首页> 外国专利> INSTALLATION AND PROPYLENE POLYMERIZATION copolymerization of propylene with ethylene and POLYPROPYLENE AND METHOD FOR PRODUCING propylene-ethylene copolymer

INSTALLATION AND PROPYLENE POLYMERIZATION copolymerization of propylene with ethylene and POLYPROPYLENE AND METHOD FOR PRODUCING propylene-ethylene copolymer

机译:丙烯与乙烯和聚丙烯的安装和丙烯聚合共聚以及制备丙烯-乙烯共聚物的方法

摘要

FIELD: chemistry.;SUBSTANCE: invention relates to a technology of production of polypropylene and a copolymer of propylene with ethylene and deals with the field of enhancement and modernisation of the industrial suspension process. Described is a device for a suspension process of polymerisation of propylene or propylene and ethylene in the presence of a catalytic Ziegler system in a medium of a hydrocarbon solvent and hydrogen as the molecular weight regulator. The device contains technological sections connected to each other by technological tubing. Additionally it includes a section of recycling a solvent centrate part in polymerisation reactors and a section of vegetable oil dosing in a stream of the centrate, which is supplied in a section of the solvent separation from an atactic polymer. Partial and regulated centrate recycling from 10 to 50% to the total centrate volume is carried out. Described is a method of obtaining polypropylene at a temperature of 10-90°C and the pressure of propylene of 1-30 atm. The catalytic system includes a titanium magnesium catalyst of the grade LYNX, triethylaluminium, methylcyclohexyldimethoxysilane. The concentration of triethylaluminium is (0.2÷1.0) g/l. Polypropylene is obtained at the molar ratio of Si/Ti=1÷10, and the copolymer of propylene and ethylene at molar ratios of Si/Ti=10÷30.;EFFECT: modernisation of a technological scheme of the propylene polymerisation installation, as well as ensuring high efficiency of exploitation of the catalytic system of the fourth generation.;8 cl, 5 dwg, 12 tbl, 27 ex
机译:技术领域本发明涉及聚丙烯和丙烯与乙烯的共聚物的生产技术,并且涉及工业悬浮法的增强和现代化领域。描述了一种在催化齐格勒系统存在下在烃溶剂和氢作为分子量调节剂的介质中用于丙烯或丙烯和乙烯的聚合的悬浮过程的装置。该设备包含通过工艺管道相互连接的工艺部分。另外,它包括在聚合反应器中再循环溶剂浓缩物部分的部分,以及在浓缩物流中计量植物油的部分,其在从无规聚合物分离溶剂的部分中提供。进行部分和规定的浓缩液回收,占浓缩液总量的10%至5​​0%。描述了一种在10-90℃的温度和1-30大气压的丙烯压力下获得聚丙烯的方法。催化体系包括LYNX级的钛镁催化剂,三乙基铝,甲基环己基二甲氧基硅烷。三乙基铝的浓度为(0.2÷1.0)g / l。聚丙烯以Si / Ti = 1÷10的摩尔比得到,丙烯和乙烯的共聚物以Si / Ti = 10÷30的摩尔比得到;效果:丙烯聚合装置的技术方案的现代化以及确保高效利用第四代催化系统。; 8 cl,5 dwg,12 tbl,27 ex

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