JPH0579245B2 - - Google Patents
Info
- Publication number
- JPH0579245B2 JPH0579245B2 JP26746889A JP26746889A JPH0579245B2 JP H0579245 B2 JPH0579245 B2 JP H0579245B2 JP 26746889 A JP26746889 A JP 26746889A JP 26746889 A JP26746889 A JP 26746889A JP H0579245 B2 JPH0579245 B2 JP H0579245B2
- Authority
- JP
- Japan
- Prior art keywords
- group
- formula
- polymer
- catalyst
- antioxidant
- 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 - Lifetime
Links
- 230000003078 antioxidant effect Effects 0.000 claims description 19
- 239000003963 antioxidant agent Substances 0.000 claims description 16
- 229920000570 polyether Polymers 0.000 claims description 14
- 239000003054 catalyst Substances 0.000 claims description 13
- 150000001875 compounds Chemical class 0.000 claims description 13
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 claims description 7
- 239000000126 substance Substances 0.000 claims description 7
- NBIIXXVUZAFLBC-UHFFFAOYSA-N phosphoric acid Substances OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 claims description 6
- 238000004519 manufacturing process Methods 0.000 claims description 5
- 229910000147 aluminium phosphate Inorganic materials 0.000 claims description 4
- 125000003118 aryl group Chemical group 0.000 claims description 4
- 238000009833 condensation Methods 0.000 claims description 4
- 230000005494 condensation Effects 0.000 claims description 4
- RQXQTENFXIOCLO-UHFFFAOYSA-N 2,6-ditert-butyl-4-(oxiran-2-ylmethoxy)phenol Chemical compound CC(C)(C)C1=C(O)C(C(C)(C)C)=CC(OCC2OC2)=C1 RQXQTENFXIOCLO-UHFFFAOYSA-N 0.000 claims description 3
- 125000003342 alkenyl group Chemical group 0.000 claims description 3
- 125000000217 alkyl group Chemical group 0.000 claims description 3
- 125000004432 carbon atom Chemical group C* 0.000 claims description 3
- 125000000753 cycloalkyl group Chemical group 0.000 claims description 3
- 238000006116 polymerization reaction Methods 0.000 claims description 3
- 125000003710 aryl alkyl group Chemical group 0.000 claims description 2
- 125000001424 substituent group Chemical group 0.000 claims description 2
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 21
- 229920000642 polymer Polymers 0.000 description 13
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 11
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 7
- 238000006243 chemical reaction Methods 0.000 description 6
- MVPPADPHJFYWMZ-UHFFFAOYSA-N chlorobenzene Chemical compound ClC1=CC=CC=C1 MVPPADPHJFYWMZ-UHFFFAOYSA-N 0.000 description 6
- NLZUEZXRPGMBCV-UHFFFAOYSA-N Butylhydroxytoluene Chemical compound CC1=CC(C(C)(C)C)=C(O)C(C(C)(C)C)=C1 NLZUEZXRPGMBCV-UHFFFAOYSA-N 0.000 description 5
- 239000000463 material Substances 0.000 description 4
- 239000000178 monomer Substances 0.000 description 4
- 229910052757 nitrogen Inorganic materials 0.000 description 4
- 235000011007 phosphoric acid Nutrition 0.000 description 4
- 230000000379 polymerizing effect Effects 0.000 description 4
- 238000005979 thermal decomposition reaction Methods 0.000 description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 239000007859 condensation product Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 239000002904 solvent Substances 0.000 description 3
- -1 3,5-di-t-butylphenyl glycidyl thioether Chemical compound 0.000 description 2
- BRLQWZUYTZBJKN-UHFFFAOYSA-N Epichlorohydrin Chemical compound ClCC1CO1 BRLQWZUYTZBJKN-UHFFFAOYSA-N 0.000 description 2
- 239000004721 Polyphenylene oxide Substances 0.000 description 2
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 description 2
- 239000003708 ampul Substances 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 238000006482 condensation reaction Methods 0.000 description 2
