000000265 homogenisation Methods 0.000 description 1
- 230000001678 irradiating effect Effects 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000012299 nitrogen atmosphere Substances 0.000 description 1
- 239000002861 polymer material Substances 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Landscapes
- Treatments Of Macromolecular Shaped Articles (AREA)
- Polymerisation Methods In General (AREA)
- Graft Or Block Polymers (AREA)
Description
【発明の詳細な説明】 (産業上の利用分野) 本発明は高分子材料の改質および高機能化において最近
とみにその有効性が確認されつつあるグラフト重合方
法、特に電離性放射線を用いる放射線グラフト重合装置
に関するものである。DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a graft polymerization method whose effectiveness has recently been confirmed in the modification and functionalization of polymeric materials, and in particular, radiation grafting using ionizing radiation. The present invention relates to a polymerization device.
(従来の技術) 放射線グラフト重合は基材の特徴を生かしながら他の性
質を付与することができるので、素材の高機能化を図る
先端産業分野で最近注目を浴びている重合方法である。
特に、基材の形状を問わないという点が放射線グラフト
重合の最大の特徴である。このため、形状による機能が
付与されているような高分子素材に対して機能性物質を
導入する等の方法により、機能の複合化あるいは高機能
化を図るという手法は、放射線グラフト重合が最も得意
とするところであり、他の方法の追随を許さない。(Prior Art) Radiation-induced graft polymerization is a polymerization method that has recently attracted attention in the advanced industrial fields for improving the functionality of materials, since it can impart other properties while making the most of the characteristics of the substrate.
In particular, the greatest feature of radiation graft polymerization is that the shape of the substrate does not matter. For this reason, radiation graft polymerization is the best method to combine functions or increase functionality by introducing functional substances into polymer materials that have functions depending on shape. And it is unrivaled by other methods.
ここで用いる電離性放射線としてはα線,β線,γ線,
紫外線,電子線などがあり、限定されるものではない
が、γ線や電子線が本発明には比較的適している。The ionizing radiations used here are α rays, β rays, γ rays,
There are ultraviolet rays, electron beams, etc., and although not limited, γ rays and electron beams are relatively suitable for the present invention.
放射線グラフト重合方法には種々の方法があり、照射方
法,モノマーとの接触のさせ方によってそれぞれ異なっ
た方法をとる。There are various methods for radiation graft polymerization, and different methods are used depending on the irradiation method and the method of contact with the monomer.
照射方法とては基材とモノマーの共存下に放射線を照射
する同時照射法と、あらかじめ基材を照射した後、モノ
マーと接触させる前照射法とがあるが、モノマーの単独
重合物の生成の少ない前照射法の方が有利であり、以
後、前照射法を前提として述べる。Irradiation methods include a simultaneous irradiation method in which radiation is applied in the coexistence of a base material and a monomer, and a pre-irradiation method in which a base material is previously irradiated and then contacted with a monomer. The less pre-irradiation method is more advantageous, and the pre-irradiation method will be described below.
更に、基材とモノマーとの接触の仕方がモノマーが溶液
の場合と蒸気の場合とがあり、前者を液相グラフト重
合、後者を気相グラフト重合と呼ぶ。Further, the method of contacting the base material with the monomer may be in the case where the monomer is a solution or in the case of vapor, and the former is called liquid phase graft polymerization and the latter is called gas phase graft polymerization.
以上のように放射線グラフト重合方法には種々の方法が
あり、しかも基材の形状が粉末,粒子,繊維(単繊維,
長繊維,織布,不織布)、膜(平膜,中空糸膜)など限
定されないので、照射方法を前照射法に限定したとして
も、放射線グラフト重合装置としては多種多様なものが
考えられる。As described above, there are various methods for radiation graft polymerization, and the shape of the base material is powder, particles, fibers (single fiber,
Since there is no limitation on long fibers, woven fabrics, non-woven fabrics), membranes (flat membranes, hollow fiber membranes) and the like, even if the irradiation method is limited to the pre-irradiation method, various radiation graft polymerization apparatuses are conceivable.
