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US4611038A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for the polymerization of olefins

Assignee: Arkema France SA
•
Filing: 1985-07-18
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Granted: 1986-09-09
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Expires: 2005-07-18
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Abstract

Abstract A process is provided for the polymerization of olefins in the gas phase wherein olefins are contacted with a catalyst system consisting of an active solid hydrocarbon having been prepared by forming a pulverulent composition by mixing a transition metal component, a porous organic or inorganic solid support and an organometallic compound of the organo-Al, organo-Mg or organo-Zn type, and polymerizing a controlled amount of one or more C 2 to C 12 olefins in the gas phase in contact with the pulverulent composition with a specific hourly conversion of the olefins to produce the active solid hydrocarbon.

Inventors

  • 👤 Claude Brun
  • 👤 Auguste Cheux
  • 👤 Robert Pelletier

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-09 04:27
CPC Classifications
C; C08; C08F; C08F10/00; Y; Y10; Y10S; Y10S526/00; Y10S526/901; Y10S526/904

Claims Analysis

Total Claims: 15
Claim 1
Independent Claim 313 words
Process for the synthesis of an olefinic polymer or copolymer in which one or more olefins are polymerized in the presence of a catalyst system, which comprises contacting said olefins with said catalyst system and recovering said polymer or copolymer therefrom, said catalyst system consisting of an active solid hydrocarbon and having been prepared by forming a homogeneous pulverulent composition by combining (a) a component comprising a transition metal compound wherein said metal is chosen from Ti, V, Zr and Cr, in the form of particles having an average diameter of between 0.1 and 500 microns, (b) an inert porous organic or inorganic solid support in the form of a powder wherein said powder has a mean particle diameter of from 1 to 5,000 microns, and (c) a liquid phase containing at least one compound chosen from the organometallic compound of the metals of group I to III of the Periodic Table of the Elements, the amounts of the component comprising the transition metal compound and of the organometallic compound or compounds being such that the ratio of the number of atoms of the metal or metals of groups I to III of the Periodic Table to the number of atoms of transition metal is between 0.1 and 800, while the amount of support powder is adjusted so that the mixture produced remains in pulverulent form, and polymerizing, in contact with the above pulverulent composition, one or more C 2 to C 12 olefins so that an active solid hydrocarbon containing an amount by weight of transition metal of between 10 and 50,000 ppm is produced, this polymerization being carried out in the gas phase at a temperature below the melting point of the active solid hydrocarbon, whilst an hourly conversion of the C 2 to C 12 olefin or olefins of less than 500,000 g per gram of transition metal is maintained.
Claim 2
Dependent Claim 313 words
Process for the synthesis of an olefinic polymer or copolymer in which one or more olefins are polymerized in the presence of a catalyst system, which comprises contacting said olefins with said catalyst system and recovering said polymer or copolymer therefrom, said catalyst system consisting of an active solid hydrocarbon and having been prepared by forming a homogeneous pulverulent composition by combining (a) a component comprising a transition metal compound wherein said metal is chosen from Ti, V, Zr and Cr, in the form of particles having an average diameter of between 0.1 and 500 microns, (b) an inert porous organic or inorganic solid support in the form of a powder wherein said powder has a mean particle diameter of from 1 to 5,000 microns, and (c) a liquid phase containing at least one compound chosen from the organometallic compound of the metals of group I to III of the Periodic Table of the Elements, the amounts of the component comprising the transition metal compound and of the organometallic compound or compounds being such that the ratio of the number of atoms of the metal or metals of groups I to III of the Periodic Table to the number of atoms of transition metal is between 0.1 and 800, while the amount of support powder is adjusted so that the mixture produced remains in pulverulent form, and polymerizing, in contact with the above pulverulent composition, one or more C 2 to C 12 olefins so that an active solid hydrocarbon containing an amount by weight of transition metal of between 10 and 50,000 ppm is produced, this polymerization being carried out in the gas phase at a temperature below the melting point of the active solid hydrocarbon, whilst an hourly conversion of the C 2 to C 12 olefin or olefins of less than 500,000 g per gram of transition metal is maintained.
