An improved process for the polymerization of olefin monomer selected from
(a) ethylene, (b) propylene, (c) mixtures of ethylene and propylene and
(d) mixtures of (a), (b) or (c) with one or more alpha-olefins in a
fluidized bed gas phase reactor, said process comprising passing a
gaseous mixture of said olefin monomers(s) through the fluidized bed
under effective polymerization conditions to provide a polymer product
containing unreacted monomer(s) and a gaseous effluent stream comprising
unreacted monomer(s), removing the polymer product to a degassing vessel,
recycling a first portion of the gaseous effluent stream to the fluidized
bed and passing a second portion of the gaseous effluent stream to
counter currently contact the polymer product in said degassing vessel to
produce a polymer product having a reduced amount of unreacted
monomer(s), characterized in that the improvements to the process
comprise: (i) removing heavy hydrocarbons from the second portion of the
effluent stream and returning said hydrocarbons to the first portion of
the effluent stream for recycle to the fluidized bed, (ii) removing
substantially all of the monomer(s) from the second portion of the
effluent stream and returning said monomers(s) to the first portion of
the effluent stream for recycle to the fluidized bed, and (iii) recycling
the second effluent stream after passage through the degassing vessel to
the gaseous effluent stream.