Process for preparing an alpha-olefin feed stream and polymerization process using the same

Patent metadata

Field	Value
Publication number	US-2026035488-A1
Application number	US-202419150048-A
Country	US
Kind code	A1
Filing date	Jan 24, 2024
Priority date	Jan 24, 2023
Publication date	Feb 5, 2026
Grant date	—

Abstract

The present invention relates to a process for preparing an alpha-olefin feed stream comprising providing a low-pressure initial stream comprising a hydrocarbon solvent at a low pressure level in the range of from below atmospheric pressure to 15 barg; pressurizing the low-pressure initial stream to a medium pressure level in the range of from greater than 15 to 45 barg to form a medium-pressure initial stream; pressurizing the medium-pressure initial stream to a high pressure level in the range of from greater than 45 to 300 barg to form a high-pressure initial stream; wherein a monomer stream comprising an alpha-olefin monomer is introduced into the medium-pressure initial stream at medium pressure level and/or into the high-pressure initial stream at high pressure level, and one or more comonomer streams comprising at least one alpha-olefin comonomer is/are introduced into the low-pressure initial stream at low pressure level, and/or into the medium-pressure initial stream at medium pressure level, and/or into the high-pressure initial stream at high pressure level; to form an alpha olefin feed stream. Alternatively, the medium pressure level may be left out, wherein a monomer stream comprising an alpha-olefin monomer is introduced into the high-pressure initial stream at high pressure level; and one or more comonomer streams comprising at least one alpha-olefin comonomer is/are introduced into the low-pressure initial stream at low pressure level, and/or into the high-pressure initial stream at high pressure level; to form said alpha olefin feed stream. The above processes enable solution polymerisation with reduced process complexity and increased process economics.

First claim

1 . Process for preparing an alpha-olefin feed stream comprising
providing a low-pressure initial stream comprising a hydrocarbon solvent at a low pressure level in the range of from below atmospheric pressure to 15 barg; pressurizing the low-pressure initial stream to a medium pressure level in the range of from greater than 15 to 45 barg to form a medium-pressure initial stream; pressurizing the medium-pressure initial stream to a high pressure level in the range of from greater than 45 to 300 barg to form a high-pressure initial stream; wherein the process further comprises introducing a monomer stream comprising an alpha-olefin monomer into the medium-pressure initial stream at medium pressure level and/or into the high-pressure initial stream at high pressure level; and introducing one or more comonomer streams comprising at least one alpha-olefin comonomer into the low-pressure initial stream at low pressure level, and/or into the medium-pressure initial stream at medium pressure level, and/or into the high-pressure initial stream at high pressure level; to form an alpha olefin feed stream, wherein the alpha-olefin monomer is selected from ethylene and propylene, wherein the at least one alpha-olefin comonomer is selected from the group consisting of 1-heptene, 1-octene, 1-nonene and 1-decene or mixtures thereof, when one or more comonomer streams are introduced into the low-pressure initial stream at low pressure level; and wherein the at least one alpha-olefin comonomer is selected from the group consisting of propene, 1-butene, 1-pentene and 1-hexene or mixtures thereof, when one or more comonomer streams are introduced into the medium-pressure initial stream at medium pressure level, and/or into the high-pressure initial stream at high pressure level.

2 . Process for preparing an alpha olefin feed stream, comprising
providing a low-pressure initial stream comprising a hydrocarbon solvent at a low pressure level in the range of from below atmospheric pressure to 15 barg; pressurizing the low-pressure initial stream to a high pressure level in the range of from greater than 45 to 300 barg to form a high-pressure initial stream; wherein the process further comprises introducing a monomer stream comprising an alpha-olefin monomer into the high-pressure initial stream at high pressure level; and introducing one or more comonomer streams comprising at least one alpha-olefin comonomer into the low-pressure initial stream at low pressure level, and/or into the high-pressure initial stream at high pressure level; to form an alpha-olefin feed stream, wherein the alpha-olefin monomer is selected from ethylene and propylene, wherein the at least one alpha-olefin comonomer is selected from the group consisting of 1-heptene, 1-octene, 1-nonene and 1-decene or mixtures thereof, when one or more comonomer streams are introduced into the low-pressure initial stream at low pressure level; and wherein the at least one alpha-olefin comonomer is selected from the group consisting of propene, 1-butene, 1-pentene and 1-hexene or mixtures thereof, when one or more comonomer streams are introduced into the high-pressure initial stream at high pressure level.

