JPS5921324B2 - Methacrylic San Methyl Cage - Google Patents

Methacrylic San Methyl Cage

Info

Publication number
JPS5921324B2
JPS5921324B2 JP13594775A JP13594775A JPS5921324B2 JP S5921324 B2 JPS5921324 B2 JP S5921324B2 JP 13594775 A JP13594775 A JP 13594775A JP 13594775 A JP13594775 A JP 13594775A JP S5921324 B2 JPS5921324 B2 JP S5921324B2
Authority
JP
Japan
Prior art keywords
temperature
polymer
methyl methacrylate
cooling
polymerization
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
Application number
JP13594775A
Other languages
Japanese (ja)
Other versions
JPS5259694A (en
Inventor
治郎 栗田
京一郎 森
住男 相原
允 本多
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.)
Asahi Chemical Industry Co Ltd
Original Assignee
Asahi 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 Asahi Chemical Industry Co Ltd filed Critical Asahi Chemical Industry Co Ltd
Priority to JP13594775A priority Critical patent/JPS5921324B2/en
Publication of JPS5259694A publication Critical patent/JPS5259694A/en
Publication of JPS5921324B2 publication Critical patent/JPS5921324B2/en
Expired legal-status Critical Current

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  • Casting Or Compression Moulding Of Plastics Or The Like (AREA)
  • Polymerisation Methods In General (AREA)

Description

【発明の詳細な説明】 本発明は、メタクリル酸メチル又はメタクリル酸メチル
を主成分とする不飽和単量体を金属板間に保持して重合
し、内部ひずみの小さい板状重合体を製造する重合の改
良方法に関するものである。
Detailed Description of the Invention The present invention involves polymerizing methyl methacrylate or an unsaturated monomer mainly composed of methyl methacrylate while holding it between metal plates to produce a plate-shaped polymer with small internal strain. This invention relates to a method for improving polymerization.

従来、メタクリル酸メチル又はメタクリル酸メチルを主
成分とする不飽和単量体混合物(以下単にモノマーと称
する)の板状重合体の製造方法として、ガスケットでシ
ールされたガラスセルの間に、モノマー又は一部重合体
を含有した粘ちような混合物(以下シラツプと称する)
を注入して水浴中又は空気浴中で重合する、いわゆるセ
ルキャスト法が知られている。さらに連続的に板状重合
体を製造する方法として、2枚の金属製エンドレスベル
トの間で重合する、いわゆる対向ベルト式連続重合方法
が知られている(米国特許第2500728号明細書)
Conventionally, as a method for producing a plate-shaped polymer of methyl methacrylate or an unsaturated monomer mixture containing methyl methacrylate as the main component (hereinafter simply referred to as monomer), the monomer or A sticky mixture containing some polymers (hereinafter referred to as syrup)
The so-called cell casting method is known, in which the polymer is injected and polymerized in a water bath or an air bath. Furthermore, as a method for continuously producing a plate-like polymer, a so-called opposed belt continuous polymerization method is known in which polymerization is carried out between two endless metal belts (US Pat. No. 2,500,728).
.

これらの重合方法は、先ず、モノマーの沸点(約100
゜c)以下の温度で重合したのち、残存する約10%程
度のモノマーを重合させるために、さらに100℃以上
の温度に加熱して、いわゆるキュアリングを行い、次い
で重合体にひずみが残らない程度にゆつくりと冷却した
後に取出されるのが普通である。この際、急冷による内
部ひずみのため重合体の熱変形温度が低下するのを防ぐ
ために、一定速度以下で冷却する方法が提案されている
(特開昭49−99187号公報)。
In these polymerization methods, first, the boiling point of the monomer (approximately 100
c) After polymerization at a temperature below, in order to polymerize about 10% of the remaining monomer, it is further heated to a temperature of 100°C or higher to perform so-called curing, so that no strain remains in the polymer. It is usually taken out after cooling down to a certain degree. At this time, in order to prevent the thermal deformation temperature of the polymer from decreasing due to internal strain caused by rapid cooling, a method has been proposed in which the polymer is cooled at a constant rate or less (Japanese Patent Laid-Open No. 49-99187).

メタクリル酸メチルには重合がある程度進行すると、急
激に重合速度が増大する、いわゆる自動促進効果がみら
れるが、このとき急激な発熱があり、その除熱が、すぐ
れた外観の板状重合体を得るために必要である。
Methyl methacrylate exhibits a so-called auto-acceleration effect, in which the polymerization rate increases rapidly once the polymerization has progressed to a certain extent.At this time, there is a sudden generation of heat, and the removal of this heat produces a plate-like polymer with an excellent appearance. necessary to obtain.

