JPH0826144B2 - Method for producing polyether copolymer having epoxy group in side chain - Google Patents
Method for producing polyether copolymer having epoxy group in side chainInfo
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- JPH0826144B2 JPH0826144B2 JP61010763A JP1076386A JPH0826144B2 JP H0826144 B2 JPH0826144 B2 JP H0826144B2 JP 61010763 A JP61010763 A JP 61010763A JP 1076386 A JP1076386 A JP 1076386A JP H0826144 B2 JPH0826144 B2 JP H0826144B2
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Description
【発明の詳細な説明】 (産業上の利用分野) 本発明はエポキシ樹脂やゴム材料としてあるいは反応
中間体,接着剤,塗料用材料として有用な、側鎖にエポ
キシ基を有するポリエーテル共重合体の製造法に関す
る。The present invention relates to a polyether copolymer having an epoxy group in its side chain, which is useful as an epoxy resin or a rubber material, or as a reaction intermediate, an adhesive or a coating material. Manufacturing method.
(従来技術) 側鎖に官能基をもつポリマーは各種の機能を期待でき
ることから重要であり、そのため官能基を有するモノマ
ーの重合研究が多くなされている。しかしながら、類似
した重合反応性を示す官能基を2個以上含むモノマーの
重合もしくは共重合では架橋反応が同時に進行するため
に不溶性ゲルを生じ、一方の官能基のみによって重合
し、他方の官能基を残存させ、可溶性もしくは熱可塑性
の、少なくとも高分子量のポリマーを得ることは通常困
難なことであった。唯、ジエン類の共重合によってエチ
レン性不飽和基を側鎖に有するポリマーを合成する例と
してエチレン−プロピレン−ジエンポリマーのような例
があるが、これは特定の触媒に対し一方の不飽和基の重
合反応性が顕著に異なるジエンを利用しているものであ
る。(Prior Art) A polymer having a functional group in its side chain is important because various functions can be expected, and therefore, many studies have been conducted on polymerization of a monomer having a functional group. However, in the polymerization or copolymerization of a monomer containing two or more functional groups having similar polymerization reactivity, an insoluble gel is formed because the crosslinking reaction proceeds at the same time, and only one functional group is polymerized and the other functional group is It has generally been difficult to obtain residual, soluble or thermoplastic, at least high molecular weight polymers. However, as an example of synthesizing a polymer having an ethylenically unsaturated group in the side chain by copolymerization of dienes, there is an example such as ethylene-propylene-diene polymer, which is one unsaturated group for a specific catalyst. It uses a diene having a markedly different polymerization reactivity.
側鎖にエポキシ基を有するポリマーとしては、ビニル
重合性官能基とエポキシ基とを両方有するモノマーをラ
ジカル開始剤によって重合させるような場合、例えばメ
タクリル酸グリシジルをパーオキシドで重合させるよう
な場合しか得られていない。The polymer having an epoxy group on the side chain can be obtained only when a monomer having both a vinyl polymerizable functional group and an epoxy group is polymerized by a radical initiator, for example, when glycidyl methacrylate is polymerized with peroxide. Not not.
ポリエーテル主鎖を持つポリマーは、一般にエポキシ
ドの開環重合によって合成することができるが、モノエ
ポキシドとジエポキシドの共重合において、ジエポキシ
ドの一方のエポキシ基のみを選択的に重合させ、他方の
エポキシ基をポリマー側鎖として残存させて可溶性ポリ
エーテルを得る例はこれまで全く知られていない。A polymer having a polyether main chain can be generally synthesized by ring-opening polymerization of an epoxide, but in copolymerization of a monoepoxide and a diepoxide, only one epoxy group of the diepoxide is selectively polymerized and the other epoxy group is polymerized. Up to now, no example has been known in which a soluble polyether is obtained by leaving the polymer as a polymer side chain.
(発明の目的) 本発明は、特定のジエポキシドとモノエポキシドを特
定の触媒を用いて重合させることによって、従来文献未
記載の、種々の用途に対応しうる、側鎖にエポキシ基を
有するポリエーテル共重合体の製造法を提供することを
目的とする。(Object of the Invention) The present invention is a polyether having an epoxy group in the side chain, which has not been described in the conventional literature and can be used for various applications, by polymerizing a specific diepoxide and a monoepoxide using a specific catalyst. It is an object to provide a method for producing a copolymer.
