# US 8,785,572 B2 · Process for the gas-phase polymerization of olefins

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- Number: US 8,785,572 B2
- Document ID: US8785572B2
- Status: Granted
- Kind: B2
- Application number: 13/703,613
- Filed: 2011-06-09
- Published: 2013-04-11
- Granted: 2014-07-22
- Earliest claimed: 2010-06-22
- Assignees: Basell Poliolefine Italia S.r.l.
- Applicants: Enrico Balestra; Tiziana Caputo; Antonio Mazzucco; Riccardo Rinaldi; Silvia Soffritti
- Inventors: Enrico Balestra; Tiziana Caputo; Antonio Mazzucco; Riccardo Rinaldi; Silvia Soffritti
- Web page: https://patentgrep.com/patent/US8785572B2

## CPC

- C08F 2/01: characterised by special features of the polymerisation apparatus used
- C08F 210/06: Propene
- C08F: MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS

## Abstract

A process for the gas-phase copolymerization of: (a) propylene, (b) at least one C4-C8 α-olefin, and (c) optionally ethylene, the process being carried out in a reactor having two interconnected polymerization zones, wherein the growing polymer particles flow through the first of said polymerization zones (riser) under fast fluidization conditions, leave said riser and enter the second of said polymerization zones (downcomer) through which they flow downward in a densified form, leave said downcomer and are reintroduced into said riser, thus establishing a circulation of polymer between the riser and the downcomer, the gas mixture present in the riser being at least partially prevented from entering the downcomer by introducing into the upper part of said downcomer a liquid barrier having a composition different from the gaseous mixture present in the riser and comprising at least one C4-C8 α-olefin in a total amount of from 0.1% to 35% by mol.

## Claims

### Claim 1

A process comprising:
polymerizing
(a) propylene,
(b) at least one C4-C8 α-olefin, and
(c) optionally ethylene, wherein the polymerizing step is carried out in the gas-phase,
wherein the process is carried out in a reactor having two interconnected polymerization zones, a riser and a downcomer,
wherein polymer particles flow through the riser under fast fluidization conditions, leave said riser and enter the downcomer,
wherein the polymer particles in the downcomer flow downward in a densified form, leave said downcomer and are reintroduced into said riser, thus establishing a circulation of polymer between the riser and the downcomer,
wherein a gas mixture present in the riser is prevented from entering the downcomer by introducing a liquid barrier into an upper part of said downcomer, thereby creating a recycle gas mixture that flows upward to a separation zone wherein the liquid barrier comprises at least one C4-C8 α-olefin in a total amount of from 0.1% to 35% by mol, and has a composition different from the gas mixture present in the riser,
wherein the recycle gas is separated into:
(i) a first stream of recycled gas, wherein the first stream of recycled gas is fed into a bottom part of the downcomer,
(ii) a second stream of recycled gas, wherein the second stream of recycled gas is fed into a bottom part of the riser; and
(iii) a third stream of recycled gas, wherein the third stream of recycled gas is fed into at least one distillation column before being recycled into the downcomer.

### Claim 2 (depends on 1)

The process according to claim 1, wherein the partial evaporation of said liquid barrier generates in the upper part of the downcomer a flow of gas moving counter-currently to the flow of descendent polymer.

### Claim 3 (depends on 1)

The process according to claim 1, wherein the C4-C8 α-olefin is 1-hexene and its amount ranges from 0.1% to 10% by mol.

### Claim 4 (depends on 3)

The process according to claim 3, wherein the liquid barrier further comprises:
from 70 to 90% by mol of propylene;
from 5 to 15% by mol of propane; and
from 0 to 5% by mol of ethylene.

### Claim 5 (depends on 4)

The process according to claim 4, wherein the obtained polyolefin contains from 0.2 to 8.0% by weight of recurring units derived from 1-hexene.

### Claim 6 (depends on 1)

The process according to claim 1, wherein the C4-C8 α-olefin is 1-butene and its amount ranges from 2% to 30% by mol.

### Claim 7 (depends on 6)

The process according to claim 6, wherein the liquid barrier further comprises:
from 50 to 90% by mol of propylene;
from 5 to 15% by mol of propane; and
from 0 to 5% by mol of ethylene.

### Claim 8 (depends on 7)

The process according to claim 7, wherein the obtained polyolefin contains from 1 to 25% by weight of recurring units derived from 1-butene.

### Claim 9 (depends on 1)

The process according to claim 1, wherein the liquid barrier derives from condensation and/or distillation of a part of the gaseous stream continuously recycled to said reactor having two interconnected polymerization zones.

### Claim 10 (depends on 9)

The process according to claim 9, wherein the composition of the liquid barrier is adjusted by feeding liquid make-up monomers and propane before introducing said liquid barrier into the upper part of the downcomer.