JPH0430413B2 - - Google Patents
Info
- Publication number
- JPH0430413B2 JPH0430413B2 JP6222384A JP6222384A JPH0430413B2 JP H0430413 B2 JPH0430413 B2 JP H0430413B2 JP 6222384 A JP6222384 A JP 6222384A JP 6222384 A JP6222384 A JP 6222384A JP H0430413 B2 JPH0430413 B2 JP H0430413B2
- Authority
- JP
- Japan
- Prior art keywords
- polymerization
- polymer
- polymer compound
- tert
- present
- 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
Links
- 229920000642 polymer Polymers 0.000 claims description 59
- 150000001875 compounds Chemical class 0.000 claims description 40
- MSVGHYYKWDQHFV-BQYQJAHWSA-N ditert-butyl (e)-but-2-enedioate Chemical compound CC(C)(C)OC(=O)\C=C\C(=O)OC(C)(C)C MSVGHYYKWDQHFV-BQYQJAHWSA-N 0.000 claims description 10
- 230000000379 polymerizing effect Effects 0.000 claims description 3
- 238000006116 polymerization reaction Methods 0.000 description 22
- 238000000034 method Methods 0.000 description 15
- 239000000178 monomer Substances 0.000 description 11
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 9
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 8
- 238000010521 absorption reaction Methods 0.000 description 8
- -1 tert-butoxycarbonylmethylene chain Chemical group 0.000 description 7
- 229920002554 vinyl polymer Polymers 0.000 description 7
- OZAIFHULBGXAKX-UHFFFAOYSA-N 2-(2-cyanopropan-2-yldiazenyl)-2-methylpropanenitrile Chemical compound N#CC(C)(C)N=NC(C)(C)C#N OZAIFHULBGXAKX-UHFFFAOYSA-N 0.000 description 6
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 6
- 238000000655 nuclear magnetic resonance spectrum Methods 0.000 description 5
- 238000010526 radical polymerization reaction Methods 0.000 description 5
- 239000007787 solid Substances 0.000 description 5
- 239000002904 solvent Substances 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 4
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical group O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- VQTUBCCKSQIDNK-UHFFFAOYSA-N Isobutene Chemical compound CC(C)=C VQTUBCCKSQIDNK-UHFFFAOYSA-N 0.000 description 4
- 238000000354 decomposition reaction Methods 0.000 description 4
- 229910052757 nitrogen Inorganic materials 0.000 description 4
- 239000003505 polymerization initiator Substances 0.000 description 4
- 238000001644 13C nuclear magnetic resonance spectroscopy Methods 0.000 description 3
- 239000004342 Benzoyl peroxide Substances 0.000 description 3
- OMPJBNCRMGITSC-UHFFFAOYSA-N Benzoylperoxide Chemical compound C=1C=CC=CC=1C(=O)OOC(=O)C1=CC=CC=C1 OMPJBNCRMGITSC-UHFFFAOYSA-N 0.000 description 3
- 239000004952 Polyamide Substances 0.000 description 3
- KYIKRXIYLAGAKQ-UHFFFAOYSA-N abcn Chemical compound C1CCCCC1(C#N)N=NC1(C#N)CCCCC1 KYIKRXIYLAGAKQ-UHFFFAOYSA-N 0.000 description 3
- 238000000862 absorption spectrum Methods 0.000 description 3
- 239000002253 acid Substances 0.000 description 3
- 235000019400 benzoyl peroxide Nutrition 0.000 description 3
- 238000012662 bulk polymerization Methods 0.000 description 3
- 239000011203 carbon fibre reinforced carbon Substances 0.000 description 3
- 150000001732 carboxylic acid derivatives Chemical class 0.000 description 3
- 125000004185 ester group Chemical group 0.000 description 3
- 239000012948 isocyanate Substances 0.000 description 3
- 150000002513 isocyanates Chemical class 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 229920005615 natural polymer Polymers 0.000 description 3
- 229920002647 polyamide Polymers 0.000 description 3
- 229920001721 polyimide Polymers 0.000 description 3
