IP Library Granted Patent US 8,372,996
Granted Patent B2
US 8,372,996 · App. 13/063,513 · Granted Feb 12, 2013

Transition metal catalytic systems and methods for preparing ethylene homopolymers or copolymers of ethylene and α-olefins using the same

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Quick Facts
Patent No.
US 8,372,996
App. No.
13/063,513
Granted
Feb 12, 2013
Kind
B2
Abstract

Provided are transition metal catalytic systems for preparing ethylene homopolymers or copolymers of ethylene with α-olefins. More specifically, provided are Group 4 transition metal catalysts, which is characterized in that the Group 4 transition metal catalyst comprises around the Group 4 transition metal a cyclopentadiene derivative, and at least one naphthoxide ligand(s) having aryl substituent(s) that function(s) as an electron donor and serve(s) to stabilize the catalyst system by surrounding an oxygen atom that links the ligand to the transition metal at 2-position, and there is no cross-linkage between the ligands; catalytic systems comprising such transition metal catalyst and aluminoxane cocatalyst or boron compound cocatalyst; and processes for preparing ethylene homopolymers or copolymers of ethylene with α-olefins by using the same.

Claims (23)

1. A transition metal compound represented by Chemical Formula (1):

wherein, M represents transition metal from Group 4 in the Periodic Table of Elements;

Cp represents a cyclopentadienyl ring which is η 5 -linkable to M, or a fused ring containing a cyclopentadienyl ring, in which the cyclopentadienyl ring or the fused ring containing a cyclopentadienyl ring is optionally further substituted by (C1-C20)alkyl, (C6-C30)aryl, (C2-C20)alkenyl or (C6-C30)ar(C1-C20)alkyl;

Ar represents (C6-C30)aryl, but Ar is not fluorenyl;

X 1 and X 2 are independently selected from a group consisting of halogen atoms, (C1-C20)alkyl, (C3-C20)cycloalkyl, (C6-C13)aryl, (C1-C10)alkyl(C6-C13)aryl, (C6-C30)ar(C1-C20)alkyl, (C1-C20)alkoxy, (C3-C20)alkylsiloxy, (C1-C20)alkylamino, (C6-C30)arylamino, (C1-C20)alkylphosphine, (C6-C30)arylphosphine, (C1-C20)alkylmercapto and (C6-C30)arylmercapto;

m is an integer selected from 0 to 4, n is an integer from 0 to 2;

R represents (C1-C10)alkyl, (C3-C10)cycloalkyl, (C6-C13)aryl, (C1-C10)alkyl(C6-C13)aryl, (C6-C13)ar(C1-C10)alkyl or (C1-C10)alkoxy, and

the alkyl, cycloalkyl, alkylaryl, aralkyl, alkoxy, alkylsiloxy, alkylamino, arylamino, alkylphosphine, arylphosphine, alkylmercapto, arylmercapto of X 1 and X 2 ; the alkyl, cycloalkyl, aryl, alkylaryl, aralkyl, alkoxy of R; and the aryl of Ar are optionally further substituted by one or more substituent(s) selected from a group consisting of (C1-C10)alkyl, (C3-C10)cycloalkyl, (C6-C13)aryl, (C1-C10)alkyl(C6-C13)aryl, (C6-C13)ar(C1-C10)alkyl and (C1-C10)alkoxy, or each of them is optionally linked to an adjacent substituent via (C3-C12)alkylene or (C3-C12)alkenylene with or without a fused ring to form an alicyclic ring, or a monocyclic or polycyclic aromatic ring.

2. The transition metal compound according to claim 1 , which is selected from those represented by one of Chemical Formulas (1-1) to (1-3):

wherein, M is selected from a group consisting of titanium, zirconium and hafnium;

Cp represents cyclopentadienyl or pentamethylcyclopentadienyl;

X 1 and X 2 are independently selected from a group consisting of chloride, methyl, methoxy, isopropoxy, benzyl and dimethylamino; and

R 1 , R 2 and R 11 through R 16 are independently selected from a group consisting of hydrogen atom, (C1-C10)alkyl, (C3-C10)cycloalkyl, (C6-C13)aryl, (C1-C10)alkyl(C6-C13)aryl, (C6-C13)aryl(C1-C10)alkyl and (C1-C10)alkoxy.

3. The transition metal compound according to claim 2 , which is selected from the following compounds:

wherein, Cp represents cyclopentadienyl or pentamethylcyclopentadienyl; and

X 1 and X 2 are independently selected from a group consisting of chloride, methyl, methoxy, isopropoxy, benzyl and dimethylamino.

4. A transition metal catalyst composition for preparing ethylene homopolymers or copolymers of ethylene with α-olefin, which comprises a transition metal compound according to claim 1 , and alkylaluminoxane or organoaluminum compound cocatalyst, or boron compound cocatalyst, or a mixture thereof.

5. The transition metal catalyst composition for preparing ethylene homopolymers or copolymers of ethylene with α-olefin according to claim 4 , wherein the ratio of transition metal to cocatalyst to be used is from 1:50 to 1:5,000 on the basis of the molar ratio of transition metal (M) to aluminum.

6. The transition metal catalyst composition for preparing ethylene homopolymers or copolymers of ethylene with α-olefin according to claim 5 , wherein the alkylaluminoxane or organoaluminum compound cocatalyst is selected from methylaluminoxane, modified methylaluminoxane, tetraisobutylaluminoxane, trialkylaluminum, triethylaluminum or triisobutylaluminum, or mixtures thereof.

7. The transition metal catalyst composition for preparing ethylene homopolymers or copolymers of ethylene with α-olefin according to claim 4 , wherein the ratio of transition metal to cocatalyst is in the range of 1:0.5˜5:10˜500 on the basis of the molar ratio of transition metal (M): boron atom : aluminum atom.

8. The transition metal catalyst composition for preparing ethylene homopolymers or copolymers of ethylene with α-olefin according to claim 7 , wherein the boron compound cocatalyst is selected from N,N-dimethylanilinium tetrakispentafluorophenylborate or triphenylmethylinium tetrakispentafluorophenylborate, or mixtures thereof.

9. A process for preparing ethylene homopolymers or copolymers of ethylene with α-olefin by using the transition metal catalyst composition according to claim 4 , wherein the comonomer to be polymerized with ethylene is one or more compound(s) selected from propylene, 1-butene, 1-pentene, 1-hexene, 1-heptene, 1-octene, 1-decene, 1-undecene, 1-dodecene, 1-tetradecene, 1-hexadecene and 1-eitosene, and ethylene content of the copolymer of ethylene with olefin is from 50 to 99% by weight.

10. The process for preparing ethylene homopolymers or copolymers of ethylene with α-olefin according to claim 9 , wherein the pressure in the reactor containing ethylene monomer is from 6 to 150 atm, and the polymerization temperature is from 60 to 250°.

Assignments (2)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Sep 23, 2015
From: SK INNOVATION CO., LTD.
To: SABIC SK NEXLENE COMPANY PTE. LTD.
Reel/Frame 036635/0906 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 11, 2011
From: OK, MYUNGAHN; SHIN, DONGCHEOL; JEONG, JISU; HAHN, JONGSOK; LEE, HOSEONG; SHIN, DAEHO
To: SK ENERGY CO., LTD.
Reel/Frame 025938/0590 →