JP3127967B2 - Manufacturing method of printing plate - Google Patents

Manufacturing method of printing plate

Info

Publication number
JP3127967B2
JP3127967B2 JP03224963A JP22496391A JP3127967B2 JP 3127967 B2 JP3127967 B2 JP 3127967B2 JP 03224963 A JP03224963 A JP 03224963A JP 22496391 A JP22496391 A JP 22496391A JP 3127967 B2 JP3127967 B2 JP 3127967B2
Authority
JP
Japan
Prior art keywords
printing plate
twin
screw
concentration
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.)
Expired - Fee Related
Application number
JP03224963A
Other languages
Japanese (ja)
Other versions
JPH0659440A (en
Inventor
勝廣 松尾
勝 南平
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.)
Toyobo Co Ltd
Original Assignee
Toyobo Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Toyobo Co Ltd filed Critical Toyobo Co Ltd
Priority to JP03224963A priority Critical patent/JP3127967B2/en
Publication of JPH0659440A publication Critical patent/JPH0659440A/en
Application granted granted Critical
Publication of JP3127967B2 publication Critical patent/JP3127967B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Landscapes

  • Extrusion Moulding Of Plastics Or The Like (AREA)
  • Photosensitive Polymer And Photoresist Processing (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、感光性樹脂層を有する
印刷用版材の製造方法に関し、さらに詳しくは、感光性
樹脂組成物の水および/または有機溶媒溶液の濃縮方法
に特徴を有する印刷用版材の製造方法に関するものであ
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a printing plate having a photosensitive resin layer, and more particularly, to a method for concentrating a solution of a photosensitive resin composition in water and / or an organic solvent. The present invention relates to a method for manufacturing a printing plate material.

【0002】[0002]

【従来の技術】従来よりゴム成分を含む感光性樹脂組成
物はフレキソ印刷用版材として使用されており、フレキ
ソ印刷用版材は特に包装材料、たとえばダンボールやフ
イルムなどの柔軟で変形し易いものに印刷する際に使用
されるため版材には適正な弾性表面を有することが必要
である。例えば水現像可能なゴム成分を含む感光性樹脂
組成物は、例えば特開平1−219735号公報に記載
されるように、Tg5℃以下の疎水性ポリマーと親水性
ポリマーとをベースとする組成物によって得られる。
2. Description of the Related Art Conventionally, photosensitive resin compositions containing a rubber component have been used as flexographic printing plates, and flexographic printing plates are particularly flexible and easily deformable such as cardboard and films. It is necessary that the plate material has an appropriate elastic surface to be used when printing on a printing plate. For example, a photosensitive resin composition containing a water-developable rubber component is, for example, a composition based on a hydrophobic polymer and a hydrophilic polymer having a Tg of 5 ° C. or lower, as described in JP-A-1-219735. can get.