もし、除熱が不充分であると内部温度が上昇して内部で
発泡など好ましくない現象が起り、得られた重合体の外
観を著しく損なうことになる。ガラスによるセルキャス
ト法の場合には、ガラスの熱伝導率が低く、かつ厚さが
大きいために伝熱が悪く、急激な発熱を除去することが
困難なため、比較的低温を用い長時間かけて重合させる
のが普通である。
If the heat removal is insufficient, the internal temperature will rise and undesirable phenomena such as foaming will occur inside, which will significantly impair the appearance of the obtained polymer. In the case of the cell casting method using glass, the thermal conductivity of glass is low and the thickness is large, so heat transfer is poor and it is difficult to remove rapid heat generation. It is common to polymerize by

この場合には冷却速度も遅いために冷却時の内部ひずみ
の発生はあまり問題にならない。これに対して熱伝導率
の大きい金属セル又は金属ベルトを使用した場合には除
熱速度が大きいため、比較的高温でかつ短時間で重合を
完結させることができる。
In this case, since the cooling rate is slow, the occurrence of internal strain during cooling is not a problem. On the other hand, when a metal cell or metal belt with high thermal conductivity is used, the heat removal rate is high, so that polymerization can be completed at a relatively high temperature and in a short time.

また、この場合には冷却速度も著しく大きくすることが
できるため冷却に要する時間を大幅に短縮することが可
能である。しかし、冷却速度を大きくした場合には重合
体内部にひずみが残存するため、熱変形温度が低下し、
溶剤接着時に亀裂やひび割れが発生しやすく、さらに熱
加工時に製品の外観を損なうなどの弊害を伴なう。
Furthermore, in this case, the cooling rate can be significantly increased, so the time required for cooling can be significantly shortened. However, when the cooling rate is increased, strain remains inside the polymer, which lowers the heat distortion temperature.
Cracks and crazing are likely to occur during solvent bonding, and furthermore, the appearance of the product may be damaged during heat processing.

これに対して、冷却速度を一定速度以下に規制する前記
特開昭49−99187号公報の方法があるが、これで
は熱伝導率の大きいセル又はベルトを使用する利点を充
分に生かすことができず、また冷却速度を常に管理しな
ければならないため、設備、操作が複雑になるという欠
点がある。
On the other hand, there is a method disclosed in Japanese Patent Application Laid-Open No. 49-99187, which regulates the cooling rate below a certain rate, but this method cannot fully utilize the advantage of using cells or belts with high thermal conductivity. Moreover, since the cooling rate must be constantly controlled, there is a drawback that the equipment and operation become complicated.

本発明者らは、熱伝導率の良い材質の特徴を生かして冷
却速度を大きくすることにより冷却所要時間を短縮し、
かつ内部にひずみの残らない方法について鋭意研究を重
ねた結果、本発明に到達した。本発明の目的はキユアリ
ング後の冷却速度を大きくし、かつ品質のすぐれた板状
の重合体を製造する方法を提供することである。
The present inventors have shortened the required cooling time by increasing the cooling rate by taking advantage of the characteristics of the material with good thermal conductivity.
As a result of intensive research into a method that does not leave any strain inside, the present invention was achieved. An object of the present invention is to provide a method for increasing the cooling rate after curing and producing a plate-like polymer of excellent quality.

本発明は、メタクリル酸メチル又はメタクリル酸メチル
を主成分とする不飽和単量体混合物を金属板間に保持し
た状態で重合し板状の重合体を製造するに当り、重合反
応の後段において120〜160℃に昇温したのち、金
属板間に保持したまま毎分25℃以上の速度で110〜
90℃まで急冷すること、及びその温度範囲内でのある
選ばれた温度に少なくとも1分間かつ可及的短時間保持
することを特徴とするメタクリル酸メチル又はメタクリ
ル酸メチルを主成分とする不飽和単量体混合物の重合体
の製造方法である。
In the present invention, when producing a plate-like polymer by polymerizing methyl methacrylate or an unsaturated monomer mixture containing methyl methacrylate as a main component while holding it between metal plates, 120 After raising the temperature to ~160°C, it is heated to 110°C at a rate of 25°C or more per minute while being held between metal plates.
Methyl methacrylate or an unsaturated product based on methyl methacrylate, characterized by rapid cooling to 90°C and holding at a selected temperature within that temperature range for at least 1 minute and as short a time as possible. This is a method for producing a polymer of a monomer mixture.

