JPH0243023A - Film or sheet excellent in thermal stability of form and manufacture thereof - Google Patents

Film or sheet excellent in thermal stability of form and manufacture thereof

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Publication number
JPH0243023A
JPH0243023A JP19480888A JP19480888A JPH0243023A JP H0243023 A JPH0243023 A JP H0243023A JP 19480888 A JP19480888 A JP 19480888A JP 19480888 A JP19480888 A JP 19480888A JP H0243023 A JPH0243023 A JP H0243023A
Authority
JP
Japan
Prior art keywords
film
stretching
weight
sheet
aromatic vinyl
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
JP19480888A
Other languages
Japanese (ja)
Inventor
Kazuhiko Hazama
和彦 間
Takao Hosokawa
孝夫 細川
Kazuhiko Koizumi
和彦 小泉
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.)
Kyowa Gas Chemical Industry Co Ltd
Original Assignee
Kyowa Gas Chemical Industry 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 Kyowa Gas Chemical Industry Co Ltd filed Critical Kyowa Gas Chemical Industry Co Ltd
Priority to JP19480888A priority Critical patent/JPH0243023A/en
Publication of JPH0243023A publication Critical patent/JPH0243023A/en
Pending legal-status Critical Current

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  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
  • Manufacture Of Macromolecular Shaped Articles (AREA)
  • Shaping By String And By Release Of Stress In Plastics And The Like (AREA)

Abstract

PURPOSE:To improve formal stability under heat, by a method wherein the title film is obtained from copolymeric resin where a composition of a monomer comprises methacrylic acid methyl, maleic anhydride and aromatic vinyl compound and MFI is not exceeding a specific value, biaxially-oriented by a tensile orientation method and ORS of each axial directions has a specific value. CONSTITUTION:The title film or sheet is of copolymer resin whose composition of a monomer is comprised of 92-45wt.% methacrylic acid methyl, 3-25wt.% maleic anhydride and a 5-30wt.% aromatic vinyl compound and melt index is not exceeding 12g/10 minutes. The title film or sheet is constituted so that the same is oriented biaxially with a tensile orientation method and ORS of axial directions each becomes 3-20kg. The film or the sheet is manufactured by a method wherein an unoriented filmy or sheetlike matter made by extrusion molding or press molding or cast polymerization is heated to an orientable temperature and tensed and oriented by a simultaneous biaxial orientation method or a successive biaxial orientation method or an inflation method. With this construction, a matter superior in thermal stability of form can be obtained while holding transparency, weather resistance and rigidity.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、たとえば銘板やオーバーヘッドプロジェクタ
−(以下OHPと略記する)用フィルムとして好適な、
透明性、加熱形状安定性、機械的強度、耐候(光)性お
よび剛性に優れたフィルムまたはシートに関し、さらに
これらの製造法に関する。
[Detailed Description of the Invention] [Industrial Application Field] The present invention provides a film suitable for, for example, a nameplate or an overhead projector (hereinafter abbreviated as OHP).
The present invention relates to films or sheets with excellent transparency, heating shape stability, mechanical strength, weather (light) resistance, and rigidity, and further relates to methods for producing these.

〔従来の技術〕[Conventional technology]

透明性、耐候(光)性および剛性に優れた素材として、
メタクリル酸メチルを主成分とする汎用のメタクリル樹
脂があり、看板、照明用カバー自動車部品などに多用さ
れている。より高い加熱形状安定性が要求される分野に
は、メタクリル酸メチル、無水マレイン酸および芳香族
ビニル化合物からなる共重合体を用いることが提案され
ている(西独特許第1231013号、特開昭59−2
21314号など)。
As a material with excellent transparency, weather resistance (light) and rigidity,
There is a general-purpose methacrylic resin whose main component is methyl methacrylate, and it is widely used in things such as signboards, lighting covers, and automobile parts. It has been proposed to use a copolymer consisting of methyl methacrylate, maleic anhydride and an aromatic vinyl compound in fields where higher heating shape stability is required (West German Patent No. 1231013, JP-A-59 -2
21314 etc.).

これらの共重合体は汎用メタクリル樹脂の透明性、耐候
(光)性および剛性を保持しつつ、かつ熱変形温度が向
上しており、これらをフィルム化あるいはシート化した
場合、たとえば透明性と加熱形状安定性が要求される銘
板やOHP用フィルムとして好適な優れた特性のフィル
ムあるいはシートが期待される。
These copolymers retain the transparency, weathering (light) resistance, and rigidity of general-purpose methacrylic resins, while also having improved heat distortion temperatures. A film or sheet with excellent properties suitable for nameplates and OHP films that require shape stability is expected.

ところが、汎用のメタクリル樹脂において問題視されて
いる機械的強度が上記共重合体においてさらに低下し、
押出し成形等により成形したものは、フィルムはもとよ
り薄いシート状物も割れやすく実用に耐えないものであ
り、また厚いシートにおいても脆性の改良が望まれてい
るのが現状である。
However, the mechanical strength, which is considered a problem with general-purpose methacrylic resins, is further reduced in the above copolymers.
Products formed by extrusion molding or the like are easily broken, not only in films but also in thin sheets, making them unusable for practical use.Currently, it is desired to improve the brittleness of thick sheets as well.