【0003】上記組成物を用いて印刷版材とするには、
該組成物を水および/または有機溶媒にて調整したの
ち、該溶媒を蒸発させ、残存する溶媒が約1重量%以下
に濃縮した後、吐出し、支持体にラミネートして厚みの
均一なシートに成型することが必要である。従来技術と
して、水または有機溶媒を含む組成物を濃縮する方法と
しては、回分式では撹拌層、ニーダーなど、連続式では
薄膜蒸発機、ベント式押出機などにより加熱、更には減
圧を併用して濃縮する方法があり、特に熱安定性が不十
分な樹脂組成物の場合には連続式が好ましく、特開昭6
0−63533号公報に記載されているように、濃縮を
ベント式押出機で行う場合の機種としては、二軸押出機
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、特に好ましいとされている。
In order to make a printing plate material using the above composition,
After adjusting the composition with water and / or an organic solvent, the solvent is evaporated, and the remaining solvent is concentrated to about 1% by weight or less, then discharged, laminated on a support, and laminated into a sheet having a uniform thickness. It is necessary to mold it. As a conventional technique, as a method of concentrating a composition containing water or an organic solvent, in a batch system, a stirring layer, a kneader, etc., in a continuous system, a thin film evaporator, heating by a vent-type extruder, etc. There is a method of concentrating, especially in the case of a resin composition having insufficient heat stability, a continuous method is preferable.
As described in Japanese Patent Publication No. 0-63333, a twin-screw extruder is particularly preferable as a model in which concentration is performed by a vented extruder, because a twin-screw extruder has a large concentration ability and does not have a vent up of the resin composition. It has been.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、二軸押
出機を用いて一段で濃縮する場合、高剪断性のためスク
リュー先端での発熱が激しく、樹脂劣化が生じやすい。
特にフレキソ印刷用版材に用いられるゴム成分を含む感
光性樹脂組成物では、残存する溶媒を約1重量%以下に
しないとレリーフとした後でカールや凸部にへこみが生
じるなど品質上問題となるため、樹脂分が99重量%以
上となるような高濃度濃縮を行う必要があり、その粘度
も数万ポイズ以上となるので発熱による樹脂劣化の防止
が必要であった。
However, when concentration is performed in one step using a twin-screw extruder, heat generation at the screw tip is severe due to high shearing property, and resin deterioration is apt to occur.
In particular, in the case of a photosensitive resin composition containing a rubber component used for a flexographic printing plate material, the remaining solvent must be reduced to about 1% by weight or less. Therefore, it is necessary to perform high-concentration concentration so that the resin content is 99% by weight or more, and its viscosity becomes tens of thousands poise or more.

【0005】樹脂劣化の防止方法としてはスクリュー軸
を中空とし、冷却水を通したり二軸押出機本体をジャケ
ットとして冷却するなどの方法があるが、冷却すること
による蒸発効率の低下、更には樹脂の温度分布の発生に
よる不均一流動の結果、流れのデッドが生じるなど好ま
しくない現象が現れる。したがって発熱を生じたその熱
量を除去する方法ではなく、発熱自体を低減させる方法
が好ましく、通常はスクリューの回転数を下げ発熱を防
止する方法がとられている。しかしながら、回転数を下
げることによって水および/または有機溶媒を含む組成
物を均一に濃縮するのに必要な表面更新が不足し、濃縮
が不均一になったり、能力が著しく低下するなど従来技
術では、品質が不安定であり生産性にも限界があった。
[0005] As a method of preventing resin deterioration, there is a method in which a screw shaft is hollow and cooling water is passed through or a twin-screw extruder body is cooled as a jacket. As a result of non-uniform flow due to the occurrence of the temperature distribution, undesirable phenomena such as dead of the flow occur. Therefore, a method of reducing the amount of heat generated, rather than a method of removing the amount of heat, is preferable, and a method of reducing the number of rotations of the screw and preventing the heat is usually employed. However, in the conventional technology, the surface renewal required for uniformly concentrating a composition containing water and / or an organic solvent is insufficient by lowering the number of revolutions, and the concentration becomes nonuniform or the capability is significantly reduced. However, the quality was unstable and the productivity was limited.

【0006】[0006]

【課題を解決するための手段】本発明者らは、上記従来
技術の諸問題を改善することを目的とし、鋭意研究努力
した結果、遂に本発明を完成するに到った。すなわち本
発明は、ゴム成分を含む感光性樹脂組成物の水および/
または有機溶媒溶液から印刷用版材を製造する方法にお
いて、濃縮工程と押出工程とを、順次少なくとも二台の
二軸押出機を用いて行い、1台目の二軸押出機により水
および/または有機溶媒を樹脂成分が85〜95重量%
となるまで濃縮し、2台目以降の二軸押出機により99
重量%以上となるまで濃縮することを特徴とする印刷用
版材の製造方法である。
Means for Solving the Problems The inventors of the present invention have intensively studied for the purpose of improving the above-mentioned problems of the prior art, and have finally completed the present invention. That is, the present invention relates to a method for preparing a photosensitive resin composition containing a rubber component by using water and / or
Alternatively, in a method of producing a printing plate material from an organic solvent solution, the concentration step and the extrusion step are sequentially performed using at least two twin-screw extruders, and water is added to the first twin-screw extruder.
And / or an organic solvent having a resin component content of 85 to 95% by weight.
And concentrated by the second and subsequent twin screw extruders.
It is a method for producing a printing plate material, comprising concentrating to a concentration of at least% by weight .

