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Process for the production of crystalline terpolymers of ethene, butene-1 and butene-2

Assignee: VESTOLEN GmbH
•
Filing: 1975-06-10
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Granted: 1977-03-08
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Expires: 1995-06-10
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Abstract

Abstract For preparing crystalline, thermoplastic, low-pressure terpolymers of ethene with 0.1-5 mol % butene-1 and 0.1-3 mol % butene-2 having a density of 0.94-0.96 g./cm 3 , a liquid phase monomer mixture consisting essentially of ethene, 0.05-10 mol % butene-1 and 20-98.9 mol % butene-2 is polymerized with a mixed polymerization catalyst comprising (a) TiCl 3 . nAlCl 3 wherein n is 0.2-0.6, and (b) isoprenylaluminum in a molar ratio Al : Ti of about 2-20 to form said terpolymer.

Inventors

  • 👤 Fritz Baxmann
  • 👤 Johann Dietrich
  • 👤 Walter Dittmann
  • 👤 Albert Frese

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-31 10:29
CPC Classifications
C; C08; C08F; C08F210/00; C08F210/16

Claims Analysis

Total Claims: 6
Claim 1
Independent Claim 87 words
A process for preparing crystalline, thermoplastic, low-pressure terpolymers of ethene with 0.1-5 mol % butene-1 and 0.1-3 mol % butene-2 having a density of 0.94-0.96 g./cm 3 , which comprises: polymerizing a liquid phase monomer mixture consisting essentially of ethene, 0.05-10 mol % butene-1 and 20-98.9 mol % butene-2 with a catalytic amount of a particulate mixed polymerization catalyst comprising a. TiCl 3 .sup.. nAlCl 3 wherein n is 0.2-0.6, and b. isoprenylaluminum in a molar ratio Al : Ti of about 2-20 to form said terpolymer.
Claim 2
Dependent Claim 87 words
A process for preparing crystalline, thermoplastic, low-pressure terpolymers of ethene with 0.1-5 mol % butene-1 and 0.1-3 mol % butene-2 having a density of 0.94-0.96 g./cm 3 , which comprises: polymerizing a liquid phase monomer mixture consisting essentially of ethene, 0.05-10 mol % butene-1 and 20-98.9 mol % butene-2 with a catalytic amount of a particulate mixed polymerization catalyst comprising a. TiCl 3 .sup.. nAlCl 3 wherein n is 0.2-0.6, and b. isoprenylaluminum in a molar ratio Al : Ti of about 2-20 to form said terpolymer.
Claim 3
Dependent Claim 26 words
A process according to claim 1 wherein the ratio of butene-1 to butene-2 in the polymerization mixture is about 1 : 1,000 to 1 : 100.
Claim 4
Dependent Claim 28 words
A process according to claim 1 wherein said liquid phase comprises a C 4 hydrocarbon mixture consisting essentially of 20-60% butane, 25-50% trans-butene-2, 10-30% cis-butene-2 and 0.1-10% butene-1.
Claim 5
Dependent Claim 14 words
A process according to claim 1 wherein the Al : Ti ratio is 5-15.
Claim 6
Dependent Claim 18 words
A process according to claim 1 wherein the resultant terpolymer has a molecular weight distribution nonuniformity of 5-40.

References Cited (Backward Citations)

US3067184A Cited
US2953552A Cited
GB967788A Cited
US3725364A Cited
US3491073A Cited
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US3645992A Cited
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US3920621A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1980-03-07 1980-09-06 1981-03-08 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1984-03-07 1984-09-06 1985-03-08 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1988-03-07 1988-09-06 1989-03-08 $7700.00 Window Closed / Lapsed

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