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US5756613A Expired / Lapsed US ⏱️ 0.0 years remaining

Catalyst support and catalyst for the polymerization of α-olefins; processes for obtaining them and polymerization of α-olefins in presence of the catalyst

Assignee: Ineos Manufacturing Belgium NV
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Filing: 1996-04-09
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Granted: 1998-05-26
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Expires: 2016-04-09
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Abstract

Abstract Catalyst support containing an α-olefin polymer which is in the form of particles of mean size from 5 to 350 μm in which the pore volume generated by the pores of radius from 1,000 to 75,000 Å is at least 0.2 cm 3 /g. Catalyst usable for the polymerization of α-olefins, including a compound containing at least one transition metal belonging to groups IIIb, IVb, IVb and VIb of the Periodic Table, bound in or on this support.

Inventors

  • 👤 Jean-Louis Costa
  • 👤 Vincent Laurent
  • 👤 Philippe Francois
  • 👤 Dirk Vercammen

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-01 09:49
CPC Classifications
C; C08; C08F; C08F10/00; C08F4/00; C08F4/02; C08F4/027; C08F110/00; C08F110/04; C08F110/06; C08F4/42; C08F4/44; C08F4/60; C08F4/62; C08F4/64; C08F4/659; C08F4/65908; C08F4/6592; C08F4/65922; C08F4/65925; Y; Y10; Y10S; Y10S526/00; Y10S526/904; Y10S526/908; Y10S526/943