(発明の構成) 本発明は、主鎖構造が実質的に下記(I)式 の構成単位5〜95モル%と下記(II)式 (但し、(II)式において、Rは水素原子および置換基
を有していてもよい、アルキル基,アルケニル基,シク
ロアルキル基,アリール基から選ばれる原子又は基であ
る。)の構成単位95〜5モル%とからなり、45℃におい
て0.1%のベンゼン溶液または80℃において0.1%のモノ
クロロベンゼン溶液で測定した還元粘度が0.01以上であ
ることを特徴とする側鎖にエポキシ基を有するポリエー
テル共重合体の製造法である。(Structure of the Invention) In the present invention, the main chain structure is substantially the following formula (I): 5 to 95 mol% of the structural unit of and the following (II) formula (However, in the formula (II), R is a hydrogen atom or an atom or a group optionally having a substituent, which is selected from an alkyl group, an alkenyl group, a cycloalkyl group, and an aryl group.) A polyether having an epoxy group in the side chain, which has a reduced viscosity of 0.01 or more as measured with a 0.1% benzene solution at 45 ° C or a 0.1% monochlorobenzene solution at 80 ° C. It is a method for producing a copolymer.
また本発明は、2,3−エポキシプロピル−2′,3′−
エポキシ−2′−メチルプロピルエーテルと下記一般式
(III) (但し、(III)式において、Rは水素原子および置換
基を有していてもよい、アルキル基,アルケニル基,シ
クロアルキル基,アリール基から選ばれる原子又は基で
ある。) から選ばれるモノマーとを下記一般式(i)〜(iv) RaSnX4-a (i) (但し、(i)式において、Rは置換基を有していても
よい炭素数1〜12のアルキル基,アルケニル基,シクロ
アルキル基,アリール基及びアラルキル基より選ばれる
基、Xはハロゲン原子,アルコキシ基,アリールオキシ
基,アシルオキシ基およびリン酸の部分エステル残基か
ら選ばれる原子又は基であり、aは1〜4を示す整数で
ある。aが2以上のとき、Rは同一でも異なっていても
よく、またaが1又は2のとき、Xは同一でも異なって
いてもよい。) RbSnOc (ii) (但し、(ii)式において、Rは(i)式におけるRと
同じである。bは1又は2であり、bが1のとき、cは
3/2であり、bが2のとき、cは1である。また(ii)
式化合物は(i)式化合物と錯体を形成していてもよ
い。) R1R2SnOSnR2R1 (iii) (但し、(iii)式において、Rは(i)式におけるR
と同じであり、R1は(i)式におけるR又はXと同じで
ある。また2個のR1は同一でも異なっていてもよい。) (R1 3Sn)dX′ (iv) (但し、(iv)式において、R1は(iii)式におけるR1
と同じであり、少なくとも1個は(i)式のRから選ば
れる基である。X′は炭酸基,リンの酸素酸基,リン酸
の部分エステル残基,多塩基性カルボン酸基,多価アル
コール残基から選ばれる基である。dはX′の塩基度に
対応する1より大きい数である。) から選ばれる有機錫化合物とリン酸アルキルエステルと
の熱縮合生成物である触媒の存在下に重合させることを
特徴とする側鎖にエポキシ基を有するポリエーテル共重
合体の製造法である。The present invention also relates to 2,3-epoxypropyl-2 ', 3'-
Epoxy-2'-methylpropyl ether and the following general formula (III) (However, in the formula (III), R is a hydrogen atom and an atom or a group optionally having a substituent, which is selected from an alkyl group, an alkenyl group, a cycloalkyl group, and an aryl group.) And the following general formulas (i) to (iv) Ra SnX 4-a (i) (wherein, in the formula (i), R is an alkyl group having 1 to 12 carbon atoms which may have a substituent, A group selected from an alkenyl group, a cycloalkyl group, an aryl group and an aralkyl group, X is an atom or a group selected from a halogen atom, an alkoxy group, an aryloxy group, an acyloxy group and a partial ester residue of phosphoric acid, and a is It is an integer representing 1 to 4. When a is 2 or more, Rs may be the same or different, and when a is 1 or 2, Xs may be the same or different.) R b SnO c (Ii) (However, in equation (ii) Te, R is .b 1 or 2 is the same as R in the formula (i), when b is 1, c is
It is 3/2, and when b is 2, c is 1. Also (ii)
The formula compound may form a complex with the formula compound (i). ) R 1 R 2 SnOSnR 2 R 1 (iii) (However, in the formula (iii), R is R in the formula (i).
And R 1 is the same as R or X in the formula (i). Two R 1's may be the same or different. ) (R 1 3 Sn) d X ′ (iv) (However, in the formula (iv), R 1 is R 1 in the formula (iii).
And at least one is a group selected from R in the formula (i). X'is a group selected from a carbonic acid group, a phosphorus oxygen acid group, a phosphoric acid partial ester residue, a polybasic carboxylic acid group, and a polyhydric alcohol residue. d is a number greater than 1 corresponding to the basicity of X '. ) Polymerization in the presence of a catalyst, which is a thermal condensation product of an organotin compound selected from the following, and an alkyl phosphate ester, is a process for producing a polyether copolymer having an epoxy group in the side chain.