- 229920001971 elastomer Polymers 0.000 description 2
- 239000003480 eluent Substances 0.000 description 2
- 229920001002 functional polymer Polymers 0.000 description 2
- 238000004817 gas chromatography Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 238000013508 migration Methods 0.000 description 2
- 230000005012 migration Effects 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000004033 plastic Substances 0.000 description 2
- 229920003023 plastic Polymers 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- YTMCUIACOKRXQA-UHFFFAOYSA-N (2-aminoacetyl) 2-aminoacetate Chemical compound NCC(=O)OC(=O)CN YTMCUIACOKRXQA-UHFFFAOYSA-N 0.000 description 1
- JFGVTUJBHHZRAB-UHFFFAOYSA-N 2,6-Di-tert-butyl-1,4-benzenediol Chemical compound CC(C)(C)C1=CC(O)=CC(C(C)(C)C)=C1O JFGVTUJBHHZRAB-UHFFFAOYSA-N 0.000 description 1
- XNWFRZJHXBZDAG-UHFFFAOYSA-N 2-METHOXYETHANOL Chemical compound COCCO XNWFRZJHXBZDAG-UHFFFAOYSA-N 0.000 description 1
- 101100410162 Caenorhabditis elegans ptc-3 gene Proteins 0.000 description 1
- 239000004593 Epoxy Substances 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- YKGPADHPUQAXRR-UHFFFAOYSA-N O.CC[Zn]CC Chemical compound O.CC[Zn]CC YKGPADHPUQAXRR-UHFFFAOYSA-N 0.000 description 1
- 239000002202 Polyethylene glycol Substances 0.000 description 1
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical group [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 150000001447 alkali salts Chemical group 0.000 description 1
- 125000005907 alkyl ester group Chemical group 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- HTZCNXWZYVXIMZ-UHFFFAOYSA-M benzyl(triethyl)azanium;chloride Chemical compound [Cl-].CC[N+](CC)(CC)CC1=CC=CC=C1 HTZCNXWZYVXIMZ-UHFFFAOYSA-M 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 238000004440 column chromatography Methods 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- JGFBRKRYDCGYKD-UHFFFAOYSA-N dibutyl(oxo)tin Chemical compound CCCC[Sn](=O)CCCC JGFBRKRYDCGYKD-UHFFFAOYSA-N 0.000 description 1
- GYZLOYUZLJXAJU-UHFFFAOYSA-N diglycidyl ether Chemical compound C1OC1COCC1CO1 GYZLOYUZLJXAJU-UHFFFAOYSA-N 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 229920005558 epichlorohydrin rubber Polymers 0.000 description 1
- 150000002118 epoxides Chemical class 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 125000003055 glycidyl group Chemical group C(C1CO1)* 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 239000002530 phenolic antioxidant Substances 0.000 description 1
- 125000004437 phosphorous atom Chemical group 0.000 description 1
- 229920001223 polyethylene glycol Polymers 0.000 description 1
- 239000002685 polymerization catalyst Substances 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 239000011541 reaction mixture Substances 0.000 description 1
- 238000007151 ring opening polymerisation reaction Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 description 1
- 125000000101 thioether group Chemical group 0.000 description 1
- STCOOQWBFONSKY-UHFFFAOYSA-N tributyl phosphate Chemical compound CCCCOP(=O)(OCCCC)OCCCC STCOOQWBFONSKY-UHFFFAOYSA-N 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Polyethers (AREA)
Description
(産業上の利用分野)
本発明は、ゴム或いはプラスチツク等の高分子
材料において、高分子酸化防止剤として有用なポ
リエーテルポリマー及びその製造法に関する。
(従来の技術)
ゴム或いはプラスチツク等の高分子材料は、そ
の酸化劣化を抑制するため、酸化防止剤が通常添
加されているが、高温下では主として揮発や表面
移行によつて、その酸化防止効果が失われる場合
が多い。これを防止する方法の1つとして、酸化
防止作用を有する基をもつモノマーを重合し、高
分子化させることが考えられる。
その際、エピクロルヒドリンゴムなどポリエー
テル系の材料には、相溶性の観点からポリエーテ
ル系の高分子酸化防止剤が望ましい。
しかしながら、側鎖に酸化防止作用をもつポリ
エーテルポリマーはこれまで殆んど開示されてお
らず、唯一つ低分子量のポリ4−ヒドロキシ−
3,5−ジt−ブチルフエニルグリシジルチオエ
ーテルがあるのみである(T.Fujisawaら,J.