上記共重合体の脆性の改良方法としてゴム成分をブレン
ドする方法(たとえば特開昭60−60150号、特開
昭60−60151号)とオリエンテーションリリース
ストL、ス(ASTM  01504、以下OR3と略
記する)が20 kg/cm”以上になるようプレス延
伸する方法が提供されている(特開昭59−15285
5号、特開昭58−171918号)。
As a method for improving the brittleness of the above copolymer, there is a method of blending a rubber component (for example, JP-A-60-60150, JP-A-60-60151) and an orientation release strike (ASTM 01504, hereinafter abbreviated as OR3). ) is 20 kg/cm" or more (Japanese Unexamined Patent Publication No. 59-15285).
No. 5, Japanese Unexamined Patent Publication No. 171918/1982).

しかしながら、前者の方法はブレンドにより透明性が低
下し、また後者の方法では連続生産が困難でバッチ方式
となるため生産性が低く、またフィルムなど厚みの薄い
ものは作りにくいという問題があり満足できる方法では
ない、さらに後者では、脆性は改良されているものの、
加熱による収縮性が強く、樹脂の改質により向上した加
熱形状安定性が損なわれるという問題があった。
However, the former method suffers from a decrease in transparency due to blending, and the latter method has low productivity because continuous production is difficult and requires a batch method, and it is difficult to produce thin products such as films, so it is not satisfactory. Although the brittleness is improved in the latter method,
There was a problem in that the shrinkage property due to heating was strong, and the heating shape stability improved by the modification of the resin was impaired.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

本発明の目的は前記共重合体のフィルムまたはシートの
問題点の解決にあり、すなわち加熱形状安定性、透明性
、耐候(光)性および剛性が良好で、かつ脆性の改良さ
れたフィルムまたはシートを開発し、提供するにある。
The object of the present invention is to solve the problems of the copolymer film or sheet, namely, to provide a film or sheet with good heating shape stability, transparency, weather (light) resistance, and rigidity, and with improved brittleness. to develop and provide.

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

上記目的は、単量体の組成がメタクリル酸メチル92〜
45重量%、無水マレイン酸3〜25重量%および芳香
族ビニル化合物5〜30重量%からなり、かつメルトフ
ローインデックス(ASTM0123B 、1条件、以
下MFIと略記する)が12g/10分以下である共重
合体樹脂のフィルムまたはシートであって、引張り延伸
法により2軸延伸され、かつ各軸方向のOR3が3〜2
0 kg/cm”であることを特徴とするフィルムまた
はシートおよびそれらの製造法によって達成される。
For the above purpose, the composition of the monomer is methyl methacrylate 92~
45% by weight, 3 to 25% by weight of maleic anhydride, and 5 to 30% by weight of an aromatic vinyl compound, and has a melt flow index (ASTM0123B, 1 condition, hereinafter abbreviated as MFI) of 12 g/10 minutes or less. A polymer resin film or sheet that is biaxially stretched by a tensile stretching method and has an OR3 of 3 to 2 in each axial direction.
0 kg/cm'' and a method for producing the same.

〔作 用〕[For production]

本発明は2軸延伸による脆性改良を応用したものであり
、延伸方法が引張り延伸法であることを必須とする。
The present invention applies brittleness improvement by biaxial stretching, and it is essential that the stretching method be a tensile stretching method.

一般に、延伸によって脆性が改良されることは知られて
おり、前記したように、本発明に使用の樹脂に関しても
プレス延伸する方法が提案されている。しかしながら、
プレス延伸法により作成した延伸物は加熱形状安定性が
劣り、延伸手法により本発明の目的を達成することは不
可能と考えられた。
It is generally known that stretching improves brittleness, and as mentioned above, a method of press stretching has been proposed for the resin used in the present invention. however,
The stretched product produced by the press stretching method had poor shape stability under heating, and it was considered impossible to achieve the object of the present invention by the stretching method.

ところが、本発明者等が本発明に使用の樹脂に関し引張
り延伸法を詳細に検討したところ、意外にも、特定の延
伸条件において脆性が改良されかつ加熱形状安定性も良
好な延伸物が得られることを見い出し本発明に至った。
However, when the present inventors investigated in detail the tensile stretching method for the resin used in the present invention, it was surprisingly possible to obtain a stretched product with improved brittleness and good heating shape stability under specific stretching conditions. This discovery led to the present invention.

第1図に、メタクリル酸メチル76重量%、無水マレイ
ン酸10重量%及びスチレン14重量%からなる共重合
物でMPU値が2g/10分の樹脂の引張り同時2軸延
伸フイルム(厚み110μ)の、ORS値と加熱収縮率
(115℃で30分加熱)および耐折回数(耐折疲労強
度、MrT型東洋情機(株)製試験機)との関係を示し
た。なお、OR3は延伸の程度を表す指標として使われ
ており、フィルムまたはシートの配向した分子が配向面
の状態に戻ろうとする際発生する応力と定義される。
Figure 1 shows a copolymer consisting of 76% by weight of methyl methacrylate, 10% by weight of maleic anhydride, and 14% by weight of styrene, and a simultaneously biaxially stretched film (thickness: 110 μm) with an MPU value of 2 g/10 min. , the relationship between the ORS value, heat shrinkage rate (heated at 115° C. for 30 minutes) and folding resistance (folding fatigue strength, MrT type testing machine manufactured by Toyo Joki Co., Ltd.) was shown. Note that OR3 is used as an index representing the degree of stretching, and is defined as the stress that occurs when the oriented molecules of the film or sheet try to return to the state of the oriented plane.