一般に内部ひずみを除去するために、一定温度で一定時
間熱処理(アニーリング)することは広く知られている
Generally, it is widely known that heat treatment (annealing) is performed at a constant temperature for a certain period of time in order to remove internal strain.

しかし一般にアニーリングは熱変形温度より10〜15
℃低い温度で、かつ数時間以上行われるのが普通であり
、本発明のように熱変形温度付近又はそれ以上の温度で
、しかも短時間行われる例はない。本発明の方法は11
0〜90℃までの冷却に引続いて一定時間保持すること
に重要な意味があり、例えば一度常温迄冷却したものを
上記条件に保持しても本発明の効果は得られない。
However, in general, annealing is 10 to 15 degrees higher than the heat distortion temperature.
Normally, the process is carried out at a temperature as low as 0.degree. C. for several hours or more, and there is no example in which the process is carried out at a temperature close to or higher than the heat distortion temperature for a short period of time as in the present invention. The method of the present invention is 11
There is an important meaning in cooling to 0 to 90° C. and then holding it for a certain period of time; for example, even if it is once cooled to room temperature and held under the above conditions, the effects of the present invention cannot be obtained.

110〜90℃迄の冷却速度は可能な限り大きくするこ
とが好ましいが、これは主として採用する冷却方法によ
る。
The cooling rate from 110 to 90°C is preferably as high as possible, but this depends primarily on the cooling method employed.

例えば所定温度の液体中に投入した場合は毎分100℃
以上の冷却速度が得られるし、冷風で強制冷却した場合
はおよそ毎分30℃以上の冷却速度が得られる。冷却方
法は上記に限らず任意の方法を採用することが可能であ
る。熱処理の温度としては90〜110℃好ましくは9
5〜105℃が用いられる。
For example, when placed in a liquid at a specified temperature, the temperature increases at 100°C per minute.
A cooling rate of approximately 30° C./min or higher can be obtained when forced cooling is performed using cold air. The cooling method is not limited to the above method, and any method can be used. The heat treatment temperature is 90 to 110°C, preferably 9
A temperature of 5 to 105°C is used.

熱処理温度が110℃より高い場合には、以後の冷却速
度の影響により再度内部ひずみが発生する可能性があり
、必ずしもその効果が期待できない。また、熱処理温度
が90℃より低い場合には従来のアニーリングに相当す
る程度長時間処理しなければひずみは完全には除去し得
ない。また95〜105℃で行つた場合は上記の事柄等
においてより好ましい効果が得られる。保持時間は長時
間にわたつても全く問題はないが、本発明の目的が短時
間で外観のすぐれた板状重合体を得ることであるので、
いたずらに長時間処理することは本来の目的から外れる
ものであり好ましくない。
If the heat treatment temperature is higher than 110° C., internal strain may occur again due to the influence of the subsequent cooling rate, and the effect cannot necessarily be expected. Further, when the heat treatment temperature is lower than 90° C., the strain cannot be completely removed unless the treatment is performed for a long time equivalent to conventional annealing. Further, when the temperature is 95 to 105°C, more favorable effects can be obtained in the above matters. There is no problem at all even if the holding time is extended for a long time, but since the purpose of the present invention is to obtain a plate-shaped polymer with an excellent appearance in a short time,
Unnecessarily long processing is not desirable as it defeats the original purpose.

他方、1分間よりも短かい時間の処理ではその効果は充
分に発揮できない。
On the other hand, the effect cannot be fully exhibited if the treatment time is shorter than 1 minute.

従つて保持時間は少なくとも1分間、かつ可及的短時間
で処理温度、重合体の板厚、プロセス上の制約などによ
り決定されるべきである。使用される金属板は、0.5
u以上で、セル又はベルトとして使用可能な程度の充分
な強度を有し、かつ充分な熱伝導率を持つもの、具体的
には10kca1/M.hr.℃程度あれば充分である
Therefore, the holding time should be determined to be at least 1 minute and as short as possible, depending on the processing temperature, the thickness of the polymer, process constraints, etc. The metal plate used is 0.5
u or more, has sufficient strength to be used as a cell or belt, and has sufficient thermal conductivity, specifically 10 kcal/M. hr. A temperature around ℃ is sufficient.