Polym.Sci.,Part B12,557(1974))。
(発明が解決しようとする課題)
しかるに、上記ポリマーでは、文献記載の如
く、エポキシ化合物の高重合触媒であるジエチル
亜鉛−水系の触媒を用いても高重合体は得られな
い。その原因の1つとしてフエノール性水酸基又
はチオエーテル基が高重合反応を阻害しているこ
とが考えられる。
(課題を解決するための手段)
以上の点に鑑み本発明者らは酸化防止効果の劣
化しない高分子酸化防止剤を得る目的で鋭意検討
した。その結果側鎖に立体障害フエノール型酸化
防止性基を有する特定のグリジルエーテルを特定
の触媒の存在下で重合させたポリエーテルポリマ
ーが上記目的を十分満足し得ることを見出し、本
発明を完成するに至つたものである。
すなわち、本発明は、繰返し単位が下記式
()で表わされ、80℃において0.1%のクロロベ
ンゼン溶液で測定した還元年度が0.1から3の範
囲であることを特徴とする側鎖に立体障害フエノ
ール型酸化防止性基を有するポリエーテルポリマ
ー()である。
(Industrial Application Field) The present invention relates to a polyether polymer useful as a polymeric antioxidant in polymeric materials such as rubber or plastic, and a method for producing the same. (Prior art) Antioxidants are usually added to polymeric materials such as rubber or plastics in order to suppress their oxidative deterioration, but at high temperatures the antioxidant effect is lost mainly through volatilization and surface migration. is often lost. One possible method for preventing this is to polymerize a monomer having a group having an antioxidant effect to form a polymer. In this case, from the viewpoint of compatibility, a polyether-based polymeric antioxidant is preferable for polyether-based materials such as epichlorohydrin rubber. However, very few polyether polymers with antioxidant activity in their side chains have been disclosed, and the only low molecular weight polyether polymer is poly(4-hydroxy-
There is only 3,5-di-t-butylphenyl glycidyl thioether (T. Fujisawa et al., J.
Polym. Sci., Part B12, 557 (1974)). (Problems to be Solved by the Invention) However, as described in the literature, a high polymer cannot be obtained even if a diethylzinc-water catalyst, which is a high polymerization catalyst for an epoxy compound, is used. One of the reasons for this is thought to be that the phenolic hydroxyl group or thioether group inhibits the high polymerization reaction. (Means for Solving the Problems) In view of the above points, the present inventors conducted extensive studies with the aim of obtaining a polymeric antioxidant whose antioxidant effect does not deteriorate. As a result, it was discovered that a polyether polymer obtained by polymerizing a specific glycyl ether having a sterically hindered phenol type antioxidant group in the side chain in the presence of a specific catalyst can fully satisfy the above objectives, and the present invention was completed. This is what I came to do. That is, the present invention provides a sterically hindered phenol in the side chain whose repeating unit is represented by the following formula ( It is a polyether polymer () with type antioxidant groups.
【化】
また本発明は、下記式()で表わされる化合
物4−ヒドロキシ−3,5−ジ−t−ブチルフエ
ニルグリシジルエーテルを下記一般式()で表
わされる有機錫化合物(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立体障害フエノー
ル型酸化防止性基を有するポリエーテルポリマー
の製造法である。[Chemical formula] The present invention also provides a method for combining the compound 4-hydroxy-3,5-di-t-butylphenyl glycidyl ether represented by the following formula () with an organotin compound (A) represented by the following general formula (). This is a method for producing a polyether polymer having a sterically hindered phenol type antioxidant group in the side chain, which is characterized by polymerizing in the presence of a catalyst that is a thermal condensation product with an acid alkyl ester (B).