脆性改良の目安となる耐折回数は、OR3値が3 kg
7cm”から急激に上昇し、8 kB7cm”で既ニ2
0kg/cm”と大差ない値となっている。耐折回数が
3回以上になると比較的平荒く取扱っても破損すること
はない。一方、加熱収縮率もOR3値によって大きく変
化し、20 kg/c+w”以下、特に15kg/c1
1z以下では小さいことがわかる。
The number of breaks that can be used as a guideline for improving brittleness is when the OR3 value is 3 kg.
It rose rapidly from 7cm" and reached 22 at 8kB7cm".
0kg/cm", which is not much different. If the number of folds is 3 or more, it will not break even if handled relatively roughly. On the other hand, the heat shrinkage rate also changes greatly depending on the OR3 value, and 20 kg/cm". /c+w” or less, especially 15kg/c1
It can be seen that it is small below 1z.

第1図にも示されたように、本発明の目的を達成するた
めには、2軸延伸物の各軸方向のOR3値は3〜20 
kg/cm”、好ましくは5〜15 kg/cmtの範
囲にある必要がある。OR3値が3 kg/cm2未満
では脆性改良が不十分であり、ま、た2 0kg/cm
”をこえた場合、加熱形状安定性が劣ったものとなる。
As shown in FIG. 1, in order to achieve the object of the present invention, the OR3 value in each axial direction of the biaxially stretched product is 3 to 20.
kg/cm2, preferably in the range of 5 to 15 kg/cmt.If the OR3 value is less than 3 kg/cm2, brittleness improvement is insufficient;
If it exceeds ", the heating shape stability will be poor.

以上の結果は、脆性を改良するのに20kg/cm″以
上のOR3値が好適とされるプレス延伸の結果と状況が
異なっている。これは両者とも配向によって脆性が改良
されるが、プレス延伸においては分子が押されなからな
るべく分子間に空隙をつくらないように配向するのに対
し、引張り延伸ではむしろ分子間の空隙が広がるような
状況すなわちより自由度が高い状況で配向し配向構造が
別種のものになった、あるいはプレス延伸においてはピ
ストンフローが完全でなく、低伸度が表層において高く
内層はど低くなり、ピストンフローが容易な引張り延伸
とは高次構造が異なった結果と考えられる。
The above results are different from the results of press stretching, in which an OR3 value of 20 kg/cm'' or more is suitable for improving brittleness.This is because in both cases, brittleness is improved by orientation, but press stretching In contrast, in tension stretching, the molecules are oriented in a situation where the spaces between molecules are widened, that is, in a situation with a higher degree of freedom, and the oriented structure is created. This may be due to the fact that the piston flow is not perfect in press stretching, and the low elongation is high in the surface layer and low in the inner layer, resulting in a higher-order structure different from that in tensile stretching, where piston flow is easy. It will be done.

すなわち本発明のフィルムまたはシートは、引張り延伸
で配向されることとOR3値が3〜20kg7cm2で
規定される、プレス延伸物とは異なる新規な高次構造を
持ったものである。
That is, the film or sheet of the present invention has a novel higher-order structure different from that of a press-stretched product, which is oriented by tension stretching and has an OR3 value of 3 to 20 kg 7 cm 2 .

また、本発明のフィルムまたはシートは、組成変更や添
加物による脆性改良の場合と異なり、本発明に使用の樹
脂の優れた透明性や耐候(光)性を保持している。剛性
は延伸により若干向上する。
Further, the film or sheet of the present invention maintains the excellent transparency and weather (light) resistance of the resin used in the present invention, unlike cases where brittleness is improved by changing the composition or adding additives. Stiffness is slightly improved by stretching.

本発明に使用される樹脂はメタクリル酸メチル92〜4
5重量%、無水マレイン酸3〜25重四%および芳香族
ビニル化合物5〜30重量%からなる共重合体であり、
より好ましくはメタクリル酸メチル86〜50重量%、
無水マレイン酸7〜25重量%および芳香族ビニル化合
物7〜25重量%からなる共重合体である。メタクリル
酸メチルが45%未満では耐候(光)性が低下し、また
透明性も損なわれやすく、92%をこえると熱変形温度
が低下し加熱形状安定性が劣ったものとなる。無水マレ
イン酸量が3%未満では熱変形温度の向上が不十分で、
また25%をこえると着色が著しくなる。芳香族ビニル
化合物は、主として無水マレイン酸の共重合性を高める
ための成分であり、5%未満では共重合性向上の効果が
少ない。
The resin used in the present invention is methyl methacrylate 92-4
A copolymer consisting of 5% by weight, 3 to 25% maleic anhydride, and 5 to 30% by weight of an aromatic vinyl compound,
More preferably 86 to 50% by weight of methyl methacrylate,
It is a copolymer consisting of 7 to 25% by weight of maleic anhydride and 7 to 25% by weight of an aromatic vinyl compound. If the content of methyl methacrylate is less than 45%, weather resistance (light) resistance is reduced and transparency is likely to be impaired, and if it exceeds 92%, the heat distortion temperature is reduced and the heating shape stability is poor. If the amount of maleic anhydride is less than 3%, the improvement in heat distortion temperature is insufficient;
Moreover, when it exceeds 25%, coloring becomes noticeable. The aromatic vinyl compound is a component mainly for improving copolymerizability of maleic anhydride, and if it is less than 5%, the effect of improving copolymerizability is small.