- 125000000999 tert-butyl group Chemical group [H]C([H])([H])C(*)(C([H])([H])[H])C([H])([H])[H] 0.000 description 3
- 238000005160 1H NMR spectroscopy Methods 0.000 description 2
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical group [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 2
- WVDDGKGOMKODPV-UHFFFAOYSA-N Benzyl alcohol Chemical compound OCC1=CC=CC=C1 WVDDGKGOMKODPV-UHFFFAOYSA-N 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 2
- 229960004217 benzyl alcohol Drugs 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 229910000019 calcium carbonate Inorganic materials 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 239000001569 carbon dioxide Chemical group 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 150000002148 esters Chemical class 0.000 description 2
- 239000011261 inert gas Substances 0.000 description 2
- 238000002329 infrared spectrum Methods 0.000 description 2
- 230000000977 initiatory effect Effects 0.000 description 2
- 239000003607 modifier Substances 0.000 description 2
- 125000004433 nitrogen atom Chemical group N* 0.000 description 2
- 239000007870 radical polymerization initiator Substances 0.000 description 2
- 238000006467 substitution reaction Methods 0.000 description 2
- 238000010557 suspension polymerization reaction Methods 0.000 description 2
- 238000003786 synthesis reaction Methods 0.000 description 2
- 238000005979 thermal decomposition reaction Methods 0.000 description 2
- 238000002411 thermogravimetry Methods 0.000 description 2
- WRDNCFQZLUCIRH-UHFFFAOYSA-N 4-(7-azabicyclo[2.2.1]hepta-1,3,5-triene-7-carbonyl)benzamide Chemical compound C1=CC(C(=O)N)=CC=C1C(=O)N1C2=CC=C1C=C2 WRDNCFQZLUCIRH-UHFFFAOYSA-N 0.000 description 1
- RZVAJINKPMORJF-UHFFFAOYSA-N Acetaminophen Chemical compound CC(=O)NC1=CC=C(O)C=C1 RZVAJINKPMORJF-UHFFFAOYSA-N 0.000 description 1
- 238000005481 NMR spectroscopy Methods 0.000 description 1
- 229920002845 Poly(methacrylic acid) Polymers 0.000 description 1
- 239000004962 Polyamide-imide Substances 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- 239000004642 Polyimide Substances 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- 239000004372 Polyvinyl alcohol Substances 0.000 description 1
- 229920002125 Sokalan® Polymers 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 238000010539 anionic addition polymerization reaction Methods 0.000 description 1
- 229910052786 argon Inorganic materials 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 238000003776 cleavage reaction Methods 0.000 description 1
- 229910001873 dinitrogen Inorganic materials 0.000 description 1
- GVGUFUZHNYFZLC-UHFFFAOYSA-N dodecyl benzenesulfonate;sodium Chemical compound [Na].CCCCCCCCCCCCOS(=O)(=O)C1=CC=CC=C1 GVGUFUZHNYFZLC-UHFFFAOYSA-N 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000007720 emulsion polymerization reaction Methods 0.000 description 1
- 239000005038 ethylene vinyl acetate Substances 0.000 description 1
- 238000010528 free radical solution polymerization reaction Methods 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000001307 helium Substances 0.000 description 1
- 229910052734 helium Inorganic materials 0.000 description 1
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 description 1
- 150000001451 organic peroxides Chemical class 0.000 description 1
- 230000003204 osmotic effect Effects 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 229920001200 poly(ethylene-vinyl acetate) Polymers 0.000 description 1
- 239000004584 polyacrylic acid Substances 0.000 description 1
- 229920002239 polyacrylonitrile Polymers 0.000 description 1