この化合物は、例えばアリルメタアリルエーテルを過
酸化水素,過酸などを用いてエポキシ化することによっ
て合成できる。This compound can be synthesized, for example, by epoxidizing allylmethallyl ether with hydrogen peroxide, peracid or the like.
この化合物は従来よく知られている開環重合触媒、例
えば有機アルミニウム−水などによって重合させると急
速に架橋反応が進行し溶剤可溶性のポリマーは得られな
い。また本発明と同様の他のモノエポキシドとの共重合
においても可溶性ポリマーは得られない。When this compound is polymerized with a conventionally well-known ring-opening polymerization catalyst such as organoaluminum-water, a crosslinking reaction proceeds rapidly and a solvent-soluble polymer cannot be obtained. Also, a soluble polymer cannot be obtained by copolymerization with other monoepoxides similar to the present invention.
本発明は、本出願人の米国特許第3,773,694号明細書
に記載された特定の有機錫化合物(A)とリン酸アルキ
ルエステル(B)との熱縮合生成物が特定のジエポキシ
ドとモノエポキシドとの開環共重合用触媒として選択的
に作用し、生成ポリマーも側鎖にエポキシ基をもつ機能
性ポリマーとして非常に有用であることを見出したこと
に基いている。The present invention provides a thermal condensation product of a specific organotin compound (A) and a phosphoric acid alkyl ester (B) described in Applicant's US Pat. No. 3,773,694 with a specific diepoxide and monoepoxide. It is based on the finding that it selectively acts as a catalyst for ring-opening copolymerization, and that the resulting polymer is also very useful as a functional polymer having an epoxy group in its side chain.
本発明のポリエーテル共重合体の構成単位(II)式を
形成させる上記一般式(III)化合物の具体例として
は、エチレンオキシド,プロピレンオキシド,ブタジエ
ンモノオキシド,ビニルシクロヘキサンオキシド,スチ
レンオキシド,エピクロロヒドリン,エピブロモヒドリ
ン、アリルグルシジルエーテル,ブチルグリシジルエー
テル,フェニルグリシジルエーテル,酢酸グリシジル,
プロピオン酸グリシジル,安息香酸グリシジル,ケイ皮
酸グリシジル,などが挙げられる。これらの一種又は二
種以上の化合物を共重合成分として用いることができ
る。即ち、本発明のポリエーテル共重合体の構成単位
(II)は上記二種以上のモノマーから形成される構成単
位が同一ポリマー鎖に存在していてもよい。Specific examples of the compound of the general formula (III) which forms the structural unit (II) of the polyether copolymer of the present invention include ethylene oxide, propylene oxide, butadiene monoxide, vinylcyclohexane oxide, styrene oxide and epichlorohydride. Phosphorus, epibromohydrin, allyl glycidyl ether, butyl glycidyl ether, phenyl glycidyl ether, glycidyl acetate,
Examples thereof include glycidyl propionate, glycidyl benzoate, and glycidyl cinnamate. One or more of these compounds can be used as a copolymerization component. That is, the constitutional unit (II) of the polyether copolymer of the present invention may have constitutional units formed from the above-mentioned two or more kinds of monomers in the same polymer chain.
本発明の触媒成分である上記(i)〜(iv)式の有機
錫化合物(A)の具体的な例としては以下のものを挙げ
ることができる。The following can be mentioned as specific examples of the organotin compound (A) of the above formulas (i) to (iv) which is the catalyst component of the present invention.
一般式(i)に属する化合物としては、 (C2H5)4Sn,(C6H5)4Sn, (CH3)3SnF,(C4H9)3SnCl, (CH3)3SnBr,(C8H17)3SnCl, (CH3)2SnF2,(C4H9)2SnCl2, (C12H23)2SnBr2, (cyclo-C6H11)2SnI2, (C4H9)SnF3,(C8H17)SnCl3, (C4H9)3SnOC4H9, (C8H17)3SnOCOCH3, (C8H17)2Sn(OCOC17H35)2, などが挙げられる。Examples of the compound belonging to the general formula (i) include (C 2 H 5 ) 4 Sn, (C 6 H 5 ) 4 Sn, (CH 3 ) 3 SnF, (C 4 H 9 ) 3 SnCl, (CH 3 ) 3 SnBr, (C 8 H 17) 3 SnCl, (CH 3) 2 SnF 2, (C 4 H 9) 2 SnCl 2, (C 12 H 23) 2 SnBr 2, (cyclo-C 6 H 11) 2 SnI 2 , (C 4 H 9 ) SnF 3 , (C 8 H 17 ) SnCl 3 , (C 4 H 9 ) 3 SnOC 4 H 9 , (C 8 H 17) 3 SnOCOCH 3, (C 8 H 17) 2 Sn (OCOC 17 H 35) 2, And the like.