また30%をこえると透明性が損なわれやすい。Moreover, when it exceeds 30%, transparency tends to be impaired.

芳香族ビニル化合物としてはスチレン、アルキルスチレ
ン、α−メチルスチレン、α−メチルアルキルスチレン
などが使用できるが、共重合体の物性および単量体の生
産性からスチレン、ビニルトルエンおよびα−メチルス
チレンが好ましい。
As the aromatic vinyl compound, styrene, alkylstyrene, α-methylstyrene, α-methylalkylstyrene, etc. can be used, but styrene, vinyltoluene, and α-methylstyrene are preferred due to the physical properties of the copolymer and the productivity of the monomer. preferable.

前記の共重合体の構成単量体のほかに、たとえばアクリ
ル酸、メタクリル酸、アクリルアミド、メタクリルアミ
ド、アクリロニトリル、メタクリロニトリル、マレイミ
ド、N−置換マレイミド、メタクリル酸メチル以外のメ
タクリル酸エステルなどの他に共重合性単量体の少量を
、本発明の効果を1員なわない範囲で共重合成分として
添加することもできる。さらに可塑剤、着色剤、紫外線
吸収剤、酸化防止剤及び滑剤などのポリマー改質剤を添
加することができる。特に耐候(光)性が要求される場
合、紫外線吸収剤の添加が有効であり、ベンゾトリアゾ
ール系、ベンゾフェノン系の紫外線吸収剤をo、 o 
o s〜3重量%用いるのがよい。
In addition to the constituent monomers of the copolymer, for example, acrylic acid, methacrylic acid, acrylamide, methacrylamide, acrylonitrile, methacrylonitrile, maleimide, N-substituted maleimide, methacrylic acid esters other than methyl methacrylate, etc. A small amount of a copolymerizable monomer can also be added as a copolymerization component to the extent that the effect of the present invention is not achieved. Additionally, polymer modifiers such as plasticizers, colorants, UV absorbers, antioxidants and lubricants can be added. In particular, when weather (light) resistance is required, it is effective to add a UV absorber, and benzotriazole-based and benzophenone-based UV absorbers are
It is preferable to use os to 3% by weight.

透明性や耐候(光)性を悪化させない範囲で他の樹脂、
たとえばポリフッ化ビニリデンなどがブレンドされてい
てもよい。
Other resins may be used as long as they do not deteriorate transparency or weather resistance (light).
For example, polyvinylidene fluoride or the like may be blended.

共重合体の分子量はあまり低すぎると延伸による脆性の
改良が実現できず、MFI値で12g/10分以下が好
ましい。また、押出成形により延伸の材料となる未延伸
フィルムあるいはシートを作製する場合、押出成形に適
したMFI値が0.2g710分のものが使用される。
If the molecular weight of the copolymer is too low, it will not be possible to improve brittleness by stretching, so the MFI value is preferably 12 g/10 minutes or less. In addition, when producing an unstretched film or sheet as a material for stretching by extrusion molding, a film having an MFI value of 0.2 g 710 min, which is suitable for extrusion molding, is used.

本発明のフィルムまたはシートは、押出成形、プレス成
形およびキャスト重合などで作られた実質的に未延伸の
フィルムあるいはシート状物を、延伸の可能な温度に加
温し、同時2軸延伸法、逐次2軸延伸法あるいはインフ
レーション法等によって引張り延伸し製造される。延伸
に適当な温度は樹脂のガラス転移温度(以下Tgと略記
する)より5〜40℃、好ましくは10〜30℃高い温
度である。Tgより5℃をこえない温度で延伸した場合
、延伸中に破断する。また、Tgより40℃をこえて高
くなると、樹脂の分子運動が激しくなるため延伸による
配向構造の形成が困難となり、OR3値が3 kg/c
m2未満の脆性の改良が不十分なものとなりやすい。
The film or sheet of the present invention can be produced by heating a substantially unstretched film or sheet material made by extrusion molding, press molding, cast polymerization, etc. to a temperature that allows stretching, and applying a simultaneous biaxial stretching method. It is manufactured by sequentially pulling and stretching by a biaxial stretching method, an inflation method, or the like. The temperature suitable for stretching is 5 to 40°C, preferably 10 to 30°C higher than the glass transition temperature (hereinafter abbreviated as Tg) of the resin. If the film is stretched at a temperature less than 5° C. below Tg, it will break during stretching. Furthermore, when the temperature exceeds Tg by 40°C, the molecular motion of the resin becomes intense, making it difficult to form an oriented structure by stretching, and the OR3 value becomes 3 kg/c.
Improvement in brittleness below m2 tends to be insufficient.

延伸倍率は、各軸方向とも1.2〜4倍、好ましくは1
.3〜3倍が選択される。1.2倍以下ではOR3値が
3 kg/cm2未満となり脆性の改良が少ない。また
、4倍を越えると延伸ムラが顕著となり、延伸中の破断
も顧発し好ましくない。
The stretching ratio is 1.2 to 4 times in each axial direction, preferably 1
.. 3-3 times is selected. If it is 1.2 times or less, the OR3 value will be less than 3 kg/cm2, resulting in little improvement in brittleness. Moreover, if it exceeds 4 times, stretching unevenness will become noticeable and breakage during stretching may occur, which is not preferable.

