JPH05132521A - Production of acrylic polymer - Google Patents
Production of acrylic polymerInfo
- Publication number
- JPH05132521A JPH05132521A JP3321510A JP32151091A JPH05132521A JP H05132521 A JPH05132521 A JP H05132521A JP 3321510 A JP3321510 A JP 3321510A JP 32151091 A JP32151091 A JP 32151091A JP H05132521 A JPH05132521 A JP H05132521A
- Authority
- JP
- Japan
- Prior art keywords
- mercapto compound
- reaction
- acrylic
- polymerization
- heat resistance
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F20/00—Homopolymers and copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride, ester, amide, imide or nitrile thereof
- C08F20/02—Monocarboxylic acids having less than ten carbon atoms, Derivatives thereof
- C08F20/10—Esters
- C08F20/12—Esters of monohydric alcohols or phenols
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F2/00—Processes of polymerisation
- C08F2/38—Polymerisation using regulators, e.g. chain terminating agents, e.g. telomerisation
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、アクリル系重合体の製
造法に関する。更に詳しくは、耐熱性にすぐれた高分子
量アクリル系重合体の製造法に関する。FIELD OF THE INVENTION The present invention relates to a method for producing an acrylic polymer. More specifically, it relates to a method for producing a high molecular weight acrylic polymer having excellent heat resistance.
【0002】[0002]
【従来の技術】特開昭55-5950号公報には、メルカプタ
ン類を連鎖移動剤に用いて重合反応を行い、メタクリル
系樹脂を得る方法が記載されているが、耐熱性を向上さ
せる目的で、重合反応の開始時からメルカプタン類を多
量に添加すると低分子量の重合体しか得られない。そこ
で、高分子量の重合体を得るには、メルカプタン類の添
加量を少なくする必要があり、しかるにこの場合には十
分な耐熱性が得られないばかりではなく、特に側鎖に架
橋部位を有する場合には、ゲル化を生ずるという問題点
を有している。2. Description of the Related Art Japanese Unexamined Patent Publication (Kokai) No. 55-5950 discloses a method of obtaining a methacrylic resin by carrying out a polymerization reaction using a mercaptan as a chain transfer agent, but for the purpose of improving heat resistance. However, if a large amount of mercaptans is added from the start of the polymerization reaction, only a low molecular weight polymer can be obtained. Therefore, in order to obtain a high-molecular weight polymer, it is necessary to reduce the amount of mercaptans added. However, in this case not only sufficient heat resistance is not obtained, but especially when the side chain has a crosslinking site. Has a problem that gelation occurs.
【0003】同様に、側鎖に架橋性基を有するアクリル
系エラストマーを溶液重合法で製造するに際し、重合反
応の最初からメルカプト連鎖移動剤を添加しておくこと
が、本出願人によって提案されているが(特開昭63-2101
13号公報)、この場合に得られるアクリル系エラストマ
ーは、加硫物性および透明性の点ではすぐれているもの
の、耐熱性の点では未だ十分とはいえない。Similarly, when producing an acrylic elastomer having a crosslinkable group in its side chain by a solution polymerization method, it has been proposed by the present applicant to add a mercapto chain transfer agent from the beginning of the polymerization reaction. (Japanese Patent Laid-Open No. 63-2101
No. 13), the acrylic elastomer obtained in this case is excellent in vulcanization physical properties and transparency, but is still insufficient in heat resistance.
【0004】また、特公昭38-14491号公報、特開昭50-1
44745号公報には、メタクリル系樹脂にブレンダなどに
よりメルカプタン類を添加し、熱安定性を改良する方法
が記載されているが、工程数の増加、異物混入の機会の
増加、作業の煩雑さなどの難点がみられる。Further, Japanese Patent Publication No. 38-14491 and Japanese Patent Laid-Open No. 50-1
44745 discloses a method of adding mercaptans to a methacrylic resin with a blender or the like to improve thermal stability, but increasing the number of steps, increasing the chances of contamination with foreign substances, and complicating work, etc. There are some difficulties.