本発明の方法は、キユアリング以前の重合条件にはなん
らの制限もなく、従来公知の条件がすべて適用できる。
すなわち重合開始剤としては、有機過酸化物、アゾ化合
物などのフリーラジカル開始剤の1種又は2種以上を混
合したもの、酸化還元系などの開始剤が使用できる。
In the method of the present invention, there are no restrictions on the polymerization conditions before curing, and all conventionally known conditions can be applied.
That is, as the polymerization initiator, one type or a mixture of two or more types of free radical initiators such as organic peroxides and azo compounds, and redox type initiators can be used.

メタクリル酸メチル単独の外、アクリル酸エステル類、
メタクリル酸エステル類、スチレン等のメタクリル酸メ
チルと共重合可能な不飽和単量体との混合物を用いるこ
ともできる。また、重合を損なわない程度に染顔料、安
定剤、離型剤等の各種添加剤を加えることもできる。重
合プロセスとしては熱伝導率が大きい金属であれば、セ
ルキヤスト法にも対向ベルト式連続重合法にも応用でき
る。特に外観のすぐれた板状重合体を得るためには鏡面
状に研摩又はメツキした金属板又はベルトが適している
。 ノ以下実施例によつて具体例を示
す。実施例 1 メタクリル酸メチル単量体に平均分子量8.4万のメタ
クリル酸メチル重合体を25重量%溶解して粘稠なシラ
ツプとし、これに重合開始剤としてアゾビスジメチルバ
レロニトリルを0.06重量%加え、減圧下で充分脱気
した後に、周囲をガスケツトでシールした、2枚の厚さ
1.5mmの鏡面ステンレスセルの間に仕込み、内部温
度測定用として熱電対を内部に挿入し、得られる重合体
の厚さが3mmとなるようにセル間隔を調整した後、8
0℃の水浴中にて25分間反応させ、次いで140℃の
空気浴中で20分間反応させたものを、直ちに98℃の
水浴中に投入する。
In addition to methyl methacrylate alone, acrylic esters,
It is also possible to use methacrylic acid esters and mixtures of methyl methacrylate and unsaturated monomers copolymerizable with each other, such as styrene. Furthermore, various additives such as dyes and pigments, stabilizers, and mold release agents can also be added to the extent that they do not impair polymerization. As for the polymerization process, if the metal has a high thermal conductivity, it can be applied to both the cell cast method and the opposed belt type continuous polymerization method. In particular, in order to obtain a plate-like polymer with an excellent appearance, a mirror-polished or plated metal plate or belt is suitable. Specific examples will be shown below using Examples. Example 1 25% by weight of methyl methacrylate polymer with an average molecular weight of 84,000 was dissolved in methyl methacrylate monomer to form a viscous syrup, and 0.06% of azobisdimethylvaleronitrile was added as a polymerization initiator. After adding % by weight and thoroughly degassing under reduced pressure, it was placed between two 1.5 mm thick mirror-finished stainless steel cells whose surroundings were sealed with a gasket, and a thermocouple was inserted inside to measure the internal temperature. After adjusting the cell spacing so that the thickness of the obtained polymer was 3 mm,
The mixture was reacted in a 0°C water bath for 25 minutes, then in a 140°C air bath for 20 minutes, and then immediately placed in a 98°C water bath.

これにより重合体の温度は約15秒間に140℃より1
00℃までほぼ直線的に低下する。この温度に3分間保
持した後に取出し、室温の空気で強制的に冷却し、重合
体温度が80℃に達したときセルより取出した。
As a result, the temperature of the polymer increases from 140°C to 1°C in about 15 seconds.
The temperature decreases almost linearly to 00°C. After maintaining this temperature for 3 minutes, the polymer was taken out, forcedly cooled with air at room temperature, and when the polymer temperature reached 80°C, it was taken out from the cell.

表面の平滑な板状重合体が得られた。このものの平均分
子量は約75万、ASTMD648−56の方法により
測定した熱変形温度は95.5゜C、残存モノマーは1
.0%であつた。実施例 2〜8 キユアリング以後は次表に示す条件で、それ以外は実施
例1の条件で製造した重合体の熱変形温度、残存モノマ
ーを次表に示す。
A plate-like polymer with a smooth surface was obtained. The average molecular weight of this material is approximately 750,000, the heat distortion temperature measured by the method of ASTM D648-56 is 95.5°C, and the residual monomer is 1.
.. It was 0%. Examples 2 to 8 After curing, the heat distortion temperatures and residual monomers of polymers produced under the conditions shown in the table below and other conditions as in Example 1 are shown in the table below.

