JPS6063533A - Manufacture of printing plate material - Google Patents

Manufacture of printing plate material

Info

Publication number
JPS6063533A
JPS6063533A JP17109883A JP17109883A JPS6063533A JP S6063533 A JPS6063533 A JP S6063533A JP 17109883 A JP17109883 A JP 17109883A JP 17109883 A JP17109883 A JP 17109883A JP S6063533 A JPS6063533 A JP S6063533A
Authority
JP
Japan
Prior art keywords
solvent
weight
parts
printing plate
resin composition
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
Application number
JP17109883A
Other languages
Japanese (ja)
Inventor
Masaki Mori
森 昌己
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.)
Toray Industries Inc
Original Assignee
Toray Industries Inc
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 Toray Industries Inc filed Critical Toray Industries Inc
Priority to JP17109883A priority Critical patent/JPS6063533A/en
Publication of JPS6063533A publication Critical patent/JPS6063533A/en
Pending legal-status Critical Current

Links

Classifications

    • GPHYSICS
    • G03PHOTOGRAPHY; CINEMATOGRAPHY; ANALOGOUS TECHNIQUES USING WAVES OTHER THAN OPTICAL WAVES; ELECTROGRAPHY; HOLOGRAPHY
    • G03FPHOTOMECHANICAL PRODUCTION OF TEXTURED OR PATTERNED SURFACES, e.g. FOR PRINTING, FOR PROCESSING OF SEMICONDUCTOR DEVICES; MATERIALS THEREFOR; ORIGINALS THEREFOR; APPARATUS SPECIALLY ADAPTED THEREFOR
    • G03F7/00Photomechanical, e.g. photolithographic, production of textured or patterned surfaces, e.g. printing surfaces; Materials therefor, e.g. comprising photoresists; Apparatus specially adapted therefor
    • G03F7/16Coating processes; Apparatus therefor

Landscapes

  • Physics & Mathematics (AREA)
  • General Physics & Mathematics (AREA)

Abstract

PURPOSE:To obtain a printing plate material having a photosensitive resin uniform in film thickness and soluble in water or an org. solvent rationally with good productivity by using a concentration means as a means for removing a solvent out of a photosensitive resin compsn. CONSTITUTION:A photosensitive resin compsn. composed essentiall of a polymer soluble in water or in an org. solvent and a photosensitive monomer is concentrated to the concn. of >=70wt% of the total weight by evaporating a solvent, and it is laminated on a support 8 in a uniform film thickness. As an embodiment of such a process, the low concd. composn. mixed and prepd. with a preparation means 1 is delivered in a constant feed rate with a pump 2 to a concentration means 3, such as a vent-provided extruder to evaporate the solvent here, and the concd. compsn. is laminated on a metallic plate or a film with a constant feed rate means 6. The monomer can be added after the concn. means 3 so as to control to the min. the time length of the resin compsn. to be subjected to heating in order to avoid polymer. Such a process permits continuous concn. of the resin compsn. even poor in heat stability to a high concn. without impariging heat stability.

Description

【発明の詳細な説明】 〔本発明の技術分野〕 本発明は水または有機溶媒に可溶な感光性樹脂層を有す
る印刷版材の製造方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Technical Field of the Invention] The present invention relates to a method for producing a printing plate material having a photosensitive resin layer soluble in water or an organic solvent.

〔従来技術およびその問題点〕[Prior art and its problems]

水または有機溶媒(以下、溶媒と略す)に可溶な感光性
樹脂組成物の均一な膜厚層(以下、感光性樹脂層と略す
)を有する印刷版材(以下、印刷版材と略す)の製造方
法のポイントは、溶媒に可溶なポリマ(以下、ポリマと
略す)と感光性モノマ(以下、モノマと略す)を主成分
とし、溶媒を含有する感光性樹脂組成物(以下、樹脂組
成物と略す)の熱安定性が2通常は不充分であるのをい
かに回避するかにある。
Printing plate material (hereinafter referred to as printing plate material) having a uniform thickness layer (hereinafter referred to as photosensitive resin layer) of a photosensitive resin composition soluble in water or an organic solvent (hereinafter referred to as solvent) The key point of the manufacturing method is that the main components are a solvent-soluble polymer (hereinafter referred to as "polymer") and a photosensitive monomer (hereinafter referred to as "monomer"), and a photosensitive resin composition (hereinafter referred to as "resin composition") containing a solvent. The problem lies in how to avoid the fact that the thermal stability of substances (hereinafter referred to as substances) is usually insufficient.

すなわち、樹脂組成物の中には多量のモノマが含有され
ているにもかかわらず、樹脂組成物の感光特性を維持し
、良好な印刷版材を得るため、樹脂組成物中の熱重合禁
止剤の添加量は少量に抑えられていることから、製造工
程において熱重合を生じやすい。
That is, even though the resin composition contains a large amount of monomer, in order to maintain the photosensitive properties of the resin composition and obtain a good printing plate material, the thermal polymerization inhibitor in the resin composition is Since the amount added is suppressed to a small amount, thermal polymerization tends to occur during the manufacturing process.

そのため、従来技術は2例えば特公昭54−16241
号公報のように、溶媒を多量に用いて80℃以下の低温
で樹脂組成物の調製、吐出、ロール成形を行ない、樹脂
組成物が製造工程で熱重合するのを防いでいる。しかし
ながら、良好な印刷版材を得るためには、感光性樹脂層
中の溶媒も比較的少量に抑える必要がある。
Therefore, the conventional technology is 2, for example,
As in the publication, the resin composition is prepared, discharged, and roll-molded at a low temperature of 80° C. or lower using a large amount of solvent, thereby preventing the resin composition from being thermally polymerized during the manufacturing process. However, in order to obtain a good printing plate material, it is necessary to suppress the amount of solvent in the photosensitive resin layer to a relatively small amount.

