Method for controlling a process for polymerisation of an olefin
View Patent ↗Method for controlling a process for polymerising at least one olefin in a reaction zone, the process including in the reaction zone a reaction mixture and polymer particles, the reaction mixture containing a principal olefin and at least one further reagent. The method involves using the ratio of at least one further reagent to principal olefin in the polymer particles in the reaction zone or in the amorphous phase of the polymer particles.
1. Method for controlling a process for polymerising at least one olefin in a reaction zone, said process comprising in the reaction zone a reaction mixture and polymer particles, the reaction mixture comprising a principal olefin and at least one further reagent, said method comprising controlling the ratio of at least one further reagent to principal olefin in the polymer particles in the reaction zone or in the amorphous phase of said polymer particles.
2. A method according to claim 1 wherein the reaction mixture comprises a principal olefin, at least one further reagent and at least one alkane having from 4 to 8 carbon atoms, and wherein the process is controlled by:
a) determining the ratio of said at least one further reagent to principal olefin in the polymer particles in the reaction zone or in the amorphous phase of the polymer particles required in order to obtain the polymer it is desired to produce,
b) determining conditions in the reactor which will result in the ratio of at least one further reagent to principal olefin determined in step (a), said conditions including at least:
a. the reaction temperature, T;
b. the partial pressure of the at least one alkane in the gas phase, P A ;
c. the partial pressure of the principal olefin in the gas phase, P O ;
d. the partial pressure of the at least one further reagent in the gas phase, P R ; and
c) adjusting conditions in the reactor to conditions based on the conditions determined in step (b), thereby adjusting the ratio of at least one further reagent to principal olefin in the polymer particles in the reaction zone or in the amorphous phase of said polymer particles to obtain a ratio based on the ratio determined in step (a), and thereby producing the desired polymer.
3. A method according to claim 2 further comprising:
d) maintaining the conditions in the reactor at conditions based on the conditions determined in step (b).
4. A method according to claim 1 for controlling a process for polymerising at least one olefin in a reaction zone during start-up or transition.
5. A method according to claim 1 wherein the at least one further reagent is selected from comonomers and chain transfer reagents.
6. A method according to claim 1 wherein the principal olefin is selected from ethylene, propylene and 1-butene.
7. A method according to claim 6 wherein a comonomer is present and is selected from olefins, other than the principal olefin, having 2 to 12 carbon atoms.
8. A method according to claim 1 wherein one or more saturated hydrocarbons selected from C4+ alkanes is present at a total partial pressure of at least 0.05 MPa.
9. A method according to claim 1 wherein at least 20 wt % of amorphous phase is present on the polymer.
10. A method according to claim 1 wherein the process is controlled using the ratio of chain transfer reagent to principal olefin and/or the ratio of olefin comonomer to principal olefin.
11. A method according to claim 1 wherein the polymerisation process is carried out continuously in the gas phase.
12. A method according to claim 1 wherein the polymerisation process is carried out in a gas-phase fluidised bed reactor.
13. A method according to claim 1 wherein the polymerisation catalyst is a metallocene catalyst.
14. A method according to claim 13 wherein hydrogen is used as the chain transfer agent and the mass ratio of hydrogen to the principal olefin in the amorphous phase is in the range 1.66×10 −5 *ln (MI) to 1.66×10 −5 *ln (10×MI), where MI is the melt index of the polymer it is desired to produce.
15. A method according to claim 13 wherein the mass ratio of comonomer to the principal olefin in the amorphous phase is in the range (953-D)/200 to (953-D)*3/100, where D is the non annealed density in kg/m 3 of the polymer that is desired to produce.
16. A method according to claim 1 wherein the catalyst is a Ziegler-Natta catalyst, hydrogen is used as a chain transfer agent, and the mass ratio of hydrogen to the principal olefin in the amorphous phase is in the range 7.1×10 −4 *ln (MI/0.7) to 0.021*ln (MI/0.7), where MI is the melt index of the polymer it is desired to produce.
17. A method according to claim 1 wherein the catalyst is a Ziegler-Natta catalyst and the mole ratio of comonomer to the principal olefin in the amorphous phase is in the range (958-D)*3/20 to (958-D)*3/2, where D is the non annealed density in kg/m 3 of the polymer that is desired to produce.
18. A process for polymerising at least one olefin in a reaction zone, said process being controlled using the method of claim 1 .
19. A method according to claim 8 wherein the one or more saturated hydrocarbons are selected from the group consisting of pentane and hexane.