Methods of modifying the melt flow ratio and/or swell of polyethylene resins

Patent metadata

Field	Value
Publication number	US-2017137551-A1
Application number	US-201515319301-A
Country	US
Kind code	A1
Filing date	Apr 9, 2015
Priority date	Jun 16, 2014
Publication date	May 18, 2017
Grant date	—

Abstract

Methods of making polyethylene resins are provided. More particularly methods of modifying the melt flow ratio and swell characteristics of polyethylene resins are provided.

First claim

1 . A method of modifying the melt flow ratio (I 21 /I 5 ) measured according to ASTM-D-1238 (I 21 and I 5 measured at 190° C. and 21.6 kg or 5 kg weight respectively) of a polyethylene resin, the method comprising:
a) feeding a catalyst system comprising at least two different catalyst compounds, hydrogen, ethylene, and optionally a comonomer to a polymerization reactor;
wherein the at least two different catalyst compounds produce different average molecular weight polyethylene at the same ratio of hydrogen to ethylene; and
b) adjusting both the ratio of hydrogen to ethylene in the reactor between 10 ppm/mole % and 15 ppm/mole % and
a ratio of the in-reactor catalyst compound ratio from 2.5 to 1.8 to maintain a flow index, I 21 , value substantially constant while modifying the melt flow ratio (I 21 /I 5 ).

2 . (canceled)

3 . The method of claim 1 wherein the melt flow ratio increases as the ratio of hydrogen to ethylene increases.

4 . The method of claim 1 further comprising adjusting the ratio of the at least two different catalyst compounds of the catalyst system.

5 . The method of claim 1 wherein both the ratio of hydrogen to ethylene and the ratio of the at least two different catalyst compounds of the catalyst system are adjusted to modify or control the flow index of the polyethylene.

6 . The method of claim 1 comprising co-feeding to the polymerization reactor a supported catalyst comprising at least two different catalyst compounds and a trim catalyst comprising at least one of the catalyst compounds of the supported catalyst.

7 . The method of claim 6 wherein the ratio of the catalyst compounds of the catalyst system is adjusted by increasing or decreasing the feed rate of the trim catalyst relative to the feed rate of the supported catalyst.

8 . The method of claim 6 wherein the trim catalyst is a non-supported catalyst compound.

9 . The method of claim 6 wherein the trim catalyst is mixed with the supported catalyst prior to feeding to the reactor.

10 . The method of claim 1 wherein the in-reactor ratio of the catalyst compounds of the catalyst system is adjusted within a range from about 0.1 to about 10.0, on a molar basis.

11 . The method of claim 1 further comprising adjusting the temperature of the polymerization reactor.

12 . The method of claim 1 wherein the catalyst system comprises at least one metallocene catalyst compound and/or at least one Group 15 and metal containing catalyst compound.

13 . The method of claim 1 wherein the catalyst system comprises bis(cyclopentadienyl) zirconium X 2 , wherein the cyclopentadienyl group may be substituted or unsubstituted, and at least one of a bis(arylamido) zirconium X 2 and a bis(cycloalkylamido) zirconium X 2 , wherein X represents a leaving group.

14 . The method of claim 1 wherein the polyethylene is a bimodal or a multimodal polyethylene.

15 . The method of claim 1 , wherein the polyethylene resin has a melt flow ratio (I 21 /I 5 ) in the range from about 10 to about 60, measured according to ASTM-D-1238 (I 21 and I 5 measured at 190° C. and 21.6 kg or 5 kg weight respectively), a flow index, I 21 , in the range from about 2 to about 60 dg/min, and a density of greater than or equal to about 0.945 g/cc, measured according to ASTM D 792.

16 . The method of claim 1 , wherein the polymerization reactor is a single reactor or multiple reactors arranged either in series or in parallel.

17 . The method of claim 16 , wherein the single polymerization reactor is a gas phase reactor.

18 . The method of claim 1 , wherein the hydrogen to ethylene ratio is adjusted to within a range from about 0.0001 to about 0.01, on a molar basis.

19 . The method of claim 12 wherein the ratio of the at least one Group 15 metal containing component to metallocene component is adjusted within a range from about 0.5 to about 6.0, on a molar basis.

20 . The method of claim 1 , wherein said comonomer comprises at least one of 1-butene, 1-hexene, and 1-octene.

21 .- 27 . (canceled)

Assignees

• Univation Tech Llc

Inventors

• Pequeno R Eric
• Savatsky Bruce J
• Martin Peter S
• Lynn Timothy R

Classifications

• B29D22/003

  Containers for packaging, storing or transporting, e.g. bottles, jars, cans, barrels, tanks · CPC title

• B29C49/0005

  characterised by the material · CPC title

• C08F210/16 Primary

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

• C08F10/02

  Ethene · CPC title