Polymerisation process

Patent metadata

Field	Value
Publication number	US-9175120-B2
Application number	US-201314382185-A
Country	US
Kind code	B2
Filing date	Mar 7, 2013
Priority date	Mar 16, 2012
Publication date	Nov 3, 2015
Grant date	Nov 3, 2015

Abstract

Polymerization of olefins in a reactor system having two reactors in series, more particularly a process for the polymerization of monomer in at least first and second reactors operated in series. The process includes contacting a first stream containing vapor derived from the effluent withdrawn from the second reactor with a feed stream to the second reactor, the feed stream containing effluent derived from the first reactor.

First claim

The invention claimed is:

1. A process for the polymerisation of monomer in at least first and second reactors operated in series, which process comprises either:
(i) contacting a first stream comprising vapour derived from the effluent withdrawn from the second reactor with a feed stream to the second reactor, said feed stream comprising effluent derived from the first reactor and said first stream having been separated from the polymer withdrawn from the second reactor at a pressure of 0.5 MPa (5 bar) or above, or
(ii) contacting a first stream comprising vapour derived from the effluent withdrawn from a subsequent reactor with a feed stream to the second reactor, said feed stream comprising effluent derived from the first reactor.

2. A process according to claim 1 which comprises first and second slurry loop polymerisation reactors connected in series.

3. A process according to claim 1 wherein the feed stream is a slurry of polymer solids in a liquid medium from a first slurry loop polymerisation reactor.

4. A process according to claim 1 wherein the effluent withdrawn from the second reactor is a slurry of polymer solids in a liquid medium comprising diluent, and wherein the first stream is derived from the effluent by flashing all or a portion of the liquid medium to form a vapour, and separating this from the polymer solids.

5. A process according to claim 4 wherein said first stream comprises a majority of the vaporised components of the liquid medium in the effluent withdrawn from the second reactor and at least 80% by weight of the first stream is in vapour form when brought into contact with the feed stream.

6. A process according to claim 1 wherein the first stream is brought into contact with the feedstream to the second reactor at a pressure of 0.5 MPa (5 bar) or above.

7. A process according to claim 1 wherein the first stream is passed from its source to the contacting step without any compression and/or wherein the first stream is passed from its source to the contacting step without passing through any filters.

8. A process according to claim 1 wherein the first stream has been separated from the polymer withdrawn from the subsequent reactor at a pressure of 0.5 MPa (5 bar) or above.

9. A process according to claim 1 which is a process for the polymerisation of monomer in two slurry loop reactors connected in series, which process comprises:
1) Polymerising in a first loop reactor, monomer in the presence of a diluent to produce a first polymer slurry comprising polymer solids suspended in a liquid medium comprising diluent and unreacted monomer,
2) Withdrawing a portion of the first polymer slurry as a first effluent comprising solid polymer, diluent and unreacted monomer, and passing said first effluent to a contactor to form a second effluent comprising solid polymer, diluent and unreacted monomer,
3) Passing said second effluent to a second loop reactor,
4) Polymerising in the second loop reactor, monomer in the presence of said second effluent, to produce a second polymer slurry comprising polymer solids suspended in a liquid medium comprising diluent and unreacted monomer,
5) Withdrawing a portion of the second polymer slurry as a third effluent comprising solid polymer, diluent and unreacted monomer, and
6) Passing said third effluent to a separation step for separating a first stream comprising vaporised diluent and unreacted monomer from said polymer solids, said separation step being a high pressure separation step at a pressure of 0.5 MPa (5 bar) or above,
characterised in that at least a portion of the first stream is passed to the contactor wherein it is contacted with the first effluent to produce said second effluent and a second stream comprising vaporised diluent and unreacted monomer.

10. A process according to claim 9 wherein the first stream comprises entrained solids which are preferentially entrained into the second effluent.

11. A process according to claim 9 wherein the first polymer slurry and the first effluent also comprise hydrogen, and the second polymer slurry and the third effluent also comprise unreacted comonomer, and wherein the contacting of the first stream and first effluent results in an increase in the hydrogen in the second stream compared to the first stream and an increase in comonomer in the second effluent compared to the first effluent.

12. A process according to claim 9 wherein the second stream is enhanced in hydrogen and poorer in comonomer than the first stream.

13. A process according to claim 9 wherein the contacting takes place in a contactor which is configured in association with a fractionator such that the second stream recovered from the contactor is passed directly to a fractionator, from which heavier components, including comonomer, are recovered and passed directly back to the contactor, whilst lighter components are recovered from the fractionator as a vapour for further treatment and recycle.

14. A process according to claim 9 wherein the separation step is in a high pressure recovery system and polymer solids are passed from the high pressure recovery system to a low pressure recovery system which comprises a low pressure separation step for separating further diluent, unreacted monomer and unreacted comonomer from said solids, and a recycle system for recycling at least a portion of the further diluent, unreacted monomer and unreacted comonomer.

15. A process according to claim 14 wherein the low pressure recovery system/recycle system comprises a lights separator and/or a heavies separator for removing such components from the process.

16. A process for treatment of a first stream comprising vapour derived from the effluent withdrawn from a polymerisation reactor, which process comprises:
i) contacting said first stream with a feed stream to the reactor to produce a vapour comprising hydrogen,
ii) treating said vapour comprising hydrogen to produce and separate from each other a first liquid stream and a third stream comprising vapour,
iii) passing said third stream to a first separations step operating at greater than 0.5 MPa and at less than −10° C. to separate hydrogen therefrom, each of steps (i), (ii) and (iii) being performed at a pressure of at least 0.5 MPa, and
iv) passing a portion of the first liquid stream to a second separations step operating at less than 0.4 MPa and at less than −10° C. to separate hydrogen therefrom.

Assignees

• Ineos Europe Ag

Inventors

• Marissal Daniel
• Van Breuseghem Philip
• Walworth Brent R

Classifications

• C08F2/01 Primary

  characterised by special features of the polymerisation apparatus used · CPC title

• C08F10/00 Primary

  Homopolymers and copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond · CPC title

• C08F6/001

  Removal of residual monomers by physical means · CPC title

• C07C7/00

  Purification; Separation; Use of additives (working-up undefined gaseous mixtures obtained by cracking hydrocarbon oils C10G70/00) · CPC title

• C08F6/005 Primary

  from solid polymers · CPC title