COMPRESSIBLE LIQUID DILUENT IN POLYOLEFIN POLYMERIZATION
    3.
    发明申请
    COMPRESSIBLE LIQUID DILUENT IN POLYOLEFIN POLYMERIZATION 审中-公开
    聚烯烃聚合中的可压缩液体稀释

    公开(公告)号:US20160346750A1

    公开(公告)日:2016-12-01

    申请号:US15169190

    申请日:2016-05-31

    IPC分类号: B01J8/00 B01J19/00 B01J19/18

    摘要: Embodiments of the present application provide a method for manufacturing a polyolefin and a system for implementing the method. The method comprises combining a catalyst with a diluent mixture containing a diluent and an olefin monomer in a polymerization reactor. The diluent may comprise propane, butane, or isobutane, or a combination thereof. The polymerization reactor is operated at a pressure above a critical pressure of the diluent, but below the critical temperature of the diluent.

    摘要翻译: 本发明的实施方案提供了制造聚烯烃的方法和用于实施该方法的系统。 该方法包括在聚合反应器中将催化剂与含有稀释剂和烯烃单体的稀释剂混合物组合。 稀释剂可以包括丙烷,丁烷或异丁烷,或其组合。 聚合反应器在高于稀释剂的临界压力但低于稀释剂的临界温度的压力下操作。

    Polymerization product pressures in olefin polymerization
    6.
    发明授权
    Polymerization product pressures in olefin polymerization 有权
    烯烃聚合中的聚合产物压力

    公开(公告)号:US09120886B2

    公开(公告)日:2015-09-01

    申请号:US14447973

    申请日:2014-07-31

    摘要: A process for making a low density polymer in a polymerization reactor system, the process comprising polymerizing an olefin monomer, and optionally an olefin comonomer, in the presence of a diluent in a polymerization reactor to make a polymerization product slurry consisting of a liquid phase and a solid phase, wherein the solid phase comprises an olefin polymer having a density of between about 0.905 g/cm3 to about 0.945 g/cm3; and discharging the polymerization product slurry from the polymerization reactor through a continuous take-off valve to make a mixture further comprising a vapor phase. The mixture comprises a pressure less than a bubble point pressure of a component in the polymerization product slurry.

    摘要翻译: 一种在聚合反应器系统中制备低密度聚合物的方法,该方法包括在稀释剂存在下在聚合反应器中聚合烯烃单体和任选的烯烃共聚单体以制备由液相和 固相,其中所述固相包含密度为约0.905g / cm 3至约0.945g / cm 3的烯烃聚合物; 并通过连续的取出阀将聚合产物浆料从聚合反应器排出,以制备进一步包含气相的混合物。 该混合物包含小于聚合产物浆料中组分的泡泡点压力的压力。