従って、従来技術の最大の問題点としては、感光性樹脂
層から溶媒を乾燥させる必要があることであり、しかる
にこの乾燥は、著しく長時間を要することである。この
ため、製造工程において乾燥が律速となり、生産性の向
上に限界がある上に。
Therefore, the biggest problem with the prior art is that it is necessary to dry the solvent from the photosensitive resin layer, but this drying process takes an extremely long time. For this reason, drying becomes rate-limiting in the manufacturing process, and there is a limit to productivity improvement.

乾燥設備が高価になることなどから、製造コストが高く
なりp必ずしも合理的な製造方法とはいい難いことにあ
る。
Since the drying equipment is expensive, the manufacturing cost is high, and it is not necessarily a rational manufacturing method.

〔本発明の目的〕[Object of the present invention]

本発明の目的は、上記従来の欠点を除去し、均一な膜厚
の水または有機溶媒に可溶な感光性樹脂層を有する印刷
版材を2合理的に、高生産性で。
The purpose of the present invention is to eliminate the above-mentioned conventional drawbacks and to produce a printing plate material having a photosensitive resin layer soluble in water or an organic solvent with a uniform film thickness in a rational manner and with high productivity.

且つ安価に製造する方法を提供せんとするものである。Moreover, it is an object of the present invention to provide a method of manufacturing at low cost.

〔本発明の構成〕[Configuration of the present invention]

本発明は、上記の目的を達成するため次の如き構成を有
するものである。
The present invention has the following configuration to achieve the above object.

すなわち、水または有機溶媒に可溶カポリマおよび感光
性を有するモノマを主成分とする感光性樹脂組成物が全
体の70重量係以上である該感光性樹脂組成物の水また
は有機溶媒溶液を吐出し。
That is, a water or organic solvent solution of the photosensitive resin composition whose main components are a water or organic solvent-soluble polymer and a photosensitive monomer accounts for 70% or more by weight of the whole is discharged. .

支持体にラミネートして、均一な膜厚に成形する印刷版
材の製造方法を特徴とするものである。
The present invention is characterized by a method for manufacturing a printing plate material, which is laminated onto a support and formed into a uniform film thickness.

本発明の印刷版材に使用されるポリマとしては。Polymers used in the printing plate material of the present invention include:

例えばポリビニルアルコール系、セルロース誘導体系、
ポリ酢酸ビニル系、ポリビニルアセクール系、ポリアミ
ド系などであシ、またモノマとしては2例えばアクリル
酸エステル、メタクリル酸エステル、エチレングリコー
ル−ジグリシジルエーテル誘導体、プロピレングリコー
ル・ジグリシジルエーテル誘導体などである。
For example, polyvinyl alcohol type, cellulose derivative type,
Examples of the monomer include polyvinyl acetate, polyvinyl acecool, and polyamide. Examples of the monomer include acrylic ester, methacrylic ester, ethylene glycol diglycidyl ether derivatives, and propylene glycol diglycidyl ether derivatives.

また、これらの主成分の溶媒としては、水、低級アルコ
ールなどが使用され、印刷版材の支持体としては、金属
板またはフィルムなどが使用され。
Water, lower alcohol, etc. are used as the solvent for these main components, and a metal plate or film is used as the support for the printing plate material.

必要に応じてカバーフィルムもラミネートされる。A cover film is also laminated if necessary.

本発明を図面に基づき更に詳しく説明する。The present invention will be explained in more detail based on the drawings.

第1図は9本発明に係る印刷版材の製造方法の一例を示
す概略図である。第1図に示す装置は。
FIG. 1 is a schematic diagram showing an example of a method for manufacturing a printing plate material according to the present invention. The apparatus shown in FIG.

低濃度樹脂組成物を溶解、混合し調製する手段(以下、
調製手段と略す)1.低濃度樹脂組成物を定量輸送する
ポンプ2.低濃度樹脂組成物から溶媒を蒸発させ、濃縮
することにより高濃度樹脂組成物を得るだめの濃縮手段
(以下、濃縮手段と略す)3.真空ポンプ4.高濃度樹
脂組成物を定量排出する手段(以下、排出手段と略す)
5.定量吐出する手段(以下、吐出手段と略す)6.ダ
イア、高濃度樹脂組成物8を、金属板またはフィルムな
どの支持体9と、必要に応じてカバーフィルム10もラ
ミネート成形するだめの手段(以下。
Means for dissolving, mixing and preparing a low concentration resin composition (hereinafter referred to as
Preparation means)1. Pump for quantitatively transporting a low concentration resin composition 2. Concentration means for obtaining a high concentration resin composition by evaporating the solvent from the low concentration resin composition and concentrating it (hereinafter abbreviated as concentration means)3. Vacuum pump 4. Means for quantitatively discharging a high concentration resin composition (hereinafter abbreviated as discharge means)
5. Means for dispensing a fixed amount (hereinafter abbreviated as discharging means) 6. A means for laminating the diamond, high concentration resin composition 8, a support 9 such as a metal plate or a film, and a cover film 10 if necessary (described below).

成形手段と略す)11.ゴムまたはスチール製ベルトを
有するコンベア12を、走行方向に清って順次配置する
如く構成する。
(abbreviated as molding means)11. Conveyors 12 with rubber or steel belts are constructed so as to be arranged one after the other in the running direction.

また、必要に応じてダイアと、成形手段11の間に短時
間の乾燥装置13を設けてもよい。
Further, a short-time drying device 13 may be provided between the diamond and the molding means 11 if necessary.

