Olefin polymerization process

Claim 2

A multiple zone process which comprises: (a) polymerizing an olefin in a first reaction zone with a single-site catalyst in the presence of a non-alumoxane activator at a temperature within the range of about 130° C. to about 200° C. to produce a first polymer having a weight average molecular weight (Mw) within the range of about 5,000 to about 500,000; and (b) transferring the first polymer to a second reaction zone at a higher temperature within the range of about 140° C. to about 280° C. with additional olefin in the presence of a Ziegler-Natta catalyst to produce a final polymer composition having a density less than about 0.98 g/mL and Ml 2 within the range of about 0.5 to about 300 dg/min.

Claim 3

The process of claim 1 wherein the temperature of the first reaction zone is within the range of about 130° C. to about 150° C.

Claim 4

An adiabatic process of claim 1.

Claim 5

A solution polymerization process of claim 1.

Claim 6

The process of claim 1 wherein the olefin is selected from the group consisting of ethylene, propylene, 1-butene, 1-pentene, 1-hexene, 1-octene, and mixtures thereof.

Claim 7

The process of claim 1 wherein the olefin is ethylene.

Claim 8

The process of claim 1 wherein the single-site catalyst contains a heteroatomic ligand selected the group consisting of boraaryl, azaborolinyl, pyridinyl, pyrrolyl, and quinolinyl.

Claim 9

The process of claim 1 wherein the non-alumoxane activator is selected from the group consisting of alkyl aluminums, alkyl aluminum halides, anionic compounds of boron or aluminum, trialkylboron compounds, and triarylboron compounds.

Claim 10

The process of claim 1 wherein the Ziegler-Natta catalyst is selected from the group consisting of titanium halides, titanium alkoxides, vanadium halides, and mixtures thereof.

Claim 11

The process of claim 1 wherein the process is performed at a pressure within the range of about 500 psi to about 5,000 psi.

Claim 12

A multiple zone process which comprises: (a) polymerizing an olefin in a first reaction zone with a single-site catalyst that contains at least one heteroatomic ligand selected from the group consisting of boraaryl, azaborolinyl, pyridinyl, pyrrolyl, and quinolinyl, in the presence of a non-alumoxane activator at a temperature within the range of about 130° C. to about 200° C. to produce a first polymer having a weight average molecular weight (Mw) within the range of about 5,000 to about 500,000; and (b) transferring the first polymer to a second reaction zone at a higher temperature within the range of about 140° C. to about 280° C. with additional olefin in the presence of a Ziegler-Natta catalyst to produce a final polymer composition having a density less than about 0.98 g/mL and Ml 2 within the range of about 0.5 to about 300 dg/min.

Claim 13

A multiple zone process which comprises: (a) polymerizing an olefin in a first reaction zone with a single-site catalyst that contains at least one heteroatomic ligand selected from the group consisting of boraaryl, azaborolinyl, pyridinyl, pyrrolyl, and quinolinyl, in the presence of a non-alumoxane activator at a temperature within the range of about 130° C. to about 200° C. to produce a first polymer having a weight average molecular weight (Mw) within the range of about 5,000 to about 500,000; and (b) transferring the first polymer to a second reaction zone at a higher temperature within the range of about 140° C. to about 280° C. with additional olefin in the presence of a Ziegler-Natta catalyst to produce a final polymer composition having a density less than about 0.98 g/mL and Ml 2 within the range of about 0.5 to about 300 dg/min.

Claim 14

A multiple stage process which comprises: (a) in a first stage, polymerizing an olefin with a single-site catalyst in a reactor in the presence of a non-alumoxane activator at a temperature within the range of about 130° C. to about 200° C. to produce a first polymer having Mw within the range of about 5,000 to about 500,000; and (b) continuing polymerization in a second stage by adding a Ziegler-Natta catalyst and additional olefin to the reactor at a higher temperature within the range of about 140° C. to about 280° C. to produce a final polymer composition having a density less than about 0.98 g/mL and Ml 2 within the range of about 0.5 to about 300 dg/min.

Claim 15

A multiple stage process which comprises: (a) in a first stage, polymerizing an olefin with a single-site catalyst in a reactor in the presence of a non-alumoxane activator at a temperature within the range of about 130° C. to about 200° C. to produce a first polymer having Mw within the range of about 5,000 to about 500,000; and (b) continuing polymerization in a second stage by adding a Ziegler-Natta catalyst and additional olefin to the reactor at a higher temperature within the range of about 140° C. to about 280° C. to produce a final polymer composition having a density less than about 0.98 g/mL and Ml 2 within the range of about 0.5 to about 300 dg/min.

Claim 16

The process of claim 12 wherein the temperature for the first stage is within the range of about 130° C. to about 150° C.

Claim 17

An adiabatic process of claim 12.

Claim 18

A solution polymerization process of claim 12.

Claim 19

The process of claim 12 wherein the olefin is selected from the group consisting of ethylene, propylene, 1-butene, 1-pentene, 1-hexene, 1-octene, and mixtures thereof.

Claim 20

The process of claim 12 wherein the olefin is ethylene.

Claim 21

The process of claim 12 wherein the single-site catalyst contains a heteroatomic ligand selected the group consisting of boraaryl, azaborolinyl, pyridinyl, pyrrolyl, and quinolinyl.

Claim 22

The process of claim 12 wherein the non-alumoxane activator is selected from the group consisting of alkyl aluminums, alkyl aluminum halides, anionic compounds of boron or aluminum, trialkylboron compounds, and triarylboron compounds.