【化】
RbSnOc (i)
(但し、()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。)
本発明のポリマーの原料モノマーである上記式
()の化合物は本出願人の出願に係る新規の物
質である(特開平2−129178号)。この化合物は、
2,6−ジ−t−ブチルヒドロキノンとエピクロ
ルヒドリンとを公知の方法により第4級塩基性塩
及び塩基の存在下で反応させることによつて合成
することができる。
本発明は、本出願人の米国特許第3773694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上記式
()の化合物であるエポキシドの開環重合用触
媒として選択的に作用し、生成ポリマーも側鎖に
立体障害フエノール型酸化防止性基をもつ高機能
性ポリマーとして非常に有効であることを見出し
たことに基づいている。
本発明の触媒成分である上記()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。
一般式()に属する化合物としては、
(CH3)2SnO,(C4H9)2SnO,(C8H17)2SnO,
(C6H5)2SnO,CH3SnO3/2C4H9SnO3/2などが挙
げられる。
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()
で表わされる正リン酸の完全若しくは部分エステ
ルが特に好ましく用いられる。
(R2O)3P=O ()
(但し、()式において、R2は水素若しくは
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、少なくともR2のうち1
個は水素原子以外の基である。)
上記()式の具体的な例としては、
(C2H5)3PO4,(C3H7)3PO4,(C4H9)3PO4,
(C8H17)3PO4,(CH2=CH−CH2)3PO4,(C6
H11)3PO4,
(ClCH2−CH2)3PO4,(Cl2C3H5)3PO4,
(C2H5)2HPO4,(C4H9)2HPO4,(C4H9)H2
PO4などが挙げられる。
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つ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。
上記触媒生成反応において、(A)成分及び(B)成分
の種類に従つ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
によつて異なるが、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つて不溶化する。
本発明のポリマー()は、上記縮合生成物を
触媒として()式化合物4−ヒドロキシ−3,
5−ジ−t−ブチルフエニルグリシジルエーテル
を溶媒の存在下又は非存在下に0〜80℃で通常攪
拌又は振盪下で重合させることによつて得られ
る。触媒の使用量は原料モノマー100重量部に対
して0.01〜3.0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。
生成ポリマーは、80℃において0.1%のクロロ
ベンゼン溶液で測定した還元粘度が0.1から3の
範囲、好ましくは0.5から3の範囲のものが適当
である。0.1以下では、酸化防止剤として用いる
際、揮発表面移行或いは抽出等が生ずるおそれが
あり、十分な効果が得られない。
(発明の効果)
本発明のポリマーは、新規な立体障害フエノー
ル型酸化防止性基をもつグリシジルエーテルをモ
ノマーとし、特定の触媒を用いて重合させること
によつて得られる、側鎖に酸化防止性基を有する
新規なポリエーテルポリマーであり、高分子量酸
化防止剤として有用な高機能ポリマーである。
(実施例)
実施例 1
(1) 4−ヒドロキシ−3,5−ジ−t−ブチルフ
エニルグリシジルエーテルの合成
攪拌器、温度計、窒素導入口と出口とを備えた
3フラスコに、2,6−ジ−t−ブチルヒドロ
キノン320g、エピクロルヒドリン1200g及びトリ
エチルベンジルアンモニウムクロリド6.6gを加
え、58〜61℃に保ちながら窒素気流下48%水酸化
ナトリウム水溶液144gを2時間で滴下し、滴下
後更に6時間この温度に保持した。
反応後濾過し、濾液から水層を分離した後これ
を濃縮すると395gの油状物質が得られた。これ
をベンゼンを溶離液としてアルミナでカラムクロ
マトグラフイーを行ない、ベンゼン溶離液を濃縮
してガスクロマトグラフイー純度95%の生績体
328gを得た(粗収率82%)。これをn−ヘキサン
で3回再結晶してガスクロマトグラフイー純度99
%以上の結晶172gを得た(収率43%)。融点55.0
〜56.0℃。
NMR (CDCl3,TMS内部基準)
δ1.44(18H,t−C4H9)
δ2.75〜4.15(5H,グリシジル基)
δ4.80(1H,水酸基)
δ6.80(2H,芳香族)
IR(KBr) νOH 3430cm-1
(2) ポリエーテルポリマーの製造
攪拌器、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サイド12.5g、トリブチ
ルホスフエート26.6gを入れ、窒素気流下に攪拌
しながら250℃で20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つた。
内容量50mlのガラス製アンプルの内部を窒素置
換し、上記触媒59mgと水分10ppm以下の上記4−
ヒドロキシ−3,5−ジ−t−ブチルフエニルグ
リシジルエーテルの25%ベンゼン溶液20mlを仕込
み、封管後アンプルを振盪しながら30℃で120時
間反応させた。
反応後反応物をヘキサン500ml中に投入してポ
リマーを析出させ、ヘキサンを傾斜除去し、減圧
乾燥してポリマー()4.1gを得た(収率83%)。
このポリマー()の80℃において0.1%クロ
ロベンゼン溶液で測定した還元粘度は2.14であつ
た。
NMR (CDCl3,TMS内部基準)
δ1.34(18H,t−C4H9)
δ4.66(1H,水酸基)
δ6.67(2H,芳香族)
IR(KBr) νOH 3610cm-1
実施例 2
実施例1においてベンゼンの代りにテトラヒド
ロフランを用いた以外は実施例1(2)と同様に反応
させて、ポリマー3.8gを得た(収率77%)。
このポリマーの80℃において0.1%クロロベン
ゼン溶液で測定した還元粘度は0.98であつた。