ここで、調製手段1としては攪拌槽、ニーダ−など、濃
縮手段3としては回分式の攪拌槽、ニーダ−など、ある
いは連続式では薄膜蒸発機、ベント押出機など、排出手
段5としてはスクリュー。
Here, the preparation means 1 is a stirring tank, a kneader, etc., the concentration means 3 is a batch type stirring tank, kneader, etc., or the continuous type is a thin film evaporator, a vent extruder, etc., and the discharge means 5 is a screw.

ギヤポンプなど、吐出手段6としては押出機、ギヤポン
プなど、成形手段11としては、キャステインク法、カ
レンダー法などが使用できる。
As the discharging means 6 such as a gear pump, an extruder or a gear pump can be used, and as the molding means 11, a cast ink method, a calender method, etc. can be used.

なお、連続式の濃縮をベント押出機で行う場合の機種と
しては、スクリューが多軸でその回転数が大なため樹脂
組成物の剪断混合が充分できる多軸押出機1例えば2軸
押用機が、濃縮能力が大きく且つ樹脂組成物のベントア
ップもないことから。
In addition, when performing continuous concentration using a vent extruder, examples of models include a multi-screw extruder 1, which can sufficiently mix the resin composition by shearing as it has multiple screws and its rotation speed is high, such as a twin-screw extruder. However, it has a large concentration ability and there is no vent-up of the resin composition.

特に好ましい。Particularly preferred.

上記の構成を備えた本発明に係る製造方法の特徴は、感
光性樹脂層から溶媒を除去する手段として、乾燥の代り
に濃縮手段3を設けていることである。
A feature of the manufacturing method according to the present invention having the above configuration is that a concentrating means 3 is provided instead of drying as a means for removing the solvent from the photosensitive resin layer.

濃縮手段3としては、熱安定性の比較的良好な樹脂組成
物の場合には回分式でも良いが、熱安定性が不充分な樹
脂組成物の場合には連続式が好ましい。
The concentration means 3 may be of a batch type in the case of a resin composition with relatively good thermal stability, but a continuous type is preferable in the case of a resin composition with insufficient thermal stability.

すなわち、溶媒を1分以下というような極度の短時間で
連続的に蒸発させ、得られる高濃度樹脂組成物を連続的
に吐出することにより、高濃度化で生ずる溶媒の沸点近
くになる高温での熱履歴時間を最短とすることで、熱重
合を回避できる。
In other words, by continuously evaporating the solvent in an extremely short period of time, such as one minute or less, and continuously discharging the resulting high-concentration resin composition, it is possible to evaporate the solvent at high temperatures close to the boiling point of the solvent that results from the high concentration. By minimizing the thermal history time, thermal polymerization can be avoided.

また、樹脂組成物・中の溶媒量は、30重量係以下の場
合には乾燥なしでそのまま、または30分以下の短時間
の乾燥のみで適正量まで溶媒が減少6− して、乾燥の負担は小さいが、溶媒量がそれ以上では乾
燥も長時間となり、高濃度化のメリットが失なわれる。
In addition, if the amount of solvent in the resin composition is less than 30% by weight, it may be left as is without drying, or the solvent may be reduced to an appropriate amount by drying for a short time of 30 minutes or less6-, thereby reducing the burden of drying. is small, but if the amount of solvent exceeds that amount, drying will take a long time, and the advantage of high concentration will be lost.

第2図は9本発明に係る印刷版材の製造方法の別の例を
示す概略図である。第2図に示す装置は。
FIG. 2 is a schematic diagram showing another example of the method for manufacturing a printing plate material according to the present invention. The apparatus shown in FIG.

ポリマを溶解する手段(以下、溶解手段と略す)14、
低濃度ポリマ溶液を定量輸送するポンプ2゜低濃度ポリ
マ溶液から溶媒を蒸発させ、濃縮することにより高濃度
ポリマ溶液を得るだめの濃縮手段3.真空ポンプ4.モ
ノマ槽15のモノマを定量輸送するポンプ2.高濃度ポ
リマ溶液とモノマを混合して、高濃度樹脂組成物8を得
るだめの混合手段(以下、混合手段と略す)16.定量
吐出する手段6.ダイア、高濃度樹脂組成物8を、金属
板またはフィルムなどの支持体9と、必要に応じてカバ
ーフィルム10をラミネート成形するための手段11.
ゴムまたはスチール製ベルトを有するコンベア12を、
走行方向に沿って順次配置する如く構成する。
means for dissolving the polymer (hereinafter abbreviated as dissolving means) 14;
Pump 2 for quantitatively transporting the low concentration polymer solution. Concentration means for obtaining a high concentration polymer solution by evaporating the solvent from the low concentration polymer solution and concentrating it. 3. Vacuum pump 4. A pump for quantitatively transporting the monomer in the monomer tank 15 2. Mixing means (hereinafter abbreviated as mixing means) for mixing the high concentration polymer solution and the monomer to obtain the high concentration resin composition 8 16. Means for dispensing a fixed amount6. A means 11 for laminating and molding the diamond, high concentration resin composition 8, a support 9 such as a metal plate or film, and a cover film 10 if necessary.
A conveyor 12 with a rubber or steel belt,
The configuration is such that they are arranged sequentially along the running direction.

ここで、溶解手段14としては攪拌槽、ニーダ−など、
混合手段16としては2回分式の攪拌槽。
Here, the dissolving means 14 includes a stirring tank, a kneader, etc.
The mixing means 16 is a two-dose stirring tank.

ニーダ−など、あるいは連続式では流体混合器。A kneader, etc., or a fluid mixer in a continuous type.

押出機などが使用できる。An extruder etc. can be used.

上記の構成を備えた本発明に係る製造方法の特徴は、感
光性樹脂層から溶媒を除去する手段として、乾燥の代り
に予めポリマ溶液を濃縮する手段3を設け、その後、高
濃度ポリマ溶液とモノマを混合する手段16を設けてい
ることである。
A feature of the manufacturing method according to the present invention having the above configuration is that a means 3 for concentrating the polymer solution in advance instead of drying is provided as a means for removing the solvent from the photosensitive resin layer, and then a high concentration polymer solution is added. Means 16 for mixing the monomers is provided.