延伸速度は、延伸温度および延伸方法によって異なるが
、たとえバッチ式のパンタグラフ式延伸機で延伸する場
合、延伸前のフィルムあるいはシートの長さに対し、通
常、各軸方向50〜5000%/分が選定され、また逐
次2軸延伸法により連続延伸する場合、縦延伸の速度は
2000−10000%に及ぶ。延伸速度が速すぎた場
合、延伸に必要な応力が大きくなり、また延伸中破断し
やすくなる。
The stretching speed varies depending on the stretching temperature and stretching method, but when stretching is performed using a batch-type pantograph stretching machine, the stretching speed is usually 50 to 5000%/min in each axial direction relative to the length of the film or sheet before stretching. When selected and continuously stretched by the sequential biaxial stretching method, the longitudinal stretching speed ranges from 2000% to 10000%. If the stretching speed is too high, the stress required for stretching becomes large and the film is likely to break during stretching.

また、いかなる方法においても、分子運動により延伸に
よる配向構造が乱され、脆性改良に必要な配向構造が形
成されないような遅い速度は避けねばならない。この温
度は延伸温度によって左右されるが、たとえばTgより
20℃高い延伸温度においては10%/分以上にすべき
である。
In addition, in any method, it is necessary to avoid such a slow speed that the oriented structure due to stretching is disturbed by molecular motion and the oriented structure necessary for improving brittleness is not formed. This temperature depends on the stretching temperature, but should be at least 10%/min at a stretching temperature 20° C. higher than Tg, for example.

結晶性の樹脂、たとえばポリエチレンテレフタレートの
延伸フィルムにおいては、結晶化度をあげるため、延伸
後延伸温度より高い温度で後熱処理される場合が多いが
、非品性樹脂においては、延伸後加熱状態におくと配向
緩和により延伸効果が低減されるので、一般に、Tgよ
り低い温度に速やかに冷却する方法が選ばれる。本発明
に使用の樹脂は非品性で、後者の方法が選ばれる。
Stretched films of crystalline resins, such as polyethylene terephthalate, are often post-heat treated at a temperature higher than the stretching temperature after stretching to increase the degree of crystallinity, but non-grade resins are heated after stretching. If the film is allowed to stand for a long time, the stretching effect will be reduced due to orientation relaxation, so generally a method is selected in which the film is rapidly cooled to a temperature lower than Tg. Since the resin used in the present invention is of inferior quality, the latter method is chosen.

延伸温度における配向緩和挙動を第2図によって説明す
る。ここで、樹脂は第1図の場合と同じものを用い、延
伸温度=145℃、延伸倍率:各軸方向に2倍、延伸速
度1000%/分の条件で引張り同時2軸延伸したのち
、そのまま緊張上延伸温度に保ち、OR3値の変化を追
跡した。図より、配向の指標であるOR3値は、延伸後
短時間の間に急激に減少することがわかる。
The orientation relaxation behavior at the stretching temperature will be explained with reference to FIG. Here, the same resin as in Fig. 1 was used, and the stretching temperature was 145°C, the stretching ratio was 2 times in each axial direction, and the stretching speed was 1000%/min. The tension and stretching temperature was maintained, and changes in the OR3 value were tracked. The figure shows that the OR3 value, which is an index of orientation, decreases rapidly within a short period of time after stretching.

以上より、脆性の改良された本発明のフィルムまたはシ
ートを得るためには、延伸後、延伸温度に留める時間は
多くとも5分以内が望ましい。
From the above, in order to obtain the film or sheet of the present invention with improved brittleness, it is desirable that the time to remain at the stretching temperature after stretching is at most 5 minutes.

本発明のフィルムまたはシートの厚みは、本質的に制限
されるものでないが、生産性から3μ〜10龍が望まし
く、特に50μ〜1nのものがよい。50μ未満では延
伸中破断しやすく、この場合他の樹脂のフィルムを補強
フィルムとして弱く、ラミネートし一緒に延伸したのち
剥す方法を用いるのがよい。また、1酊をこえるシート
の製造においては、材料となる未延伸シートの厚みが厚
くなり、オーブン中にセットしても未延伸シートの内部
まで延伸温度に到達するのに長時間を要し、生産性が低
下する。たとえば5鶴の未延伸シートを延伸する場合、
15分以上加熱するのが望ましい。なお、本発明におい
ては、200μ以下の厚みのものをフィルム、200μ
をこえるものをシートと区別した。
The thickness of the film or sheet of the present invention is not essentially limited, but from the viewpoint of productivity, a thickness of 3 μm to 10 μm is desirable, and a thickness of 50 μm to 1 nm is particularly preferable. If it is less than 50 μm, it is likely to break during stretching, and in this case, it is preferable to use a method of laminating the reinforcing film with another resin film, stretching it together, and then peeling it off. In addition, in the production of sheets that exceed 1 degree, the thickness of the unstretched sheet becomes thicker, and even if it is placed in an oven, it takes a long time for the inside of the unstretched sheet to reach the stretching temperature. Productivity decreases. For example, when stretching an unstretched sheet of 5 Tsuru,
It is desirable to heat for 15 minutes or more. In addition, in the present invention, a film with a thickness of 200μ or less, a film with a thickness of 200μ or less
Those exceeding 100% were distinguished from sheets.