【0005】[0005]
【発明が解決しようとする課題】本発明の目的は、重合
体自身の改質によって、耐熱性にすぐれかつ高分子量の
アクリル系重合体を製造する方法を提供することにあ
る。SUMMARY OF THE INVENTION An object of the present invention is to provide a method for producing an acrylic polymer having a high heat resistance and a high molecular weight by modifying the polymer itself.
【0006】[0006]
【課題を解決するための手段】かかる本発明の目的は、
アクリル酸エステルまたはメタクリル酸エステルを溶液
重合するに際し、重合反応を終了させる直前に有機メル
カプト化合物を添加してアクリル系重合体を製造するこ
とによって達成される。The object of the present invention is as follows.
This can be achieved by adding an organic mercapto compound immediately before the termination of the polymerization reaction during the solution polymerization of an acrylic acid ester or a methacrylic acid ester to produce an acrylic polymer.
【0007】重合反応に供せられるアクリル酸エステル
またはメタクリル酸エステルとしては、メチルアクリレ
ート、エチルアクリレート、プロピルアクリレート、ブ
チルアクリレート、ジシクロペンテニルアクリレート、
ジシクロペンテニルオキシエチルアクリレート、エチレ
ングリコールジアクリレート、プロピレングリコールジ
アクリレート、ポリエチレングリコールジアクリレート
またはこれらに対応するメタクリレートなどの1種また
は2種以上が用いられ、2種以上が用いられる場合に
は、一般にアルキル(メタ)アクリレートを主成分とし、
他の(メタ)アクリレートはこれと共重合させる形で用い
られる。更に、これらと共重合性を有する他のビニル化
合物を共重合させることもできる。Examples of the acrylic acid ester or methacrylic acid ester used for the polymerization reaction include methyl acrylate, ethyl acrylate, propyl acrylate, butyl acrylate, dicyclopentenyl acrylate,
One or more of dicyclopentenyloxyethyl acrylate, ethylene glycol diacrylate, propylene glycol diacrylate, polyethylene glycol diacrylate or their corresponding methacrylates are used, and when two or more are used, they are generally used. Alkyl (meth) acrylate as the main component,
Other (meth) acrylates are used in the form of copolymerization therewith. Furthermore, other vinyl compounds having copolymerizability with these can be copolymerized.
【0008】重合反応は、重合開始剤の存在下で、溶液
重合法によって約50〜70℃で行われる。反応溶媒として
は、メチルエチルケトン、アセトン、アセトニトリル、
クロロホルム、トルエンなどが一般に用いられる。この
重合反応を終了させる直前、具体的には予め重合液中の
生成重合体の数平均分子量を測定しておき、その変化の
過程を重合液の撹拌トルクなどでモニターしておき、つ
まりトルク値と数平均分子量との関係を求めておき、重
合反応実施時に所望の数平均分子量に相当するトルクに
なった時点で、有機メルカプト化合物を添加し、更に約
1〜30分間程度撹拌を継続することにより、有機メルカ
プト化合物を生成重合体に結合させる。The polymerization reaction is carried out at about 50 to 70 ° C. by the solution polymerization method in the presence of a polymerization initiator. As the reaction solvent, methyl ethyl ketone, acetone, acetonitrile,
Chloroform, toluene and the like are generally used. Immediately before the termination of this polymerization reaction, specifically, the number average molecular weight of the polymer produced in the polymerization solution is measured in advance, and the process of the change is monitored by the stirring torque of the polymerization solution, that is, the torque value. The relationship between the number average molecular weight and the number average molecular weight is obtained in advance, and when the torque corresponding to the desired number average molecular weight is reached during the polymerization reaction, the organic mercapto compound is added,
By continuing stirring for about 1 to 30 minutes, the organic mercapto compound is bonded to the produced polymer.
