GAS-PHASE OLEFIN POLYMERIZATION PROCESS
    51.
    发明授权
    GAS-PHASE OLEFIN POLYMERIZATION PROCESS 有权
    方法的烯烃气相聚合

    公开(公告)号:EP1613668B1

    公开(公告)日:2012-08-08

    申请号:EP04725050.1

    申请日:2004-04-01

    Abstract: A continuous process for the olefin polymerization in a fluidized bed reactor, said process comprising continuously passing a gaseous stream comprising one or more α-olefin monomers through the fluidized bed in the presence of a polymerization catalyst under reactive conditions, withdrawing polymeric product and unreacted fluids from the reactor, cooling part of said unreacted fluids below the dew point to form a two-phase mixture of gas and condensed liquid and reintroducing said two-phase mixture into the reactor, the process being characterized in that said two­phase mixture is reintroduced under the distribution plate of the reactor so that a part of condensed liquid is separated from the gas and is successively fed above the fluidized bed through an external pipe connecting the bottom of the reactor to a point situated above the upper limit of the fluidized bed of polymer particles.

    GAS-PHASE OLEFIN POLYMERIZATION PROCESS
    57.
    发明公开
    GAS-PHASE OLEFIN POLYMERIZATION PROCESS 有权
    方法的烯烃气相聚合

    公开(公告)号:EP1613668A1

    公开(公告)日:2006-01-11

    申请号:EP04725050.1

    申请日:2004-04-01

    Abstract: A continuous process for the olefin polymerization in a fluidized bed reactor, said process comprising continuously passing a gaseous stream comprising one or more α-olefin monomers through the fluidized bed in the presence of a polymerization catalyst under reactive conditions, withdrawing polymeric product and unreacted fluids from the reactor, cooling part of said unreacted fluids below the dew point to form a two-phase mixture of gas and condensed liquid and reintroducing said two-phase mixture into the reactor, the process being characterized in that said two­phase mixture is reintroduced under the distribution plate of the reactor so that a part of condensed liquid is separated from the gas and is successively fed above the fluidized bed through an external pipe connecting the bottom of the reactor to a point situated above the upper limit of the fluidized bed of polymer particles.

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