以下に、発明の説明において用いた加熱収縮率及び耐折
回数の測定方法を示す。
The methods for measuring the heat shrinkage rate and the number of folds used in the description of the invention are shown below.

・加熱収縮率:被測定物に150mmの長さの直線を記
入し、所定温度に保たれた強制温風式恒温オーブン内で
30分間加熱後、記入した直線の長さ(7!m)をスケ
ールで読みとり、下記計算式により加熱収縮率を求めた
・Heating shrinkage rate: Draw a straight line with a length of 150 mm on the object to be measured, and after heating it for 30 minutes in a forced hot air constant temperature oven kept at a specified temperature, measure the length of the drawn straight line (7! m). It was read on a scale and the heat shrinkage rate was determined using the following calculation formula.

耐折回数二被測定物を15mmrlの短■として、MI
T型耐折疲労試験機(東洋精機(株)製、折り曲げ速度
30回/分)により破断するまでの折り曲げ回数を求め
た。
The number of folding times 2 The object to be measured is a short 15 mm rl, and the MI
The number of times of bending until breakage was determined using a T-type bending fatigue tester (manufactured by Toyo Seiki Co., Ltd., bending speed: 30 times/min).

また、TgはサーマルアナライザーDT−40型(島津
製作所(株)製)を用いて測定した。
Further, Tg was measured using a thermal analyzer DT-40 model (manufactured by Shimadzu Corporation).

〔実施例〕〔Example〕

以下、実施例を挙げて本発明をさらに具体的に説明する
Hereinafter, the present invention will be explained in more detail with reference to Examples.

実施例1〜3 メタクリル酸メチル76重慴%、無水マレイン酸10重
量%及びステレノ14重遣%からなる共重合体(MFI
値1g/10分、Tg120°C)をシリンダー径20
龍の押出機で押出し、厚さ4801t−1000μの未
延伸シートを作製した。
Examples 1 to 3 A copolymer (MFI) consisting of 76% by weight of methyl methacrylate, 10% by weight of maleic anhydride and 14% by weight of stereno
value 1g/10min, Tg 120°C) with cylinder diameter 20
An unstretched sheet having a thickness of 4801t-1000μ was produced by extrusion using a Ryu extruder.

パンタグラフ式2軸延伸試験機(東洋精機(掬製)を用
い、第1表に示した延伸温度及び延伸倍率で引張り同時
2軸延伸を行ない、OR3値が5〜15JH/cm”の
範囲の延伸物を得た。
Using a pantograph type biaxial stretching tester (manufactured by Toyo Seiki Co., Ltd.), simultaneous biaxial stretching was carried out at the stretching temperature and stretching ratio shown in Table 1, and stretching was performed with an OR3 value in the range of 5 to 15 JH/cm. I got something.

これらの加熱形状安定性は良好で、110℃、30分の
加熱で1%未満の収縮率、115℃、30分の加熱で3
%未満の収縮率であった。
The heating shape stability of these products is good, with a shrinkage rate of less than 1% when heated at 110°C for 30 minutes, and a shrinkage rate of 3% when heated at 115°C for 30 minutes.
The shrinkage rate was less than %.

また、脆性改良の指標となる耐折性も、未延伸フィルム
が最初の折り曲げによって破…するのに比べ大きく改良
された。測定値を第1表に示す。
In addition, the folding durability, which is an indicator of brittleness improvement, was significantly improved compared to the unstretched film, which breaks at the first bend. The measured values are shown in Table 1.

なお延伸速度は各軸方向1000%/分であり、延伸終
了後20秒以内に延伸物を冷風で′Fg以下の温度まで
冷却した。
The stretching speed was 1000%/min in each axial direction, and the stretched product was cooled to a temperature below 'Fg with cold air within 20 seconds after the stretching was completed.

比較例1 実施例1に記載の共重合体から実施例1と同様の方法に
より、厚さ110μの未延伸フィルムを作製した。該フ
ィルムは非常に跪く、折り曲げにより容易に破損した。
Comparative Example 1 An unstretched film having a thickness of 110 μm was produced from the copolymer described in Example 1 in the same manner as in Example 1. The film was very bulky and broke easily by folding.

比較例2〜3 実施例1の方法において、延伸温度および延伸倍率を第
1表に記載の条件にかえて延伸物を得た。
Comparative Examples 2 to 3 In the method of Example 1, stretched products were obtained by changing the stretching temperature and stretching ratio to the conditions listed in Table 1.

OR3値が20 kg/cm”をこえた比較例2では加
熱形状女性が劣り、また165℃の温度で延伸した比較
例3ではOR3値が3 kg/cm”未満であり、耐折
性の改善がなく折り曲げにより容易に破…した。
In Comparative Example 2, in which the OR3 value exceeded 20 kg/cm'', the heated shape was inferior, and in Comparative Example 3, which was stretched at a temperature of 165°C, the OR3 value was less than 3 kg/cm'', indicating improvement in folding durability. It was easily broken by bending.