これまでに実用化された放射線グラフト重合装置の唯一
の例は、前照射液相グラフト重合法に関するものであ
り、基材の形状としては平膜を利用している。該装置に
おいては、グラフト反応は照射した平膜をローラーを使
用して順次薬液槽に送り出すという方法を採用してい
る。The only example of the radiation graft polymerization apparatus that has been put to practical use so far relates to the pre-irradiation liquid phase graft polymerization method, and a flat film is used as the shape of the substrate. In this apparatus, the graft reaction employs a method of sequentially sending the irradiated flat membrane to a chemical bath using a roller.
(発明が解決しようとする課題) 上記の装置はその構造上、液相でしかも膜状の基材にし
か適用できない。基材の形状が変った場合や気相グラフ
ト重合を行いたい場合は、その都度、反応装置を考案し
て設計製作しなければならない。このように、種々の形
状の基材を液相、気相のいずれにおいてもグラフト重合
できる装置は未だ存在しない。(Problems to be Solved by the Invention) Due to its structure, the above device can be applied only to a liquid-phase film-shaped substrate. When the shape of the substrate changes or when it is desired to carry out gas phase graft polymerization, the reactor must be devised and designed each time. As described above, there is still no apparatus capable of graft-polymerizing substrates having various shapes in both the liquid phase and the gas phase.
本発明の目的は種々の形状の基材を、液相,気相のいず
れにおいても容易にグラフト重合ができる汎用の放射線
グラフト重合装置を提供することである。An object of the present invention is to provide a general-purpose radiation graft polymerization apparatus capable of easily graft-polymerizing substrates having various shapes in both liquid phase and gas phase.
(課題を解決するための手段) 本発明による放射線グラフト重合装置は、縦型にも横型
にも使用可能な円筒の内側に、該円筒と同心の回転可能
な内筒を1個以上設けたことを特徴としている。(Means for Solving the Problems) In the radiation graft polymerization apparatus according to the present invention, one or more rotatable inner cylinders that are concentric with the cylinder are provided inside the cylinder that can be used both vertically and horizontally. Is characterized by.
(作用) この内筒は回転方向及び回転数が可変であり、しかも着
脱自在であり、液相および気相グラフト重合において、
次のような役割を帯びている。(Operation) This inner cylinder is variable in the direction of rotation and the number of rotations and is detachable, and in the liquid phase and gas phase graft polymerization,
It has the following roles.
基材の収納容器 固液分離のフィルタ(液相) モノマーおよび基材の攪拌、均一化 長い基材のための巻きとり用ロール モノマー蒸発面積の増加(気相) (実施例) 以下基材の形状が粉末,粒子、カット繊維長繊維
(チューブ状も含む)帯状のもの(不織布、平膜等)
の各場合における液相および気相グラフト重合について
の本発明の重合装置の実施態様を図で示しながら説明す
る。Storage container for base material Filter for solid-liquid separation (liquid phase) Stirring and homogenization of monomer and base material Rolling roll for long base material Increasing monomer evaporation area (gas phase) (Example) Powder, particles, cut fibers, long fibers (including tubes), band-shaped (nonwoven fabric, flat membrane, etc.)
The embodiments of the polymerization apparatus of the present invention for the liquid phase and gas phase graft polymerization in each case will be described with reference to the drawings.