一般式(ii)に属する化合物としては、 (CH3)2SnO,(C4H9)2SnO, (C8H17)2SnO,(C6H5)2SnO, CH3SnO3/2,C4H9SnO3/2, などが挙げられ、また一般式(i)と一般式(ii)の化
合物の錯体の例としては、 (CH3)2SnO・(C2H5)2SnBr2, (CH3)2SnO・(CH3)2SnCl2, CH3〔(CH3)2SnO〕2CH3・ (CH3)2SnBr2 などが挙げられる。Examples of the compound belonging to the general formula (ii) include (CH 3 ) 2 SnO, (C 4 H 9 ) 2 SnO, (C 8 H 17 ) 2 SnO, (C 6 H 5 ) 2 SnO, CH 3 SnO 3 / 2 , C 4 H 9 SnO 3/2 , etc., and examples of the complex of the compounds of the general formula (i) and the general formula (ii) include (CH 3 ) 2 SnO. (C 2 H 5 ) 2 SnBr 2, and the like (CH 3) 2 SnO · ( CH 3) 2 SnCl 2, CH 3 [(CH 3) 2 SnO] 2 CH 3 · (CH 3) 2 SnBr 2.
一般式(iii)に属する化合物としては、 (CH3)3SnOSn(CH3)3, Cl(C4H9)2SnOSn(C4H9)Cl, (CH3COO)(C6H5)Sn(C6H5)(CH3COO) などが挙げられる。The compounds belonging to general formula (iii), (CH 3) 3 SnOSn (CH 3) 3, Cl (C 4 H 9) 2 SnOSn (C 4 H 9) Cl, (CH 3 COO) (C 6 H 5 ) Sn (C 6 H 5 ) (CH 3 COO) and the like.
一般式(iv)に属する化合物としては、 〔(CH3)3Sn〕2CO3, 〔(C4H9)3Sn〕2CO3, (C4H9)3SnOP(O)(OC8H17)2, 〔(C8H17)3Sn〕3PO4, (C4H9)3SnOCH2CH2OSn, (C4H9)3, (C4H9)2(CH3O)Sn-OCOCH2)4-OCO-Sn(OCH3)(C4H9)2, などが挙げられる。The compounds belonging to general formula (iv), [(CH 3) 3 Sn] 2 CO 3, [(C 4 H 9) 3 Sn] 2 CO 3, (C 4 H 9) 3 SnOP (O) (OC 8 H 17) 2, [(C 8 H 17) 3 Sn] 3 PO 4, (C 4 H 9) 3 SnOCH 2 CH 2 OSn, (C 4 H 9) 3, (C 4 H 9) 2 (CH 3 O) Sn-OCOCH 2 ) 4- OCO-Sn (OCH 3 ) (C 4 H 9 ) 2 , And the like.
本発明の触媒を構成する他の成分であるリン酸アルキ
ルエステル(B)としては、下記一般式(IV)で表わさ
れる正リン酸の完全もしくは部分エステルが用いられ
る。As the phosphoric acid alkyl ester (B) which is another component constituting the catalyst of the present invention, a complete or partial ester of orthophosphoric acid represented by the following general formula (IV) is used.
(R2O)3P=O (IV) (但し、(IV)式において、R2は水素もしくは炭素数2
以上のアルキル基,アルケニル基又はシクロアルキル基
であり、少くともR2のうち1個は水素原子以外の基であ
る。) 上記(IV)式の具体的な例としては、 (C2H5)3PO4,(C3H7)3PO4, (C4H9)3PO4,(C8H17)3PO4, (CH2=CH-CH2)3PO4, (C6H11)3PO4, (ClCH2-CH2))3PO4, (Cl2C3H5)PO4,(C2H5)2HPO4, (C4H9)2HPO4,(C4H9)H2PO4 などが挙げられる。(R 2 O) 3 P = O (IV) (In the formula (IV), R 2 is hydrogen or has 2 carbon atoms.
The above alkyl group, alkenyl group or cycloalkyl group, and at least one of R 2 is a group other than a hydrogen atom. ) Specific examples of the above formula (IV) include (C 2 H 5 ) 3 PO 4 , (C 3 H 7 ) 3 PO 4 , (C 4 H 9 ) 3 PO 4 , and (C 8 H 17 ). 3 PO 4 , (CH 2 = CH-CH 2 ) 3 PO 4 , (C 6 H 11 ) 3 PO 4 , (ClCH 2 -CH 2 )) 3 PO 4 , (Cl 2 C 3 H 5 ) PO 4 , (C 2 H 5) 2 HPO 4, (C 4 H 9) 2 HPO 4, and the like (C 4 H 9) H 2 PO 4.