実施例4 実施例1の方法により作製した未延伸シートをパンタグ
ラフ式延伸機により、第1表に示した延伸条件で未延伸
シートの押出し方向を最初に延伸し、1分後、押出し方
向と直角の方向を延伸して逐次延伸物を得た。第1表に
示すように延伸物は耐折性および加熱形状安定性に優れ
ていた。なお延伸速度および延伸後の冷却は実施例1の
方法と同様に行なった。
Example 4 The unstretched sheet produced by the method of Example 1 was first stretched in the extrusion direction of the unstretched sheet using a pantograph stretching machine under the stretching conditions shown in Table 1, and after 1 minute, the unstretched sheet was stretched perpendicular to the extrusion direction. A sequentially stretched product was obtained by stretching in the direction of . As shown in Table 1, the stretched product had excellent folding durability and heating shape stability. Note that the stretching speed and cooling after stretching were performed in the same manner as in Example 1.

実施例5〜6 実施例1と同様の方法により、第2表に記載の樹脂から
厚さ300μの未延伸シートを作製し、第2表に記載の
条件で、実施例1と同様の方法により各軸方向2倍の倍
率で同時2軸延伸を行なった。第2表に示すように延伸
物は耐折性および加熱形状安定性に優れていた。
Examples 5 to 6 An unstretched sheet with a thickness of 300 μm was prepared from the resin listed in Table 2 by the same method as in Example 1, and was processed in the same manner as in Example 1 under the conditions listed in Table 2. Simultaneous biaxial stretching was performed at a magnification of 2 times in each axial direction. As shown in Table 2, the stretched product had excellent folding durability and heating shape stability.

〔発明の効果〕〔Effect of the invention〕

耐熱性のメタクリル酸メチル系共重合体樹脂に関し、好
適な延伸方法を開発した結果、透明性、耐候(光)性及
び剛性を保持しつつ、脆性が大巾に改良されかつ加熱形
状安定性に優れた新規なフィルムまたはシートが得られ
た。
As a result of developing a suitable stretching method for heat-resistant methyl methacrylate-based copolymer resin, the brittleness has been greatly improved and the heating shape stability has been improved while maintaining transparency, weather resistance (light) resistance, and rigidity. An excellent new film or sheet was obtained.

該フィルムまたはシートは、従来のメタクリル酸脂のフ
ィルムまたはシートの用途分野における、機械的強度お
よび加熱形状安定性向上に対する強い要望に対応でき、
またこれらの特性が不足したため採用されなかった用途
分野にも通用できるものである。
The film or sheet can meet the strong demand for improved mechanical strength and heating shape stability in the field of application of conventional methacrylic acid resin films or sheets,
It can also be used in fields of application that have not been adopted due to lack of these characteristics.

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

第1図は、引張り2軸延伸したフィルムのORSと加熱
収縮率の関係(a)、およびOR3と耐折回数の関係(
b)を示すグラフであり、第2図は延伸温度における配
向緩和性を示すグラフである。
Figure 1 shows the relationship between ORS and heat shrinkage (a) of a tensile biaxially stretched film, and the relationship between OR3 and the number of folds (a).
FIG. 2 is a graph showing orientation relaxation at stretching temperature.

Claims (10)