実施例 3
実施例1で得たポリエーテルポリマー()の
酸化防止機能を調べるために、下記のようにポリ
エチレングリコールモノメチルエーテル(Mn=
2000,以下PEG−Mという。)に添加してその熱
分解温度を測定した。理学電機(株)製示差熱天秤
「PTC−3」を使用し、空気雰囲気中、昇温速度
10℃/minの測定条件で行つた。
すなわち、夫々ポリマー()5mg,10mgをベ
ンゼン5mlに溶解させた溶液中に、PEG−M1g
を添加し、室温で乾燥して、0.5%()添加の
試料A,1.0%()添加の試料Bを得た。
試料A、試料Bの熱分解開始温度は夫々164℃,
170℃であつた。一方、無添加のPEG−Mの熱分
解開始温度は135℃であつた。
比較例
夫々4−ヒドロキシ−3,5−ジ−tブチルト
ルエン(BHT)5mg,10mgをベンゼン5mlに溶
解させた溶液中に、PEG−M1gを添加し、室温
で乾燥して、0.5%BHT添加の試料C、1.0%
BHT添加の試料Dを得た。
試料C、試料Dの熱分解開始温度は夫々151℃,
154℃であつた。
上記の実施例3及び比較例の試験結果により、
本発明のポリエーテルポリマーが、一般に良好な
酸化防止剤として知られるBHTと比較して、優
れた酸化防止能を有し、高分子量酸化防止剤とし
て有用であることが分る。[Chemical formula] RbSnOc (i) (However, in formula (), R is selected from an alkyl group having 1 to 12 carbon atoms which may have a substituent, an alkenyl group, a cycloalkyl group, an aryl group, and an aralkyl group. (b is 1 or 2, when b is 1, c is 3/2, and when b is 2, c is 1.) The above formula () which is a raw material monomer of the polymer of the present invention The compound is a new substance filed by the present applicant (Japanese Patent Application Laid-Open No. 129178/1999). This compound is
It can be synthesized by reacting 2,6-di-t-butylhydroquinone and epichlorohydrin in the presence of a quaternary basic salt and a base by a known method. The present invention provides that the thermal condensation product of a specific organotin compound (A) and a phosphoric acid alkyl ester (B) described in U.S. Patent No. 3,773,694 by the present applicant is a compound of the above formula (). This is based on the discovery that it acts selectively as a catalyst for the ring-opening polymerization of epoxides, and that the resulting polymer is also highly effective as a highly functional polymer having sterically hindered phenolic antioxidant groups in its side chains. Specific examples of the organotin compound (A) of the above formula () which is a catalyst component of the present invention include the following. Compounds belonging to general formula () 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 Examples include C 4 H 9 SnO 3/2 . The phosphoric acid alkyl ester (B), which is another component constituting the catalyst of the present invention, has the following general formula ()
A complete or partial ester of orthophosphoric acid represented by is particularly preferably used. (R 2 O) 3 P=O () (However, in formula (), R 2 is hydrogen or an alkyl group, alkenyl group, or cycloalkyl group having 2 or more carbon atoms, and at least one of R 2
is a group other than a hydrogen atom. ) Specific examples of the above formula () are: (C 2 H 5 ) 3 PO 4 , (C 3 H 7 ) 3 PO 4 , (C 4 H 9 ) 3 PO 4 , (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 ) 3 PO 4 , (C 2 H 5 ) 2 HPO 4 , (C 4 H 9 ) 2 HPO 4 , ( C4H9 ) H2
Examples include PO 4 . 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 to 300°C. A solvent may be used if necessary.
