首页> 外国专利> PROCESS FOR PREPARING HIGHER MOLECULAR WEIGHT POLYEPOXIDE PRODUCTS BY REACTING A POLYEPOXIDE WITH A PHENOL IN PRESENCE OF TETRAALKYLAMMONIUM HALIDES

PROCESS FOR PREPARING HIGHER MOLECULAR WEIGHT POLYEPOXIDE PRODUCTS BY REACTING A POLYEPOXIDE WITH A PHENOL IN PRESENCE OF TETRAALKYLAMMONIUM HALIDES

机译:在存在四烷基铵的情况下通过与苯酚反应聚环氧乙烷制备更高分子量的聚环氧乙烷产品的方法

摘要

1364804 Polyepoxides SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ NV 19 Jan 1973 [21 Jan 1972] 3101/72 Heading C3B A polyepoxide product is prepared by condensing a polyhydric phenol at a temperature of 120-200‹ C. with a polyepoxide starting material having a molecular weight which is below 3500 which is lower than the M.wt. of the polyepoxide product, in the presence of from 0-1% wt., based on polyepoxide starting material, of an inert solvent having an atmospheric boiling point of at least 140‹ C. and which is miscible with the product and reactants, and in the presence of 0À05 to 2 milliequivalents of a quaternary ammonium halide catalyst per 100 g. of polyepoxide starting material, the initial ratio of phenolic hydroxyl groups to epoxy group being below 1 : 1À05. Preferred polyepoxide starting materials are glycidyl polyethers of polyhydric phenols such as Novolac resins, 1,1 - bis - (4 - hydroxyphenyl)ethane, bis - (4 - hydroxyphenyl)methane, bis - (4- hydroxyphenyl)sulphone and 2,2 - bis - (4- hydroxyphenyl)propane. Preferred polyhydric phenols are bisphenols particularly 2,2-bis- (hydroxyphenyl)propane. Preferred catalysts are tetra-alkylammonium halides. In Examples 1 and 2 polyepoxides are prepared in the absence of an inert solvent by condensing either (I) 2,2 - bis - (4 - hydroxyphenyl)propane or (II) a mixture of (I) with a minor amount of 2-(4- hydroxyphenyl) - 2 - (2 - hydroxyphenyl)propane with either the diglycidyl ether of (I) or the diglycidyl ether of (II) in the presence of tetramethylammonium chloride as catalyst. The polyepoxide products were mixed with a polyamino-amide curing agent (VERSAMID, Registered Trade Mark), titania pigment and an organic solvent and sprayed on to steel panels. The coatings were cured at 23‹ C. for 7 days. In Example 4 similar polyepoxides are prepared using instead as catalyst either hexadecyltrimethylammonium bromide or glycidyl trimethylammonium chloride.
机译:1364804聚环氧化物壳牌国际研究公司(MAATSCHAPPIJ NV)1973年1月19日[1972年1月21日] 3101/72标题C3B通过在120-200°C的温度下将多元酚与分子量为低于3500,低于M.wt。在多聚环氧化合物原料的0-1%(重量)存在下,一种常压沸点至少为140℃的惰性溶剂,该惰性溶剂可与该产物和反应物混溶;每100克存在0‑05至2毫克当量的卤化季铵催化剂。在多环氧化物原料中,酚羟基与环氧基的初始比例低于1∶1-5。优选的聚环氧化物原料是多元酚的缩水甘油基聚醚,例如酚醛清漆树脂,1,1-双-(4-羟基苯基)乙烷,双-(4-羟基苯基)甲烷,双-(4-羟基苯基)砜和2,2-双-(4-羟苯基)丙烷。优选的多元酚是双酚,特别是2,2-双-(羟基苯基)丙烷。优选的催化剂是四烷基卤化铵。在实施例1和2中,在不存在惰性溶剂的情况下,通过缩合(I)2,2-双-(4-羟苯基)丙烷或(II)(I)与少量2-的混合物制备聚环氧化物。 (4-羟苯基)-2-(2-羟苯基)丙烷与(I)的二环氧甘油醚或(II)的二环氧甘油醚在氯化四甲基铵的存在下作为催化剂。将聚环氧化物产物与聚氨基酰胺固化剂(VERSAMID,注册商标),二氧化钛颜料和有机溶剂混合,并喷涂到钢板上。该涂层在23℃下固化7天。在实施例4中,使用十六烷基三甲基溴化铵或缩水甘油基三甲基氯化铵代替催化剂制备类似的聚环氧化物。

著录项

  • 公开/公告号US3824212A

    专利类型

  • 公开/公告日1974-07-16

    原文格式PDF

  • 申请/专利权人 SHELL OIL COUS;

    申请/专利号US19730324698

  • 发明设计人 SINNEMA FNL;VAN ZWET HNL;

    申请日1973-01-18

  • 分类号C08G30/04;

  • 国家 US

  • 入库时间 2022-08-23 04:56:30

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