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Ultra high efficiency catalyst for polymerizing olefins

Assignee: Dow Chemical Co
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Filing: 1979-09-28
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Granted: 1981-02-10
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Expires: 1999-09-28
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Abstract

Abstract Compositions consisting of the reaction product or complex resulting from the mixing of a transition metal compound such as a tetraalkoxy titanium compound and a zinc compound such as a dialkyl zinc compound are useful in the preparation of catalysts for polymerizing α-olefins as ultra-high efficiencies at high polymerization temperatures.

Inventors

  • 👤 Randall S. Shipley

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-02 19:19
CPC Classifications
C; C08; C08F; C08F10/00; C08F4/00; C08F4/02; C08F4/022

Claims Analysis

Total Claims: 7
Claim 1
Independent Claim 430 words
A process for polymerizing one or more α-olefins which comprises conducting the polymerization under Ziegler polymerization conditions in the presence of a catalyst composition containing: the catalyst reaction product of (A) the reaction product or complex formed from the admixture of (1) at least one transition metal compound represented by the formulae Tm(OR) y X x-y or Tm(OR) x-2 O wherein Tm is a transition metal selected from groups IVB, VB or VIB; each R is independently a hydrocarbyl group, having from 1 to about 20 carbon atoms; each X is independently a halogen; x has a value equal to the valence of Tm and y has a value from 1 to the valance of Tm; and (2) at least one zinc compound represented by the formulae R 2 Zn and RZnX wherein each R is independently a hydrocarbyl group having from 1 to about 20 carbon atoms and X is a halogen; and (B) a magnesium halide resulting from the reaction of (1) an organomagnesium compound represented by the formulae MgR" 2 .xMR" y wherein M is aluminum or zinc, each R" is independently a hydrocarbyl or hydrocarbyloxy group having from 1 to about 20 carbon atoms, x has a value from zero to 10 and y has a value corresponding to the valence of M; with (2) a halide source selected from (a) an active non-metallic halide, said non-metallic halide corresponding to the formula R'X wherein R' is hydrogen or a hydrocarbyl group such that the hydrocarbyl halide is at least as active as sec-butyl chloride and does not poison the catalyst and X is halogen or (b) a metallic halide corresponding to the formula MR y-a X a wherein M is a metal of Group IIB, IIIA or IVA of Mendeleev's Periodic Table of Elements, R is a monovalent hydrocarbyl radical, X is halogen, y is a number corresponding to the valence of M and a is a number of 1 to y; and (C) when the organomagnesium component and/or the halide source provides insufficient quantities of aluminum, an aluminum compound represented by the formula AlR y' X y" wherein R and X are as defined above and y' and y" each have a value of from zero to three with the sum of y' and y" being three; and wherein the components are employed in quantities which provide at atomic ratio of the elements Mg:Tm of from about 1:1 to about 200:1; Zn:Tm at least about 0.03:1; Al:Tm of from about 0.1:1 to about 200:1 and an excess X:Al of from about 0.005:1 to about 10:1.
Claim 2
Dependent Claim 430 words
A process for polymerizing one or more α-olefins which comprises conducting the polymerization under Ziegler polymerization conditions in the presence of a catalyst composition containing: the catalyst reaction product of (A) the reaction product or complex formed from the admixture of (1) at least one transition metal compound represented by the formulae Tm(OR) y X x-y or Tm(OR) x-2 O wherein Tm is a transition metal selected from groups IVB, VB or VIB; each R is independently a hydrocarbyl group, having from 1 to about 20 carbon atoms; each X is independently a halogen; x has a value equal to the valence of Tm and y has a value from 1 to the valance of Tm; and (2) at least one zinc compound represented by the formulae R 2 Zn and RZnX wherein each R is independently a hydrocarbyl group having from 1 to about 20 carbon atoms and X is a halogen; and (B) a magnesium halide resulting from the reaction of (1) an