すなわち、樹脂組成物の熱安定性が不充分な理由は多量
のモノマを含有していることであるから。
That is, the reason why the thermal stability of the resin composition is insufficient is that it contains a large amount of monomer.

モノマの添加する時期をできるだけおくらせることによ
り、樹脂組成物の高濃度化で生ずる高温での熱履歴蒔間
を最短とするととができ、熱重合を回避できる。
By delaying the addition of the monomer as much as possible, it is possible to minimize the period of heat history at high temperatures that occurs due to the high concentration of the resin composition, and to avoid thermal polymerization.

この場合、ポリマ溶液のみでは熱安定性は良好であるか
ら、濃縮手段3としては1回分式でも連続式でも自由に
選択できる。
In this case, since the polymer solution alone has good thermal stability, the concentration means 3 can be freely selected from either a batch type or a continuous type.

また、混合手段16としては、熱安定性め比較的良好な
樹脂組成物の場合には回分式でも良いが。
Further, the mixing means 16 may be of a batch type in the case of a resin composition having relatively good thermal stability.

熱安定性の不充分な樹脂組成物の場合には連続式%式% さらに、高濃度ポリマ液とモノマの相溶性、粘度比によ
シ樹脂組成物の混合度が異々す、印刷版の感光特性に影
響することから、相溶性が不充分で粘度比が大の場合は
ど、剪断速度の大きい上記の多軸押出機を混合手段16
として用いるのが好ましい。
In the case of resin compositions with insufficient thermal stability, continuous formula % formula If the compatibility is insufficient and the viscosity ratio is large, the above-mentioned multi-screw extruder with a high shear rate may be used as the mixing means 16, since this may affect the photosensitive properties.
It is preferable to use it as

そして、この場合の濃縮手段6にも多軸押出機を使用す
れば、一体の装置で濃縮と混合が可能となり9合理的な
製造方法として、さらに好ましい。
In this case, if a multi-screw extruder is also used as the concentration means 6, concentration and mixing can be performed in an integrated device, which is more preferable as a rational manufacturing method.

第6図は2本発明に係る印刷版材の製造方法のさらに別
の例を示す概略図である。第6図に示す装置は、ポリマ
供給量をコントロールする機構18を備えたポリマのフ
ィーダー17.溶融助剤槽19の溶媒および可塑剤を定
量輸送するポンプ2、少量の溶融助剤によりポリマを可
塑化、加温し、溶融するだめの溶融手段(以下、溶融手
段と略−t)20. モノマ槽15のモノマを定量輸送
するポンプ2.高濃度ポリマ溶融液とモノマを混合して
、高濃度樹脂組成物8を得るための混合手段16、高濃
度樹脂組成物8を定量吐出する手段6゜ダイア、高濃度
樹脂組成物8を、金属板またはフィルムなどの支持体9
と、必要に応じてカバーフィルム10をラミネート成形
するだめの手段11゜ゴムまたはスチール製ベルトを有
するコンベア12をt走行方向に沿って順次配置する如
く構成する。
FIG. 6 is a schematic view showing still another example of the method for manufacturing a printing plate material according to the present invention. The apparatus shown in FIG. 6 includes a polymer feeder 17. Pump 2 for quantitatively transporting the solvent and plasticizer in the melting aid tank 19; a melting means (hereinafter abbreviated as melting means -t) for plasticizing, heating, and melting the polymer with a small amount of melting aid 20. A pump for quantitatively transporting the monomer in the monomer tank 15 2. A mixing means 16 for mixing a high concentration polymer melt and a monomer to obtain a high concentration resin composition 8, a means 6° for discharging a fixed amount of the high concentration resin composition 8, Support 9 such as a plate or film
and a means 11 for laminating the cover film 10 as required.A conveyor 12 having a belt made of rubber or steel is arranged sequentially along the traveling direction.

ここで、溶融手段20および混合手段16としては、ニ
ーダ−1押出機などが使用できる。
Here, as the melting means 20 and the mixing means 16, a kneader 1 extruder or the like can be used.

上記の構成を備えた本発明に係る製造方法の特徴は、感
光性樹脂層から溶媒を除去する手段として、当初から乾
燥不要の少量の溶媒しか添加せずポリマを高濃度で溶融
する手段20と、その後。
The manufacturing method according to the present invention having the above configuration is characterized by a means 20 for removing the solvent from the photosensitive resin layer by melting the polymer at a high concentration by adding only a small amount of solvent from the beginning without the need for drying. ,after that.

高濃度ポリマ溶融液とモノマを混合する手段16を設け
ていることである。
A means 16 for mixing the high concentration polymer melt and the monomer is provided.

すなわち、溶媒を少量しか用いていないから。In other words, only a small amount of solvent is used.

濃縮あるいは乾燥する必要がなく、さらに溶融手段20
と混合手段16を同一の装置とし、好ましくけ上記の多
軸押出機を使用すれば、連続的に溶融および混合ができ
、きわめて簡素化された製造方法となる。しかも、連続
的に吐出していることから、樹脂組成物の高濃度化で生
ずる高温での熱履歴時間が最短となり、熱重合を回避で
きる。
There is no need for concentration or drying, and there is no need for melting means 20.
By using the same device as the mixing means 16, and preferably using the above-mentioned multi-screw extruder, continuous melting and mixing can be achieved, resulting in an extremely simplified manufacturing method. Furthermore, since the resin composition is continuously discharged, the heat history time at high temperatures caused by increasing the concentration of the resin composition is minimized, and thermal polymerization can be avoided.