- 229920002312 polyamide-imide Polymers 0.000 description 1
- 238000012643 polycondensation polymerization Methods 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 229920002451 polyvinyl alcohol Polymers 0.000 description 1
- 229920000915 polyvinyl chloride Polymers 0.000 description 1
- 239000004800 polyvinyl chloride Substances 0.000 description 1
- 238000000425 proton nuclear magnetic resonance spectrum Methods 0.000 description 1
- 238000010926 purge Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000005297 pyrex Substances 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000001953 recrystallisation Methods 0.000 description 1
- 238000001226 reprecipitation Methods 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 230000007017 scission Effects 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 229940080264 sodium dodecylbenzenesulfonate Drugs 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 238000001228 spectrum Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000005292 vacuum distillation Methods 0.000 description 1
Landscapes
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
Description
本発明は、主鎖がtert−ブトキシカルボニルメ
チレン連鎖から成ることとを特徴とし、低屈曲性
若しくは剛直性(以下単に剛直性という)を有す
る新規な高分子化合物に関する。
より詳細には、モノマーとしてジ−tert−ブチ
ルフマレートを従来公知の適当なラジカル重合開
始方法により重合させて容易に得られる、剛直性
を有しtert−ブトキシカルボニルメチレン連鎖か
ら成る新規な高分子化合物に関する。
従来から、剛直性の主鎖を有する棒状高分子化
合物及びそれらを与える方法は種々知られてお
り、例えば、セルロース等の天然高分子化合物;
ポリブチルイソシアナート等の二、三のイソシア
ナート系高分子化合物;ポリ−p−フエニレンテ
レフタルアミド系高分子化合物、ポリピロメリツ
トアミド系高分子化合物、ポリアミドヒドラジド
系高分子化合物等の多くのポリアミド、ポリイミ
ド系高分子化合物等が挙げられる。しかし、これ
らの内、天然高分子化合物は、いわゆる汎用ビニ
ルポリマー類の改質材としては不適なものであ
り、他の合成される剛直性の高分子化合物類も、
その欠点としてモノマー自身の合成に複雑な手法
を必要とする上に、その重合方法としてアニオン
重合あるいは縮合重合によるため、重合中に発生
する水等の低分子化合物の除去に工夫を要し、さ
らには多くの汎用ビニルポリマー類、例えばポリ
エチレン、ポリ塩化ビニル、ポリスチレン、ポリ
アクリル酸とそのエステル類、ポリメタクリル酸
とそのエステル類、エチレン−酢酸ビニル共重合
体、ポリアクリロニトリル等をはじめ、上市され
ている種々の汎用樹脂の重合に工業的に好んで使
用されているラジカル重合技術を用いることがで
きないなど、その製造に手数を要するので、決し
て好ましいものではない。さらに汎用ビニルポリ
マー類の改質には、添加された改質材分子中に多
量の窒素原子が存在することは好ましくなく、こ
れらの意味で上記のポリアミド、ポリイミド系の
高分子化合物は改善が必要とされる。
本発明者らは、これらの従来技術の中で改良を
望まれている点として、モノマー自身の合成が容
易なこと、汎用ビニルポリマー類の重合に多く用
いられるラジカル重合方法の条件下で、容易に満
足すべき剛直性の主鎖を有する高分子化合物を与
えること、さらには該剛直性主鎖中に窒素原子を
含まず、好ましくは主鎖が炭素−炭素結合のみか
ら成るべきことに着目し、鋭意研究した結果、モ
ノマーとしてジ−tert−ブチルフマレートを用
い、適当なラジカル重合方法で重合させた場合に
は、上記の望まれている改善点をすべて満足する
剛直性の炭素−炭素結合のみから成る主鎖を有す
る新規な高分子化合物が容易に得られることを見
いだし、本発明を完成した。
すなわち、本発明は、式
で示される繰り返し単位を有し、数平均分子量が
5000〜300000で、主鎖がtert−ブトキシカルボニ
ルメチレン連鎖より成る剛直性を有する新規な高
分子化合物に関する。
ジ−tert−ブチルフマレートの重合には、種々
の公知の重合技術を用いることができるが、好ま
しくは選ばれたラジカル重合開始剤の存在下、溶
媒中若しくは溶媒なしで大気圧下あるいは加圧下
若しくは減圧下で行なわれる。さらには反応系内
を選ばれた不活性ガス、例えば窒素、ヘリウム、
アルゴン、二酸化炭素等で置換するか、あるいは
これらの不活性ガスの気流を通じる方法も実施で
きる。
この際ジ−tert−ブチルフマレートは、重合に
供する以前にあらかじめ再結晶あるいは、減圧蒸
留等の公知の方法で精製することが望ましい。
重合に当つては、もちろん種々の適切な反応温
度を選ぶことができるが、高い温度を選べば生成
高分子化合物の分子量は小さく、低い温度で行な
えば分子量は大きくなり、目的に応じて適当に選
択することができる。本発明においては、数平均
分子量を5000〜300000とすることが好ましく、
5000未満では生成高分子化合物が剛直性に乏し
く、300000を超えるものは製造することが困難で
ある。
ラジカル重合開始剤としては、例えば従来公知
の種々の有機過酸化物類、アゾ系化合物類、レド
ツクス試薬類、過ハロゲン酸塩類等が用いられる
が、光、酸素、放射線等による重合開始方法も行
なわれ、さらには目的によりこれらの二種若しく
はそれ以上を組み合わせることも可能である。溶
媒としては、従来公知のラジカル重合に用いるこ
とのできる溶媒及びそれらの組み合わせは、すべ
て不都合なく使用することができる。重合方法と
しては、塊状重合、溶液重合、懸濁重合、乳化重
合、スラリー重合等の種々の公知の従来技術が応
用可能である。さらに必要に応じて、得られた該
高分子化合物をそれぞれの目的に適した精製方法
で精製することも可能である。もちろんこれらの
方法で重合を行なう場合、好ましくない低分子化
合物、例えば水、炭酸ガス等の発生は一切なく、
これも本発明の利点の一つである。
こうして得られる新規な高分子化合物は、主鎖
がtert−ブトキシカルボニルメチレン連鎖から成
り、剛直性を有するものであつて、これまでに公
知の天然高分子化合物、イソシアナート系高分子
化合物あるいはポリアミド、ポリイミド系高分子
化合物と同様の剛直性を示す。
さらに該高分子化合物の側鎖となるtert−ブチ
ルエステル基は、高温でイソブテンとカルボン酸
とに容易に分解し、ポリカルボン酸を与えること
も可能であり、汎用ビニルポリマー類の改質材と
して十分応用することができる。これらの点から
本発明の新規な高分子化合物は、剛直性高分子化
合物として有用であるばかりでなく、他の汎用ビ