organomagnesium compound represented by the formulae MgR" 2 .xMR" y wherein M is aluminum or zinc, each R" is independently a hydrocarbyl or hydrocarbyloxy group having from 1 to about 20 carbon atoms, x has a value from zero to 10 and y has a value corresponding to the valence of M; with (2) a halide source selected from (a) an active non-metallic halide, said non-metallic halide corresponding to the formula R'X wherein R' is hydrogen or a hydrocarbyl group such that the hydrocarbyl halide is at least as active as sec-butyl chloride and does not poison the catalyst and X is halogen or (b) a metallic halide corresponding to the formula MR y-a X a wherein M is a metal of Group IIB, IIIA or IVA of Mendeleev's Periodic Table of Elements, R is a monovalent hydrocarbyl radical, X is halogen, y is a number corresponding to the valence of M and a is a number of 1 to y; and (C) when the organomagnesium component and/or the halide source provides insufficient quantities of aluminum, an aluminum compound represented by the formula AlR y' X y" wherein R and X are as defined above and y' and y" each have a value of from zero to three with the sum of y' and y" being three; and wherein the components are employed in quantities which provide at atomic ratio of the elements Mg:Tm of from about 1:1 to about 200:1; Zn:Tm at least about 0.03:1; Al:Tm of from about 0.1:1 to about 200:1 and an excess X:Al of from about 0.005:1 to about 10:1.
Claim 3
Dependent Claim 206 words
The process of claim 1 wherein: (a) in component (A-1), Tm is titanium, each R is independently a hydrocarbyl group having from 1 to about 10 carbon atoms and X is chlorine or bromine; (b) in component (A-2), the zinc compound is represented by the formula ZnR 2 wherein R is a hydrocarbyl group having from 1 to about 10 carbon atoms; (c) in component (B-1), M is aluminum and R" is a hydrocarbyl group having from 1 to about 10 carbon atoms and x has a value of from about 0.001 to about 5; (d) in component (B-2-a), R' is hydrogen or a tertiary butyl group and X is chlorine; (e) in component (B-2-b), M is a metal from Groups IIIA or IVA, y-a is zero or 1 and X is chlorine; (f) in component (C), the aluminum compound is a trialkyl aluminum compound wherein each alkyl group independently has from 1 to about 10 carbon atoms; and (g) the components are employed in quantities so as to provide atomic ratios of Mg:Ti of from about 2:1 to about 200:1; Zn:Ti from about 0.12:1 to about 5:1; Al:Ti of from about 0.5:1 to about 200:1 and excess X:Al of from about 0.002:1 to about 2:1.
Claim 4
Dependent Claim 73 words
The process of claim 2 wherein: (a) in component (A-1), R is a saturated aliphatic hydrocarbyl group; (b) in component (B-1) x has a value of from about 0.15 to about 2.5; and (c) the components are employed in quantities so as to provide atomic ratios of Mg:Ti of from about 5:1 to about 75:1; Zn:Ti of from about 0.25:1 to about 2:1 and excess X:Al of from about 0.01:1 to about 1.4:1.
Claim 5
Dependent Claim 68 words
The process of claim 3 wherein: (a) component (A-1) is titanium tetraethoxide, titanium tetra-n-propoxide, titanium tetra-isopropoxide, titanium tetra-n-butoxide, or titanium tetra-(2-ethylhexoxide); (b) component (A-2) is dimethyl zinc, diethyl zinc or diphenyl zinc; (c) component (B-1) is a dialkyl magnesium compound wherein each alkyl group independently has from 1 to about 10 carbon atoms; and (d) component (B-2) is substantially anhydrous hydrogen chloride, ethyl aluminum dichloride or tin tetrachloride.
Claim 6
Dependent Claim 24 words
The process of claims 1, 2, 3 or 4 wherein the components are added in the order (B-1), (B-2), (C) if employed and (A).
Claim 7
Dependent Claim 36 words
The process of claims 1, 2, 3 or 4 wherein the components are added in the order (B-1), (B-2), (A) and (C) if employed, and provided that the halide source, (B-2), is not a tin compound.

References Cited (Backward Citations)

GB1305610A Cited
US4172050A Cited
GB1500878A Cited
US4120820A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1984-02-10 1984-08-11 1985-02-10 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1988-02-10 1988-08-11 1989-02-10 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1992-02-10 1992-08-11 1993-02-10 $7700.00 Window Closed / Lapsed

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