Claims Analysis

Total Claims: 11
Claim 1
Independent Claim 239 words
A catalyst for polymerization of α-olefins, comprising: a compound (b) which comprises at least one transition metal belonging to Periodic Table groups IIIb, IVb, Vb and VIb bound in, or on, a support comprising at least one α-olefin polymer which is in a form of particles of mean size from 5 to 350 μm, in which a pore volume generated by pores of radius from 1,000 to 75,000 Å is at least 0.2 cm 3 /g and obtained by polymerizing one or more alpha olefins by means of a catalyst system (S) containing a catalytic compound (a) and an activator chosen from organoaluminium compounds, said catalytic compound (a) being obtained by heat treatment, in a presence of a halogen-containing agent, of a liquid material resulting from placing titanium tetrachloride (TiCl 4 ), pretreated with an electron-donor compound, into contact with a compound (D) corresponding to the general formula AlR.sub.p (Y).sub.q X.sub.3-(p+q) in which R denotes a hydrocarbon radical; Y denotes a group chosen from --OR', --SR' and --NR'R" in which each of R' and R" denotes a hydrocarbon radical or a hydrogen atom; X denotes a halogen; p is any number such that 0.5<p≦2.5; q is any number such that 0.5<q<3, the sum (p+q) being such that 0.5<(p+q)≦3 wherein a quantity of catalyst residue, expressed as g of compound (a) per kg of support, is at least approximately 5 g and smaller than or equal to approximately 170 g.
Claim 2
Dependent Claim 239 words
A catalyst for polymerization of α-olefins, comprising: a compound (b) which comprises at least one transition metal belonging to Periodic Table groups IIIb, IVb, Vb and VIb bound in, or on, a support comprising at least one α-olefin polymer which is in a form of particles of mean size from 5 to 350 μm, in which a pore volume generated by pores of radius from 1,000 to 75,000 Å is at least 0.2 cm 3 /g and obtained by polymerizing one or more alpha olefins by means of a catalyst system (S) containing a catalytic compound (a) and an activator chosen from organoaluminium compounds, said catalytic compound (a) being obtained by heat treatment, in a presence of a halogen-containing agent, of a liquid material resulting from placing titanium tetrachloride (TiCl 4 ), pretreated with an electron-donor compound, into contact with a compound (D) corresponding to the general formula AlR.sub.p (Y).sub.q X.sub.3-(p+q) in which R denotes a hydrocarbon radical; Y denotes a group chosen from --OR', --SR' and --NR'R" in which each of R' and R" denotes a hydrocarbon radical or a hydrogen atom; X denotes a halogen; p is any number such that 0.5<p≦2.5; q is any number such that 0.5<q<3, the sum (p+q) being such that 0.5<(p+q)≦3 wherein a quantity of catalyst residue, expressed as g of compound (a) per kg of support, is at least approximately 5 g and smaller than or equal to approximately 170 g.
Claim 3
Dependent Claim 42 words
The catalyst according to claim 1, wherein the compound (b) is a solid based on titanium trichloride complexed with an electron-donor chosen from organic compounds containing one or more atoms or groups which have one or a number of free electron pairs.
Claim 4
Dependent Claim 110 words
The catalyst according to claim 2, obtained by heat treatment, in a presence of a halogen-containing agent and of support particles, of a liquid material obtained by placing TiCl 4 pretreated with an electron-donor compound in contact with a composition (O) corresponding to a general formula AlR.sub.m (Y).sub.n X.sub.3-(m+n) (III) in which R denotes a hydrocarbon radical; Y denotes a group chosen from --OR', --SR' and --NR'R" in which each of R' and R" denote a hydrocarbon radical or a hydrogen atom; X denotes a halogen; n is any number such that 0<n≦0.5; m is any number such that 0<m<3, the sum (m+n) being less than or equal to 3.
Claim 5
Dependent Claim 14 words
The catalyst according to claim 3, wherein the halogen-containing agent is TiCl 4 .
Claim 6
Dependent Claim 37 words
The catalyst according to claim 4, wherein the total quantity of TiCl 4 used is such that a molar ratio of titanium to radicals R originating from the composition (O) is lower than or equal to 2.7.
Claim 7
Dependent Claim 240 words
A catalyst for polymerization of α-olefins, comprising: a compound (b) which comprises at least one transition metal belonging to the Periodic Table groups IIIb, IVb, Vb and VIb bound in, or on, a support comprising at least one α-olefin polymer which is in a form of particles of mean size from 5 to 350 μm, in which a pore volume generated by pores of radius from 1,000 to 75,000 Å is at least 0.2 cm 3 /g and obtained by polymerizing one or more alpha olefins by means of a catalyst system (S) containing a catalytic compound (a) and an activator chosen from organoaluminium compounds, said catalytic compound (a) being obtained by heat treatment, in a presence of a halogen-containing agent, of a liquid material resulting from placing titanium tetrachloride (TiCl 4 ), pretreated with an electron-donor compound, into contact with a compound (D) corresponding to the general formula AlR.sub.p (Y).sub.q X.sub.3-(p+q) in which R denotes a hydrocarbon radical; Y denotes a group chosen from --OR', --SR' and --NR'R" in which each of R' and R" denotes hydrocarbon radical or a hydrogen atom; X denotes a halogen; p is any number such that 0<p≦2.5; q is any number such that 0.5<q<3, the sum (p+q) being such that 0.5<(p+q)<3 wherein a quantity of catalyst residue, expressed as g of compound (a) per kg of support, is at least from approximately 2 g to approximately 170 g of compound (a) per kg.
Claim 8
Dependent Claim 240 words
A catalyst for polymerization of α-olefins, comprising: a compound (b) which comprises at least one transition metal belonging to the Periodic Table groups IIIb, IVb, Vb and VIb bound in, or on, a support comprising at least one α-olefin polymer which is in a form of particles of mean size from 5 to 350 μm, in which a pore volume generated by pores of radius from 1,000 to 75,000 Å is at least 0.2 cm 3 /g and obtained by polymerizing one or more alpha olefins by means of a catalyst system (S) containing a catalytic compound (a) and an activator chosen from organoaluminium compounds, said catalytic compound (a) being obtained by heat treatment, in a presence of a halogen-containing agent, of a liquid material resulting from placing titanium tetrachloride (TiCl 4 ), pretreated with an electron-donor compound, into contact with a compound (D) corresponding to the general formula AlR.sub.p (Y).sub.q X.sub.3-(p+q) in which R denotes a hydrocarbon radical; Y denotes a group chosen from --OR', --SR' and --NR'R" in which each of R' and R" denotes hydrocarbon radical or a hydrogen atom; X denotes a halogen; p is any number such that 0<p≦2.5; q is any number such that 0.5<q<3, the sum (p+q) being such that 0.5<(p+q)<3 wherein a quantity of catalyst residue, expressed as g of compound (a) per kg of support, is at least from approximately 2 g to approximately 170 g of compound (a) per kg.
Claim 9
Dependent Claim 46 words
In a method of polymerizing an α-olefin, the improvement, comprising: utilizing a catalyst system containing the catalyst of claim 1, an activator chosen from an organoaluminium compound containing at least on aluminum-carbon bond and, optionally, one third constituent known to improve their stereospecificity and/or their activity.
Claim 10
Dependent Claim 46 words
In a method of polymerizing an α-olefin, the improvement, comprising: utilizing a catalyst system containing the catalyst of claim 2, an activator chosen from an organoaluminium compound containing at least one alumium-carbon bond and, optionally, on third constituent known to improve their stereospecificity and/or their activity.
Claim 11
Dependent Claim 46 words
In a method of polymerizing an α-olefin, the improvement, comprising: utilizing a catalyst system containing the catalyst of claim 3, an activator chosen from an organoaluminium compound containing at least one aluminum-carbon bond and, optionally, one third constituent known to improve their stereospecificity and/or their activity.

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 2001-05-25 2001-11-24 2002-05-26 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 2005-05-25 2005-11-24 2006-05-26 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2009-05-25 2009-11-24 2010-05-26 $7700.00 Window Closed / Lapsed

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