Granted Patent B2

US 7,807,761 · App. 11/883,048 · Granted Oct 5, 2010

Abstract

Claims (23)

1. Equipment for the gas-phase polymerization of olefin(s), comprising:

a reactor with a fluidized or mechanically stirred bed and with a vertical side wall, provided at its base with a fluidization grid, the vertical side wall of the reactor extending a height H above the fluidization grid,

a conduit for external circulation of a reaction gas mixture, connecting the top of the reactor to the base of the reactor under the fluidization grid and including a compressor and at least one piece of equipment for heat removal,

a bed level controller,

at least one withdrawal conduit for withdrawing polymer,

at least one uplift conduit,

at least one recovery gas lock hopper equipped with a discharge valve, and

at least one degassing chamber, wherein

(i) the at least one withdrawal conduit connects the reactor to the at least one recovery gas lock hopper, the at least one withdrawal conduit has an isolation valve prior to the recovery gas lock hopper and the at least one withdrawal conduit leaves the side wall of the reactor at a height of the reactor wall above the fluidization grid ranging from 0 H to 0.15 H, whilst being directed in a downwards fashion at an angle A with the horizontal plane ranging from 20 to 75 degrees below the horizontal plane, and said withdrawal conduit having an internal diameter of between 5.0 and 20.5 cm,

(ii) the recovery gas lock hopper has a volume of at least 200 liters,

(iii) the at least one uplift conduit is connected between the recovery gas lock hopper and an inlet of the degassing chamber and has a vertical height of at least 20 m and an internal diameter of between 5.0 and 20.5 cm, and provides transport in an upwards direction in the direction of flow between the reactor and the inlet of the degassing chamber,

(iv) the inlet of the at least one degassing chamber is disposed at a vertical height above the vertical height at which the withdrawal conduit leaves the side wall of the reactor, and

(v) at least one means is provided for flushing the at least one uplift conduit.

2. Equipment according to claim 1 wherein the bed level controller resets the withdrawal rate for the withdrawal conduit in order to maintain the reactor bed level at a constant height.

3. Equipment according to claim 1 wherein the withdrawal conduits have an internal diameter above 6.0 cm and below 10.5 cm.

4. Equipment according to claim 3 wherein the withdrawal conduits have an internal diameter above 6.0 cm and below 8 cm.

5. Equipment according to claim 1 further comprising at least two withdrawal conduits exiting the reactor and subsequently at least two gas lock hoppers.

6. Equipment according to claim 5 wherein the at least two gas lock hoppers are interconnected by a pressure equalizer conduit which is equipped with an interconnection valve.

7. Equipment according to claim 1 further comprising a delumper in at least one of the polymer withdrawal conduits.

8. Process for the polymerisation of olefins, which process comprises providing an equipment according to claim 1 , and

a) polymerising one or more olefin monomers in said reactor of said equipment in the presence of a polymerization catalyst in a fluidized or mechanically stirred bed, said polymerization also comprising removing a reaction gas mixture from the top of the reactor, compressing and removing heat therefrom and recycling the mixture to the base of the reactor under the fluidization grid, and controlling the level of the fluidised or mechanically stirred bed by a bed level controller,

b) withdrawing polymer through said at least one withdrawal conduit, and passing the polymer to said at least one recovery gas lock hopper equipped with a discharge valve and which has a volume of at least 200 liters, and

c) subsequently passing the polymer via said at least one uplift conduit to said inlet of said at least one degassing chamber.

Assignments (17)