【0007】本発明方法において、少なくとも2台の二
軸押出機、特にベント式二軸押出機を用いることによっ
て、まず、1段階目の濃縮機にて感光性樹脂組成物が急
激な粘度上昇が起こらない程度に濃縮する。これによっ
て一段で高濃度濃縮を行う場合と比較して粘度上昇がな
いため、従って均一な濃縮に必要な回転数まで高めるこ
とが出来、更に回転数を高くすることによってスクリュ
ーによる表面更新が良くなり濃縮の効率が上がり生産性
が向上する。急激な粘度上昇が起こらない程度の濃縮
は、好ましくは感光性樹脂組成物が85乃至95重量%
である。なお85重量%以下であると二段目以降の濃縮
負荷が大きくなり一段で高濃度濃縮する場合と同じ結果
となるので好ましくない。又、95重量%以上の濃縮を
行うと粘度が急上昇し発熱が著しく、樹脂劣化が生じる
ので好ましくない。発熱による樹脂劣化が生じる樹脂温
度はスクリューによる剪断力の大きさや滞留時間によっ
て異なるが、ゴム成分を含む感光性樹脂組成物では、9
0乃至100℃以上であり、樹脂劣化防止のためには樹
脂温度を90℃以下とすることが好ましい。次に二段目
以降のベント式二軸押出機にて残った溶媒を蒸発し、吐
出する。2台目以降のベント式二軸押出機は残溶媒量が
少なく1台目と比較し、表面更新も少なくてすむため発
熱を防止するための回転数を容易に得ることができる。
In the method of the present invention, by using at least two twin-screw extruders, in particular, a vent-type twin-screw extruder, first, a sharp increase in the viscosity of the photosensitive resin composition occurs in the first-stage concentrator. Concentrate to the extent that does not occur. As a result, there is no increase in viscosity as compared with the case of performing high-concentration concentration in a single step, so that the number of revolutions required for uniform concentration can be increased, and further increasing the number of revolutions improves the surface renewal by the screw. The efficiency of concentration is increased, and the productivity is improved. Concentration that does not cause a sharp increase in viscosity is preferably performed when the photosensitive resin composition is 85 to 95% by weight.
It is. If the concentration is less than 85% by weight, the load of concentration in the second and subsequent stages increases, and the same result as in the case of performing high concentration concentration in one stage is not preferable. On the other hand, when the concentration is 95% by weight or more, the viscosity rises sharply, heat generation is remarkable, and resin deterioration occurs, which is not preferable. The resin temperature at which the resin is degraded due to heat generation varies depending on the magnitude of the shearing force by the screw and the residence time.
The temperature is 0 to 100 ° C. or higher, and the resin temperature is preferably 90 ° C. or lower to prevent resin deterioration. Next, the remaining solvent is evaporated and discharged by the second and subsequent vented twin-screw extruders. The second and subsequent vented twin-screw extruders have less residual solvent and require less surface renewal than the first, so that the number of rotations for preventing heat generation can be easily obtained.