〔本発明の効果〕[Effects of the present invention]

本発明は上記した如き構成を有するだめに1次の如きす
ぐれた作用効果を奏するものである。
The present invention has the above-mentioned configuration, and therefore exhibits excellent effects as shown in the first order.

先ず、熱安定性が良好な樹脂組成物はもちろんのこと、
熱安定性が不充分な樹脂組成物でも連続的に濃縮、また
はポリマ液とモノマを連続的に混合することで樹脂組成
物の高温での熱履歴時間が極度に短時間となり、熱安定
性を保持し、高濃度化ができる。
First of all, not only a resin composition with good thermal stability,
Even for resin compositions with insufficient thermal stability, continuous concentration or continuous mixing of polymer liquid and monomer can extremely shorten the thermal history time of the resin composition at high temperatures, improving thermal stability. can be retained and highly concentrated.

また、樹脂組成物の高濃度吐出が可能となシ。In addition, it is possible to discharge the resin composition at a high concentration.

感光性樹脂層を乾燥なしで、あるいは短時間の乾燥のみ
で成形できる。従って、多大な乾燥設備が不要となり、
均一な膜厚の水または有機溶媒に可溶な感光性樹脂層を
有する印刷版材を2合理的に。
The photosensitive resin layer can be molded without drying or with only a short drying time. Therefore, a large amount of drying equipment is not required,
2. Rational printing plate material with a photosensitive resin layer soluble in water or organic solvent with uniform thickness.

高生産性で安価に製造するという初期の目的を達成でき
る。安価な印刷版の提供は1作業性などから待望されて
いる印刷版材の樹脂板化上きわめて好ましいものである
The initial objective of manufacturing at low cost with high productivity can be achieved. The provision of inexpensive printing plates is highly desirable in terms of the long-awaited use of resin plates for printing plate materials from the viewpoint of workability and the like.

また、樹脂組成物を高濃度化していることから高粘度が
得られ、従って通常の高温での成形技術であるキャステ
ィング法、カレンダー法、エクストルージョン法などが
適用できる。このため、樹脂組成物を容易に均一な膜厚
に成形でき、良好々厚精度の印刷版材を得ることができ
る。
Furthermore, since the resin composition is highly concentrated, a high viscosity can be obtained, and therefore, ordinary high temperature molding techniques such as casting method, calender method, extrusion method, etc. can be applied. Therefore, the resin composition can be easily molded into a uniform film thickness, and a printing plate material with good thickness accuracy can be obtained.

実施例1 第1図に示す装置を用いて印刷版を製造した。Example 1 A printing plate was manufactured using the apparatus shown in FIG.

ポリエーテル・セグメントを50重量係有寸る共重合ポ
リアミド100重量部、N−ブチルベンゼン・スルフォ
ンアミド40重量部、エタノール20重量部、水60重
量部を攪拌槽に添加し、攪拌下75℃、3時間かけてポ
リアミドを溶解した。
100 parts by weight of a copolyamide containing 50 parts by weight of polyether segments, 40 parts by weight of N-butylbenzene sulfonamide, 20 parts by weight of ethanol, and 60 parts by weight of water were added to a stirring tank, and the mixture was heated at 75°C under stirring. The polyamide was dissolved over a period of 3 hours.

溶解後、β−ヒドロキシ・エチルβ′−アクリロイルオ
キシ・エチルフタレート55重量部、α−メトキシ・ベ
ンゾイン・メチルエーテル2重量部。
After dissolving, 55 parts by weight of β-hydroxy ethyl β'-acryloyloxy ethyl phthalate and 2 parts by weight of α-methoxy benzoin methyl ether.

ハイドロキノン・モノメチルエーテル002重量部を添
加し、75℃、30分混合した。
2 parts by weight of hydroquinone monomethyl ether 000 was added and mixed at 75°C for 30 minutes.

混合後、8CMo、真空度400Torr、30分で濃
縮し、エタノールと水の混合溶媒20.6重量部を蒸発
させる。次に、濃縮で得た高濃度樹脂組成物をポンプに
より2次の押出機に輸送し、押出機で脱泡、温調してダ
イから支持フィルム上に定量吐出した。
After mixing, the mixture is concentrated under 8CMo and a vacuum degree of 400 Torr for 30 minutes to evaporate 20.6 parts by weight of the mixed solvent of ethanol and water. Next, the highly concentrated resin composition obtained by concentration was transported to a secondary extruder by a pump, defoamed in the extruder, temperature controlled, and discharged in a fixed amount from a die onto a support film.

吐出後、60℃、10分の熱風乾燥でエタノールと水の
混合溶媒75重量部を乾燥し、90℃に加温したニップ
圧201cg/anの1対の押圧ロールでカバーフィル
ムのラミネートと膜厚の調整を行ない、短時間の乾燥の
みで感光性樹脂層を有する印刷版を得た。
After discharging, 75 parts by weight of the mixed solvent of ethanol and water was dried by hot air drying at 60°C for 10 minutes, and the cover film was laminated and the film thickness was laminated using a pair of press rolls heated to 90°C and a nip pressure of 201 cg/an. A printing plate having a photosensitive resin layer was obtained with only a short drying time.

実施例2 第1図に示す装置を用いて印刷版を製造した。Example 2 A printing plate was manufactured using the apparatus shown in FIG.

ε−カプロラクタムとN、N’−ビス(アミノ・プロピ
ル)ピペラジンの共重合ポリアミド(共重合比35対6
5重量部)100重量部、メタノール54重量部、水5
4重量部を攪拌槽に添加し、実施例1と同様にポリアミ
ドを溶解した。
Copolyamide of ε-caprolactam and N,N'-bis(aminopropyl)piperazine (copolymerization ratio 35:6
5 parts by weight) 100 parts by weight, 54 parts by weight of methanol, 5 parts by weight of water
4 parts by weight were added to a stirring tank, and the polyamide was dissolved in the same manner as in Example 1.