本発明の触媒は、上記有機錫化合物(A)とリン酸ア
ルキルエステル(B)との混合物を150℃〜300℃の温度
範囲で加熱することによって縮合生成物として得られ
る。溶媒は必要があれば使用してもよい。上記(A)成
分と(B)成分は通常含まれる錫原子とリン原子との比
で1:10〜10:1の範囲になるように用いられる。The catalyst of the present invention is obtained as a condensation product by heating a mixture of the organotin compound (A) and the phosphoric acid alkyl ester (B) in a temperature range of 150 ° C to 300 ° C. The solvent may be used if necessary. The above-mentioned components (A) and (B) are used so that the ratio of tin atoms and phosphorus atoms usually contained is in the range of 1:10 to 10: 1.
上記触媒生成反応において、(A)成分及び(B)成
分の種類に従って種々の比較的簡単な物質が縮合反応で
生成脱離する。得られた縮合物は縮合度の種々の段階で
目的とする活性を示す。最適の縮合度は、(A)成分と
(B)成分の種類と比率によって異なるが、それらは実
験的に容易に定めることができる。縮合物は、一般に初
期においてはヘキサン,ベンゼンなどの溶媒に可溶であ
るが、縮合反応の進行によって不溶化する。In the catalyst formation reaction, various relatively simple substances are formed and eliminated by the condensation reaction according to the types of the component (A) and the component (B). The obtained condensate exhibits the desired activity at various stages of the degree of condensation. The optimum condensation degree varies depending on the types and ratios of the component (A) and the component (B), but they can be easily determined experimentally. The condensate is generally soluble in a solvent such as hexane or benzene at the initial stage, but becomes insoluble as the condensation reaction proceeds.
本発明のポリエーテル共重合体は、上記縮合生成物を
触媒として2,3−エポキシプロピル−2′,3′−エポキ
シ−2′−メチルプロピルエーテルと上記(III)式化
合物を通常脂肪族炭化水素類,芳香族炭化水素類などの
溶媒の存在下又は非存在下に10〜80℃で通常攪拌又は振
盪下で重合させることによって得られる。触媒の使用量
は総原料モノマー100重量部に対して0.01〜1.0重量部の
範囲が適当である。反応の際反応系の水分は可能な限り
低くすることが望ましい。In the polyether copolymer of the present invention, 2,3-epoxypropyl-2 ', 3'-epoxy-2'-methylpropyl ether and the above formula (III) compound are usually aliphatic carbonized using the above condensation product as a catalyst. It can be obtained by polymerizing in the presence or absence of a solvent such as hydrogens and aromatic hydrocarbons at 10 to 80 ° C, usually with stirring or shaking. The amount of the catalyst used is appropriately in the range of 0.01 to 1.0 parts by weight based on 100 parts by weight of the total raw material monomers. It is desirable that the water content of the reaction system during the reaction be as low as possible.
本発明のポリエーテル共重合体は、式(I)と式(I
I)の構成単位の量比が5〜95:95〜5モル%のものであ
って、45℃において0.1%のベンゼン溶液または80℃に
おいて0.1%のモノクロロベンゼン溶液で測定した還元
粘度が0.01以上、好ましくは0.01〜5、特に好ましくは
0.05〜3の範囲のものが良好な利用性をもっている。エ
ポキシ樹脂として利用する場合、構成モル比は式(I)
が30モル%以上のものがよく、またゴムとして利用する
場合は、式(I)が5モル%前後のものが好ましい。反
応中間体として利用する場合は、その用途に応じて多彩
な組成が考えられる。The polyether copolymer of the present invention has the formula (I) and the formula (I
The ratio of the constituent units of I) is 5 to 95:95 to 5 mol% and the reduced viscosity measured with a 0.1% benzene solution at 45 ° C or a 0.1% monochlorobenzene solution at 80 ° C is 0.01 or more. , Preferably 0.01 to 5, particularly preferably
The range of 0.05 to 3 has good usability. When used as an epoxy resin, the constituent molar ratio is represented by the formula (I)
Is preferably 30 mol% or more, and when used as a rubber, a compound of the formula (I) having about 5 mol% is preferable. When used as a reaction intermediate, various compositions are conceivable depending on the application.
