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GAS PHASE FLUIDIZED BED METHOD AND ETHYLENE HOMO- AND COPOLYMERS OBTAINED USING SAID METHOD

机译:气相流化床方法和采用均值法获得的乙烯均聚物和共聚物

摘要

A continuous vapor-phase fluidized-bed process for the preparation of ethylene homopolymers and copolymers having a density of from 0.87 to 0.97 g/cm3 in which ethylene or mixtures of ethylene and C3-C8 a-monoolefins are (co)polymerized in the presence of a supported chromium catalyst in the polymerization zone of a vapor-phase fluidized-bed reactor under pressures ranging from 1 to 100 bar and at temperatures ranging from 30° to 125° C. in the vapor phase in an agitated bed of bulk material comprising particulate polymer, the resultant heat of polymerization is removed by cooling the recirculated reactor gas and the resulting (co)polymer is removed from the vapor-phase fluidized-bed reactor, wherein, for the preparation of a (co)polymer of a specific density d, the (co)polymerization is carried out at a temperature which is in a range restricted by an upper envelope defined by equation Iand a lower envelope defined by equation IIin which the variables have the following meanings:TH is the highest reaction temperature in ° C.;TL is the lowest reaction temperature in ° C.;d' is the numerical value of the density d of the (co)polymer to be synthesized.
机译:用于制备密度为0.87至0.97g / cm 3的乙烯均聚物和共聚物的连续气相流化床方法,其中使乙烯或乙烯与C 3 -C 8α-单烯烃的混合物进行(共)聚合在气相流化床反应器的聚合区中在负载铬催化剂的存在下,在压力为1至100 bar,温度为30至125°C的气相搅拌床中包含颗粒状聚合物的松散材料,通过冷却再循环的反应器气体除去聚合反应产生的热量,并将所得的(共)聚合物从气相流化床反应器中除去,其中,为了制备在特定密度d的条件下,(共)聚合反应的温度在方程式I定义的上包络线和方程式II定义的下包络线所限制的范围内,其中变量具有以下含义:是最高的反应温度,以℃为​​单位; TL是最低的反应温度,以℃为​​单位; d'是要合成的(共)聚合物的密度d的数值。

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