The above components (A) and (B) are used so that the ratio of tin atoms to phosphorus atoms contained is usually in the range of 1:10 to 10:1. In the above catalyst production reaction, various relatively simple substances are produced and eliminated in the condensation reaction depending on the types of components (A) and (B). The resulting condensate exhibits the desired activity at various stages of the degree of condensation. The optimal degree of condensation varies depending on the type and ratio of components (A) and (B), but can be easily determined experimentally. The condensate is generally initially soluble in a solvent such as hexane or benzene, but becomes insolubilized as the condensation reaction progresses. The polymer () of the present invention is a compound of the formula (4-hydroxy-3,
It is obtained by polymerizing 5-di-t-butylphenyl glycidyl ether in the presence or absence of a solvent at 0 to 80°C, usually with stirring or shaking. The appropriate amount of the catalyst to be used is 0.01 to 3.0 parts by weight per 100 parts by weight of the raw material monomer. During the reaction, it is desirable to keep the water content of the reaction system as low as possible. The resulting polymer suitably has a reduced viscosity in the range of 0.1 to 3, preferably in the range of 0.5 to 3, as measured in a 0.1% chlorobenzene solution at 80°C. If it is less than 0.1, when used as an antioxidant, there is a risk that volatile surface migration or extraction will occur, and sufficient effects will not be obtained. (Effects of the Invention) The polymer of the present invention is obtained by polymerizing a glycidyl ether having a novel sterically hindered phenol type antioxidant group as a monomer using a specific catalyst. It is a novel polyether polymer having groups, and is a highly functional polymer useful as a high molecular weight antioxidant. (Example) Example 1 (1) Synthesis of 4-hydroxy-3,5-di-t-butylphenyl glycidyl ether In 3 flasks equipped with a stirrer, a thermometer, a nitrogen inlet and an outlet, 2, Add 320 g of 6-di-t-butylhydroquinone, 1200 g of epichlorohydrin, and 6.6 g of triethylbenzylammonium chloride, and dropwise add 144 g of a 48% aqueous sodium hydroxide solution under a nitrogen stream while maintaining the temperature at 58 to 61°C over 2 hours. It was held at this temperature for an hour. After the reaction, the reaction mixture was filtered, and the aqueous layer was separated from the filtrate and concentrated to obtain 395 g of an oily substance. This was subjected to column chromatography on alumina using benzene as an eluent, and the benzene eluent was concentrated and gas chromatography was performed to obtain a living body with a purity of 95%.
Obtained 328g (crude yield 82%). This was recrystallized three times from n-hexane and the gas chromatography purity was 99.