先ず、基材の形状が粉末,粒子,カット繊維等であり且
つ液相グラフト重合する装置を第1図に示す。これ等の
基材はモノマー溶液中でスラリーとして取扱える。円筒
1は横型のものであり、その内部がグラフト重合部とな
っている。内筒2は円筒1に囲繞され且つ円筒1と同軸
の円筒形状を有し、軸6を中心に回転できる構造となっ
ている。放射線を照射された基材4は内筒2の内側に投
入され、モノマー溶液5が円筒1の内部に導入される。
内筒2を構成する材料としては、モノマー溶液を通過さ
せるが基材を通過させず、モノマー溶液によって劣化せ
ず、且つ適当な強度を有するものであればいかなるもの
でも使用できる。例えば、金網,サランネット,布等を
骨材に張り円筒状にしたものが使用できる。また、内筒
2の内周には数ケ所にじゃま板3が配設される。内筒2
が軸6を中心に回転すると、じゃま板3の攪拌効果によ
り基材4とモノマー溶液5は均一に接触する。基材の材
質とモノマー溶液との組合せにもよるが、静止状態で反
応させると気泡の発生等により均一反応が困難な場合が
あるが、第1図の例ではこのようなことは全くない。し
かも、モノマー液量は基材が含浸する程度でよいため、
従来の液相グラフト重合と比べても節約効果が顕著であ
る。重合の途中で回転方向を変えることは、攪拌効果の
点でも好ましい。グラフト反応が終了すると、モノマー
溶液の抜き出しを経て洗浄工程へ移るが、横型円筒1の
底部に設けたドレン7を開としてモノマー溶液の抜き出
しを行えば内筒2がフィルターの役割を果すことにな
り、固液分離にも役立つ。また、基材4の形状が微粉末
のような場合は、液の抜出しに長時間を要するので横型
のままでよいが、第2図に示す如く、円筒1を縦型とし
て内筒2の回転数を上げ、遠心分離により固液分離を行
えば最終グラフト物を得るまでの時間を大幅に短縮する
ことができる。即ち、ここでは内筒2に攪拌と固液分離
(ろ過又は遠心分離)の作用を行わせている。First, FIG. 1 shows an apparatus in which the shape of the substrate is powder, particles, cut fibers, etc. and liquid phase graft polymerization is performed. These substrates can be handled as slurries in the monomer solution. The cylinder 1 is a horizontal type, and the inside thereof is a graft polymerization part. The inner cylinder 2 has a cylindrical shape surrounded by the cylinder 1 and coaxial with the cylinder 1, and has a structure capable of rotating around a shaft 6. The base material 4 irradiated with the radiation is introduced into the inner cylinder 2, and the monomer solution 5 is introduced into the cylinder 1.
As a material for forming the inner cylinder 2, any material can be used as long as it allows a monomer solution to pass but does not pass through a base material, is not deteriorated by the monomer solution, and has appropriate strength. For example, a wire mesh, a saran net, a cloth, etc., which are attached to an aggregate to form a cylindrical shape can be used. Further, baffle plates 3 are arranged at several locations on the inner circumference of the inner cylinder 2. Inner cylinder 2
When is rotated about the axis 6, the base material 4 and the monomer solution 5 are brought into uniform contact with each other due to the stirring effect of the baffle plate 3. Depending on the combination of the material of the base material and the monomer solution, when the reaction is performed in a stationary state, it may be difficult to carry out a uniform reaction due to generation of bubbles or the like, but in the example of FIG. 1, this is not the case at all. Moreover, since the amount of the monomer liquid may be such that the base material is impregnated,
The saving effect is remarkable compared to the conventional liquid phase graft polymerization. Changing the rotation direction during the polymerization is also preferable from the viewpoint of stirring effect. When the grafting reaction is completed, the monomer solution is withdrawn and the washing process is performed. However, if the drain 7 provided at the bottom of the horizontal cylinder 1 is opened to withdraw the monomer solution, the inner cylinder 2 serves as a filter. Also useful for solid-liquid separation. Further, when the base material 4 is in the form of fine powder, it may take a long time to extract the liquid, so that it may be left in the horizontal shape, but as shown in FIG. 2, the cylinder 1 is vertical and the inner cylinder 2 rotates. If the number is increased and solid-liquid separation is performed by centrifugation, the time until the final graft product is obtained can be greatly shortened. That is, here, the inner cylinder 2 is caused to perform the functions of stirring and solid-liquid separation (filtration or centrifugation).
基材の形状が長繊維(チューブ状も含む)で、且つこれ
を液相グラフト重合する場合は、例えば横型円筒を用い
て第3図のような方法で繊維を取扱えば容易にグラフト
重合することができる。即ち、内筒2の外側に基材であ
る長繊維4を巻いて反応させるのである。この場合、内
筒2は攪拌と繊維を巻きつけるためのロールの役割を果
たしており、構成材料は必ずしも金網、サランネット状
のものである必要はなく、骨材のままでもよい。When the shape of the base material is long fiber (including tube shape) and it is subjected to liquid phase graft polymerization, it can be easily graft-polymerized by handling the fiber by the method as shown in Fig. 3 using a horizontal cylinder. You can That is, the long fibers 4, which are the base material, are wound on the outside of the inner cylinder 2 to cause a reaction. In this case, the inner cylinder 2 plays the role of a roll for stirring and winding the fiber, and the constituent material does not necessarily have to be a wire mesh or a saran net, and may be an aggregate as it is.