ただし、熱処理温度が100℃以上の場合は水浴に代え
て油浴を使用する。比較例 1 キユアリングまでは実施例1と同じ条件で行い、その直
後40℃の水浴中に投入し約45秒間で140℃から6
0℃まで冷却した重合体の熱変形温度は84.5℃、残
存モノマーは1.3%であつた。
However, if the heat treatment temperature is 100°C or higher, an oil bath is used instead of a water bath. Comparative Example 1 The curing process was carried out under the same conditions as in Example 1, and immediately after that, it was placed in a 40°C water bath and heated from 140°C to 6°C in about 45 seconds.
The heat distortion temperature of the polymer cooled to 0°C was 84.5°C, and the residual monomer content was 1.3%.

この重合体をさらに82℃で2時間アニーリングしたも
のの熱変形温度は95℃であり、一方、95℃で20分
間アニーリングしたものの熱変形温度は89℃であつた
。比較例 2 キユアリングまでは実施例1と同じ条件で行い、その後
室温まで放冷し、約20分間に80℃まで冷却した状態
で取出した重合体の熱変形温度は99℃であつた。
When this polymer was further annealed at 82°C for 2 hours, the heat distortion temperature was 95°C, while when annealed at 95°C for 20 minutes, the heat distortion temperature was 89°C. Comparative Example 2 The curing process was carried out under the same conditions as in Example 1, and then the polymer was allowed to cool to room temperature, and the heat deformation temperature of the polymer taken out after being cooled to 80°C for about 20 minutes was 99°C.

比較例 3 キユアリングまでは実施例1と同じ条件で行い、その後
120℃の油浴中に投入して5分間保持し、実施例1と
同条件で冷却し、約1.5分間で80℃まで冷却して取
出した重合体の熱変形温度は91℃であつた。
Comparative Example 3 The curing process was carried out under the same conditions as in Example 1, then it was placed in an oil bath at 120°C and held for 5 minutes, and then cooled under the same conditions as in Example 1 until it reached 80°C in about 1.5 minutes. The heat distortion temperature of the polymer taken out after cooling was 91°C.

比較例 4 熱処理時間を30秒にした他は実施例4と同条件で製造
した重合体の熱変形温度は89℃であつた。
Comparative Example 4 The heat distortion temperature of a polymer produced under the same conditions as in Example 4 except that the heat treatment time was 30 seconds was 89°C.

Claims (1)

【特許請求の範囲】[Claims] 1 メタクリル酸メチル又はメタクリル酸メチルを主成
分とする不飽和単量体混合物を、金属板間に保持した状
態で重合し、板状の重合体を製造するに当り、重合反応
の後段において、120〜160℃に昇温したのち金属
板間に保持した状態のままで毎分25℃以上の冷却速度
で90〜110℃の温度まで急冷すること及び冷却中、
前記温度範囲内の所定温度に少なくとも1分間かつ可及
的短時間に維持する処理を施こすことを特徴とするメタ
クリル酸メチル系重合体の製造方法。
1. When methyl methacrylate or an unsaturated monomer mixture containing methyl methacrylate as a main component is polymerized while being held between metal plates to produce a plate-shaped polymer, in the latter stage of the polymerization reaction, 120 After raising the temperature to ~160°C, rapidly cooling it to a temperature of 90 to 110°C at a cooling rate of 25°C or more per minute while being held between metal plates, and during cooling,
A method for producing a methyl methacrylate polymer, which comprises performing a treatment of maintaining a predetermined temperature within the above temperature range for at least 1 minute and as short a time as possible.
JP13594775A 1975-11-12 1975-11-12 Methacrylic San Methyl Cage Expired JPS5921324B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13594775A JPS5921324B2 (en) 1975-11-12 1975-11-12 Methacrylic San Methyl Cage

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13594775A JPS5921324B2 (en) 1975-11-12 1975-11-12 Methacrylic San Methyl Cage

Publications (2)

Publication Number Publication Date
JPS5259694A JPS5259694A (en) 1977-05-17
JPS5921324B2 true JPS5921324B2 (en) 1984-05-19

Family

ID=15163551

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13594775A Expired JPS5921324B2 (en) 1975-11-12 1975-11-12 Methacrylic San Methyl Cage

Country Status (1)

Country Link
JP (1) JPS5921324B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1985005314A1 (en) * 1984-05-16 1985-12-05 Washi Kosan Co., Ltd. Method of continuously producing plastic board and an apparatus therefor
JP5155507B2 (en) * 2001-07-12 2013-03-06 三菱レイヨン株式会社 Methacrylate resin plate and process for producing the same

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