【0009】有機メルカプト化合物としては、例えばブ
チルメルカプタン、オクチルメルカプタン、ドデシルメ
ルカプタン、ラウリルメルカプタン、メルカプトエタノ
ールなどが、原料単量体に対して約0.05〜3モル%、好ま
しくは約0.5〜1モル%の割合で用いられる。これ以下で
は十分な耐熱性が得られず、これ以上の割合で添加する
と着色や臭気が問題となる。As the organic mercapto compound, for example, butyl mercaptan, octyl mercaptan, dodecyl mercaptan, lauryl mercaptan, mercaptoethanol and the like are contained in an amount of about 0.05 to 3 mol%, preferably about 0.5 to 1 mol% based on the raw material monomer. Used in proportion. If it is less than this, sufficient heat resistance cannot be obtained, and if it is added in a proportion higher than this, coloring and odor become problems.
【0010】反応終了後は、反応混合物に生成重合体の
貧溶媒を加えて再沈させ、その後良溶媒-貧溶媒による
再沈をくり返して、精製アクリル系重合体を得る。After completion of the reaction, a poor solvent for the produced polymer is added to the reaction mixture for reprecipitation, and then reprecipitation with a good solvent and a poor solvent is repeated to obtain a purified acrylic polymer.
【0011】[0011]
【発明の効果】アクリル酸エステルまたはメタクリル酸
エステルを溶液重合するに際し、重合反応を終了させる
直前に有機メルカプト化合物を添加することにより、重
合反応の最初から有機メルカプト化合物を添加した場合
と比較して、有機メルカプト化合物の結合量がほぼ同じ
でありながら、より耐熱性にすぐれかつより高分子量の
アクリル系重合体が得られる。しかも、アクリル系重合
体が本来有するすぐれた透過性は殆んど損なわれること
はない。[Effects of the Invention] In solution polymerization of acrylic acid ester or methacrylic acid ester, by adding the organic mercapto compound immediately before the termination of the polymerization reaction, compared with the case where the organic mercapto compound is added from the beginning of the polymerization reaction. While the amount of the organic mercapto compound bonded is almost the same, an acrylic polymer having higher heat resistance and higher molecular weight can be obtained. Moreover, the excellent permeability inherent in the acrylic polymer is hardly impaired.
【0012】従って、このような特徴を有する本発明の
アクリル系重合体は、高可とう性ライトガイド、レンズ
などの光通信や光学部品の分野に有効に利用することが
できる。Therefore, the acrylic polymer of the present invention having such characteristics can be effectively used in the field of optical communication such as a highly flexible light guide and a lens, and the field of optical parts.
【0013】[0013]
【実施例】次に、実施例について本発明を説明する。EXAMPLES The present invention will now be described with reference to examples.
【0014】実施例1 撹拌トルク検出器付き重合釜内で、エチルアクリレート
200.2g(2.0モル)、アゾビスイソブチロニトリル0.164g
およびメチルエチルケトン144.2gの混合物を54℃に加熱
し、撹拌トルクが数平均分子量=9×104に相当する値に
なった時点(重合反応開始後2時間40分)で、オクチルメ
ルカプタン2.93g(0.02モル)を加え、10分間撹拌して重
合反応を終了させた。Example 1 Ethyl acrylate was placed in a polymerization kettle equipped with a stirring torque detector.
200.2g (2.0mol), azobisisobutyronitrile 0.164g
And a mixture of methyl ethyl ketone (144.2 g) were heated to 54 ° C., and when the stirring torque reached a value corresponding to a number average molecular weight = 9 × 10 4 (2 hours and 40 minutes after the initiation of the polymerization reaction), 2.93 g (0.02 g) of octyl mercaptan Mol) was added and stirred for 10 minutes to terminate the polymerization reaction.
【0015】反応混合物に70重量%メタノール水溶液を
加えて再沈させ、メチルエチルケトンとメタノール水溶
液による再沈を3回行って得られた重合体は、数平均分
子量が1.2×105であり、一方反応混合物溶液中の未反応
オクチルメルカプタンの定量値(2.02g)から、重合体末
端に用いられたオクチルメルカプタンの31%が結合して
いるものと考えられる。A polymer obtained by adding 70% by weight aqueous methanol solution to the reaction mixture for reprecipitation and reprecipitating with methyl ethyl ketone and aqueous methanol solution three times has a number average molecular weight of 1.2 × 10 5 , while the reaction From the quantitative value (2.02 g) of unreacted octyl mercaptan in the mixture solution, it is considered that 31% of the octyl mercaptan used at the polymer end is bound.
