Bimodal PE resins with improved melt strength

Patent metadata

Field	Value
Publication number	US-11186707-B2
Application number	US-201916710839-A
Country	US
Kind code	B2
Filing date	Dec 11, 2019
Priority date	Apr 20, 2017
Publication date	Nov 30, 2021
Grant date	Nov 30, 2021

Abstract

A method comprising introducing a polymerization feed comprising an α-olefin, a diluent, and a diene to a polymerization system, under polymerization conditions, whereby a polymer product is produced, wherein the diene is present at a level in the range of from about 1 ppm to about 1000 ppm based on the diluent.

First claim

What is claimed is:

1. A method comprising:
introducing a polymerization feed comprising an ethylene, a diluent selected from the group consisting of propane, cyclohexane, isobutane, n-butane, N-pentane, isopentane, neopentane, and n-hexane, and a diene to a first polymerization zone or a second polymerization zone of a polymerization system comprising the first and the second polymerization zones in series, wherein the diene is present in the polymerization feed to the first polymerization zone or the second polymerization zone at a level of less than or equal to about 20 ppm based on an amount of the diluent in said polymerization feed to the first polymerization zone or the second polymerization zone,
polymerizing the ethylene and the diene to produce a polymer product, wherein the polymer product is a bimodal polyethylene resin, and wherein the bimodal polyethylene resin comprises a high molecular weight (HMW) component and a low molecular weight (LMW) component, wherein the HMW component and the LMW component comprise the diene; and
adjusting the amount of the diene, the type of the diene, or both the amount and the type of the diene introduced to the first polymerization zone or the second polymerization zone to alter melt strength, impact strength, crossover modulus, or a combination thereof of the polymer product.

2. The method of claim 1 , wherein the diene is selected from dienes having a boiling point of less than or equal to about 110° C.

3. The method of claim 1 , wherein the diene is selected from the group consisting of conjugated dienes, non-conjugated dienes, and combinations thereof.

4. The method of claim 3 , wherein the diene is selected from the group consisting of C6-C15 straight chain hydrocarbon non-conjugated dienes, C6-C15 branched chain hydrocarbon non-conjugated dienes, C6-C15 cyclic hydrocarbon non-conjugated dienes, and combinations thereof.

5. The method of claim 3 , wherein the non-conjugated diene is selected from the group consisting of straight chain acyclic dienes; branched chain acyclic dienes; single ring alicyclic dienes; multi-ring alicyclic fused and bridged ring dienes; and combinations thereof.

6. The method of claim 3 , wherein the diene is a conjugated diene selected from the group consisting of 1,3-hexadiene, 2,4-hexadiene, 1,3-pentadiene, 1,3-butadiene, 2-methyl-1,3-butadiene, 4-methyl-1,3-pentadiene, 1,3-cyclopentadiene, and combinations thereof.

7. The method of claim 1 , wherein the polymer product exhibits a λ, which is the number of long chain branches (LCB) per million carbon atoms, that is greater than that of a polymer product produced via the same method but absent the presence of the diene.

8. The method of claim 7 , wherein the polymer product exhibits a λ greater than or equal to about 15 LCB/10 6 carbons.

9. The method of claim 1 , wherein the polymer product exhibits an LCB content, as determined by α, which is the fraction of the total carbons that are long chain vertexes determined according to the equation:

α
=

υ
3

M
w

/

M
0

where
υ 3 =number of long branch vertexes,
M W =weight average molecular weight (g/mol), and
M 0 =molecular weight of repeating unit (Da),
that is greater than that of a polymer product produced via the same method but absent the presence of the diene.

10. The method of claim 1 , wherein the polymerization system comprises one or more reactors selected from the group consisting of loop slurry reactors, fluidized bed gas phase reactors, multi-zone reactors, batch reactors, and CSTR reactors.

11. The method of claim 1 , wherein the first and second polymerization zones in series comprise dual loop slurry reactors in series.

12. The method of claim 1 , wherein the LMW component has a weight average molecular weight (M W ) ranging from about 350 g/mol to about 40,000 g/mol; and
wherein the HMW component has a M W ranging from about 50,000 g/mol to about 1,000,000 g/mol.

13. The method of claim 1 , wherein the polymerization is carried out in the presence of a polymerization catalyst selected from the group consisting of chromium catalysts, Ziegler-Naha catalysts, metallocene catalysts, and combinations thereof.

14. The method of claim 1 further comprising producing the HMW component in the first polymerization zone, and wherein the first polymerization zone is upstream of the second polymerization zone.

15. The method of claim 1 , wherein the LMW component has a weight average molecular weight (M W ) ranging from about 1,000 g/mol to about 40,000 g/mol, and wherein the HMW component has a M W ranging from about 50,000 g/mol to about 100,000 g/mol.

16. A method comprising:
enhancing a long chain branching (LCB) of a bimodal polyethylene (PE) polymer comprising a high molecular weight (HMW) component and a low molecular weight (LMW) component while the bimodal PE polymer is being produced in a serial dual loop slurry reactor process by introducing a feed comprising an ethylene, optionally a comonomer, a diluent selected from the group consisting of propane, cyclohexane, isobutane, n-butane, n-pentane, isopentane, neopentane, and n--hexane, and a diene to a polymerization zone in which the HMW component is being produced or to a polymerization zone in which the LMW component is being produced, and adjusting the amount of the diene, the type of the diene, or both the amount and the type of the diene introduced to the polymerization zone in which the HMW component is being produced or the polymerization zone in which the LMW component is being produced to alter melt strength, impact strength, crossover modulus, or a combination thereof of the bimodal PE polymer, and wherein the diene is introduced to the polymerization zone in which the HMW component is being produced or to the polymerization zone in which the LMW component is being produced at a level of less than or equal to about 20 ppm in the feed to the polymerization zone in which the HMW component is being produced or to the polymerization zone in which the LMW component is being produced based on an amount of the diluent present in the feed to the polymerization zone in which the HMW component is being produced or to the polymerization zone in which the LMW component is being produced.

17. The method of claim 16 , wherein the diene is selected from the group consisting of dienes having a boiling point of less than or equal to about 110° C.

18. The method of claim 16 , wherein the diene is selected from the group consisting of conjugated dienes, non-conjugated dienes, and combinations thereof.

19. The method of claim 16 , wherein the diene is selected from the group consisting of 1,5-hexadiene; 1,3-butadiene; isoprene; 1,4-pentadiene; 1,6-heptadiene; 1,7-octadiene; 1,4 hexadiene; 1,9-decadiene; and combinations thereof.

20. The method of claim 16 , wherein the bimodal polyethylene polymer is a bimodal polyethylene (PE) copolymer, wherein the comonomer is present in an amount of less than about 0.5 wt. % based on the total weight of the copolymer, and wherein the comonomer is selected from the group, cons

Assignees

• Chevron Phillips Chemical Co Lp

Inventors

• Beaulieu William B
• Ding Errun

Classifications

• C08L2205/025

  containing two or more polymers of the same hierarchy C08L, and differing only in parameters such as density, comonomer content, molecular weight, structure · CPC title

• C08L2314/02

  Ziegler natta catalyst · CPC title

• C08L2207/068

  Ultra high molecular weight polyethylene · CPC title

• C08L23/083 Primary

  with aliphatic polyenes, i.e. containing two or more carbon-to-carbon double bonds · CPC title

• C08L2207/066

  LDPE (radical process) · CPC title