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US4429087A Expired / Lapsed US ⏱️ 0.0 years remaining

Polymerization catalyst and process

Assignee: Phillips Petroleum Co
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Filing: 1982-03-11
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Granted: 1984-01-31
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Expires: 2002-03-11
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Abstract

Abstract A transition metal compound such as titanium tetrahydrocarbyloxides and a metal hydrocarbyloxide compound such as magnesium hydrocarbyloxides are chemically combined to form a first catalyst component which is treated with a second catalyst component comprising an organometallic compound precipitating agent to produce an active olefin polymerization catalyst. High polymer yields are realized per gram of catalyst when the catalyst thus produced is treated with a halide ion exchanging source and used with an organometallic cocatalyst.

Inventors

  • 👤 Charles E. Capshew

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-01 05:11
CPC Classifications
C; C08; C08F; C08F10/00

Claims Analysis

Total Claims: 13
Claim 1
Independent Claim 392 words
A polymerization process comprising contacting at least one aliphatic mono-olefin under polymerization conditions in the presence of a catalyst which is formed by (1) mixing together a first catalyst component comprising a metal hydrocarbyloxide compound having the formula M(OR) 2 ) where M is a metal selected from Group IIA and Group IIB of the Mendeleev Periodic Table and R is the same or different and is a hydrocarbyl group having from 1 to 20 carbon atoms and a transition metal hydrocarbyloxide compound in which the transition metal is selected from the group consisting of Group IVB and Group VB transition metals of the Mendeleev Periodic Table and wherein the hydrocarbyl group is as defined above in a molar ratio of transition metal compound to metal compound ranging from about 2:1 to about 1:2, (2) heating the first catalyst component solution formed in (1), (3) cooling the first catalyst component solution to a temperature below about 25° C. and optionally filtering the first catalyst component solution to remove any undissolved material from the cooled first catalyst component solution, (4) adding a precipitating agent comprising a second catalyst component in a molar ratio of transition metal compound to the precipitating agent within a range of about 2:1 to about 1:3 to the cooled first catalyst component solution which is at a temperature ranging from about -50° C. to about 25° C. under conditions so as to avoid a significant temperature rise in the solution and to produce a solid catalyst in the form of a slurry with the solvent, said second catalyst component comprising an organoaluminum halide represented by the formulas R Al X.sub.2 R.sub.2 Al X, and R.sub.3 Al.sub.2 X.sub.3 wherein each R in the above formulas is as defined before and each R can be the same or different, and X is a halogen atom, (5) washing and drying the solid catalyst component thus formed and contacting same with a transition metal halide ion exchange source selected from titanium tetrachloride, vanadium oxychloride (VOCl 3 ), and zirconium tetrachloride in a weight ratio of transition metal halide to said solid catalyst component ranging from about 7:1 to about 1:4, (6) separating the solid catalyst component formed in (5) and washing same, and, (7) combining the washed and dried solid catalyst component separated in (6) with a cocatalyst component comprising an organoaluminum compound.
Claim 2
Dependent Claim 392 words
A polymerization process comprising contacting at least one aliphatic mono-olefin under polymerization conditions in the presence of a catalyst which is formed by (1) mixing together a first catalyst component comprising a metal hydrocarbyloxide compound having the formula M(OR) 2 ) where M is a metal selected from Group IIA and Group IIB of the Mendeleev Periodic Table and R is the same or different and is a hydrocarbyl group having from 1 to 20 carbon atoms and a transition metal hydrocarbyloxide compound in which the transition metal is selected from the group consisting of Group IVB and Group VB transition metals of the Mendeleev Periodic Table and wherein the hydrocarbyl group is as defined above in a molar ratio of transition metal compound to metal compound ranging from about 2:1 to about 1:2, (2) heating the first catalyst component solution formed in (1), (3) cooling the first catalyst component solution to a temperature below about 25° C. and optionally filtering the first catalyst component solution to remove any undissolved material from the cooled first catalyst component solution, (4) adding