【0016】比較例1 実施例1において、最初からオクチルメルカプタンを加
えた混合物を53℃に加熱し、12時間重合反応させると、
数平均分子量=5.7×104の重合体が得られた。より高分
子量の重合体を得るために、この温度で更に12時間重合
反応を継続したが、数平均分子量=6.3×104の重合体が
得られたにすぎなかった。COMPARATIVE EXAMPLE 1 In Example 1, the mixture containing octyl mercaptan from the beginning was heated to 53 ° C. and polymerized for 12 hours.
A polymer having a number average molecular weight = 5.7 × 10 4 was obtained. The polymerization reaction was continued at this temperature for a further 12 hours in order to obtain a higher molecular weight polymer, but only a polymer having a number average molecular weight of 6.3 × 10 4 was obtained.
【0017】実施例1と同様に、未反応のオクチルメル
カプタン量を定量すると1.93gであり、この結果から用
いられたオクチルメルカプタンの34%が重合体末端に結
合しているものと考えられる。As in Example 1, the amount of unreacted octyl mercaptan was determined to be 1.93 g, and from this result, it is considered that 34% of the octyl mercaptan used was bound to the polymer terminal.
【0018】実施例2 実施例1の重合釜内で、n-ブチルアクリレート241.0g
(1.88モル)、ジシクロペンテニルアクリレート24.5g(0.
12モル)、アゾビスイソブチロニトリル0.164gおよびメ
チルエチルケトン144.2gの混合物を56℃に加熱し、撹拌
トルクが数平均分子量=1.1×105に相当する値になった
時点(重合反応開始後2時間)で、2-メルカプトエタノー
ル1.25g(0.016モル)を加え、15分間撹拌して重合反応を
終了させた。Example 2 In the polymerization kettle of Example 1, 241.0 g of n-butyl acrylate
(1.88 mol), dicyclopentenyl acrylate 24.5 g (0.
(12 mol), 0.164 g of azobisisobutyronitrile and 144.2 g of methyl ethyl ketone are heated to 56 ° C., and when the stirring torque reaches a value corresponding to number average molecular weight = 1.1 × 10 5 (2 1.25 g (0.016 mol) of 2-mercaptoethanol was added and stirred for 15 minutes to terminate the polymerization reaction.
【0019】反応混合物からメチルエチルケトン-メタ
ノール水溶液で再沈して得られた共重合体は、数平均分
子量が1.5×105であり、未反応2-メルカプトエタノール
の定量値(0.71g)から、用いられた2-メルカプトエタノ
ールの43%が共重合体末端に結合しているものと考えら
れる。The copolymer obtained by reprecipitation from the reaction mixture with an aqueous solution of methyl ethyl ketone-methanol had a number average molecular weight of 1.5 × 10 5 , and was used based on the quantitative value (0.71 g) of unreacted 2-mercaptoethanol. It is considered that 43% of the obtained 2-mercaptoethanol is bound to the end of the copolymer.
【0020】以上の実施例1〜2および比較例1でそれ
ぞれ得られた重合体について、130℃の空気中に保持し
たときの数平均分子量の変化を経時的に測定すると図1
に示されるような結果が得られ、また光透過スペクトル
を測定すると図2〜3に示されるような結果が得られ
た。これらの結果は、各実施例で得られた重合体は、耐
熱性および光透過性のいずれにおいてもすぐれているこ
とが分かる。With respect to the polymers obtained in each of Examples 1 to 2 and Comparative Example 1 above, changes in the number average molecular weight when kept in air at 130 ° C. were measured with time.
The results shown in Fig. 2 were obtained, and the results shown in Figs. 2 to 3 were obtained by measuring the light transmission spectrum. These results show that the polymers obtained in each example are excellent in both heat resistance and light transmission.
