Polymerization control process
View Patent ↗The present invention relates to a continuous process for controlling the gas-phase co-polymerisation of olefins in a fluidised bed reactor. The present invention further relates to a method for the continuous gas-phase (co-)polymerisation of olefins in a fluidised bed reactor in the presence of a polymerisation catalyst wherein the density of the polymer powder particles leaving the reactor is maintained constant by controlling the particle size distribution of the polymerisation catalyst. The present invention also relates to a process for controlling the particle size distribution of a polymerisation catalyst in order to achieve the production of a polymer powder of constant density during the continuous gas-phase (co-)polymerisation of olefins in a fluidised bed reactor.
1. Process for controlling the density of polymer powder particles leaving a reactor, comprising forming polymer powder particles in an olefin(s) continuous gas-phase (co-)polymerisation process in a single fluidised bed reactor having a polymerization zone, withdrawing from the reactor a hot recycle stream comprising a principal monomer and at least another unreacted reactant, cooling part or all of said recycle stream withdrawn from said reactor, and recycling part or all of said cooled recycle stream comprising the principal monomer and the unreacted reactant(s) through the polymerisation zone in said reactor in the presence of a polymerisation catalyst under reactive conditions, wherein the density of the polymer powder particles is maintained constant by controlling the particle size distribution SPAN of the polymerisation catalyst.
2. Process according to claim 1 wherein more than 99% of the polymer powder particles leaving the reactor have densities in an interval of plus to minus 2.5 g/cm 3 around the average density of the polymer powder particles forming the bed.
3. Process according to claim 1 or 2 wherein the SPAN is maintained below 1.6.
4. Process according to claim 1 wherein the principal monomer is ethylene or propylene.
5. Processing according to claim 4 wherein the principal monomer is ethylene.
6. Process according to claim 5 wherein the polymer produced is a copolymer of ethylene having a density between 0.880 and 0.925 g/cm 3 .
7. Process according to claim 1 wherein the polymerisation catalyst is a metallocene or a Phillips chromium catalyst.
8. Process according to claim 7 wherein the polymerisation catalyst is a metallocene.
9. Process according to claim 3 wherein the SPAN is maintained below 1.5.
10. Process according to claim 9 wherein the SPAN is maintained below 1.4.
11. Process according to claim 1 wherein the polymerisation catalyst is a supported polymerisation catalyst and the density is maintained by controlling the particle size distribution SPAN of the polymerization catalyst's support.