ニルポリマー類の改質材としても優れた特性を有
しているものである。
以下に、実施例によつて本発明を具体的に説明
するが、これらは本発明の範囲を限定するもので
はない。
実施例 1
内容積20mlのパイレツクスガラス製重合管に、
精製したジ−tert−ブチルフマレート5g及び重
合開始剤としてアゾビスイソブチロニトリル
(AIBN)0.016gをとり、内部の窒素置換と脱気
を十分に繰り返した後溶封した。この重合管を80
℃±0.1℃に保つた振とう式湯浴中に入れ、1時
間塊状重合を行なつた後重合管を開封し、内容物
をベンゼンに溶解させ、多量のメタノール中に投
じてポリマーを沈殿させた、得られたポリマーに
ついてベンゼン−メタノール系から再沈殿精製を
繰り返し、白色固体状ポリマーを得た。結果を第
1表にまとめた。
実施例 2
重合開始剤としてアゾビスシクロヘキサンカル
ボニトリル(ACN)0.024gを用い、重合時間を
4時間とした以外は、実施例1に準じて重合を行
ない、白色固体状ポリマーを得た。結果を第1表
にまとめた。
実施例 3
重合開始剤として過酸化ベンゾイル(BPO)
0.024gを用い、重合時間を3時間とした以外は、
実施例1に準じて重合を行ない。白色固体状ポリ
マーを得た。結果を第1表にまとめた。
実施例 4
重合開始剤としてACN0.024gを用い、重合温
度を90℃±0.1℃、重合時間を4時間とした以外
は、実施例1に準じて重合を行ない、白色固体状
ポリマーを得た。結果を第1表にまとめた。
実施例 5
実施例1と同様の重合管に、ジ−tert−ブチル
フマレート5.7g、ベンゼン5ml、AIBN0.052g
をとり、内部の窒素置換、脱気を十分に繰り返し
溶封した後、60℃±0.1℃で10時間塊状重合を行
ない、白色固体状ポリマーを得た。結果を第1表
にまとめた。
実施例 6
内容積500mlの四ツ口フラスコに、部分ケン化
ポリビニルアルコールの0.2重量%水溶液200ml、
炭酸カルシウム2g、ドデシルベンゼンスルホン
酸ナトリウムの1重量%水溶液2.5gをとり、さ
らにジ−tert−ブチルフマレート50gにBPO 0.5
gを溶解させたものを加えて、窒素ガスを導入し
つつかくはんを行ない、80℃±0.1℃で24時間懸
濁重合を行なつた。重合終了後、反応器内に塩酸
を加えて酸性として炭酸カルシウムを溶解させ、
沈殿した粒子状ポリマーを別し、十分水洗及び
湯洗を行ない、最後にメタノールで洗浄した後、
減圧乾燥して白色粒子状ポリマーを得た。結果を
第1表にまとめた。
The present invention relates to a novel polymer compound characterized by a main chain consisting of a tert-butoxycarbonylmethylene chain and having low flexibility or rigidity (hereinafter simply referred to as rigidity). More specifically, a novel polymer having rigidity and consisting of tert-butoxycarbonylmethylene chains, which can be easily obtained by polymerizing di-tert-butyl fumarate as a monomer by a conventionally known suitable radical polymerization initiation method. Regarding compounds. Hitherto, various rod-shaped polymer compounds having rigid main chains and methods for providing them have been known. For example, natural polymer compounds such as cellulose;
Two or three isocyanate-based polymer compounds such as polybutyl isocyanate; many polyamides such as poly-p-phenylene terephthalamide-based polymer compounds, polypyromellitamide-based polymer compounds, polyamide hydrazide-based polymer compounds, etc. , polyimide-based polymer compounds, and the like. However, among these, natural polymer compounds are unsuitable as modifying materials for so-called general-purpose vinyl polymers, and other synthesized rigid polymer compounds also
Its disadvantages are that it requires complicated techniques to synthesize the monomer itself, and that the polymerization method is anionic polymerization or condensation polymerization, which requires ingenuity to remove low-molecular compounds such as water generated during polymerization. is commercially available, including many general-purpose vinyl polymers such as polyethylene, polyvinyl chloride, polystyrene, polyacrylic acid and its esters, polymethacrylic acid and its esters, ethylene-vinyl acetate copolymer, polyacrylonitrile, etc. It is not at all preferable because it requires a lot of effort to manufacture, such as not being able to use radical polymerization techniques that are industrially preferred for polymerizing various general-purpose resins. Furthermore, when modifying general-purpose vinyl polymers, it is undesirable for a large amount of nitrogen atoms to exist in the added modifier molecules, and in this sense, the polyamide and polyimide-based polymers mentioned above need improvement. It is said that The present inventors have found that improvements in these conventional techniques are desired, such as ease of synthesis of the monomer itself, and ease of synthesis under the conditions of the radical polymerization