% or more crystals were obtained (yield 43%). Melting point 55.0
~56.0℃. NMR (CDCl 3 , TMS internal standard) δ1.44 (18H, t-C 4 H 9 ) δ2.75-4.15 (5H, glycidyl group) δ4.80 (1H, hydroxyl group) δ6.80 (2H, aromatic) IR (KBr) ν OH 3430cm -1 (2) Production of polyether polymer Put 12.5 g of dibutyltin oxide and 26.6 g of tributyl phosphate into a three-necked flask equipped with a stirrer, thermometer, and distillation device, and stir under a nitrogen stream. While heating at 250° C. for 20 minutes, the distillate was distilled off, and a solid condensation material was obtained as a residue. The following polymerization was carried out using this product as a catalyst. The inside of a glass ampoule with a content capacity of 50 ml was replaced with nitrogen, and 59 mg of the above catalyst and the above 4-3 with a moisture content of 10 ppm or less were added.
20 ml of a 25% benzene solution of hydroxy-3,5-di-t-butylphenyl glycidyl ether was charged, and after sealing the tube, the ampoule was reacted at 30° C. for 120 hours with shaking. After the reaction, the reaction product was poured into 500 ml of hexane to precipitate a polymer, the hexane was decanted, and the mixture was dried under reduced pressure to obtain 4.1 g of polymer () (yield: 83%). The reduced viscosity of this polymer () measured with a 0.1% chlorobenzene solution at 80°C was 2.14. NMR (CDCl 3 , TMS internal standard) δ1.34 (18H, t-C 4 H 9 ) δ4.66 (1H, hydroxyl group) δ6.67 (2H, aromatic) IR (KBr) ν OH 3610cm -1 Example 2 The reaction was carried out in the same manner as in Example 1 (2) except that tetrahydrofuran was used instead of benzene in Example 1 to obtain 3.8 g of polymer (yield 77%). The reduced viscosity of this polymer measured in a 0.1% chlorobenzene solution at 80°C was 0.98. Example 3 In order to investigate the antioxidant function of the polyether polymer () obtained in Example 1, polyethylene glycol monomethyl ether (Mn=
2000, hereinafter referred to as PEG-M. ) and its thermal decomposition temperature was measured. Using a differential thermal balance “PTC-3” manufactured by Rigaku Denki Co., Ltd., we measured the temperature increase rate in an air atmosphere.
The measurement conditions were 10°C/min. That is, 1 g of PEG-M was added to a solution of 5 mg and 10 mg of polymer () dissolved in 5 ml of benzene.
was added and dried at room temperature to obtain sample A with 0.5% () addition and sample B with 1.0% () addition. The starting temperature of thermal decomposition of Sample A and Sample B is 164℃, respectively.
It was 170℃. On the other hand, the thermal decomposition onset temperature of additive-free PEG-M was 135°C. Comparative Example 1 g of PEG-M was added to a solution of 5 mg and 10 mg of 4-hydroxy-3,5-di-t-butyltoluene (BHT) dissolved in 5 ml of benzene, dried at room temperature, and 0.5% BHT was added. Sample C, 1.0%
Sample D with BHT added was obtained. The thermal decomposition onset temperatures of Sample C and Sample D are 151℃ and 151℃, respectively.
It was 154℃. According to the test results of Example 3 and Comparative Example above,
It can be seen that the polyether polymer of the present invention has superior antioxidant ability compared to BHT, which is generally known as a good antioxidant, and is useful as a high molecular weight antioxidant.
