Gas-phase polymerization process
View Patent ↗A process for polymerizing one or more olefins in a gas-phase polymerization reactor is provided. The gas-phase reactor has a fluidized bed and a fluidizing medium. The fluidizing medium has an operating density and an operating velocity. The process includes determining a critical gas velocity and/or determining a critical gas velocity for the polymerization. The operating gas density and/or the operating gas velocity for the fluidizing medium is then adjusted to be less than or equal to its respective critical value. The process includes increasing the bulk density of the fluidized bed. The increase in the fluidized bed bulk density increases productivity without increasing reactor residence time.
1. A process for polymerizing one or more olefins in a gas-phase reactor having a fluidized bed and a fluidizing medium having an operating gas density, the process comprising:
determining a critical gas density for the fluidizing medium with the following equation,
(
a
×
A
P
S
×
S
B
D
S
G
V
)
b
wherein
a is a constant having a value of 4.0,
b is a constant having a value of 2.3,
APS is an average particle size of the fluidized bed as measured in inches,
SBD is a settled bulk density of polymer particles of the bed measured in lb/ft 3 ,
SGV is a gas velocity of the fluidizing medium as measured in ft/second; and
adjusting the operating gas density of the fluidizing medium to be less than or equal to the critical gas density.
2. The process of claim 1 comprising maintaining the fluidized bed in at a least turbulent fluidization regime during the adjusting.
3. The process of claim 1 wherein the adjusting is selected from the group consisting of adjusting a partial pressure of a gas in the fluidizing medium, adjusting the composition of the fluidizing medium, adjusting a reactor pressure, and combinations thereof.
4. The process of claim 1 wherein the adjusting comprises moving the fluidized bed from a fast fluidization regime to a turbulent fluidization regime.
5. The process of claim 1 comprising maintaining the fluidized bed in at least a turbulent fluidization regime; and increasing, with the adjusting, a bulk density of the fluidized bed.
6. The process of claim 1 comprising moving the fluidized bed from a fast fluidization regime to a turbulent fluidization regime and increasing a bulk density of the fluidized bed.
7. The process of claim 1 wherein the fluidizing medium comprises propylene gas and at least one other gas, the process comprising maintaining the fluidized bed in at least a turbulent fluidization regime; decreasing a propylene partial pressure of the fluidizing medium; and increasing a bulk density of the fluidized bed.
8. The process of claim 1 comprising decreasing the operating gas density from above the critical gas density to below the critical gas density and increasing a bulk density of the fluidized bed.
9. The process of claim 1 comprising introducing a catalyst composition into the reactor and forming a fluidized bed having an APS from about 0.356 mm (0.014 inches) to about 3.048 mm (0.12 inches).
10. The process of claim 1 comprising producing polymer particles having an SBD from about 240.28 kg/m 3 (15 lb/ft 3 ) to 560.65 kg/m 3 (35 lb/ft 3 ).
11. The process of claim 1 comprising passing the fluidizing medium through the reactor at a velocity from about 0.24 m/second (0.8 ft/second) to about 1.52 m/second (5.0 ft/second).
12. A process for polymerizing one or more olefins in a gas-phase reactor having a fluidized bed and a fluidizing medium having an operating gas density and an operating gas velocity, the process comprising:
determining a critical gas velocity for the fluidizing medium with the following equation;
a
×
A
P
S
×
S
B
D
(
F
M
D
)
1
/
b
wherein
a is a constant having a value of 4.0,
b is a constant having a value of 2.3,
APS is an average particle size of the fluidized bed,
SBD is a settled bulk density of the fluidized bed,
FMD is a density of the fluidizing medium; and
adjusting the operating gas density or the operating gas velocity so that the operating gas velocity is less than or equal to the critical gas velocity.
13. The process of claim 12 comprising adjusting the operating gas density and adjusting the operating gas velocity so the operating gas velocity is less than the critical gas velocity.
14. The process of claim 12 comprising decreasing the operating gas velocity from a velocity greater than the critical gas velocity to a velocity less than the critical gas velocity; and increasing a bulk density of the fluidized bed.