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    • 7. 发明申请
    • PROCESS FOR COPOLYMERIZING ETHYLENE AND ESTERS OF VINYL ALCOHOL
    • 乙烯醇和乙烯醇共聚合方法
    • WO2014095708A1
    • 2014-06-26
    • PCT/EP2013/076683
    • 2013-12-16
    • BASELL POLYOLEFINE GMBH
    • FINETTE, Andre-ArmandWOLF, ChristophKHAYRULLIN, DanirMEI, GiuliaMOHRBUTTER, JuergenLITTMANN, Dieter
    • C08F210/02C08F2/00C07C67/54
    • C08F210/02C08F2/00C08F218/08
    • Process for copolymerizing ethylene and esters of vinyl alcohol in the presence of free-radical polymerization initiators at pressures in the range of from 110 MPa to 500 MPa and temperatures in the range of from 100°C to 350°C in a continuously operated polymerization apparatus comprising a polymerization reactor and one or more compressors, which compress the monomer mixture fed to the polymerization reactor to the polymerization pressure, wherein the monomer mixture is compressed by a sequence of compression stages in which the compressed gas mixture is cooled after each compression stage and the fraction of the monomer mixture, which is liquid after this cooling, is separated off and returned to the polymerization apparatus in liquid form, and wherein at least a part of the liquid fractions obtained after compressing the monomer mixture in the respective compression stage to a pressure of from 0.2 MPa to 10 MPa is purified before being returned to the polymerization process.
    • 在自由基聚合引发剂的存在下,在连续操作的聚合装置中在110MPa至500MPa的范围内和在100℃至350℃的温度范围内共聚乙烯和乙烯醇的酯的方法 包括聚合反应器和一个或多个压缩机,其将进料到聚合反应器的单体混合物压缩至聚合压力,其中单体混合物通过一系列压缩阶段压缩,其中压缩气体混合物在每个压缩阶段之后被冷却, 在该冷却后液体的单体混合物的分数被分离出并返回到液体形式的聚合装置中,并且其中在各个压缩阶段将单体混合物压缩后获得的至少一部分液体馏分为 在返回到聚合过程之前,将0.2MPa至10MPa的压力进行纯化。
    • 8. 发明申请
    • MULTISTAGE PROCESS FOR THE POLYMERIZATION OF OLEFINS
    • 烯烃聚合的多步法
    • WO2013083548A2
    • 2013-06-13
    • PCT/EP2012/074324
    • 2012-12-04
    • BASELL POLYOLEFINE GMBH
    • COVEZZI, MassimoPENZO, GiuseppeMEI, GabrieleMEI, GiuliaBAITA, PietroMEIER, GerhardusDE LUCIA, AntonioSCHUELLER, UlfFERRARO, Gianpiero
    • C08F10/00
    • C08F110/02C08F2/001C08F2/34C08F10/00C08F10/02C08F2500/12C08F2500/18C08F2500/24C08F2/00C08F2/01
    • Process for transferring polyolefin particles from a first gas-phase polymerization reactor to a second gas-phase polymerization reactor in a multistage polymerization of olefins carried out in at least two serially connected gas-phase polymerization reactors, wherein the first gas-phase reactor is a fluidized-bed reactor comprising a gas distribution grid and a settling pipe, which is integrated with its upper opening into the distribution grid and contains a bed of polyolefin particles which moves from top to bottom of the settling pipe, the process comprising the steps of introducing a fluid into the settling pipe in an amount that an upward stream of the fluid is induced in the bed of polyolefin particles above the fluid introduction point; withdrawing polyolefin particles from the lower end of the settling pipe; and transferring the withdrawn polyolefin particles into the second gas-phase polymerization reactor, process for polymerizing olefins comprising such a process for transferring polyolefin particles, reactor suitable as first gas-phase polymerization reactor in the process for polymerizing olefins and process for discharging polyolefin particles from a fluidized-bed reactor.
    • 将聚烯烃颗粒从第一气相聚合反应器转移到第二气相聚合反应器中在至少两个串联连接的气相聚合反应器中进行的烯烃的多级聚合中的方法,其中 第一气相反应器是流化床反应器,其包括气体分配格栅和沉降管,沉降管与其上部开口一体形成分配格栅并且包含聚合物颗粒床,所述聚合物颗粒床从沉降管的顶部移动到底部 所述方法包括以下步骤:将流体引入沉降管中的量为在流体引入点上方的聚烯烃颗粒床中引起流体的向上流; 从沉降管的下端排出聚烯烃颗粒; 和将取出的聚烯烃颗粒转移到第二气相聚合反应器中的方法,包括这种转移聚烯烃颗粒的方法的烯烃聚合方法,适合作为烯烃聚合方法中的第一气相聚合反应器的反应器以及从 一个流化床反应器。