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US4448944A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for the preparation of a polyolefin, and a catalyst for this process

Assignee: Hoechst AG
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Filing: 1982-06-14
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Granted: 1984-05-15
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Expires: 2002-06-14
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Abstract

Abstract Polyolefins having a broad molecular weight distribution are obtained in a very high yield even using a catalyst based on a reaction product of a magnesium alcoholate with titanium tetrachloride, if the hydrocarbon-insoluble product of the reaction of the magnesium alcoholate with titanium tetrachloride is heated to a fairly high temperature with a chloroalkoxytitanate, in order to split off alkyl chlorides.

Inventors

  • 👤 Joachim Berthold
  • 👤 Bernd Diedrich
  • 👤 Rainer Franke
  • 👤 Jurgen Hartlapp
  • 👤 Werner Schafer
  • 👤 Wolfgang Strobel

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-09 03:51
CPC Classifications
C; C08; C08F; C08F10/00

Claims Analysis

Total Claims: 4
Claim 1
Independent Claim 245 words
A process for the polymerization of ethylene alone or in combination with a minor amount of a 1-olefin of the formula R 4 -CH═CH 2 in which R 4 denotes an alkyl radical having 1 to 10 carbon atoms, in the presence of a catalyst comprised of a component which contains magnesium and titanium (component A) and an organometallic compound of the Groups I to III of the periodic system (component B), which comprises carrying out the polymerization in the presence of a catalyst in which the component A has been prepared by a procedure in which, in a first reaction stage, a magnesium alcoholate of the formula Mg(OR) 2 , wherein R represents identical or different alkyl radicals having from 1 to 6 carbon atoms, is reacted with titanium tetrachloride in a hydrocarbon at a temperature of 50° to 100° C., 1 to 5 moles of titanium tetrachloride per mole of magnesium alcoholate being employed, the soluble constituents are then removed by washing with a hydrocarbon and the resulting solid is suspended in a hydrocarbon and is subjected, in a second reaction stage, with the addition of 0.1 to 3 moles chloroalkoxytitanate per mole of magnesium alcoholate, to a heat treatment for 10 to 100 hours at a temperature of 110° to 200° C., with evolution of alkyl chloride, until no further alkyl chloride is split off, and the solid is then freed from soluble reaction products by washing several times with a hydrocarbon.
Claim 2
Dependent Claim 245 words
A process for the polymerization of ethylene alone or in combination with a minor amount of a 1-olefin of the formula R 4 -CH═CH 2 in which R 4 denotes an alkyl radical having 1 to 10 carbon atoms, in the presence of a catalyst comprised of a component which contains magnesium and titanium (component A) and an organometallic compound of the Groups I to III of the periodic system (component B), which comprises carrying out the polymerization in the presence of a catalyst in which the component A has been prepared by a procedure in which, in a first reaction stage, a magnesium alcoholate of the formula Mg(OR) 2 , wherein R represents identical or different alkyl radicals having from 1 to 6 carbon atoms, is reacted with titanium tetrachloride in a hydrocarbon at a temperature of 50° to 100° C., 1 to 5 moles of titanium tetrachloride per mole of magnesium alcoholate being employed, the soluble constituents are then removed by washing with a hydrocarbon and the resulting solid is suspended in a hydrocarbon and is subjected, in a second reaction stage, with the addition of 0.1 to 3 moles chloroalkoxytitanate per mole of magnesium alcoholate, to a heat treatment for 10 to 100 hours at a temperature of 110° to 200° C., with evolution of alkyl chloride, until no further alkyl chloride is split off, and the solid is then freed from soluble reaction products by washing several times with a hydrocarbon.
Claim 3
Dependent Claim 138 words
The process as claimed in claim 1, wherein the component A is prepared in a first reaction stage by reacting a magnesium alcoholate with titanium tetrachloride in a hydrocarbon at a temperature of 50° to 100° C., then removing the soluble constituents by washing with a hydrocarbon, and suspending the resulting solid in a hydrocarbon and subjecting it, in a second reaction stage, with the additiion of a chloroalkoxytitanate of the formula TiCl n (OR 1 ) 4-n , in which R 1 denotes identical or different alkyl radicals having 1 to 20 carbon atoms and n denotes 1 to 3, to a heat treatment at a temperature of 110° to 200° C. until no further alkyl chloride is split off, and then freeing the solid from soluble reaction products by washing it several times with a hydrocarbon.
Claim 4
Dependent Claim 21 words
A process as claimed in claim 1, wherein the resulting polyethylene or ethylene/1-olefin copolymer has an Mn/Mn value greater than 10.

References Cited (Backward Citations)

GB1154884A Cited
US3644318A Cited
US4250284A Cited
GB1498862A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1987-05-15 1987-11-14 1988-05-15 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1991-05-15 1991-11-14 1992-05-15 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1995-05-15 1995-11-14 1996-05-15 $7700.00 Window Closed / Lapsed

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