3 . The process according to claim 1 , wherein the at least one alpha-olefin comonomer introduced into the low-pressure initial stream at low pressure level and the at least one alpha-olefin comonomer introduced into the medium-pressure initial stream at medium pressure level, and/or into the high-pressure initial stream at high pressure level, differ from each other.

4 . The process according to claim 1 , which further comprises introducing a chain transfer agent stream comprising at least one chain transfer agent, preferably hydrogen, into the medium-pressure stream and/or into the high-pressure initial stream at high pressure level.

5 . The process according to claim 1 , which further comprises introducing a hydrocarbon solvent stream comprising additional hydrocarbon solvent into the low-pressure initial stream at low pressure level.

6 . The process according to claim 1 , wherein the low pressure level is a pressure in the range of from 2 to 10 barg, and/or
wherein the medium pressure level is a pressure in the range of from 20 to 40 barg, and/or, wherein the high pressure level is a pressure in the range of from 50 to 250 barg.

7 . The process according to claim 1 , wherein the medium-pressure initial stream is cooled after the pressurization and/or after the introduction of the monomer stream and the one or more comonomer streams and/or wherein the high-pressure initial stream is cooled after the pressurization and/or after the introduction of the monomer stream and the one or more comonomer streams.

8 . The process according to claim 1 , wherein the temperature of the low-pressure initial stream is in the range of from 10 to 50° C., preferably of from 20 to 40° C.; wherein the temperature of the medium-pressure initial stream is in the range of from 20 to 50° C., preferably of from 25 to 45° C.; and/or wherein the temperature of the high-pressure initial stream is in the range of from −40 to 50° C., preferably from −30 to 40° C.

9 . The process according to claim 1 , wherein the concentration of the alpha-olefin monomer in the medium-pressure initial stream is in the range of from 0 to 22 wt.-%, and/or
the concentration of the at least one alpha-olefin comonomer in the medium-pressure initial stream is in the range of from 0 to 35 wt.-%,; or alternatively in the range of from 0.01 to 50 wt.-% and/or wherein the concentration of the alpha-olefin monomer in the high-pressure initial stream is in the range of from 10 to 20 wt.-%, and/or the concentration of the at least one alpha-olefin comonomer in the high-pressure initial stream is in the range of from 0 to 35 wt.-%, or alternatively in the range of from 0 to 50 wt.-%.

10 . The process according to claim 1 , wherein the streams are liquid or in the supercritical phase.

11 . The process according to claim 1 , wherein the low-pressure initial stream is a recycle stream.

12 . Process for the polymerization of an alpha-olefin polymer operated in liquid or under supercritical conditions, comprising preparing an alpha-olefin feed stream according to claim 1 ;
passing the alpha-olefin feed stream into one or more polymerization reactors arranged in parallel, in series, or a combination thereof; and contacting the alpha-olefin feed stream with a catalyst in the one or more polymerization reactors to form a reaction mixture comprising an alpha-olefin polymer.

Assignees

• Borealis Ag

Inventors

• Al-Haj Ali Mohammad
• Sleijster Henry
• Sattar Mubashar
• Zitting Samuli
• Räsänen Jukka
• Vijay Sameer

Classifications

• C08F210/16 Primary

  Copolymers of ethene with alpha-alkenes, e.g. EP rubbers · CPC title

• C08F2/06 Primary

  Organic solvent · CPC title

• C08F2400/00

  Characteristics for processes of polymerization · CPC title

• C08L23/0815

  with aliphatic 1-olefins containing one carbon-to-carbon double bond · CPC title

• C08F2/01

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