溶解後、エチレングリコール・ジグリシジルエーテル・
ジアクリレート60重量部、ペンゾフエ13− ノン2重量部、ハイドロキノン0.1重量部を添加し、
75℃、30分混合した。
After dissolving, ethylene glycol, diglycidyl ether,
Adding 60 parts by weight of diacrylate, 2 parts by weight of Penzofe 13-non, and 0.1 part by weight of hydroquinone,
Mixing was performed at 75°C for 30 minutes.

混合後、ポンプで薄膜蒸発機に輸送し、90℃。After mixing, it was transported to a thin film evaporator using a pump and heated to 90°C.

真空度400 Torr 、1分で連続濃縮し、メタノ
ールと水の混合溶媒794重量部を蒸発させた。
Continuous concentration was performed for 1 minute at a vacuum degree of 400 Torr to evaporate 794 parts by weight of a mixed solvent of methanol and water.

次に、濃縮で得た高濃度樹脂組成物を実施例1と同様に
定量吐出し、但し、この場合は乾燥なしで直接に支持フ
ィルムとカバーフィルムのラミネートおよび膜厚の調整
を行ない、感光性樹脂層を有する印刷版を得た。
Next, the high-concentration resin composition obtained by concentration was dispensed in a fixed amount in the same manner as in Example 1, except that in this case, the support film and cover film were directly laminated without drying, and the film thickness was adjusted. A printing plate having a resin layer was obtained.

実施例6 第2図に示す装置を用いて印刷版を製造した。Example 6 A printing plate was manufactured using the apparatus shown in FIG.

N−メトキシ・メチル化6ボリアミド100重量部、N
−エチルトルエン・スルホンアミド60重量部、エタノ
ール80重量部、水53,3重量部を攪拌槽に添加し、
実施例1と同様にポリアミドを溶解する。
100 parts by weight of N-methoxy methylated 6-bolyamide, N
- Adding 60 parts by weight of ethyltoluene sulfonamide, 80 parts by weight of ethanol, and 53.3 parts by weight of water to a stirring tank,
Polyamide is dissolved in the same manner as in Example 1.

溶解度、90℃、真空度400Torr、60分で濃縮
し、エタノールと水の混合溶媒100.7重量部を蒸発
させ、高濃度ポリマ溶液を得た。
Concentration was carried out for 60 minutes at a solubility of 90° C. and a vacuum of 400 Torr, and 100.7 parts by weight of the mixed solvent of ethanol and water was evaporated to obtain a highly concentrated polymer solution.

14− 次に、この高濃度ポリマ溶液とβ−ヒドロキシ・エチル
β′−アクリロイル・オキシエチルフタレート38重量
部、α−メトキシ・ベンゾイン・メチルエーテル2重量
部、ハイドロキノン0.02重量部の混合物を各々ポン
プで定量輸送し、流体混合器により90℃にて連続的に
混合し、高濃度樹脂組成物を得た。
14- Next, a mixture of this highly concentrated polymer solution, 38 parts by weight of β-hydroxy ethyl β'-acryloyl oxyethyl phthalate, 2 parts by weight of α-methoxy benzoin methyl ether, and 0.02 parts by weight of hydroquinone was added to each. A high concentration resin composition was obtained by transporting a fixed amount using a pump and continuously mixing at 90°C using a fluid mixer.

その後、実施例2と同様に成形して、感光性樹脂層を有
する印刷版を得た。
Thereafter, it was molded in the same manner as in Example 2 to obtain a printing plate having a photosensitive resin layer.

実施例4 第2図に示す装置を用いて印刷版を製造した。Example 4 A printing plate was manufactured using the apparatus shown in FIG.

ポリビニル・アルコール(ケン化度82モル係。Polyvinyl alcohol (saponification degree 82 moles).

重合度5QO)100重量部、水186.8重量部をニ
ーグーに添加し、実施例1と同様に溶解した。
100 parts by weight (degree of polymerization: 5QO) and 186.8 parts by weight of water were added to Nigu and dissolved in the same manner as in Example 1.

溶解後、100℃、真空度300 Torr 、 6 
Q分で濃縮し、水125.6重量部を蒸発させ、高濃度
ポリマ溶液を得た。
After melting, 100°C, vacuum level 300 Torr, 6
It was concentrated for Q minutes, and 125.6 parts by weight of water was evaporated to obtain a highly concentrated polymer solution.

次に、この高濃度ポリマ溶液とβ−ヒドロキシエチル・
メタクリレート240重量部、ベンゾイン6.9重量部
、ハイドロキノン0.01重量部の混合物を各々ポンプ
で定量輸送し、2軸押用機により98℃にて連続的に混
合、脱泡し、高濃度樹脂組成物を得た。
Next, this highly concentrated polymer solution and β-hydroxyethyl
A mixture of 240 parts by weight of methacrylate, 6.9 parts by weight of benzoin, and 0.01 part by weight of hydroquinone was transported quantitatively using a pump, and continuously mixed and defoamed at 98°C using a twin-screw pusher to form a highly concentrated resin. A composition was obtained.

その後、実施例2と同様に成形してt感光性樹脂層を有
する印刷版を得た。
Thereafter, it was molded in the same manner as in Example 2 to obtain a printing plate having a t-photosensitive resin layer.

実施例5 第2図に示す装置を用いて印刷版を製造した。Example 5 A printing plate was manufactured using the apparatus shown in FIG.

ポリビニル・アルコール(ケン化度80モル係。Polyvinyl alcohol (saponification degree 80 mol).