method often used for the polymerization of general-purpose vinyl polymers. The present invention aims to provide a polymer compound having a main chain with a rigidity that satisfies the above requirements, and further focuses on the fact that the main chain does not contain nitrogen atoms and preferably consists of only carbon-carbon bonds. As a result of extensive research, we found that when di-tert-butyl fumarate is used as a monomer and polymerized using an appropriate radical polymerization method, a rigid carbon-carbon bond that satisfies all of the desired improvements mentioned above has been created. The present invention was completed based on the discovery that a novel polymer compound having a main chain consisting of That is, the present invention provides the formula It has a repeating unit represented by , and the number average molecular weight is
5,000 to 300,000 and has a main chain consisting of a tert-butoxycarbonylmethylene chain. Various known polymerization techniques can be used to polymerize di-tert-butyl fumarate, but preferably in the presence of a selected radical polymerization initiator, in a solvent or without a solvent, at atmospheric pressure or under pressure. Alternatively, it is carried out under reduced pressure. Furthermore, a selected inert gas such as nitrogen, helium,
Substitution with argon, carbon dioxide, etc., or a method of passing a stream of these inert gases can also be carried out. In this case, it is desirable that di-tert-butyl fumarate be purified in advance by a known method such as recrystallization or vacuum distillation before being subjected to polymerization. Of course, various suitable reaction temperatures can be selected for polymerization, but if a high temperature is selected, the molecular weight of the polymer compound produced will be small, and if carried out at a low temperature, the molecular weight will be large. You can choose. In the present invention, the number average molecular weight is preferably 5000 to 300000,
If it is less than 5,000, the resulting polymer compound will have poor rigidity, and if it is more than 300,000, it will be difficult to produce. As the radical polymerization initiator, for example, various conventionally known organic peroxides, azo compounds, redox reagents, perhalogenates, etc. can be used, but polymerization initiation methods using light, oxygen, radiation, etc. can also be used. Furthermore, it is also possible to combine two or more of these types depending on the purpose. As the solvent, all conventionally known solvents that can be used in radical polymerization and combinations thereof can be used without any disadvantage. As the polymerization method, various known conventional techniques such as bulk polymerization, solution polymerization, suspension polymerization, emulsion polymerization, and slurry polymerization can be applied. Furthermore, if necessary, the obtained polymer compound can be purified by a purification method suitable for each purpose. Of course, when polymerization is carried out using these methods, there is no generation of undesirable low-molecular compounds such as water or carbon dioxide, and
