Method, an arrangement and use of an arrangement for olefin polymerisation
An olefin polymerisation method and arrangement comprising polymerising at least one olefin in gas phase in a fluidised bed in the presence of an olefin polymerisation catalyst in a polymerisation reactor having a vertical body; a generally conical downwards tapering bottom zone; a generally cylindrical middle zone, above and connected to said bottom zone; and a generally conical upwards tapering top zone above and connected to said middle zone wherein (i) fluidisation gas is introduced to the bottom zone of the reactor from where it passes upwards through the reactor; (ii) the fluidisation gas is withdrawn from the top zone of the reactor; (iii) a fluidised bed is formed within the reactor where the growing polymer particles are suspended in the upwards rising gas stream; and wherein the polymerisation reactor has an operating temperature set point and which reactor comprises at least one temperature measurement sensor, wherein a temperature difference (DT) between the temperature measurement sensor (Tm), and the operating temperature set point (Ts) of the reactor is equal to or less than 10° C.
1. An olefin polymerisation method comprising polymerising at least one olefin in gas phase in a fluidised bed in the presence of an olefin polymerisation catalyst in a polymerisation reactor having a vertical body; a generally conical downwards tapering bottom zone; a generally cylindrical middle zone, above and connected to said bottom zone; and a generally conical upwards tapering top zone above and connected to said middle zone wherein (i) fluidisation gas is introduced to the bottom zone of the polymerisation reactor from where it passes upwards through the polymerisation reactor; (ii) the fluidisation gas is withdrawn from the top zone of the polymerisation reactor; (iii) a fluidised bed is formed within the reactor where the growing polymer particles are suspended in the upwards rising gas stream; and wherein the polymerisation reactor has an operating temperature set point and which polymerisation reactor comprises at least one temperature measurement sensor, wherein a temperature difference (DT) between each temperature measurement sensor (Tm), and the operating temperature set point (Ts) of the reactor is equal to or less than 10° C., and wherein the polymerisation reactor comprises polymer particles having a d 90 of equal to or more than 700 μm.
2. The method according to claim 1 wherein the polymerisation reactor has a superficial gas velocity, which is chosen such that a dimensionless number N Br is in the range or from 2.5 to 7.
3. The method according to claim 1 , wherein the polymerisation reactor has a height to diameter ratio L/D of at least 4.
4. The method according to claim 1 , wherein there is no fluidisation grid in the polymerisation reactor.
5. The method according to claim 1 , wherein the fluidisation gas withdrawn from the top zone of the polymerisation reactor is compressed, cooled, optionally condensed and returned into the bottom zone of the polymerisation reactor.
6. The method according to claim 1 , wherein the olefin gas is ethylene and/or propylene.
7. The method according to claim 1 , wherein the polymerisation is done in the presence of an alpha-olefin comonomer.
8. The method according to claim 1 , wherein the ratio of partial pressure of 1-butene to the partial pressure of ethylene in the polymerisation reactor is equal to or above 0.5.
9. The method according to claim 1 , wherein the ratio of partial pressure of 1-hexene to the partial pressure of ethylene in the polymerisation reactor is equal to or above 0.25.
10. The method according to claim 1 , wherein the pressure of ethylene in the reactor is equal to or more than 3 bar.
11. An apparatus comprising a polymerisation reactor for polymerising at least one olefin in gas phase in a fluidised bed in the presence of an olefin polymerisation catalyst, the polymerisation reactor having a vertical body; a generally conical downwards tapering bottom zone; a generally cylindrical middle zone, above and connected to said bottom zone; and a generally conical upwards tapering top zone above and connected to said middle zone wherein (i) means for introducing fluidisation gas to the bottom zone of the polymerisation reactor from where it passes upwards through the polymerisation reactor; (ii) means for withdrawing the fluidisation gas from the top zone of the polymerisation reactor; (iii) a fluidised bed within the polymerisation reactor where the growing polymer particles are suspended in the upwards rising gas stream; and wherein the polymerisation reactor has an operating temperature set point and which polymerisation reactor comprises at least one temperature measurement sensor, wherein a temperature difference (DT) between each temperature measurement sensor (Tm) and the operating temperature set point of the reactor (Ts) is equal to or less than 10° C., and wherein the polymerisation reactor comprises polymer particles having a d 90 of equal to or more than 700 μm.
12. A process comprising producing olefin polymer with the apparatus of claim 11 .
13. The method according to claim 7 , wherein the polymerisation is done in the presence of C4-C8 alpha-olefin comonomer.
14. The method according to claim 13 , wherein the polymerisation is done in the presence of 1-butene, 1-hexene, 1-octene or combination of two or more comonomers.