重合度500 )100重量部、ジエチレン・グリコー
ル30重量部、エタノール32.6重量部、水75.4
重量部を攪拌槽に添加し、実施例1と同様に溶解した。
Polymerization degree 500) 100 parts by weight, diethylene glycol 30 parts by weight, ethanol 32.6 parts by weight, water 75.4 parts by weight
Parts by weight were added to a stirring tank and dissolved in the same manner as in Example 1.

溶解後、2軸押用機にて100°0で連続的に濃縮し、
エタノールと水の混合溶媒77.8重量部を蒸発させ、
高濃度ポリマ溶液を得た。
After dissolving, it is continuously concentrated at 100°0 using a twin-screw extrusion machine,
Evaporate 77.8 parts by weight of a mixed solvent of ethanol and water,
A highly concentrated polymer solution was obtained.

次に、プロピレングリコール・ジグリシジルエーテル・
ジアクリレート68重量部、α−メトキシ、ベンゾイン
・メチルエーテル2重量部の混合物をポンプで2軸押用
機の途中に定量輸送し、先の高濃度ポリマ溶液と2軸押
用機により98°Cにて連続的に混合、脱泡し、高濃度
樹脂組成物を得た。
Next, propylene glycol diglycidyl ether
A mixture of 68 parts by weight of diacrylate, α-methoxy, and 2 parts by weight of benzoin methyl ether was quantitatively transported to the middle of the twin-screw extruder using a pump, and heated to 98°C by the high concentration polymer solution and the twin-screw extruder. The mixture was continuously mixed and defoamed to obtain a highly concentrated resin composition.

その後、実施例2と同様に成形して、感光性樹脂層を有
する印刷版を得た。
Thereafter, it was molded in the same manner as in Example 2 to obtain a printing plate having a photosensitive resin layer.

実施例6 第3図に示す装置を用いて印刷版を製造した。Example 6 A printing plate was manufactured using the apparatus shown in FIG.

ポリビニル・アルコール(ケン化&80モルチ。Polyvinyl alcohol (saponified & 80 molt.

重合度500)100重量部、水33.9重量部を2軸
押用機に供給し、水でポリマを可塑化し、100℃に加
温し溶融した。
100 parts by weight (degree of polymerization: 500) and 33.9 parts by weight of water were supplied to a twin-screw extruder, the polymer was plasticized with water, and heated to 100°C to melt.

ポリマ溶融後、2軸押用機の途中に、N−メチロール・
アクリルアミドとジエチレン−グリコールのビスエーテ
ル60重量部、ダイア七トン・アクリルアミド60重量
部、α−メトキシ・ベンゾイン・メチルエーテル2重量
部の混合物を定量輸送し、2軸押用機により98℃にて
連続的に混合。
After melting the polymer, N-methylol and
A mixture of 60 parts by weight of acrylamide and diethylene glycol bisether, 60 parts by weight of dia-7ton acrylamide, and 2 parts by weight of α-methoxy benzoin methyl ether was quantitatively transported and continuously heated at 98°C using a twin-screw extrusion machine. mixed.

脱泡し、高濃度樹脂組成物を得た。Defoaming was performed to obtain a highly concentrated resin composition.

その後、実施例2と同様に成形して、感光性樹脂層を有
する印刷版を得た。
Thereafter, it was molded in the same manner as in Example 2 to obtain a printing plate having a photosensitive resin layer.

実施例7 第6図に示す装置を用いて印刷版を製造した。Example 7 A printing plate was manufactured using the apparatus shown in FIG.

ポリビニル0アルコール(ケン化度80モル係。Polyvinyl 0 alcohol (saponification degree 80 mol).

重合度500 )100重量部、ジエチレン・グリコー
ル30重量部、水299重量部を2軸押用機に供給し、
水およびジエチレン・グリコールでポリマを可塑化し、
100℃に加温し溶融した。
100 parts by weight of polymerization degree 500), 30 parts by weight of diethylene glycol, and 299 parts by weight of water were fed to a twin-screw extrusion machine,
Plasticize the polymer with water and diethylene glycol,
It was heated to 100°C and melted.

ポリマ溶融後、2軸押用機の途中にプロピレン0グリコ
ール龜ジグリシジルエーテル・ジアクリレート68重量
部、α−メトキシ・ベンゾイン。
After melting the polymer, 68 parts by weight of propylene glycol diglycidyl ether diacrylate and α-methoxy benzoin were placed in the middle of the twin-screw extruder.

メチルエーテル2重量部の混合物を定量輸送し。A quantitative amount of a mixture of 2 parts by weight of methyl ether was transported.

2軸押用機により98℃にて連続的に混合、脱泡し、高
濃度樹脂組成物を得た。
The mixture was continuously mixed and defoamed at 98° C. using a twin-screw extrusion machine to obtain a highly concentrated resin composition.

その後、実施例2と同様に成形して、感光性樹脂層を有
する印刷版を得た。
Thereafter, it was molded in the same manner as in Example 2 to obtain a printing plate having a photosensitive resin layer.

実施例8 第3図に示す装置を用いて印刷版を製造した。Example 8 A printing plate was manufactured using the apparatus shown in FIG.

ε−カプロラクタムおよびN、7−ビス(アミノ。ε-caprolactam and N,7-bis(amino.

プロピル)ピペラジンの共重合ポリアミド(共重合比6
5対65重量部)100重量部、水28.6重量部を2
軸押用機に供給し、水でポリマを可塑化し、100℃に
加温し溶融した。
Copolymerized polyamide (copolymerization ratio 6) of piperazine (propyl)
5 to 65 parts by weight) 100 parts by weight, 28.6 parts by weight of water to 2
The polymer was supplied to a shaft extrusion machine, plasticized with water, and heated to 100°C to melt it.

