Polymerization process in the presence of antistatic agent

Patent metadata

Field	Value
Publication number	US-9932465-B1
Application number	US-201615560424-A
Country	US
Kind code	B1
Filing date	Mar 23, 2016
Priority date	Mar 26, 2015
Publication date	Apr 3, 2018
Grant date	Apr 3, 2018

Abstract

A process for preparing a polyolefin, including polymerizing olefins in the presence of an antistatic agent made from or containing an alkylene oxide derived polymer made from or containing in average from about 10 to about 200 repeating units —(CH 2 —CHR—O)— with R being hydrogen or an alkyl group having from 1 to 6 carbon atoms, wherein the alkylene oxide derived polymer is a random copolymer of ethylene oxide and other alkylene oxides and a ratio of n:m is in the range of from 6:1 to 1:1, wherein (n) is the average number of repeating units —(CH 2 —CH 2 —O)— derived from ethylene oxide and (m) is the average number of repeating units —(CH 2 —CHR′—O)— derived from the other alkylene oxides with R′ being an alkyl group having from 1 to 6 carbon atoms, and the end groups of the alkylene oxide derived polymer are —OH groups.

First claim

The invention claimed is:

1. A process for preparing a polyolefin comprising:
(a) polymerizing olefins at temperatures of from about 20 to about 200° C. and pressures of from about 0.1 to 20 MPa in the presence of a polymerization catalyst in a polymerization reactor,
wherein the polymerization is carried out in the presence of an antistatic agent comprising
(i) an alkylene oxide derived polymer comprising
(A) an average of 10 to 200 repeating units of the formula —(CH 2 —CHR—O)—, with R being hydrogen or an alkyl group having from 1 to 6 carbon atoms,
wherein the alkylene oxide derived polymer comprises
(1) a random copolymer of ethylene oxide and other alkylene oxides and
(2) a ratio of n:m in the range of from 6:1 to 1:1,
 wherein n is the average number of repeating units of the formula —(CH 2 —CH 2 —O)— derived from ethylene oxide and m is the average number of repeating units —(CH 2 —CHR′—O)— derived from the other alkylene oxides, wherein R′ comprises an alkyl group having from 1 to 6 carbon atoms and end groups of the alkylene oxide derived polymer are —OH groups.

2. The process of claim 1 , wherein the ratio of n:m is in the range of 2:1 to 4:1.

3. The process of claim 1 , wherein the alkylene oxide derived polymer is a linear polymer of the general formula (I):
HO—(CH 2 —CH 2 —O) n —(CH 2 —CHR′—O) m —H  (I)

wherein R′ is a alkyl group having from 1 to 6 carbon atoms, and n is in a range of from 10 to 180 and m is in a range of from 2 to 120.

4. The process of claim 1 , wherein the alkylene oxide derived polymer is a random copolymer of ethylene oxide and propylene oxide.

5. The process of claim 4 , wherein the ethylene oxide/propylene oxide polymer is a linear ethylene oxide/propylene oxide copolymer of the general formula (II):
HO—(CH 2 —CH 2 —O) n —(CH 2 —CH(CH 3 )—O) m —H  (II)

wherein n is in a range of from 10 to 180 and m is in a range of from 2 to 120.

6. The process of claim 1 , wherein the polymerization is a gas-phase polymerization and the antistatic agent is introduced into the gas-phase polymerization reactor by feeding the antistatic agent to a part of the reactor where the density of solid polymer particles is at least about 30 kg/m 3 .

7. The process of claim 1 , wherein the antistatic agent is introduced into the polymerization reactor by a feed stream of a liquid hydrocarbon and the weight ratio of the antistatic agent to the liquid hydrocarbon in the combined stream introduced into the reactor is in the range from 1:10 to 1:5000.

8. The process of claim 1 , wherein the polymerization is carried out in a polymerization reactor cascade comprising
(I) a fluidized-bed reactor; and
(II) a multizone circulating reactor,
wherein in the multizone circulating reactor, the growing polymer particles flow upward through a first polymerization zone under fast fluidization or transport conditions, leave the first polymerization zone and enter a second polymerization zone through which the particles flow downward under the action of gravity, leave the downcomer and are reintroduced into the riser, thereby establishing a circulation of polymer, and the fluidized-bed reactor is arranged upstream of the multizone circulating reactor.

9. The process of claim 1 , wherein the polymerization is carried out in a polymerization reactor cascade comprising
(I) a fluidized-bed reactor; and
(II) a multizone circulating reactor,
wherein a lower molecular weight polyolefin polymer component is obtained in the fluidized-bed reactor and a higher molecular weight polyolefin polymer component is obtained in the multizone circulating reactor.