This is also one of the advantages of the present invention. The novel polymer compound obtained in this way has a main chain consisting of a tert-butoxycarbonylmethylene chain and has rigidity, and is a conventional polymer compound such as a known natural polymer compound, an isocyanate-based polymer compound, or a polyamide. Shows rigidity similar to polyimide polymer compounds. Furthermore, the tert-butyl ester group, which forms the side chain of the polymer compound, can easily decompose into isobutene and carboxylic acid at high temperatures, giving polycarboxylic acid, which can be used as a modifying material for general-purpose vinyl polymers. It can be fully applied. From these points of view, the novel polymer compound of the present invention is not only useful as a rigid polymer compound, but also has excellent properties as a modifier for other general-purpose vinyl polymers. . EXAMPLES The present invention will be specifically explained below with reference to Examples, but these are not intended to limit the scope of the present invention. Example 1 In a Pyrex glass polymer tube with an internal volume of 20 ml,
5 g of purified di-tert-butyl fumarate and 0.016 g of azobisisobutyronitrile (AIBN) as a polymerization initiator were taken, and after sufficiently repeating nitrogen substitution and deaeration inside the reactor, it was melt-sealed. This polymerization tube is 80
The tube was placed in a shaking water bath maintained at ±0.1°C and subjected to bulk polymerization for 1 hour, then the polymerization tube was opened, the contents were dissolved in benzene, and the contents were poured into a large amount of methanol to precipitate the polymer. The obtained polymer was then repeatedly purified by reprecipitation from a benzene-methanol system to obtain a white solid polymer. The results are summarized in Table 1. Example 2 Polymerization was carried out according to Example 1, except that 0.024 g of azobiscyclohexanecarbonitrile (ACN) was used as a polymerization initiator and the polymerization time was 4 hours, to obtain a white solid polymer. The results are summarized in Table 1. Example 3 Benzoyl peroxide (BPO) as a polymerization initiator
Except that 0.024 g was used and the polymerization time was 3 hours.
Polymerization was carried out according to Example 1. A white solid polymer was obtained. The results are summarized in Table 1. Example 4 Polymerization was carried out according to Example 1, except that 0.024 g of ACN was used as a polymerization initiator, the polymerization temperature was 90°C±0.1°C, and the polymerization time was 4 hours, to obtain a white solid polymer. The results are summarized in Table 1. Example 5 Into the same polymerization tube as in Example 1, 5.7 g of di-tert-butyl fumarate, 5 ml of benzene, and 0.052 g of AIBN were added.
After sufficiently repeating nitrogen purging and deaeration, the polymer was melt-sealed, and then bulk polymerization was carried out at 60°C±0.1°C for 10 hours to obtain a white solid polymer. The results are summarized in Table 1. Example 6 In a four-necked flask with an internal volume of 500 ml, 200 ml of a 0.2% by weight aqueous solution of partially saponified polyvinyl alcohol was added.
Take 2 g of calcium carbonate and 2.5 g of a 1% by weight aqueous solution of sodium dodecylbenzenesulfonate, and add 0.5 g of BPO to 50 g of di-tert-butyl fumarate.
A solution of g was added thereto, stirring was performed while introducing nitrogen gas, and suspension polymerization was carried out at 80°C±0.1°C for 24 hours. After polymerization, add hydrochloric acid to the reactor to make it acidic and dissolve calcium carbonate.
Separate the precipitated particulate polymer, wash thoroughly with water and hot water, and finally wash with methanol.
A white particulate polymer was obtained by drying under reduced pressure. The results are summarized in Table 1.