【0008】本発明を図面に基づき更に詳しく説明す
る。図1は、本発明印刷用版材の製造方法に用いる装置
の一例を示す概略図である。図1に示す装置はゴム成分
を含む感光性樹脂組成物を、水および/または有機溶剤
にて混合し、調整する混合タンク1、混合タンク1より
定量移送するポンプ2、水および/または有機溶剤を樹
脂成分が85〜95重量%となるまで蒸発する1台目の
ベント式二軸押出機3、同様に樹脂成分を99%以上に
濃縮し、且つ吐出する2台目のベント式二軸押出機4、
高粘度物を定量排出するためのポンプ5、高粘度物をシ
ート状に成型するためのダイ6、感光性樹脂組成物を金
属又はフイルムなどの支持体7、とカバーフイルム8、
とによりラミネート成型するラミネート機9、ラミネー
トされた印刷用版材を引き取るための引取コンベア1
0、から構成される。ここで混合タンク1は該組成物の
混合、調整を短時間に均一化するために加熱することが
効果的で、通常加熱された熱媒体をジャケットとした
合タンク1に通すことにより加熱できる。定量移送ポン
プ2はスクリューあるいはギアポンプなどが使用でき
る。2台目のベント式二軸押出機3は大量の水および/
または有機溶媒を蒸発するため、真空ポンプ11によっ
てベント口より蒸気の排出をすることが効果的である。
更に供給口後部にベント口aを設けることによってその
効果が著しく増大される。なお1台目のベント式二軸押
出機3に用いるスクリュー形状は特に限定されるもので
はないが、水および/または有機溶剤の蒸発を促進させ
るためには表面更新にすぐれた形状が好ましく、例えば
深ミゾのフライトタイプや練り効果のあるニーデングデ
スクを適宜配置したスクリューなどがある。2台目のベ
ント式二軸押出機4は1台目のベント式二軸押出機3と
同じ構造のものを用いることが出来るが、スクリューは
低回転で高吐出タイプの形状のものが発熱防止に効果的
である。高粘度物を定量排出するためのポンプ5はスク
リュー、ギアポンプなどが使用できる。
The present invention will be described in more detail with reference to the drawings. FIG. 1 is a schematic view showing an example of an apparatus used in the method for producing a printing plate material of the present invention. The apparatus shown in FIG. 1 mixes a photosensitive resin composition containing a rubber component with water and / or an organic solvent and adjusts it. A mixing tank 1, a pump 2 for transferring a fixed amount from the mixing tank 1, water and / or an organic solvent Vent-type twin-screw extruder 3 which evaporates the resin component to 85 to 95% by weight, and similarly vent-type twin-screw extruder which concentrates and discharges the resin component to 99% or more Machine 4,
A pump 5 for quantitatively discharging the high-viscosity material, a die 6 for molding the high-viscosity material into a sheet, a support 7 of the photosensitive resin composition such as a metal or a film, and a cover film 8,
Laminating machine 9 for laminating and molding, take-up conveyor 1 for taking over laminated printing plate material
0. Here, it is effective to heat the mixing tank 1 in order to make the mixing and adjustment of the composition uniform in a short time, and the mixing tank 1 is usually passed through the mixing tank 1 having a heated heat medium as a jacket. Can be heated. As the fixed amount transfer pump 2, a screw or a gear pump can be used. The second vented twin-screw extruder 3 has a large amount of water and / or
Alternatively, to evaporate the organic solvent, it is effective to discharge the vapor from the vent port by the vacuum pump 11.
Further, by providing the vent port a at the rear of the supply port, the effect is remarkably increased. The shape of the screw used in the first vented twin-screw extruder 3 is not particularly limited, but a shape excellent in surface renewal is preferable in order to promote evaporation of water and / or an organic solvent. There is a deep groove flight type and a screw with a kneading desk with a kneading effect appropriately arranged. The second vent-type twin-screw extruder 4 can have the same structure as the first vent-type twin-screw extruder 3, but the screw has a low rotation and a high discharge type to prevent heat generation. It is effective for A screw, a gear pump, or the like can be used as the pump 5 for quantitatively discharging the high-viscosity material.