【特許請求の範囲】[Claims] (1)単量体の組成がメタクリル酸メチル92〜45重
量%、無水マレイン酸3〜25重量%および芳香族ビニ
ル化合物5〜30重量%からなり、かつメルトフローイ
ンデックスが12g/10分以下である共重合体樹脂か
ら得られ、引張り延伸法により2軸延伸され、かつ各軸
方向のオリエンテーションリリースストレスが3〜20
kg/cm^2であることを特徴とする加熱形状安定性
に優れたフィルムまたはシート。
(1) The monomer composition is 92 to 45% by weight of methyl methacrylate, 3 to 25% by weight of maleic anhydride, and 5 to 30% by weight of an aromatic vinyl compound, and the melt flow index is 12 g/10 minutes or less. It is obtained from a certain copolymer resin, biaxially stretched by a tensile stretching method, and has an orientation release stress of 3 to 20 in each axial direction.
A film or sheet having excellent heating shape stability, characterized by having a heating shape stability of kg/cm^2.
(2)オリエンテーションリリースストレスが5〜15
kg/cm^2である特許請求の範囲第1項に記載のフ
ィルムまたはシート。
(2) Orientation release stress is 5-15
The film or sheet according to claim 1, which has a weight of kg/cm^2.
(3)単量体の組成がメタクリル酸メチル50〜86重
量%、無水マレイン酸7〜25重量%、および芳香族ビ
ニル化合物7〜25重量%からなる共重合体樹脂である
特許請求の範囲第1〜2項記載のフィルムまたはシート
(3) A copolymer resin whose monomer composition is 50 to 86% by weight of methyl methacrylate, 7 to 25% by weight of maleic anhydride, and 7 to 25% by weight of an aromatic vinyl compound. The film or sheet according to items 1 and 2.
(4)芳香族ビニル化合物がスチレン、ビニルトルエン
およびα−メチルスチレンよりなる群より選ばれた少な
くとも1種である特許請求の範囲第1〜3項記載のフィ
ルムまたはシート。
(4) The film or sheet according to any one of claims 1 to 3, wherein the aromatic vinyl compound is at least one selected from the group consisting of styrene, vinyltoluene, and α-methylstyrene.
(5)単量体の組成がメタクリル酸メチル92〜45重
量%、無水マレイン酸3〜25重量%および芳香族ビニ
ル化合物5〜30重量%からなり、かつメルトフローイ
ンデックスが12g/10分以下である共重合体樹脂の
フィルムまたはシートの製造法において、ガラス転移温
度より5〜40℃高い延伸温度でかつ各軸方向1.2〜
4倍の延伸倍率で各軸方向のオリエンテーションリリー
スストレスが3〜20kg/cm^2になるように、引
張り延伸法により2軸延伸することを特徴とする加熱形
状安定性に優れたフィルムまたはシートの製造法。
(5) The monomer composition is 92 to 45% by weight of methyl methacrylate, 3 to 25% by weight of maleic anhydride, and 5 to 30% by weight of an aromatic vinyl compound, and the melt flow index is 12 g/10 minutes or less. In a method for producing a film or sheet of a certain copolymer resin, the stretching temperature is 5 to 40°C higher than the glass transition temperature and the stretching temperature is 1.2 to 1.2°C in each axial direction.
A film or sheet with excellent heating shape stability characterized by being biaxially stretched by a tensile stretching method so that the orientation release stress in each axial direction is 3 to 20 kg/cm^2 at a stretching ratio of 4 times. Manufacturing method.
(6)オリエンテーションリリースストレスが5〜15
kg/cm^2である特許請求の範囲第5項記載のフィ
ルムまたはシートの製造法。
(6) Orientation release stress is 5-15
6. The method for producing a film or sheet according to claim 5, wherein the film or sheet has a weight of 1 kg/cm^2.
(7)単量体の組成がメタクリル酸メチル86〜50重
量%、無水マレイン酸7〜25重量%および芳香族ビニ
ル化合物7〜25重量%からなる共重合体樹脂である特
許請求の範囲第5〜6項記載のフィルムまたはシートの
製造法。
(7) A copolymer resin having a monomer composition of 86 to 50% by weight of methyl methacrylate, 7 to 25% by weight of maleic anhydride, and 7 to 25% by weight of an aromatic vinyl compound. A method for producing a film or sheet according to item 6.
(8)芳香族ビニル化合物がスチレン、ビニルトルエン
およびα−メチルスチレンよりなる群より選ばれた少な
くとも1種である特許請求の範囲第5〜7項記載のフィ
ルムまたはシートの製造法。
(8) The method for producing a film or sheet according to claims 5 to 7, wherein the aromatic vinyl compound is at least one selected from the group consisting of styrene, vinyltoluene, and α-methylstyrene.
(9)延伸温度がガラス転移温度より10〜30℃高い
温度である特許請求の範囲第5〜8項記載のフィルムま
たはシートの製造法。
(9) The method for producing a film or sheet according to claims 5 to 8, wherein the stretching temperature is 10 to 30°C higher than the glass transition temperature.
(10)延伸倍率が1.3〜3倍である特許請求の範囲
第5〜9項記載のフィルムまたはシートの製造法。
(10) The method for producing a film or sheet according to claims 5 to 9, wherein the stretching ratio is 1.3 to 3 times.
JP19480888A 1988-08-04 1988-08-04 Film or sheet excellent in thermal stability of form and manufacture thereof Pending JPH0243023A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP19480888A JPH0243023A (en) 1988-08-04 1988-08-04 Film or sheet excellent in thermal stability of form and manufacture thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP19480888A JPH0243023A (en) 1988-08-04 1988-08-04 Film or sheet excellent in thermal stability of form and manufacture thereof

Publications (1)

Publication Number Publication Date
JPH0243023A true JPH0243023A (en) 1990-02-13

Family

ID=16330602

Family Applications (1)

Application Number Title Priority Date Filing Date
JP19480888A Pending JPH0243023A (en) 1988-08-04 1988-08-04 Film or sheet excellent in thermal stability of form and manufacture thereof

Country Status (1)

Country Link
JP (1) JPH0243023A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0639894A (en) * 1992-07-23 1994-02-15 Tsutsunaka Plast Ind Co Ltd Preparation of artificial marble by extrusion molding
JP2010539279A (en) * 2007-09-17 2010-12-16 エルジー・ケム・リミテッド Optical film and manufacturing method thereof
WO2018147234A1 (en) * 2017-02-07 2018-08-16 株式会社クラレ Acrylic resin biaxially oriented film and method for producing same

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0639894A (en) * 1992-07-23 1994-02-15 Tsutsunaka Plast Ind Co Ltd Preparation of artificial marble by extrusion molding
JP2010539279A (en) * 2007-09-17 2010-12-16 エルジー・ケム・リミテッド Optical film and manufacturing method thereof
US8758655B2 (en) 2007-09-17 2014-06-24 Lg Chem, Ltd. Optical film and method of manufacturing the same
US9187633B2 (en) 2007-09-17 2015-11-17 Lg Chem, Ltd. Optical film and method of manufacturing the same
WO2018147234A1 (en) * 2017-02-07 2018-08-16 株式会社クラレ Acrylic resin biaxially oriented film and method for producing same
JPWO2018147234A1 (en) * 2017-02-07 2019-11-21 株式会社クラレ Acrylic resin biaxially stretched film and method for producing the same

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