【表】
極限粘度は、溶媒にベンゼンを用い
て30℃で測定した値である。
以下、機器分析によつて、本発明の高分子化合
物の同定及びその特性について説明する。
第1図、第3図、第5図に、本発明の原料であ
るジ−tert−ブチルフマレートモノマー(以下モ
ノマーという)の赤外吸収スペクトル(IR)、核
磁気共鳴スペクトル( 1H及び13C−NMR)をそ
れぞれ示し、第2図、第4図、第6図に、実施例
1で得られた本発明の高分子化合物(以下ポリマ
ーという)のIR、 1H−NMR及び13C−NMRス
ペクトルをそれぞれ示した。第1図、第2図の
IRスペクトルにおいて、モノマーの二重結合に
基づく吸収(1663cm-1)が、ポリマーでは消失
し、また第3図、第4図の 1H−NMRスペクト
ルにおいて、モノマーの6.6ppmの二重結合のメ
チンプロトンの吸収が、ポリマーでは消失して
3ppm付近に非常にブロードな吸収となつて現わ
れている。さらに第5図、第6図の13C−NMR
スペクトルにおいて、モノマーで現われる二重結
合の炭素の吸収(134.39ppm)がポリマーでは消
失していることが分るが、主鎖の炭素の吸収は、
非常に小さくノイズに含まれてしまつているもの
と思われる。以上のことから、モノマーの重合は
内部二重結合の開裂により進行し、tert−ブトキ
シカルボニルメチレン連鎖から成るポリマーを与
えることが分る。
次に、ポリマーの熱重量分析の結果を第7図に
示す。第7図から明らかなように、ポリマーの初
期分解温度は190℃、最大分解温度は205℃、500
℃での残渣は10.1%である。210℃での残渣は
48.0%となるが、ポリマーのtert−ブチルエステ
ル基がイソブテンを放出しながらカルボン酸にな
るとするとその値は51%になり、205℃での分解
は側鎖のtert−ブチルエステル基の分解に対応し
ていることが分る。また、ポリマーを窒素気流下
200℃で2時間熱分解し、その残渣のIRスペクト
ルを測定し第8図を得た。第8図には、カルボン
酸の吸収がみられること、及び水酸基の吸収がみ
られることから、熱分解によりポリカルボン酸が
生成していることが明らかである。
実施例6で得られた本発明の高分子化合物を、
ベンゼン−メタノール系を用いてポリマーを分別
し、分子量の異なる重合体を得た。それぞれの重
合体の極限粘度を測定し、また分子量は浸透圧法
により算出して、分子量と極限粘度との関係を求
めたところ、下式に従うことが分つた。
〔η〕=3.08×10-3M1.41
(〔η〕;極限粘度
M ;分子量)
一般に、極限粘度と分子量との関係は下式で表
わされることが知られている。
〔η〕=KM〓
(Kおよびαは定数)
一般の重合体では、通常αは1より小さく屈曲
性を示すが、αが1より大きくなると剛直性重合
体であると考えられている。
実施例6の本発明の高分子化合物においては、
上記のようにαが1よりかなり大きいことから、
剛直性高分子化合物ということができる。
以上のことから、本発明の高分子化合物は、主
鎖が炭素−炭素結合のみから成り、tert−ブトキ
シカルボニルメチレン連鎖構造を有する剛直性高
分子化合物であることは明らかである。また、加
熱により容易にポリカルボン酸を与えることので
きる高分子化合物で、汎用ビニルポリマー類の改
質材としても有用なものである。[Table] Intrinsic viscosity is the value measured at 30°C using benzene as the solvent.
Identification of the polymer compound of the present invention and its properties will be explained below using instrumental analysis. Figures 1, 3, and 5 show infrared absorption spectra (IR) and nuclear magnetic resonance spectra ( 1H and 13 Figures 2, 4, and 6 show the IR, 1 H-NMR, and 13 C-NMR of the polymer compound of the present invention (hereinafter referred to as polymer) obtained in Example 1. NMR spectra are shown for each. Figures 1 and 2
In the IR spectrum, the absorption (1663 cm -1 ) based on the double bond of the monomer disappears in the polymer, and in the 1 H-NMR spectra of Figures 3 and 4, the absorption (1663 cm -1 ) based on the double bond of the monomer disappears at 6.6 ppm of the double bond of the monomer. Proton absorption disappears in polymers
It appears as a very broad absorption around 3ppm. Furthermore, 13 C-NMR in Figures 5 and 6
In the spectrum, it can be seen that the double bond carbon absorption (134.39 ppm) that appears in the monomer disappears in the polymer, but the main chain carbon absorption
It seems that it is very small and is included in the noise. From the above, it can be seen that the polymerization of the monomer proceeds by cleavage of internal double bonds to yield a polymer consisting of tert-butoxycarbonylmethylene chains. Next, the results of thermogravimetric analysis of the polymer are shown in FIG. As is clear from Figure 7, the initial decomposition temperature of the polymer is 190℃, the maximum decomposition temperature is 205℃, and the
The residue at °C is 10.1%. The residue at 210℃ is
However, if the tert-butyl ester group of the polymer becomes a carboxylic acid while releasing isobutene, the value becomes 51%, and the decomposition at 205℃ corresponds to the decomposition of the tert-butyl ester group in the side chain. I know what you're doing. In addition, the polymer was tested under a nitrogen stream.