【0009】[0009]

【作用】上記の構成を備えた本発明に係わる製造方法の
特徴としては、ゴム成分を含む感光性樹脂組成物から水
および/または有機溶剤を除去する手段として、濃縮の
機能と高粘度物の押出機能とを少なくとも2段階に分け
て持たせることによって、スクリュー回転による発熱が
防止され、品質の安定した印刷用版材が得られるものと
思われる。
The manufacturing method according to the present invention having the above-mentioned structure is characterized in that as a means for removing water and / or an organic solvent from a photosensitive resin composition containing a rubber component, it has a function of concentrating and a method of removing a high-viscosity substance. By providing the extruding function in at least two stages, heat generation due to screw rotation is prevented, and a printing plate material of stable quality is expected to be obtained.

【0010】[0010]

【実施例】次に本発明を実施例を用いて具体的に説明す
るが、本発明はこれらに限定されるものではない。 実施例1 ヘキサメチレンジイソシアネート21.8部、ジメチロ
ールプロピオン酸15.4部、ポリテトラメチレングリ
コール7.6部、及びジラウリン酸ジ−n−ブチルスズ
1部をテトラヒドロララン300部を溶解した溶液を撹
拌機の付いたタンクに入れ撹拌を続けながらタンクを6
5℃に加熱し3時間反応を続けた。別の容器で、末端ア
ミノ基含有アクリロニトリル・ブタジエンオリゴマー5
5.3部をメチルエチルケトン100部に溶解して調整
した溶液を上記のタンク内に室温下で撹拌しながら添加
した。得られたポリマー溶液を減圧乾燥してテトラヒド
ロフラン、メチルエチルケトンを除去し、平均分子量が
21.000のポリマーを得た。次に該ポリマー100
部をメチルエチルケトン100部に溶解した溶液に、水
酸化リチウム4.8部をメチルアルコール100部に溶
解した溶液を室温下で撹拌しながら添加し、更に30分
撹拌することによって親水性ポリマーを得た。次に上記
親水性ポリマー5部、疎水性ポリマーとして塩素化ポリ
エチレン20部、スチレンブタジエンゴム5部、ブタジ
エンオリゴアクリレート14部ベンジルジメチルケター
ル0.5部、ハイドロキノンモノメチルエーテル0.2
5部、水、メチルエチルケトンおよびテトラヒドロフラ
ンの混合溶媒55部を混合し感光性樹脂組成物溶液を得
た。
Next, the present invention will be described in detail with reference to examples, but the present invention is not limited to these examples. Example 1 A solution prepared by dissolving 21.8 parts of hexamethylene diisocyanate, 15.4 parts of dimethylolpropionic acid, 7.6 parts of polytetramethylene glycol, and 1 part of di-n-butyltin dilaurate in 300 parts of tetrahydrolaran was stirred. Place the tank in the tank equipped with
The reaction was heated to 5 ° C. and continued for 3 hours. In a separate container, acrylonitrile-butadiene oligomer 5 containing a terminal amino group
A solution prepared by dissolving 5.3 parts in 100 parts of methyl ethyl ketone was added to the above tank while stirring at room temperature. The obtained polymer solution was dried under reduced pressure to remove tetrahydrofuran and methyl ethyl ketone to obtain a polymer having an average molecular weight of 21.000. Next, the polymer 100
A solution of 4.8 parts of lithium hydroxide in 100 parts of methyl alcohol was added to a solution of 100 parts of methyl ethyl ketone while stirring at room temperature, and further stirred for 30 minutes to obtain a hydrophilic polymer. . Next, 5 parts of the above hydrophilic polymer, 20 parts of chlorinated polyethylene as a hydrophobic polymer, 5 parts of styrene butadiene rubber, 14 parts of butadiene oligoacrylate 0.5 part of benzyldimethyl ketal, 0.2 part of hydroquinone monomethyl ether 0.2 part
5 parts, water, 55 parts of a mixed solvent of methyl ethyl ketone and tetrahydrofuran were mixed to obtain a photosensitive resin composition solution.