ポリマ溶融後、2軸押用機の途中にエチレングリコール
・ジグリシジルエーテル・ジアクリレート60重量部、
ベンゾフェノン2重量部、ノーイドロキノン0.1重量
部の混合物を定量輸送し、2軸押用機により90℃にて
連続的に混合、脱泡し。
After melting the polymer, 60 parts by weight of ethylene glycol diglycidyl ether diacrylate was placed in the middle of the twin-screw extrusion machine.
A mixture of 2 parts by weight of benzophenone and 0.1 part by weight of nohydroquinone was quantitatively transported, and continuously mixed and defoamed at 90°C using a twin-screw pusher.

高濃度樹脂組成物を得た。A highly concentrated resin composition was obtained.

その後、実施例2と同様に成形して、感光性樹脂層を有
する印刷版を得た。
Thereafter, it was molded in the same manner as in Example 2 to obtain a printing plate having a photosensitive resin layer.

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

第1図は9本発明を実施するだめの製造方法の一例を示
す概略図である。 第2図、第3図は2本発明を実施するだめの製造方法の
、各々他の例を示す概略図である。 1:低濃度樹脂組成物の調製手段 2:ポンプ 3:濃縮手段 4:真空ポンプ 5:排出手段 6:吐出手段 7:グイ 8:高濃度樹脂組成物 9:支持体 10:カバーフィルム 11:成形手段 12:コンベア 13:乾燥装置 14:ポリマ溶解手段 15:モノマ槽 16:混合手段 17:ポリマのフィーダー 18:ポリマ供給量コントロール機構 19;溶融助剤槽 20:ポリマ溶融手段 特許出願人 東 し 株 式 会 社 第1図 第2ryJ 第3rgJ
FIG. 1 is a schematic diagram showing an example of a method of manufacturing a container according to the present invention. FIGS. 2 and 3 are schematic diagrams showing other examples of two methods of manufacturing a container according to the present invention. 1: Preparation means for low concentration resin composition 2: Pump 3: Concentration means 4: Vacuum pump 5: Discharge means 6: Discharge means 7: Gui 8: High concentration resin composition 9: Support 10: Cover film 11: Molding Means 12: Conveyor 13: Drying device 14: Polymer melting means 15: Monomer tank 16: Mixing means 17: Polymer feeder 18: Polymer supply amount control mechanism 19; Melting aid tank 20: Polymer melting means Patent applicant Azuma Shi Co., Ltd. Formula Company Fig. 1 Fig. 2 ryJ 3rd rgJ

Claims (1)

【特許請求の範囲】[Claims] 水または有機溶媒に可溶なポリマおよび感光性を有する
モノマを主成分とする感光性樹脂組成物が全体の70重
量係以上でちる該感光性樹脂組成物の水または有機溶媒
溶液を吐出し、支持体にラミネートして均一な膜厚に成
形することを特徴とする印刷版材の製造方法。
Discharging a water or organic solvent solution of a photosensitive resin composition containing a water or organic solvent-soluble polymer and a photosensitive monomer as main components in a proportion of 70% or more by weight of the whole; A method for producing a printing plate material, which comprises laminating it onto a support and forming it into a uniform film thickness.
JP17109883A 1983-09-19 1983-09-19 Manufacture of printing plate material Pending JPS6063533A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17109883A JPS6063533A (en) 1983-09-19 1983-09-19 Manufacture of printing plate material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17109883A JPS6063533A (en) 1983-09-19 1983-09-19 Manufacture of printing plate material

Publications (1)

Publication Number Publication Date
JPS6063533A true JPS6063533A (en) 1985-04-11

Family

ID=15916945

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17109883A Pending JPS6063533A (en) 1983-09-19 1983-09-19 Manufacture of printing plate material

Country Status (1)

Country Link
JP (1) JPS6063533A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006065064A1 (en) * 2004-12-14 2006-06-22 Hyung Woo Kim A sterilizing apparatus

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006065064A1 (en) * 2004-12-14 2006-06-22 Hyung Woo Kim A sterilizing apparatus

Similar Documents

Publication Publication Date Title
US5135827A (en) Process for the manufacture of photopolymer plates
KR101500799B1 (en) Adhesive for polarizing plate, polarizing plate comprising the same and method for preparing thereof
JPH0231661B2 (en)
TWI276660B (en) Aromatic liquid crystal polyester and film thereof
CN105367969B (en) Optical film and its manufacturing method, polaroid protective film, polarizing film and liquid crystal display device
TWI633388B (en) Photosensitive resin element
CN101168296A (en) Preparation of polyvinyl fluoride thin film by solution casting method
EP2118176B1 (en) Method for dissolving aramid polymer in sulfuric acid using a double shaft kneader
JP4093390B2 (en) Method for producing polyvinyl alcohol film for polarizing film
WO2020138445A1 (en) Hydraulic transfer base film, and hydraulic transfer printing film
CN105467475A (en) Optical film, polarizing plate protective film, polarizing plate, and liquid crystal display device
JPS6063533A (en) Manufacture of printing plate material
JPH05305642A (en) Manufacture of polyvinyl alcohol-based polymer film and device thereof
CN106795256B (en) Block copolymer hydride and the stretched film formed by it
JPS5894431A (en) Manufacture of reactive plane-shaped shape having high thickness accuracy and stability
TWI324084B (en) Method and apparatus for producing dope
JP3997892B2 (en) Method for producing polyvinyl alcohol film for polarizing film
JPH0250927B2 (en)
JP6801250B2 (en) Manufacturing method of polyvinyl alcohol film
CN106626188A (en) Preparation process of cellulose triacetate film
TW200402331A (en) Method of forming coating
JPH05301239A (en) Method and apparatus for producing polyvinyl alcohol polymer film
JP2002059475A (en) Method for manufacturing polyvinyl alcohol film
CN107266804A (en) A kind of dumb light PS sheet materials and its manufacture method
JP2002161109A (en) Method for removing organic solvent and manufacturing pellet from solution of isobutylene-based block copolymer