【0021】また、130℃の空気中に100時間保持したと
きの、耐熱試験前後における可視光透過率(JIS R-3106)
の値は次の如くであった。 Further, visible light transmittance (JIS R-3106) before and after the heat resistance test when kept in air at 130 ° C. for 100 hours.
The values of were:
【0022】比較例2 実施例2において、最初から2-メルカプトエタノールを
加えた混合物を55℃に加熱し、3時間35分重合反応させ
ると、数平均分子量=8.8×104の共重合体が得られた。
より高分子量の共重合体を得るために、この温度で更に
重合反応を継続させたところ、急速にゲル化し、成形材
料などに供し得る共重合体が得られなくなった。Comparative Example 2 In Example 2, the mixture containing 2-mercaptoethanol from the beginning was heated to 55 ° C. and polymerized for 3 hours and 35 minutes to give a copolymer having a number average molecular weight of 8.8 × 10 4. Was obtained.
When the polymerization reaction was further continued at this temperature in order to obtain a higher molecular weight copolymer, it rapidly gelled, and a copolymer which could be used as a molding material or the like could not be obtained.
【図1】実施例1〜2および比較例1でそれぞれ得られ
た重合体の耐熱性を示すグラフである。FIG. 1 is a graph showing the heat resistance of the polymers obtained in Examples 1 and 2 and Comparative Example 1, respectively.
【図2】実施例1(実線)および比較例1(点線)でそれぞ
れ得られた重合体の光透過スペクトルである。FIG. 2 is light transmission spectra of the polymers obtained in Example 1 (solid line) and Comparative Example 1 (dotted line), respectively.
【図3】実施例2で得られた重合体の光透過スペクトル
である。FIG. 3 is a light transmission spectrum of the polymer obtained in Example 2.
Claims (1)
エステルを溶液重合するに際し、重合反応を終了させる
直前に有機メルカプト化合物を添加することを特徴とす
るアクリル系重合体の製造法。1. A method for producing an acrylic polymer, which comprises adding an organic mercapto compound immediately before the termination of the polymerization reaction during solution polymerization of an acrylic acid ester or a methacrylic acid ester.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3321510A JPH05132521A (en) | 1991-11-11 | 1991-11-11 | Production of acrylic polymer |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3321510A JPH05132521A (en) | 1991-11-11 | 1991-11-11 | Production of acrylic polymer |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH05132521A true JPH05132521A (en) | 1993-05-28 |
Family
ID=18133375
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3321510A Pending JPH05132521A (en) | 1991-11-11 | 1991-11-11 | Production of acrylic polymer |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH05132521A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2012021142A (en) * | 2010-06-15 | 2012-02-02 | Nippon Synthetic Chem Ind Co Ltd:The | Acrylic resin solution, acrylic pressure-sensitive adhesive composition, acrylic pressure-sensitive adhesive, acrylic pressure-sensitive adhesive for optical element, optical element with pressure-sensitive agent layer, and method of producing acrylic resin solution |
US8142717B2 (en) | 2007-04-23 | 2012-03-27 | Toyo Boseki Kabushiki Kaisha | Oxygenator of a hollow fiber membrane type |
US8236913B2 (en) | 2006-12-07 | 2012-08-07 | Toyo Boseki Kabushiki Kaisha | (Meth)acrylate copolymer, a method for producing the same and a medical device |
-
1991
- 1991-11-11 JP JP3321510A patent/JPH05132521A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8236913B2 (en) | 2006-12-07 | 2012-08-07 | Toyo Boseki Kabushiki Kaisha | (Meth)acrylate copolymer, a method for producing the same and a medical device |
US8142717B2 (en) | 2007-04-23 | 2012-03-27 | Toyo Boseki Kabushiki Kaisha | Oxygenator of a hollow fiber membrane type |
JP2012021142A (en) * | 2010-06-15 | 2012-02-02 | Nippon Synthetic Chem Ind Co Ltd:The | Acrylic resin solution, acrylic pressure-sensitive adhesive composition, acrylic pressure-sensitive adhesive, acrylic pressure-sensitive adhesive for optical element, optical element with pressure-sensitive agent layer, and method of producing acrylic resin solution |
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