基材がチューブ状の場合には、第3図のように巻くこと
も出来るが、それが不可能ならば第4図に示すごとく内
筒2の内部に置いて反応させることができる。第1図に
示す円筒1および内筒2の長さがチューブの長さになる
まで延長されたものとみなすことができる。When the substrate is tubular, it can be wound as shown in FIG. 3, but if that is not possible, it can be placed inside the inner cylinder 2 and reacted as shown in FIG. It can be considered that the lengths of the cylinder 1 and the inner cylinder 2 shown in FIG. 1 are extended to the length of the tube.
基材の形状が帯状(平膜,織布,不織布)であり且つ液
相グラフトする場合は、例えば第5図のような方法が採
用できる。照射済み帯状の基材4を間に適当なスペーサ
9をはさみ込みながら内筒2の外側に巻きとり、これを
回転させながらモノマー溶液5と接触させるのである。
この場合、内筒2は基材4を巻きとるためのロールの役
割と、回転によるモノマー溶液との均一接触の役割を果
している。When the base material has a strip shape (flat membrane, woven fabric, non-woven fabric) and liquid-phase grafting is performed, the method shown in FIG. 5 can be employed, for example. The irradiated strip-shaped base material 4 is wound around the outer side of the inner cylinder 2 while sandwiching an appropriate spacer 9 therebetween, and is rotated to make contact with the monomer solution 5.
In this case, the inner cylinder 2 plays a role of a roll for winding the base material 4 and a role of uniform contact with the monomer solution by rotation.
一方、気相グラフト重合においてはモノマー蒸気と基材
とを接触させるので、モノマー液面を下げる必要があ
る。即ち、第1図の例を参考にすれば、モノマー液面は
内筒2より下方に位置させる必要がある。内筒2の回転
により基材4はモノマー蒸気と均一に接触するが、モノ
マー蒸気圧が低い場合は、ラジカル数に較べてモノマー
供給量が少ないので、所定のグラフト率を得るのに、長
時間を要す。モノマー蒸発量は蒸発面積にも依存するの
で、第6図に示す如く内筒2の外側にさらに内筒8を設
け、その一部分がモノマー溶液と接触するようにしてお
けば、内筒8の内部にモノマー溶液が保持され、結局、
内筒8全体がモノマー蒸発面となってグラフト速度をあ
げることができ、モノマー蒸気濃度の均一化も図ること
ができる。内筒8の構成材料としては、表面積の大きな
もの、例えばマット状のもの,織布状のもの,不織布状
のものが好ましく、内筒2の構成材料としては蒸気拡散
のよい金網等が好ましい。On the other hand, in the vapor phase graft polymerization, the monomer vapor and the base material are brought into contact with each other, so that it is necessary to lower the liquid level of the monomer. That is, referring to the example of FIG. 1, the liquid surface of the monomer needs to be positioned below the inner cylinder 2. The base material 4 comes into uniform contact with the monomer vapor due to the rotation of the inner cylinder 2, but when the monomer vapor pressure is low, the monomer supply amount is small compared to the number of radicals, so it takes a long time to obtain a predetermined graft ratio. Required. Since the amount of monomer evaporation also depends on the evaporation area, if an inner cylinder 8 is further provided outside the inner cylinder 2 as shown in FIG. Holds the monomer solution in the
The entire inner cylinder 8 serves as a monomer evaporation surface to increase the grafting rate, and it is possible to make the monomer vapor concentration uniform. A material having a large surface area, for example, a mat-shaped material, a woven material, or a non-woven material is preferable as a constituent material of the inner cylinder 8, and a wire net or the like having good vapor diffusion is preferable as a constituent material of the inner cylinder 2.