(発明の効果) 本発明のポリマーは、新規な特定ジエポキシドを用
い、これにモノエポキシドを組合せ、特定の触媒を用い
て重合させることによって得られる、側鎖にエポキシ基
を有する新規なポリエーテル共重合体であり、エポキシ
樹脂,ゴム材料,反応性中間体,接着剤,塗料用材料な
どに有用な高機能ポリマーである。(Effect of the invention) The polymer of the present invention is a novel polyether copolymer having an epoxy group in the side chain, which is obtained by using a novel specific diepoxide, combining it with a monoepoxide, and polymerizing it using a specific catalyst. It is a polymer and is a high-performance polymer useful for epoxy resins, rubber materials, reactive intermediates, adhesives, paint materials, etc.
(実施例) 実施例1 攪拌機、温度計及び蒸留装置を付した三ツ口フラスコ
にジブチル錫オキシド10.0g、トリブチルホスフェート2
3.4gを入れ、窒素気流下に攪拌しながら260℃で15分間
加熱して留出物を留去させ、残留物として固体状の縮合
物質を得た。このものを触媒として以下の重合を行っ
た。(Example) Example 1 In a three-necked flask equipped with a stirrer, a thermometer, and a distillation device, 10.0 g of dibutyltin oxide and 2 parts of tributylphosphate were added.
3.4 g was added, the mixture was heated under a nitrogen stream at 260 ° C. for 15 minutes with stirring to distill off the distillate, and a solid condensed substance was obtained as a residue. The following polymerization was carried out using this as a catalyst.
内容量50mlのガラス製アンプルの内部を窒素置換し、
上記縮合物質30mgと水分10ppm以下の2,3−エポキシプロ
ピル−2′,3′−エポキシ−2′−メチルプロピルエー
テル12g及びプロピレンオキシド20gを仕込み、封管後ア
ンプルを振盪しながら40℃で50時間反応させた。反応後
反応物をメタノール(2,2′−メチレンビス(4−メチ
ル−6−第三ブチルフェノール)0.5重量%含有)100ml
中に投入して一晩浸漬後メタノールを傾斜除去し、更
に、上記メタノール100mlによる洗浄を二度繰り返した
後、減圧下100℃にて8時間乾燥して粘着状ゴム質ポリ
マー29gを得た。第1表に仕込みモノマーモル比、反応
条件及び生成ポリマーの各成分組成比等を示した。また
本例によって得られた共重合体の赤外線吸収スペクトル
を第1図に示し、1HNMRスペクトルを第5図に示した。Replace the inside of a glass ampoule with an internal capacity of 50 ml with nitrogen,
Charge 30 mg of the above condensation substance and 12 g of 2,3-epoxypropyl-2 ′, 3′-epoxy-2′-methylpropyl ether having a water content of 10 ppm or less and 20 g of propylene oxide, seal the tube, and shake at 50 ° C. at 40 ° C. while shaking the ampoule. Reacted for hours. After the reaction, the reaction product was added with 100 ml of methanol (containing 0.5% by weight of 2,2'-methylenebis (4-methyl-6-tert-butylphenol)).
The mixture was placed in the flask and immersed overnight, the methanol was decanted off, and the washing with 100 ml of the above methanol was repeated twice, followed by drying at 100 ° C. for 8 hours under reduced pressure to obtain 29 g of an adhesive rubbery polymer. Table 1 shows the molar ratio of charged monomers, the reaction conditions, and the composition ratio of each component of the produced polymer. The infrared absorption spectrum of the copolymer obtained in this example is shown in FIG. 1 , and the 1 H NMR spectrum is shown in FIG.
実施例2〜4 実施例1と同じ触媒を用いて同様の方法で、第1表に
示されるようなモル比の仕込みモノマー、触媒量及び反
応条件で共重合を行い、それぞれ共重合体を得た。得ら
れた共重合体の成分組成比を第1表に示した。ここに示
した共重合体の成分組成比は1HNMRにより求めた。また
実施例2〜4によって得られた共重合体の赤外線吸収ス
ペクトルをそれぞれ第2図〜第4図に示し、実施例2に
よって得られた共重合体の1HNMRスペクトルを第6図に
示した。Examples 2 to 4 Copolymerization was performed using the same catalyst as in Example 1 in the same manner as described above, but with the molar ratio of the charged monomer, the amount of catalyst, and the reaction conditions shown in Table 1, to obtain copolymers. It was The component composition ratio of the obtained copolymer is shown in Table 1. The component composition ratio of the copolymer shown here was determined by 1 H NMR. The infrared absorption spectra of the copolymers obtained in Examples 2 to 4 are shown in FIGS. 2 to 4, respectively, and the 1 H NMR spectrum of the copolymers obtained in Example 2 is shown in FIG. .
第1図〜第4図は、それぞれ実施例1〜4によって得ら
れた共重合体の赤外線吸収スペクトルであり、第5図〜
第6図は、それぞれ実施例1〜2によって得られた共重
合体の1HNMRスペクトルである。1 to 4 are infrared absorption spectra of the copolymers obtained in Examples 1 to 4, respectively, and FIGS.
