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Production of polyolefins in high condensation mode in turbulent conditions in a fluidized bed.

机译:在流化床中在湍流条件下以高冷凝模式生产聚烯烃。

摘要

A process for alpha-olefin polymerization in gas phase reactor having a fluidized bed and a fluidizing medium wherein the gas phase reactor is operated stably in a mode turbulent operating and wherein the fluidizing medium serves to controlling the cooling capacity of said reactor, the process comprising employing in the fluidizing medium a level of liquid entering the reactor which is at least 17.5 weight percent based on the total weight of the fluidizing medium and wherein the superficial gas velocity is greater than the transition speed bubbling regime to turbulent fluidization U c, and is below the transport velocity Uk, and the ratio of fluidized bulk density to settled bulk density of the resin varies from 0, 4 to 0.55.
机译:在具有流化床和流化介质的气相反应器中进行α-烯烃聚合的方法,其中所述气相反应器以湍流模式稳定运行,并且其中所述流化介质用于控制所述反应器的冷却能力,所述方法包括在流化介质中采用进入反应器的液体水平,该水平至少为流化介质总重量的17.5重量%,并且其中表观气体速度大于湍流流化U c的起泡速度,并且为低于运输速度Uk,并且树脂的流化堆积密度与沉降堆积密度之比在0、4至0.55之间变化。

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