a precipitating agent comprising a second catalyst component in a molar ratio of transition metal compound to the precipitating agent within a range of about 2:1 to about 1:3 to the cooled first catalyst component solution which is at a temperature ranging from about -50° C. to about 25° C. under conditions so as to avoid a significant temperature rise in the solution and to produce a solid catalyst in the form of a slurry with the solvent, said second catalyst component comprising an organoaluminum halide represented by the formulas R Al X.sub.2 R.sub.2 Al X, and R.sub.3 Al.sub.2 X.sub.3 wherein each R in the above formulas is as defined before and each R can be the same or different, and X is a halogen atom, (5) washing and drying the solid catalyst component thus formed and contacting same with a transition metal halide ion exchange source selected from titanium tetrachloride, vanadium oxychloride (VOCl 3 ), and zirconium tetrachloride in a weight ratio of transition metal halide to said solid catalyst component ranging from about 7:1 to about 1:4, (6) separating the solid catalyst component formed in (5) and washing same, and, (7) combining the washed and dried solid catalyst component separated in (6) with a cocatalyst component comprising an organoaluminum compound.
Claim 3
Dependent Claim 18 words
A process according to claim 1 wherein the polymerizable compound comprises at least about 90 weight percent ethylene.
Claim 4
Dependent Claim 13 words
A process according to claim 1 wherein said polymerizable compound is essentially ethylene.
Claim 5
Dependent Claim 43 words
A process according to claim 1 wherein the polymerization temperature is within the range of about 50° C. to about 120° C., the partial pressure of the polymerizable compound is within the range of about 0.5 MPa to about 5 MPa (70-725 psig).
Claim 6
Dependent Claim 68 words
A process according to claim 1 further comprising a cocatalyst which comprises at least one organoaluminum compound represented by the general formulas R"'.sub.3 Al, R"'AlX.sub.2, R"'.sub.2 AlX, and R"'.sub.3 Al.sub.2 X.sub.3 wherein R"' is individually selected from linear and branched chain hydrocarbyl radicals containing from 1 to about 20 carbon atoms for radical and each R' can be the same or different and X is a halogen atom.
Claim 7
Dependent Claim 32 words
A process according to claim 1 wherein the catalyst is formed from magnesium diethoxide (1), titanium tetrabutoxide (2), and ethylaluminum dichloride (precipitating agent), and the halide ion exchanging source is titanium tetrahalide.
Claim 8
Dependent Claim 13 words
A process according to claim 6 further comprising a cocatalyst which is triethylaluminum.
Claim 9
Dependent Claim 51 words
A process according to claim 1 wherein the resulting catalyst formed in (4) is contacted with a halide ion exchange source selected from titanium tetrachloride, vanadium oxychloride (VOCl 3 ), and zirconium tetrachloride in a hydrocarbon diluent at a temperature within the range of about 0° C. to about 150° C.
Claim 10
Dependent Claim 31 words
A process according to claim 8 wherein said first and second catalyst components are formed from magnesium diethoxide, titanium tetra-n-butoxide, and ethylaluminum dichloride, and the halide ion source is titanium tetrachloride.
Claim 11
Dependent Claim 20 words
A process according to claim 9 wherein the polymerizable compound is ethylene and the catalyst further comprises a triethylaluminum cocatalyst.
Claim 12
Dependent Claim 69 words
A process according to claim 1 comprising contacting ethylene under polymerization conditions with a catalyst which forms on mixing a first catalyst component and a second catalyst component, wherein the first catalyst component is formed by mixing magnesium diethoxide and titanium tetra-n-butoxide, wherein said second catalyst component is ethylaluminum dichloride, wherein the catalyst is treated with titanium tetrachloride, and wherein said contacting is carried out employing a triethylaluminum cocatalyst.
Claim 13
Dependent Claim 51 words
A process according to claim 11 wherein the first and second catalyst components are mixed at a temperature within the range of from about -50° C. to about 25° C. and the resulting catalyst is treated with titanium tetrachloride at a temperature within the range of 0° C. to 150° C.

References Cited (Backward Citations)

US3901863A Cited
US4039472A Cited
US4218339A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1987-01-30 1987-08-01 1988-01-31 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1991-01-30 1991-08-01 1992-01-31 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1995-01-30 1995-08-01 1996-01-31 $7700.00 Window Closed / Lapsed

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