초록 ▼

The invention relates to continuous gas fluidised bed polymerisation of olefins, especially ethylene, propylene, or mixtures of these with other alpha olefins, wherein the monomer-containing recycle gas employed to fluidise the bed is cooled to condense out at least some liquid hydrocarbon. The cond

The invention relates to continuous gas fluidised bed polymerisation of olefins, especially ethylene, propylene, or mixtures of these with other alpha olefins, wherein the monomer-containing recycle gas employed to fluidise the bed is cooled to condense out at least some liquid hydrocarbon. The condensed liquid, which can be a monomer or an inert liquid, is separated from the recycle gas and is fed directly to the bed to produce cooling by latent heat of evaporation. The liquid feeding to the bed can be through gas-induced atomiser nozzles (FIG. 2), or through liquid-only nozzles. The process provides substantially improved productivity of gas fluidised bed polymerisation of olefins.

대표청구항 ▼

[ We claim:] [1.] A continuous gas fluidized bed process for the polymerization of olefin monomer selected from the group consisting of (a) ethylene, (b) propylene, (c) mixtures of ethylene and propylene, and (d) mixtures of (a), (b), or (c) with one or more other alpha-olefins comprising passing a

[ We claim:] [1.] A continuous gas fluidized bed process for the polymerization of olefin monomer selected from the group consisting of (a) ethylene, (b) propylene, (c) mixtures of ethylene and propylene, and (d) mixtures of (a), (b), or (c) with one or more other alpha-olefins comprising passing a gaseous stream containing said olefin monomer through a fluidized bed in a reactor in the presence of a polymerization catalyst under reactive conditions to polymerize some of said monomer, withdrawing a gaseous stream comprising at least some unreacted monomer from said reactor; cooling at least part of said gaseous stream withdrawn from said reactor to a temperature at which liquid condenses out of the gaseous stream, separating at least part of the condensed liquid from the cooled gaseous stream, continuously recycling at least part of the separated cooled gas back to the reactor, and introducing at least part of the separated liquid directly into the fluidized bed at or above the point at which the gaseous stream passing through the fluidized bed has substantially reached the temperature of the gaseous stream being withdrawn from the reactor, wherein the polymerization catalyst is introduced into the fluidized bed directly with the separated liquid.