Claims (1)
℃において0.1%のクロロベンゼル溶液で測定し
た還元粘度が0.1から3の範囲であることを特徴
とする側鎖に立体障害フエノール型酸化防止性基
を有するポリエーテルポリマー。 【化】 2 下記式()で表わされる化合物4−ヒドロ
キシ−3,5−ジ−t−ブチルフエニルグリシジ
ルエーテルを下記一般式()で表わされる有機
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
とする請求項1に記載の側鎖に立体障害フエノー
ル型酸化防止基を有するポリエーテルポリマーの
製造法。 【化】 RbSnOc (i) (但し、()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。)[Claims] 1. The repeating unit is represented by the following formula (), and 80
A polyether polymer having a sterically hindered phenol type antioxidant group in a side chain, characterized in that the reduced viscosity measured in a 0.1% chlorobenzel solution at °C is in the range of 0.1 to 3. [Chemical formula] 2 Thermal condensation of the compound 4-hydroxy-3,5-di-t-butylphenyl glycidyl ether represented by the following formula () with an organotin compound represented by the following general formula () and a phosphoric acid alkyl ester. 2. The method for producing a polyether polymer having a sterically hindered phenol type antioxidant group in a side chain according to claim 1, wherein the polymerization is carried out in the presence of a catalyst as a product. [Chemical formula] RbSnOc (i) (However, in formula (), R is selected from an alkyl group having 1 to 12 carbon atoms which may have a substituent, an alkenyl group, a cycloalkyl group, an aryl group, and an aralkyl group. (b is 1 or 2; when b is 1, c is 3/2; when b is 2, c is 1).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP26746889A JPH03128931A (en) | 1989-10-13 | 1989-10-13 | Polyether polymer having antioxidant group and its production |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP26746889A JPH03128931A (en) | 1989-10-13 | 1989-10-13 | Polyether polymer having antioxidant group and its production |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH03128931A JPH03128931A (en) | 1991-05-31 |
| JPH0579245B2 true JPH0579245B2 (en) | 1993-11-01 |
Family
ID=17445263
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP26746889A Granted JPH03128931A (en) | 1989-10-13 | 1989-10-13 | Polyether polymer having antioxidant group and its production |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH03128931A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101989727B1 (en) | 2015-08-26 | 2019-06-14 | 에보니크 데구사 게엠베하 | Use of specific polymers as charge carriers |
| EP3262094B1 (en) | 2015-08-26 | 2018-12-26 | Evonik Degussa GmbH | Use of certain polymers as charge storage |
-
1989
- 1989-10-13 JP JP26746889A patent/JPH03128931A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPH03128931A (en) | 1991-05-31 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CA2244597A1 (en) | A process for the preparation of high-purity organosilicon disulphanes | |
| US4948888A (en) | Process for the preparation of stabilizers for organic polymers | |
| KR0171398B1 (en) | Organosilane compounds | |
| US4709054A (en) | Silylation method and organic silanes made therefrom | |
| US4414384A (en) | Synthesis and polymerization of 3-azidooxetane | |
| US4467105A (en) | Method of preparing glycol esters of organosilanes | |
| Soga et al. | Alternating copolymerization of propylene oxide and carbon dioxide with an alumina supported diethylzinc catalyst | |
| US3598866A (en) | Adducts of alkenyl isocyanates with bisphenol a and derivatives thereof | |
| JPH0579245B2 (en) | ||
| US4604477A (en) | Method for making silylaroylhalides and reaction products | |
| JPH0826144B2 (en) | Method for producing polyether copolymer having epoxy group in side chain | |
| EP0112434B1 (en) | Hydrogen bearing silyl carbamates | |
| US6759461B2 (en) | Phenolic phosphite antioxidants and polymer compositions containing said antioxidant | |
| US5449736A (en) | Water soluble phosphorylated polysiloxanes | |
| US5900494A (en) | Method of making d,l-α-tocopherol | |
| KR100321296B1 (en) | Temperature-sensitive cyclotriphosphazene derivatives and their preparation method | |
| US3564036A (en) | Preparation of di-lithio (perfluoroalkylethylsilyl) neocarboranes | |
| Borisov et al. | Preparation of bis (ω-hydroxyalkl) phosphites and polyurethanes from them | |
| Varbanov et al. | Furfuryl-containing tertiary phosphine oxides and polymers based on some of them | |
| US3678093A (en) | Process for the preparation of 2-(hydroxyhydrocarbyl)acrylates | |
| JP3022008B2 (en) | Composition comprising a mixture of t-butoxy carbonates of trisphenols | |
| Ulrich et al. | Reaction of phosgene with N-methyleneaniline derivatives | |
| JP4110844B2 (en) | Method for producing hydroxyaldehydes | |
| RU2283826C1 (en) | Method for production of 3,6-dimethyl-1,8-dialkyl(phenyl)-2,6-octadiens | |
| US4960919A (en) | Process for the preparation of alkyl alkenylphosphinates |