The mixture was thermally decomposed at 200°C for 2 hours, and the IR spectrum of the residue was measured, as shown in Figure 8. In FIG. 8, absorption of carboxylic acid and absorption of hydroxyl groups are observed, so it is clear that polycarboxylic acid is produced by thermal decomposition. The polymer compound of the present invention obtained in Example 6 was
The polymers were fractionated using a benzene-methanol system to obtain polymers with different molecular weights. The intrinsic viscosity of each polymer was measured, and the molecular weight was calculated by an osmotic pressure method, and the relationship between the molecular weight and the intrinsic viscosity was determined, and it was found that the following formula was followed. [η]=3.08×10 -3 M 1.41 ([η]; intrinsic viscosity M; molecular weight) It is generally known that the relationship between the intrinsic viscosity and the molecular weight is expressed by the following formula. [η] = KM (K and α are constants) In general polymers, α is usually less than 1 and exhibits flexibility, but when α is greater than 1, it is considered to be a rigid polymer. In the polymer compound of the present invention in Example 6,
Since α is much larger than 1 as mentioned above,
It can be called a rigid polymer compound. From the above, it is clear that the polymer compound of the present invention is a rigid polymer compound whose main chain consists only of carbon-carbon bonds and has a tert-butoxycarbonylmethylene chain structure. Moreover, it is a polymer compound that can easily give polycarboxylic acid by heating, and is also useful as a modifying material for general-purpose vinyl polymers.
第1図及び第2図は、それぞれ本発明の原料で
あるジ−tert−ブチルフマレートモノマーとそれ
から得られた本発明の剛直性高分子化合物との赤
外吸収スペクトルを示すグラフである。第3図及
び第4図は、それぞれジ−tert−ブチルフマレー
トモノマーと本発明の剛直性高分子化合物との核
磁気共鳴スペクトル( 1H−NMR)を示すグラ
フ、第5図及び第6図は、同様に核磁気共鳴スペ
クトル(13C−NMR)を示すグラフである。第
7図は、本発明の剛直性高分子化合物の熱重量分
析の結果を、第8図は、本発明の剛直性高分子化
合物の熱分解残渣の赤外吸収スペクトルをそれぞ
れ示すグラフである。
FIGS. 1 and 2 are graphs showing infrared absorption spectra of di-tert-butyl fumarate monomer, which is a raw material of the present invention, and a rigid polymer compound of the present invention obtained therefrom, respectively. Figures 3 and 4 are graphs showing nuclear magnetic resonance spectra ( 1H-NMR) of di-tert-butyl fumarate monomer and the rigid polymer compound of the present invention, and Figures 5 and 6 are graphs showing nuclear magnetic resonance spectra (1H -NMR), respectively. is a graph similarly showing a nuclear magnetic resonance spectrum ( 13 C-NMR). FIG. 7 is a graph showing the results of thermogravimetric analysis of the rigid polymer compound of the present invention, and FIG. 8 is a graph showing the infrared absorption spectrum of the thermal decomposition residue of the rigid polymer compound of the present invention.
Claims (1)
5000〜300000の剛直性高分子化合物。 2 ジ−tert−ブチルフマレートをラジカル重合
させたものである特許請求の範囲第1項記載の剛
直性高分子化合物。[Claims] 1 formula Number average molecular weight with a repeating unit represented by
5000~300000 rigid polymer compound. 2. The rigid polymer compound according to claim 1, which is obtained by radical polymerizing di-tert-butyl fumarate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP6222384A JPS60208306A (en) | 1984-03-31 | 1984-03-31 | Novel high-molecular-weight compound with high stiffness and toughness |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP6222384A JPS60208306A (en) | 1984-03-31 | 1984-03-31 | Novel high-molecular-weight compound with high stiffness and toughness |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS60208306A JPS60208306A (en) | 1985-10-19 |
| JPH0430413B2 true JPH0430413B2 (en) | 1992-05-21 |
Family
ID=13193935
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP6222384A Granted JPS60208306A (en) | 1984-03-31 | 1984-03-31 | Novel high-molecular-weight compound with high stiffness and toughness |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS60208306A (en) |
-
1984
- 1984-03-31 JP JP6222384A patent/JPS60208306A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS60208306A (en) | 1985-10-19 |
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