基材の形状が長繊維,チューブ状,帯状等のいずれの場
合においても、気相グラフトを行う際、モノマー液面を
内筒2より下方に位置せしめて基材と直接接触させない
ように留意するのは先に述べたとおりであり、さらに、
内筒8を内筒2の外側に設け、モノマー蒸発面積を増加
させる方法も先に述べた方法と全く同様に行える。即
ち、気相グラフト重合における内筒2の役割は、基材が
モノマー溶液と直接接触しないための収納容器であると
同時にモノマー蒸気と均一に接触させることであり、内
筒8はモノマー蒸発面積を増加させてグラフト速度を上
げることと、モノマー蒸気濃度を均一化することであ
る。Regardless of the shape of the base material such as long fiber, tube shape, band shape, etc., when vapor phase grafting is performed, be careful not to place the monomer liquid surface below the inner cylinder 2 so as to avoid direct contact with the base material. Is as described above, and in addition,
The method of increasing the monomer evaporation area by providing the inner cylinder 8 on the outer side of the inner cylinder 2 can be performed in the same manner as the above-mentioned method. That is, the role of the inner cylinder 2 in the gas phase graft polymerization is to make the base material a container for preventing direct contact with the monomer solution, and at the same time to make uniform contact with the monomer vapor. Increasing the grafting rate by increasing it and homogenizing the monomer vapor concentration.
以上述べたように基材の形状に見合った内筒を何種類か
用意しておけば、内筒をとり換えるだけで、種々の基材
を液相のみならず気相においてもグラフト重合すること
ができる。As mentioned above, if you prepare several kinds of inner cylinders matching the shape of the base material, you can graft-polymerize various base materials not only in the liquid phase but also in the gas phase simply by replacing the inner cylinder. You can
(実験例) 外径約1mm、長さ15cmのポリエチレン製多孔質中空糸膜5
00本に加速電子線を窒素雰囲気中で20Mrad照射した後、
50メッシュの金網よりなる直径15cm、長さ20cmの第4図
に示すような円筒のカゴに入れ、さらに、このカゴを内
径17cm、長さ25cmのポリプロピレン製の不織布を巻いた
円筒の中に挿入し、これを内径20cm、長さ26cmの横型円
筒の中に第6図に示すような配置で配置した。モノマー
溶液にはスチレンを使用し、2個の内筒は30rpmで回転
させて気相グラフト重合を行った。5時間経過後のグラ
フト率は173%であり、グラフトむらは認められなかっ
た。(Experimental example) Porous hollow fiber membrane 5 made of polyethylene with an outer diameter of approximately 1 mm and a length of 15 cm
After irradiating 00 lines with 20 Mrad of accelerated electron beam in a nitrogen atmosphere,
Put it in a cylindrical basket made of 50 mesh wire mesh with a diameter of 15 cm and a length of 20 cm, as shown in Fig. 4, and then insert this basket into a cylinder wrapped with polypropylene non-woven fabric with an inner diameter of 17 cm and a length of 25 cm. Then, it was placed in a horizontal cylinder having an inner diameter of 20 cm and a length of 26 cm as shown in FIG. Styrene was used as the monomer solution, and the two inner cylinders were rotated at 30 rpm to carry out gas phase graft polymerization. The graft ratio after 5 hours was 173%, and no graft unevenness was observed.
(比較例) 実験例と同様の条件で照射したポリエチレン製多孔質中
空糸膜を、内径15cm、高さ25cmのガラスアンプルに入
れ、スチレンをアンプル底部に導入して気相グラフト重
合を行った。なお、スチレンの液面2cm上方を50メッシ
ュの金網で仕切り、中空糸膜とスチレンが直接接触しな
いようにした。5時間経過後のグラフト率は146%であ
ったが、ほとんど全ての中空糸の径がモノマー液側で非
常に太くなっており、グラフト重合が均一に行われてい
ないことは明らかであった。Comparative Example A polyethylene porous hollow fiber membrane irradiated under the same conditions as in the experimental example was placed in a glass ampoule having an inner diameter of 15 cm and a height of 25 cm, and styrene was introduced into the bottom of the ampoule to carry out gas phase graft polymerization. In addition, 2 cm above the liquid surface of styrene was partitioned by a wire mesh of 50 mesh to prevent direct contact between the hollow fiber membrane and styrene. The graft ratio after 5 hours was 146%, but the diameters of almost all the hollow fibers were very large on the monomer liquid side, and it was clear that the graft polymerization was not carried out uniformly.