【0011】次に図1に示す装置を用いて前記組成物溶
液をギアポンプにて1台目の二軸押出機へ移送し、スク
リュー回転数毎分100回転、真空度20Torrに
て、ベント部より溶剤を蒸発させ感光性樹脂組成物濃度
が90重量%となるように濃縮した。この時の樹脂組成
物の温度は85℃であった。次に2台目の二軸押出機へ
移送し、スクリュー回転数毎分30回転、真空度10T
orrにて、感光性樹脂組成物濃度が99.5重量%と
なるように濃縮した。2台目の二軸押出機の出口におけ
る樹脂組成物の温度を測定したところ90℃であった。
次にギアポンプにてダイより吐出し、100℃に加熱し
た1対の金属ロールにてポリエステルフイルムの支持
体、ポリエステルフィルムのカバーフイルムを用いてラ
ミネートし、厚み3mmの印刷用版材を得た。次に得ら
れた印刷用版材の最上層のポリエステルフイルムを剥離
して感光性樹脂層上に画像を有するネガフイルムを密着
して水銀灯で、照度25W/m2 、5分間露光を行っ
た。ネガフイルムを除いた後、アルキルナフタレンスル
ホン酸ソーダ2重量%を含有する中性水で40℃15分
間、ブラシによる現象を行ったところレリーフの深度
1.2mmの鮮明な画像パターンが得られた。
Next, using the apparatus shown in FIG. 1, the composition solution was transferred to the first twin-screw extruder by a gear pump, and the screw was rotated 100 times per minute at a vacuum of 20 Torr from the vent. The solvent was evaporated and concentrated so that the concentration of the photosensitive resin composition became 90% by weight. At this time, the temperature of the resin composition was 85 ° C. Next, it is transferred to the second twin screw extruder, where the screw rotation speed is 30 rotations per minute, and the degree of vacuum is 10T.
At orr, the photosensitive resin composition was concentrated so as to have a concentration of 99.5% by weight. When the temperature of the resin composition at the outlet of the second twin screw extruder was measured, it was 90 ° C.
Next, the mixture was discharged from a die by a gear pump and laminated with a pair of metal rolls heated to 100 ° C. using a polyester film support and a polyester film cover film to obtain a printing plate material having a thickness of 3 mm. Next, the polyester film of the uppermost layer of the obtained printing plate material was peeled off, and a negative film having an image was adhered to the photosensitive resin layer, and exposed to light with a mercury lamp at an illuminance of 25 W / m 2 for 5 minutes. After removing the negative film, a brushing phenomenon was performed with neutral water containing 2% by weight of sodium alkylnaphthalenesulfonate at 40 ° C. for 15 minutes. As a result, a clear image pattern having a relief depth of 1.2 mm was obtained.

【0012】比較例1 実施例1と同様に調整した感光性樹脂組成物溶液をギア
ポンプにて1台の二軸押出機にてスクリュー回転数毎分
100回転、真空度20Torrにて、ベント部より溶
剤を蒸発させ感光性樹脂組成物濃度が99.5重量%と
なるように一段で濃縮した。この時の樹脂組成物の温度
は110℃であった。次にギアポンプにてダイより吐出
し、100℃に加熱した1対の金属ロールにてポリエス
テルフイルムの支持体とポリエステルフィルムのカバー
フイルムを用いてラミネートし、厚み3mmの印刷用版
材を得た。得られた印刷用版材を実施例1と同じ条件に
てブラシによる現像を行った結果、レリーフの深度が
0.5mm程度で、ネガフイルムの画像を再現すること
が出来なかった。
Comparative Example 1 The photosensitive resin composition solution prepared in the same manner as in Example 1 was rotated by a single pump using a gear pump at a screw speed of 100 revolutions per minute at a vacuum of 20 Torr from the vent. The solvent was evaporated and the photosensitive resin composition was concentrated in one step so that the concentration became 99.5% by weight. At this time, the temperature of the resin composition was 110 ° C. Next, the film was discharged from a die by a gear pump, and laminated with a pair of metal rolls heated to 100 ° C. using a polyester film support and a polyester film cover film to obtain a printing plate material having a thickness of 3 mm. The resulting printing plate material was developed with a brush under the same conditions as in Example 1. As a result, the relief film had a depth of about 0.5 mm, and a negative film image could not be reproduced.