10. The process of claim 1 , wherein the polyolefin is a multimodal polyolefin.

11. The process of claim 1 , wherein the polyolefin is a polyethylene prepared by homopolymerizing ethylene or copolymerizing ethylene and up to about 20 wt. % of C 3 -C 8 1-alkenes, based upon the total weight of the polyethylene.

12. The process of claim 11 , wherein the polyethylene has a MFR 21.6 according to DIN EN ISO 1133:2005 at a temperature of 190° C. under a load of 21.6 kg in a range of from about 0.5 g/10 min to about 350 g/10 min.

13. The process according to claim 11 , wherein the polyethylene has a density in the range of from about 0.935 g/cm 3 to about 0.970 g/cm 3 .

14. The process of claim 11 , wherein the polyethylene is prepared in a polymerization reactor cascade, comprising
(I) a fluidized-bed reactor; and
(II) a multizone circulating reactor,
wherein
(a1) the fluidized-bed reactor is arranged upstream of the multizone circulating reactor, and
(a2) the polyethylene is an ethylene homopolymer or ethylene copolymer, having a MFR 2.16 according to DIN EN ISO 1133:2005 at a temperature of 190° C. under a load of 2.16 kg in a range of from about 0.1 g/10 min to about 300 g/10 min, is produced in the fluidized-bed reactor.

15. The process of claim 1 , wherein the polymerization catalyst is selected from the group consisting of a Ziegler catalyst, a Ziegler-Natta catalyst, a Phillips catalyst, a single-site catalyst and a mixture of catalysts comprising a single-site catalyst.

16. A process for the preparation of polyolefins by polymerizing olefins at temperatures of from 20 to 200° C. and pressures of from 0.1 to 20 MPa in the presence of a polymerization catalyst in a polymerization reactor, wherein the polymerization is carried out in the presence of an antistatic agent comprising an alkylene oxide derived polymer comprising an average of 10 to 200 repeating units of the formula —(CH 2 —CHR—O)—, wherein R comprises hydrogen or an alkyl group having from 1 to 6 carbon atoms, wherein the alkylene oxide derived polymer is a random copolymer of ethylene oxide and other alkylene oxides and a ratio n:m of repeating units of the formula —(CH 2 —CH 2 —O)— derived from ethylene oxide to repeating units —(CH 2 —CHR′—O)— derived from the other alkylene oxides, wherein R′ comprises an alkyl group having from 1 to 6 carbon atoms is in a range of from 1:1 to 6:1, and all end groups of the alkylene oxide derived polymer are —OH groups, and wherein the antistatic agent is introduced into the polymerization reactor by a feed stream of a liquid hydrocarbon and the weight ratio of the antistatic agent to the liquid hydrocarbon in the combined stream introduced into the reactor is in a range from 1:10 to 1:5000.

17. The process of claim 16 , wherein the alkylene oxide derived polymer is a linear polymer of the general formula (I):
HO—(CH 2 —CH 2 —O) n —(CH 2 —CHR′—O) m —H  (I)

wherein R′ comprises an alkyl group having from 1 to 6 carbon atoms, and n and m are the average number of repeating units, wherein n is in a range of from 10 to 180 and m is in a range of from 2 to 120.

18. The process of claim 16 , wherein the alkylene oxide derived polymer is a random copolymer of ethylene oxide and propylene oxide.

19. The process of claim 16 , wherein the polymerization is carried out in a polymerization reactor cascade comprising a fluidized-bed reactor and a multizone circulating reactor, and in the multizone circulating reactor the growing polymer flows upward through a first polymerization zone under fast fluidization or transport conditions, leaves said first polymerization zone and enter a second polymerization zone through which the particles flow downward under the action of gravity, leaves said downcomer and are reintroduced into the riser, thus establishing a circulation of polymer, and the fluidized-bed reactor is arranged upstream of the multizone circulating reactor.

Assignees

• Basell Polyolefine Gmbh

Inventors

• Mannebach Gerd
• Marczinke Bernd Lothar
• Meier Gerhardus
• Schueller Ulf
• Mihan Shahram
• Maus Andreas
• Baita Pietro
• Di Diego Maria
• Marturano Lorella

Classifications

• B01J8/24

  according to "fluidised-bed" technique (B01J8/20 takes precedence) · CPC title

• C08F2/34 Primary

  Polymerisation in gaseous state · CPC title

• C08F2500/12

  Melt flow index or melt flow ratio · CPC title

• C08F10/00 Primary

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

• C08F2500/04

  Broad molecular weight distribution, i.e. Mw/Mn > 6 · CPC title