(発明の効果) 本発明によって、種々の形状の基材を液相のみならず気
相においても容易にグラフト重合できる汎用の放射線グ
ラフト重合装置が可能となった。これによって、放射線
グラフト重合に寄せられている先端産業からの期待に十
分応え得るハード面での対応が可能となったのである。(Effects of the Invention) The present invention has enabled a general-purpose radiation graft polymerization apparatus capable of easily graft-polymerizing substrates of various shapes not only in the liquid phase but also in the gas phase. As a result, it has become possible to meet the expectations from the leading industries involved in radiation graft polymerization in terms of hardware.
第1図は横型円筒を用いた本発明の放射線グラフト重合
装置の断面図であり、第2図は縦型円筒を用いた本発明
の放射線グラフト重合装置の断面図であり、第3図〜第
5図は基材形状に応じた内筒への基材収納状態の態様を
示す図であり、第6図は気相グラフト重合に用いるべく
なされた本発明による放射線グラフト重合装置を示す断
面図である。 1……円筒、2……内筒 3……じゃま板、4……基材 5……モノマー溶液、6……軸 7……ドレン、8……内筒 9……スペーサFIG. 1 is a sectional view of a radiation graft polymerization apparatus of the present invention using a horizontal cylinder, FIG. 2 is a sectional view of a radiation graft polymerization apparatus of the present invention using a vertical cylinder, and FIGS. FIG. 5 is a view showing a state of the base material stored in the inner cylinder according to the shape of the base material, and FIG. 6 is a sectional view showing a radiation graft polymerization apparatus according to the present invention, which is adapted to be used for gas phase graft polymerization. is there. 1 ... Cylinder, 2 ... Inner cylinder 3 ... Baffle plate, 4 ... Substrate 5 ... Monomer solution, 6 ... Shaft 7 ... Drain, 8 ... Inner cylinder 9 ... Spacer
───────────────────────────────────────────────────── フロントページの続き (72)発明者 藤原 邦夫 群馬県高崎市綿貫町1233番地 日本原子力 研究所高崎研究所内 (72)発明者 関口 英明 千葉県市原市青葉台6―17―8 (56)参考文献 特公 昭45−7720(JP,B1) ─────────────────────────────────────────────────── --- Continuation of the front page (72) Kunio Fujiwara, Kunio Fujiwara, 1233 Watanuki-cho, Takasaki-shi, Gunma Japan Atomic Energy Research Institute Takasaki Research Institute (72) Inventor Hideaki Sekiguchi 6-17-8 Aobadai, Ichihara-shi, Chiba (56) Reference Reference Japanese Patent Publication Sho-45-7720 (JP, B1)
Claims (4)
前記円筒と同心の回転可能な内筒を1個以上設けたこと
を特徴とする放射線グラフト重合装置。1. A radiation graft polymerization apparatus characterized in that one or more rotatable inner cylinders concentric with the cylinder are provided inside a cylinder that can be used both vertically and horizontally.
基材は通過できない材料よりなる、請求項1に記載の装
置。2. The apparatus according to claim 1, wherein the inner cylinder is made of a material through which a monomer can easily pass but a substrate cannot pass.
ある、請求項1または請求項2に記載の装置。3. The apparatus according to claim 1, wherein the rotation speed and the rotation direction of the inner cylinder are variable.
し請求項3のいずれかに記載の装置。4. The device according to claim 1, wherein the inner cylinder is removable.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63043566A JPH0713124B2 (en) | 1988-02-26 | 1988-02-26 | Radiation graft polymerization equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63043566A JPH0713124B2 (en) | 1988-02-26 | 1988-02-26 | Radiation graft polymerization equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH01217021A JPH01217021A (en) | 1989-08-30 |
| JPH0713124B2 true JPH0713124B2 (en) | 1995-02-15 |
Family
ID=12667292
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP63043566A Expired - Fee Related JPH0713124B2 (en) | 1988-02-26 | 1988-02-26 | Radiation graft polymerization equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0713124B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20040087677A1 (en) * | 2001-02-22 | 2004-05-06 | Takanobu Sugo | Method for graft polymerization to polymer substrate |
| JP4753062B2 (en) * | 2001-05-08 | 2011-08-17 | 独立行政法人 日本原子力研究開発機構 | Method and apparatus for radiation graft polymerization of fiber material |
-
1988
- 1988-02-26 JP JP63043566A patent/JPH0713124B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH01217021A (en) | 1989-08-30 |
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