Method of production of ethylene-based polymer particles and stretch-molded article obtained from ethylene-based polymer particles
US-9181359-B2 · Nov 10, 2015 · US
US9493587B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9493587-B2 |
| Application number | US-201213980920-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jan 19, 2012 |
| Priority date | Jan 20, 2011 |
| Publication date | Nov 15, 2016 |
| Grant date | Nov 15, 2016 |
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Use of homogeneous catalytic systems which include as a pre-catalyst a complex of a group 4 metal and a Salan ligand in the polymerization of alpha-olefins, is disclosed. The Salan ligand is characterized by a sequential diamino-containing skeleton unit which is non-symmetric, and the pre-catalysts can also be such that are devoid of a symmetry element. The disclosed polymerization results in alpha-olefin polymers such as polypropylene which are characterized by high levels of tacticity. Also disclosed are novel Salan ligands and novel complexes thereof with group 4 metals.
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What is claimed is: 1. A process of polymerizing an alpha-olefin, the process comprising contacting the alpha-olefin with a catalyst system which comprises: (i) a pre-catalyst comprising a group 4 element being in coordination with a Salan ligand, said Salan ligand comprising two substituted or unsubstituted phenol moieties and a sequential diamino-containing skeleton unit linking said phenol moieties, wherein said sequential diamino-containing skeleton unit is non-symmetric and said pre-catalyst is devoid of a symmetry element; and (ii) a co-catalyst, thereby polymerizing the alpha-olefin. 2. The process of claim 1 , wherein said pre-catalyst is represented by general Formula II: wherein: Q is MXn, whereas M is a group 4 element; X is a labile group; and n is 0, 1, 2, 3 or 4; Z and Y are each independently a substituted or unsubstituted alkylene chain being from 1 to 5 carbon atoms in length, such that Z and Y form together an alkylene chain that is 2 to 10 carbon atoms in length; each of R 1 -R 8 is independently selected from the group consisting of hydrogen, alkyl, cycloalkyl, aryl, halogen, alkoxy, aryloxy, heteroalicyclic, heteroaryl, and nitro, provided that at least one of R 1 -R 4 is other than hydrogen; and each of R and R′ is independently selected from the group consisting of hydrogen, alkyl, cycloalkyl and aryl, provided that at least one of R and R′ is hydrogen; and provided that when R and R′ are the same. Y is different from Z; and (ii) a co-catalyst, thereby polymerizing the alpha-olefin. 3. The process of claim 2 , wherein each of R 1 -R 4 is independently halogen. 4. The process of claim 2 , wherein at least one of R 1 -R 4 is a bulky substituent. 5. The process of claim 4 , wherein said bulky substituent comprises a bulky rigid group. 6. The process of claim 4 , wherein R 1 is adamantyl. 7. The process of claim 2 , wherein Z is selected from the group consisting of (CRaRb), (CRaRb)(CRcRd) and (CRaRb)(CRcRd)(CReRf), and Y is selected from the group consisting of (CRgRh), (CRgRh)(CRiRj) and (CRgRh)(CRiRj)(CRkRp), wherein each of Ra-Rp is independently selected from the group consisting of hydrogen, alkyl, cycloalkyl, aryl, halogen, alkoxy, aryloxy, and/or at least two of Ra-Rp, R′ and R form together a five-or six-membered, aromatic or non-aromatic ring. 8. The process of claim 2 , wherein R′ is hydrogen. 9. The process of claim 8 , wherein R is alkyl. 10. The process of claim 1 , wherein said alpha-olefin is propylene. 11. A process of polymerizing an alpha-olefin, the process comprising contacting the alpha-olefin with a catalyst system which comprises: (i) a pre-catalyst comprising a group 4 element being in coordination with a Salan ligand, said Salan ligand comprising two substituted or unsubstituted phenol moieties and a sequential diamino-containing skeleton unit linking said phenol moieties, wherein said sequential diamino-containing skeleton unit is non-symmetric and said pre-catalyst is devoid of a symmetry element; and (ii) a co-catalyst, thereby polymerizing the alpha-olefin, wherein said pre-catalyst is represented by general Formula II: wherein: Q is MXn, whereas M is a group 4 element; X is a labile group; and n is 0, 1, 2, 3 or 4; Z and Y are each independently a substituted or unsubstituted alkylene chain being from 1 to 5 carbon atoms in length, such that Z and Y form together an alkylene chain that is 2 to 10 carbon atoms in length; each of R 1 -R 4 is independently halogen; each of R 5 -R 8 is independently selected from the group consisting of hydrogen, alkyl, cycloalkyl, aryl, halogen, alkoxy, aryloxy, heteroalicyclic, heteroaryl, and nitro; and each of R and R′ is independently selected from the group consisting of hydrogen, alkyl, cycloalkyl and aryl, provided that at least one of R and R′ is hydrogen; and provided that when R and R′ are the same, Y is different from Z. 12. A process of polymerizing an alpha-olefin, the process comprising contacting the alpha-olefin with a catalyst system which comprises: (i) a pre-catalyst comprising a group 4 element being in coordination with a Salan ligand, said Salan ligand comprising two substituted or unsubstituted phenol moieties and a sequential diamino-containing skeleton unit linking said phenol moieties, wherein said sequential diamino-containing skeleton unit is non-symmetric and said pre-catalyst is devoid of a symmetry element; and (ii) a co-catalyst, thereby polymerizing the alpha-olefin, wherein said pre-catalyst is represented by general Formula II: wherein: Q is MXn, whereas M is a group 4 element; X is a labile group; and n is 0, 1, 2, 3 or 4; Z and Y are each independently a substituted or unsubstituted alkylene chain being from 1 to 5 carbon atoms in length, such that Z and Y form together an alkylene chain that is 2 to 10 carbon atoms in length; each of R 1 -R 8 is independently selected from the group consisting of hydrogen, alkyl, cycloalkyl, aryl, halogen, alkoxy, aryloxy, heteroalicyclic, heteroaryl, and nitro, provided that at least one of R 1 -R 4 is a bulky substituent which comprises a bulky rigid group; and each of R and R′ is independently selected from the group consisting of hydrogen, alkyl, cycloalkyl and aryl, provided that at least one of R and R′ is hydrogen; and provided that when R and R′ are the same, Y is different from Z. 13. A process of polymerizing an alpha-olefin, the process comprising contacting the alpha-olefin with a catalyst system which comprises: (i) a pre-catalyst comprising a group 4 element being in coordination with a Salan ligand, said Salan ligand comprising two substituted or unsubstituted phenol moieties and a sequential diamino-containing skeleton unit linking said phenol moieties, wherein said sequential diamino-containing skeleton unit is non-symmetric and said pre-catalyst is devoid of a symmetry element; and (ii) a co-catalyst, thereby polymerizing the alpha-olefin, wherein said pre-catalyst is represented by general Formula II: wherein: Q is MXn, whereas M is a group 4 element; X is a labile group; and n is 0, 1, 2, 3 or 4; Z and Y are each independently a substituted or unsubstituted alkylene chain being from 1 to 5 carbon atoms in length, such that Z and Y form together an alkylene chain that is 2 to 10 carbon atoms in length; R 1 is adamantyl; each of R 2 -R 8 is independently selected from the group consisting of hydrogen, alkyl, cycloalkyl, aryl, halogen, alkoxy, aryloxy, heteroalicyclic, heteroaryl, and nitro; and each of R and R′ is independently selected from the group consisting of hydrogen, alkyl, cycloalkyl and aryl, provided that at least one of R and R′ is hydrogen; and provided that when R and R′ are the same, Y is different from Z.
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