【0013】[0013]

【発明の効果】以上かかる構成よりなる本発明方法を採
用することにより、スクリュー回転による発熱が防止さ
れ、品質の安定した印刷用版材を得ることができるの
で、産業界に寄与すること大である。
By adopting the method of the present invention having the above-described structure, heat generation due to screw rotation is prevented, and a printing plate having a stable quality can be obtained, which contributes to the industry. is there.

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

【図1】図1は本発明方法の一実施態様例を示す概略図
である。
FIG. 1 is a schematic view showing an embodiment of the method of the present invention.

【符号の説明】[Explanation of symbols]

1:混合タンク 2:ポンプ 3:一段目のベント式二軸押出機 4:二段目のベント式二軸押出機 5:ポンプ 6:ダイ 7:支持体 8:カバーフイルム 9:ラミネート機 10:引き取りコンベア 11:真空ポンプ 1: Mixing tank 2: Pump 3: First-stage vented twin-screw extruder 4: Second-stage vented twin-screw extruder 5: Pump 6: Die 7: Support body 8: Cover film 9: Laminating machine 10: Pickup conveyor 11: vacuum pump

───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) G03F 7/00 G03F 7/16 B29C 47/00 ──────────────────────────────────────────────────続 き Continued on the front page (58) Field surveyed (Int. Cl. 7 , DB name) G03F 7/00 G03F 7/16 B29C 47/00

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】ゴム成分を含む感光性樹脂組成物の水およ
び/または有機溶媒溶液から印刷用版材を製造する方法
において、濃縮工程と押出工程とを、順次少なくとも二
台の二軸押出機を用いて行い、1台目の二軸押出機によ
り水および/または有機溶媒を樹脂成分が85〜95重
量%となるまで濃縮し、2台目以降の二軸押出機により
99重量%以上となるまで濃縮することを特徴とする印
刷用版材の製造方法。
1. A method for producing a printing plate material from a solution of a photosensitive resin composition containing a rubber component in water and / or an organic solvent, wherein a concentration step and an extrusion step are sequentially performed by at least two twin screw extruders. Using the first twin-screw extruder.
Water and / or organic solvent with a resin component of 85 to 95
% Until it reaches a volume% and the second and subsequent twin screw extruders
A method for producing a printing plate material, comprising concentrating to 99% by weight or more .
JP03224963A 1991-08-09 1991-08-09 Manufacturing method of printing plate Expired - Fee Related JP3127967B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP03224963A JP3127967B2 (en) 1991-08-09 1991-08-09 Manufacturing method of printing plate

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP03224963A JP3127967B2 (en) 1991-08-09 1991-08-09 Manufacturing method of printing plate

Publications (2)

Publication Number Publication Date
JPH0659440A JPH0659440A (en) 1994-03-04
JP3127967B2 true JP3127967B2 (en) 2001-01-29

Family

ID=16821952

Family Applications (1)

Application Number Title Priority Date Filing Date
JP03224963A Expired - Fee Related JP3127967B2 (en) 1991-08-09 1991-08-09 Manufacturing method of printing plate

Country Status (1)

Country Link
JP (1) JP3127967B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2353839B1 (en) 2010-01-27 2014-12-10 Coperion GmbH Method and plant for degasing polymer melts

Also Published As

Publication number Publication date
JPH0659440A (en) 1994-03-04

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