Reversible chain-transfer in polyolefin polymerization with pyridyldiamide catalysts
AssigneeExxonMobil Chemical Patents Inc.
InventorsJohn R. Hagadorn, Jian Yang, Patrick J. Palafox
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Abstract
A process of producing ethylene α-olefin copolymers, especially ethylene block copolymers, comprising contacting ethylene and a C3 to C10 α-olefin with a transition metal pyridyldiamide (MPN3) catalyst component and an activator, as well as from 10 equivalents to 1000 equivalents relative to the catalyst component of chain transfer agent; isolating an ethylene-α-olefin copolymer having a Tm of less than 140° C., a MWD of less than 2.5, and a weight average molecular weight (Mw) within the range of from 5 kDa to 500 kDa. The chain transfer agent can be selected from Group 2, 12 or Group 13 alkyl or aryl compounds.
Claims64
A process of producing ethylene α-olefin copolymers comprising:
- contacting ethylene and a C3 to C10 α-olefin with a transition metal pyridyldiamide catalyst component and an activator, as well as from 10 equivalents to 1000 equivalents relative to the catalyst component of chain transfer agent;
- isolating an ethylene-α-olefin copolymer having a Tm of less than 140° C., a Mw/Mn of less than 2.5, and a weight average molecular weight (Mw) within the range of from 5 kDa to 500 kDa, wherein the contacting first takes place in the absence of the chain transfer agent and ethylene-α-olefin copolymer is first isolated having a weight average molecular weight (Mw) within the range of greater than 200 kDa;
- followed by addition of the chain transfer agent and isolation of ethylene-α-olefin copolymer having a Mw of less than 400 kDa.
A process of producing ethylene α-olefin copolymers comprising:
- contacting ethylene and a C3 to C10 α-olefin with a transition metal pyridyldiamide catalyst component and an activator, as well as from 10 equivalents to 1000 equivalents relative to the catalyst component of chain transfer agent;
- isolating an ethylene-α-olefin copolymer having a Tm of less than 140° C., a Mw/Mn of less than 2.5, and a weight average molecular weight (Mw) within the range of from 5 kDa to 500 kDa, wherein the contacting first takes place in the absence of the chain transfer agent and ethylene-α-olefin copolymer is first isolated having a Mw/Mn within the range of from 1.5 to 2.5;
- followed by addition of the chain transfer agent and isolation of ethylene-α-olefin copolymer having a Mw/Mn of less than 2.0.
A process of producing ethylene α-olefin copolymers comprising:
- contacting ethylene and a C3 to C10 α-olefin with a transition metal pyridyldiamide catalyst component and an activator, as well as from 10 equivalents to 1000 equivalents relative to the catalyst component of chain transfer agent;
- wherein the contacting first takes place in the absence of the chain transfer agent and ethylene-α-olefin copolymer is first isolated having a weight average molecular weight (Mw) within the range of greater than 200 kDa;
- followed by addition of chain transfer agent and isolation of ethylene-α-olefin copolymer having a Mw of less than 400 kDa, or within a range of from 5 kDa to 200 kDa.
A process of producing ethylene α-olefin copolymers comprising:
- contacting ethylene and a C3 to C10 α-olefin with a transition metal pyridyldiamide catalyst component and an activator, as well as from 10 equivalents to 1000 equivalents relative to the catalyst component of chain transfer agent;
- wherein the contacting first takes place in the absence of chain transfer agent and ethylene-α-olefin copolymer is first isolated having a Mw/Mn within the range of from 1.5 to 2.5;
- followed by addition of the chain transfer agent and isolation of ethylene-α-olefin copolymer having a Mw/Mn of less than 2.0.
A process of producing ethylene α-olefin copolymers comprising:
- contacting ethylene and a C3 to C10 α-olefin with a transition metal pyridyldiamide catalyst component and an activator, as well as from 10 equivalents to 1000 equivalents relative to the catalyst component of diphenyl zinc chain transfer agent;
- isolating an ethylene-α-olefin copolymer having a Tm of less than 140° C., a Mw/Mn of less than 2.5, and a weight average molecular weight (Mw) within the range of from 5 kDa to 500 kDa, wherein the presence of the chain transfer agent increases the activity of the catalyst component by a factor of at least 2 relative to the activity under the same conditions when chain transfer agent is not present.
Dependencies are inferred from the claim text.