Claim 3
Dependent Claim 31 words
Process according to claim 1, wherein a monoolefin is polymerized in contact with the active solid hydrocarbon, the said monoolefin being selected from the group consisting of ethylene, propene or but-1-ene.
Claim 4
Dependent Claim 62 words
Process according to claim 1, wherein a mixture of at least two C 2 to C 12 olefins is polymerized in contact with the active solid hydrocarbon, and when said mixture is in contact with the active solid hydrocarbon, it contains a total molar proportion of C 3 to C 12 alphaolefins of between 0.1 and 75%, preferably between 1 and 50%.
Claim 5
Dependent Claim 67 words
Process according to claim 1, wherein a mixture of propene with at least one member of ethylene or a C 4 to C 12 alpha-olefine is polymerized in contact with the active solid hydrocarbon, the said mixture, when it is in contact with the said active solid hydrocarbon, containing a total molar proportion of C 4 to C 12 alpha-olefins and/or ethylene of between 0.1 and 75%.
Claim 6
Dependent Claim 39 words
Process according to claim 1, wherein mixtures of ethylene and propene are polymerized and, when they are in contact with the active solid hydrocarbon, the molar ratio of ethylene:propene is between 0.02:1 and 50:1, preferably between 0.05:1 and 1:1.
Claim 7
Dependent Claim 24 words
Process according to claim 1, wherein the polymerization in the presence of the active solid hydrocarbon is carried out in an inert liquid medium.
Claim 8
Dependent Claim 33 words
Process according to claim 1, wherein the polymerization in the presence of the active solid hydrocarbon is carried out in the gas phase in at least one of a fluidized or stirred bed.
Claim 9
Dependent Claim 51 words
Process according to claim 7, wherein a mixture of ethylene and one or more C 3 to C 12 alpha-olefins is polymerized, the mixture containing, when it is in contact with the active solid hydrocarbon, a total molar proportion of C 3 to C 12 alpha-olefins of between 1 and 50%.
Claim 10
Dependent Claim 26 words
Process according to claim 1, wherein the polymerization in contact with the active solid hydrocarbon is carried out in the presence of a chain transfer agent.
Claim 11
Dependent Claim 112 words
Process according to claim 1, wherein an additional amount of one or more organometallic compounds of metals of groups I to III of the Periodic Table of Elements, which may or may not be similar to those used for the preparation of the active solid hydrocarbon, is added to the polymerization mixture of the olefin in the presence of the said active solid hydrocarbon in order to adjust the ratio of the number of atoms of metal or metals of groups I to III of the Periodic Table of the Elements to the number of atoms of transition metal originating from the transition metal component to the value chosen for the polymerization.
Claim 12
Dependent Claim 38 words
Process according to claim 1, wherein if the active solid hydrocarbon does not contain an electron donor, the latter is added to the polymerization mixture of the olefin or olefins in the presence of the active solid hydrocarbon.
Claim 13
Dependent Claim 38 words
Process according to claim 11, wherein if the active solid hydrocarbon does not contain an electron donor, the latter is added to the polymerization medium as a mixture with the additional amount of the organometallic compound or compounds.
Claim 14
Dependent Claim 42 words
Process according to claim 11, wherein the additional amount of the organometallic compound or compounds and/or the electron donor are added to the active solid hydrocarbon after preparation of the latter but before this is used in the polymerization of the olefin.
Claim 15
Dependent Claim 35 words
Process according to claim 13, wherein the active solid hydrocarbon containing the said additional amount of the organometallic compound or compounds is used as the only catalytic component for gas phase polymerization of the olefin.

References Cited (Backward Citations)

US4123386A Cited
US4287328A Cited
GB2066274A Cited
US4309521A Cited
US4304891A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1989-09-08 1990-03-10 1990-09-09 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1993-09-08 1994-03-10 1994-09-09 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1997-09-08 1998-03-10 1998-09-09 $7700.00 Window Closed / Lapsed

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