FIG. 6 is 1 H NMR spectra of the copolymers obtained in Examples 1 and 2, respectively.
Claims (2)
キシ−2′−メチルプロピルエーテルと、下記一般式
(III)から選ばれるモノマーとを、一般式(i)〜(i
v)から選ばれる有機錫化合物と、リン酸アルキルエス
テルとの熱縮合生成物である触媒の存在下に重合させる
ことによって得られる、主鎖構造が実質的に下記(I)
式の構成単位5〜95モル%と下記(II)式の構成単位95
〜5モル%とからなり、45℃において0.1%のベンゼン
溶液または80℃において0.1%のモノクロロベンゼン溶
液で測定した還元粘度が0.01以上であることを特徴とす
る側鎖にエポキシ基を有するポリエーテル共重合体の製
造法。 (但し、(II)式及び(III)式において、R3は水素原
子および置換基を有していてもよい、アルキル基,アル
ケニル基,シクロアルキル基,アリール基から選ばれる
原子又は基であり、(III)式において、異なるR3を有
する構成単位が同一ポリマー鎖に存在していてもよ
い。) RaSnX4-a (i) (但し、(i)式において、Rは置換基を有していても
よい炭素数1〜12のアルキル基,アルケニル基,シクロ
アルキル基,アリール基及びアラルキル基より選ばれる
基、Xはハロゲン原子,アルコキシ基,アリールオキシ
基,アシルオキシ基およびリン酸の部分エステル残基か
ら選ばれる原子又は基であり、aは1〜4を示す整数で
ある。aが2以上のとき、Rは同一でも異なっていても
よく、またaが1又は2のとき、Xは同一でも異なって
いてもよい。) RbSnOc (ii) (但し、(ii)式において、Rは(i)式におけるRと
同じである。bは1又は2であり、bが1のとき、cは
3/2であり、bが2のとき、cは1である。 また(ii)式化合物は(i)式化合物と錯体を形成して
いてもよい。) R1R2SnOSnR2R1 (iii) (但し、(iii)式において、Rは(i)式におけるR
と同じであり、R1は(i)式におけるR又はXと同じで
ある。また2個のR1は同一でも異なっていてもよい。) (R1 3Sn)dX′ (iv) (但し、(iv)式において、R1は(iii)式におけるR1
と同じであり、少なくとも1個は(i)式のRから選ば
れる基である。X′は炭酸基,リンの酸素酸基,リン酸
の部分エステル残基,多塩基性カルボン酸基,多価アル
コール残基から選ばれる基である。dはX′の塩基度に
対応する1より大きい数である。)1. A compound of general formulas (i) to (i) containing 2,3-epoxypropyl-2 ', 3'-epoxy-2'-methylpropyl ether and a monomer selected from the following general formula (III).
The main chain structure obtained by polymerization in the presence of a catalyst, which is a thermal condensation product of an organotin compound selected from v) and an alkyl phosphate ester, is substantially the following (I).
5 to 95 mol% of the structural unit of the formula and the structural unit 95 of the following formula (II)
A polyether having an epoxy group in the side chain, which has a reduced viscosity of 0.01 or more as measured with a 0.1% benzene solution at 45 ° C or a 0.1% monochlorobenzene solution at 80 ° C. Method for producing copolymer. (In the formulas (II) and (III), R 3 is a hydrogen atom or an atom or a group which may have a substituent and is selected from an alkyl group, an alkenyl group, a cycloalkyl group and an aryl group. , In the formula (III), constitutional units having different R 3 may be present in the same polymer chain.) R a SnX 4-a (i) (In the formula (i), R is an optionally substituted alkyl group having 1 to 12 carbon atoms, an alkenyl group, a cycloalkyl group, an aryl group and an aralkyl group. A group selected from the above, X is an atom or a group selected from a halogen atom, an alkoxy group, an aryloxy group, an acyloxy group and a partial ester residue of phosphoric acid, and a is an integer of 1 to 4. a is 2 In the above cases, R may be the same or different, and when a is 1 or 2, X may be the same or different.) R b SnO c (ii) (However, in the formula (ii), R is the same as R in the formula (i), b is 1 or 2, and when b is 1, c is
It is 3/2, and when b is 2, c is 1. The compound of formula (ii) may form a complex with the compound of formula (i). ) R 1 R 2 SnOSnR 2 R 1 (iii) (However, in the formula (iii), R is R in the formula (i).
And R 1 is the same as R or X in the formula (i). Two R 1's may be the same or different. ) (R 1 3 Sn) d X ′ (iv) (However, in the formula (iv), R 1 is R 1 in the formula (iii).