Claim 23

The process of claim 12 wherein the Ziegler-Natta catalyst is selected from the group consisting of titanium halides, titanium alkoxides, vanadium halides, and mixtures thereof.

Claim 24

The process of claim 12 wherein the process is performed under pressure of about 500 psi to about 5,000 psi.

Claim 25

A multiple stage process which comprises: (a) in a first stage, polymerizing an olefin with a single-site catalyst that contains at least one heteroatomic ligand selected from the group consisting of boraaryl, azaborolinyl, pyridinyl, pyrrolyl, and quinolinyl, in a reactor in the presence of a non-alumoxane activator at a temperature within the range of about 130° C. to about 200° C. to produce a first polymer having Mw within the range of about 5,000 to about 500,000; and (b) continuing polymerization in a second stage by adding a Ziegler-Natta catalyst and additional olefin to the reactor at a higher temperature within the range of about 140° C. to about 280° C. to produce a final polymer composition having a density less than about 0.98 g/mL and Ml 2 within the range of about 0.5 to about 300 dg/min.

Claim 26

A multiple stage process which comprises: (a) in a first stage, polymerizing an olefin with a single-site catalyst that contains at least one heteroatomic ligand selected from the group consisting of boraaryl, azaborolinyl, pyridinyl, pyrrolyl, and quinolinyl, in a reactor in the presence of a non-alumoxane activator at a temperature within the range of about 130° C. to about 200° C. to produce a first polymer having Mw within the range of about 5,000 to about 500,000; and (b) continuing polymerization in a second stage by adding a Ziegler-Natta catalyst and additional olefin to the reactor at a higher temperature within the range of about 140° C. to about 280° C. to produce a final polymer composition having a density less than about 0.98 g/mL and Ml 2 within the range of about 0.5 to about 300 dg/min.

Claim 27

A parallel multiple zone process which comprises: (a) polymerizing an olefin in a first reaction zone with a single-site catalyst in the presence of a non-alumoxane activator at a temperature within the range of about 130° C. to about 200° C. to produce a first polymer having Mw within the range of about 5,000 to about 500,000; (b) polymerizing an olefin in a second reaction zone that is parallel to the first reaction zone at a higher temperature within the range of about 140° C. to about 280° C. in the presence of a Ziegler-Natta catalyst to produce a second polymer having Mw within the range of about 20,000 to about 500,000; and (c) combining the first and second polymers in a third reaction zone to continue the polymerization at a temperature within the range of about 140° C. to about 280° C. with additional olefin in the presence of a Ziegler-Natta catalyst to produce a final polymer composition having a density less than about 0.98 g/mL and Ml 2 within the range of about 0.5 to about 300 dg/min.

Claim 28

A parallel multiple zone process which comprises: (a) polymerizing an olefin in a first reaction zone with a single-site catalyst in the presence of a non-alumoxane activator at a temperature within the range of about 130° C. to about 200° C. to produce a first polymer having Mw within the range of about 5,000 to about 500,000; (b) polymerizing an olefin in a second reaction zone that is parallel to the first reaction zone at a higher temperature within the range of about 140° C. to about 280° C. in the presence of a Ziegler-Natta catalyst to produce a second polymer having Mw within the range of about 20,000 to about 500,000; and (c) combining the first and second polymers in a third reaction zone to continue the polymerization at a temperature within the range of about 140° C. to about 280° C. with additional olefin in the presence of a Ziegler-Natta catalyst to produce a final polymer composition having a density less than about 0.98 g/mL and Ml 2 within the range of about 0.5 to about 300 dg/min.

Claim 29

A parallel multiple zone process which comprises: (a) polymerizing an olefin in a first reaction zone with a single-site catalyst that contains at least one heteroatomic ligand selected from the group consisting of boraaryl, azaborolinyl, pyridinyl, pyrrolyl, and quinolinyl, in the presence of a non-alumoxane activator at a temperature within the range of about 130° C. to about 200° C. to produce a first polymer having Mw within the range of about 5,000 to about 500,000; (b) polymerizing an olefin in a second reaction zone that is parallel to the first reaction zone at a higher temperature within the range of about 140° C. to about 280° C. in the presence of a Ziegler-Natta catalyst to produce a second polymer having Mw within the range of about 20,000 to about 500,000; and (c) combining the first and second polymers in a third reaction zone to continue the polymerization at a temperature within the range of about 140° C. to about 280° C. with additional olefin in the presence of a Ziegler-Natta catalyst to produce a final polymer composition having a density less than about 0.98 g/mL and Ml 2 within the range of about 0.5 to about 300 dg/min.

Claim 30

A parallel multiple zone process which comprises: (a) polymerizing an olefin in a first reaction zone with a single-site catalyst that contains at least one heteroatomic ligand selected from the group consisting of boraaryl, azaborolinyl, pyridinyl, pyrrolyl, and quinolinyl, in the presence of a non-alumoxane activator at a temperature within the range of about 130° C. to about 200° C. to produce a first polymer having Mw within the range of about 5,000 to about 500,000; (b) polymerizing an olefin in a second reaction zone that is parallel to the first reaction zone at a higher temperature within the range of about 140° C. to about 280° C. in the presence of a Ziegler-Natta catalyst to produce a second polymer having Mw within the range of about 20,000 to about 500,000; and (c) combining the first and second polymers in a third reaction zone to continue the polymerization at a temperature within the range of about 140° C. to about 280° C. with additional olefin in the presence of a Ziegler-Natta catalyst to produce a final polymer composition having a density less than about 0.98 g/mL and Ml 2 within the range of about 0.5 to about 300 dg/min.