Methods of changing polyolefin production rate with the composition of the induced condensing agents

Patent metadata

Field	Value
Publication number	US-10174142-B2
Application number	US-201515527997-A
Country	US
Kind code	B2
Filing date	Nov 24, 2015
Priority date	Nov 25, 2014
Publication date	Jan 8, 2019
Grant date	Jan 8, 2019

Abstract

Polyolefin polymerization performed by contacting in a reactor an olefin monomer and optionally a comonomer with a catalyst system in the presence of induced condensing agents (ICA) and optionally hydrogen. The ICA may include two or more ICA components where the composition of the ICA (i.e., the concentration of each ICA component) may affect the polyolefin production rate. Changes to the relative concentration of the two or more ICA components may be according to ICA equivalency factors that allow for increasing the polyolefin production rate while maintain a sticking temperature, increasing polyolefin production rate while increasing the dew point approach temperature of the ICA, or a combination thereof.

First claim

The invention claimed is:

1. A method comprising:
contacting in a fluidized bed gas phase reactor an olefin monomer with a catalyst system in the presence of an induced condensing agent (ICA) and optionally hydrogen to produce a polyolefin having a sticking temperature, wherein the ICA comprises a first ICA component and a second ICA component;
operating the fluidized bed gas phase reactor at an operating temperature lower than the sticking temperature of the polyolefin;
withdrawing a gas phase composition comprising at least some of the olefin, at least some of the ICA, and optionally at least some hydrogen;
condensing a portion of the ICA from the gas phase composition yielding a condensed ICA;
recycling at least a portion of the condensed ICA and at least a portion of the gas phase composition to the fluidized bed gas phase reactor; and
changing a mole percent of total reactor gas for each of the first and the second ICA components according to a first ICA to second ICA equivalency factor whereby one mole of the second ICA component is substituted with a predetermined number of moles of the first ICA component so as to cause a dew point approach temperature of the ICA to increase, wherein the dew point approach temperature is an operating temperature of the reactor minus a dew point of the condensed recycle stream.

2. The method of claim 1 further comprising:
contacting in the fluidized bed gas phase reactor the olefin monomer and at least one comonomer with the catalyst system in the presence of the ICA and optionally hydrogen to produce the polyolefin.

3. The method of claim 2 , wherein the olefin monomer is ethylene and the at least one comonomer is selected from the group consisting of propylene, 1-butene, 1-pentene, 1-hexene, 1-heptene, 1-octene, 4-methylpent-1-ene, 1-decene, 1-dodecene, 1-hexadecene, 1,3-hexadiene, 1,4-hexadiene, cyclopentadiene, dicyclopentadiene, 4-vinylcyclohex-1-ene, methyloctadiene, 1-methyl-1,6-octadiene, 7-methyl-1,6-octadiene, 1,5-cyclooctadiene, norbornadiene, ethylidene norbornene, 5-vinylidene-2-norbornene, 5-vinyl-2-norbornene, isoprene, styrene, butadiene, isobutylene, chloroprene, acrylonitrile, and a cyclic olefin.

4. The method of claim 1 , wherein the first ICA is n-butane, the second ICA is isopentane, and the first ICA to second ICA equivalency factor is about 1.5 to about 3.5.

5. The method of claim 1 , wherein the first ICA is n-pentane, the second ICA is isopentane, and the first ICA to second ICA equivalency factor is about 0.8 to about 1.2.

6. The method of claim 1 , wherein the first ICA is hexane, the second ICA is isopentane, and the first ICA to second ICA equivalency factor is about 0.2 to about 0.4.

7. A method comprising:
contacting in a fluidized bed gas phase reactor an olefin monomer with a catalyst system in the presence of an induced condensing agent (ICA) and optionally hydrogen to produce a polyolefin having a sticking temperature, wherein the ICA comprises a first ICA component and a second ICA component;
operating the fluidized bed gas phase reactor at an operating temperature lower than the sticking temperature of the polyolefin;
withdrawing a gas phase composition comprising at least some of the olefin, at least some of the ICA, and optionally at least some hydrogen;
condensing a portion of the ICA from the gas phase composition yielding a condensed ICA;
recycling at least a portion of the condensed ICA and at least a portion of the gas phase composition to the fluidized bed gas phase reactor; and
changing a mole percent of total reactor gas for each of the first and the second ICA components according to a first ICA component to second ICA component equivalency factor whereby one mole of the second ICA component is substituted with a predetermined number of moles of the first ICA component thereby maintaining the sticking temperature of the polyolefin and increasing the dew point approach temperature.

8. The method of claim 7 further comprising:
contacting in the fluidized bed gas phase reactor the olefin monomer and at least one comonomer with the catalyst system in the presence of the ICA and optionally hydrogen to produce the polyolefin.

9. The method of claim 7 , wherein the first ICA is n-butane, the second ICA is isopentane, and the first ICA to second ICA equivalency factor is about 1.5 to about 3.5.

10. The method of claim 7 , wherein the first ICA is n-pentane, the second ICA is isopentane, and the first ICA to second ICA equivalency factor is about 0.8 to about 1.2.

11. The method of claim 7 , wherein the first ICA is hexane, the second ICA is isopentane, and the first ICA to second ICA equivalency factor is about 0.2 to about 0.4.

12. A method comprising:
contacting in a fluidized bed gas phase reactor an olefin monomer with a catalyst system in the presence of an induced condensing agent (ICA) and optionally hydrogen to produce a polyolefin having a sticking temperature, wherein the ICA comprises a first ICA component and a second ICA component;
operating the fluidized bed gas phase reactor at an operating temperature lower than the sticking temperature of the polyolefin;
withdrawing a gas phase composition comprising at least some of the olefin, at least some of the ICA, and optionally at least some hydrogen;
condensing a portion of the ICA from the gas phase composition yielding a condensed ICA;
recycling at least a portion of the condensed ICA and at least a portion of the gas phase composition to the fluidized bed gas phase reactor; and
increasing a polyolefin production rate by changing a mole percent of total reactor gas for each of the first and the second ICA components according to a first ICA component to second ICA component equivalency factor whereby one mole of the second ICA component is substituted with a predetermined number of moles of the first ICA component while maintaining the sticking temperature, thereby increasing a dew point approach temperature of the ICA, wherein the dew point approach temperature is an operating temperature of the reactor minus a dew point of the condensed recycle stream.

13. The method of claim 12 further comprising:
contacting in the fluidized bed gas phase reactor the olefin monomer and at least one comonomer with the catalyst system in the presence of the ICA and optionally hydrogen to produce the polyolefin.

14. The method of claim 12 , wherein the first ICA is n-butane, the second ICA is isopentane, and the first ICA to second ICA equivalency factor is about 1.5 to about 3.5.

15. The method of claim 12 , wherein the first ICA is n-pentane, the second ICA is isopentane, and the first ICA to second ICA equivalency factor is about 0.8 to about 1.2.

16. The method of claim 12 , wherein the first ICA is hexane, the second ICA is isopentane, and the first ICA to second ICA equivalency factor is about 0.2 to about 0.4.

Assignees

• Univation Tech Llc

Inventors

• Savatsky Bruce J
• Locklear Brandon C
• Pequeno R Eric
• Hari Abarajith S
• Glowczwski David M

Classifications

• B01J2208/00061

  of the reactants · CPC title

• B01J2219/00213

  Fixed parameter value · CPC title

• B01J8/24

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

• C08F10/02

  Ethene · CPC title

• B01J2219/002

  inside the reactor · CPC title