And at least one is a group selected from R in the formula (i). X'is a group selected from a carbonic acid group, a phosphorus oxygen acid group, a phosphoric acid partial ester residue, a polybasic carboxylic acid group, and a polyhydric alcohol residue. d is a number greater than 1 corresponding to the basicity of X '. )
ンオキシド,プロピレンオキシド,スチレンオキシド,
エピクロロヒドリン,エピブロモヒドリン,アリルグリ
シジルエーテル,ブチルグリシジルエーテル,フェニル
グリシジルエーテルおよび酢酸グリシジルから選ばれる
モノマーである特許請求の範囲第1項記載の共重合体の
製造法。2. The monomer forming the formula (II) is ethylene oxide, propylene oxide, styrene oxide,
The method for producing the copolymer according to claim 1, which is a monomer selected from epichlorohydrin, epibromohydrin, allyl glycidyl ether, butyl glycidyl ether, phenyl glycidyl ether and glycidyl acetate.
Priority Applications (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61010763A JPH0826144B2 (en) | 1986-01-20 | 1986-01-20 | Method for producing polyether copolymer having epoxy group in side chain |
US06/925,270 US4711950A (en) | 1985-11-05 | 1986-10-31 | Polyether polymer or copolymer, monomer therefor, and process for production thereof |
DE3650211T DE3650211T2 (en) | 1985-11-05 | 1986-11-04 | Polyether homo- or copolymer, monomer therefor and process for their preparation. |
EP86308583A EP0222586B1 (en) | 1985-11-05 | 1986-11-04 | Polyether polymer or copolymer, monomer therefor, and process for production thereof |
US07/204,563 USRE33367E (en) | 1985-11-05 | 1988-06-09 | Polyether polymer or copolymer, monomer therefor, and process for production thereof |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61010763A JPH0826144B2 (en) | 1986-01-20 | 1986-01-20 | Method for producing polyether copolymer having epoxy group in side chain |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS62169823A JPS62169823A (en) | 1987-07-27 |
JPH0826144B2 true JPH0826144B2 (en) | 1996-03-13 |
Family
ID=11759370
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP61010763A Expired - Fee Related JPH0826144B2 (en) | 1985-11-05 | 1986-01-20 | Method for producing polyether copolymer having epoxy group in side chain |
Country Status (1)
Country | Link |
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JP (1) | JPH0826144B2 (en) |
Families Citing this family (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AU2651097A (en) * | 1996-05-08 | 1997-11-26 | Daiso Co. Ltd. | Cross-linked solid polyelectrolyte and use thereof |
US6162563A (en) * | 1996-08-20 | 2000-12-19 | Daiso Co., Ltd | Polymer Solid Electrolyte |
EP0838487B1 (en) * | 1996-10-28 | 2003-06-18 | Daiso Co., Ltd. | Polyether copolymer and polymer solid electrolyte |
US6180287B1 (en) | 1996-12-09 | 2001-01-30 | Daiso Co., Ltd. | Polyether copolymer and solid polymer electrolyte |
JP4164131B2 (en) | 1997-06-25 | 2008-10-08 | ダイソー株式会社 | Polyether copolymer, polymer solid electrolyte and battery |
JP3301378B2 (en) * | 1998-03-24 | 2002-07-15 | ダイソー株式会社 | Polyether copolymer and crosslinked polymer solid electrolyte |
JP3491539B2 (en) | 1998-10-13 | 2004-01-26 | ダイソー株式会社 | Polymer solid electrolyte and its use |
US6858351B2 (en) | 2001-11-07 | 2005-02-22 | Daiso Co., Ltd. | Polyethylene oxide-based electrolyte containing silicon compound |
WO2004113443A1 (en) | 2003-06-19 | 2004-12-29 | Daiso Co., Ltd. | Crosslinked polymer electrolyte and use thereof |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3297783A (en) | 1962-11-16 | 1967-01-10 | Union Carbide Corp | Vinyl halide resin plasticized with a linear copolymer of a diepoxide with a 1, 2-alkylene oxide |
US3773694A (en) | 1968-08-16 | 1973-11-20 | Osaka Soda Co Ltd | Process for the polymerization of oxides and catalyst for the polymerization |
-
1986
- 1986-01-20 JP JP61010763A patent/JPH0826144B2/en not_active Expired - Fee Related
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3297783A (en) | 1962-11-16 | 1967-01-10 | Union Carbide Corp | Vinyl halide resin plasticized with a linear copolymer of a diepoxide with a 1, 2-alkylene oxide |
US3773694A (en) | 1968-08-16 | 1973-11-20 | Osaka Soda Co Ltd | Process for the polymerization of oxides and catalyst for the polymerization |
Also Published As
Publication number | Publication date |
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JPS62169823A (en) | 1987-07-27 |
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