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US3981849A Expired / Lapsed US ⏱️ 0.0 years remaining

Low pressure process for the production of low density co- and terpolymers of ethylene

Assignee: Huels AG
•
Filing: 1974-10-02
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Granted: 1976-09-21
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Expires: 1994-10-02
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Abstract

Abstract High molecular weight, low density copolymers of ethylene and propylene and/or butene-1 are prepared by a low pressure liquid phase polymerization process using a titanium halide - organoaluminum catalyst in a polymerization solvent containing butene-2. Consistently comparable ethylene copolymers can be obtained from monomer mixtures of varying composition.

Inventors

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

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 23:14
CPC Classifications
C; C08; C08F; C08F210/00

Claims Analysis

Total Claims: 13
Claim 1
Independent Claim 247 words
In a process for the production of low density thermoplastic ethylene copolymers by low pressure copolymerization of ethylene with 0.1 to 20 molar percent of an α-olefin comonomer selected from the group consisting of propylene, butene-1 and mixtures thereof with a particulate mixed polymerization catalyst consisting essentially of (a) titanium trichloride and (b) a trialkylaluminum or a dialkylaluminum hydride in a molar ratio Al:Ti of 0.5 - 4.0, the improvement which comprises conducting the polymerization as a liquid phase solution polymerization employing a polymerization solvent consisting essentially of C 4 or a mixture of C 3 and C 4 hydrocarbons containing 0.1-20 molar percent of said α-olefin, 1-60 molar percent of butane, propane or mixtures thereof and 20-98.0 molar percent of butene-2 to form said copolymer product substantially free of homopolymers, provided that the maximum amount of butene-1 present in the solvent mixture is not greater than 5 molar percent and the maximum amount of propylene is not greater than 3 molar percent at a polymerization temperature of 70 to 100°C.; the maximum amount of butene-1 present in the solvent mixture is not greater than 10 molar percent and the maximum amount of propylene is not greater than 5 molar percent at a polymerization temperature of 50 to 70°C.; and the maximum amount of butene-1 present in the solvent mixture is not greater than 20 molar percent and the maximum amount of propylene is not greater than 15 molar percent at a polymerization temperature of 20°to 50°C.
Claim 2
Dependent Claim 247 words
In a process for the production of low density thermoplastic ethylene copolymers by low pressure copolymerization of ethylene with 0.1 to 20 molar percent of an α-olefin comonomer selected from the group consisting of propylene, butene-1 and mixtures thereof with a particulate mixed polymerization catalyst consisting essentially of (a) titanium trichloride and (b) a trialkylaluminum or a dialkylaluminum hydride in a molar ratio Al:Ti of 0.5 - 4.0, the improvement which comprises conducting the polymerization as a liquid phase solution polymerization employing a polymerization solvent consisting essentially of C 4 or a mixture of C 3 and C 4 hydrocarbons containing 0.1-20 molar percent of said α-olefin, 1-60 molar percent of butane, propane or mixtures thereof and 20-98.0 molar percent of butene-2 to form said copolymer product substantially free of homopolymers, provided that the maximum amount of butene-1 present in the solvent mixture is not greater than 5 molar percent and the maximum amount of propylene is not greater than 3 molar percent at a polymerization temperature of 70 to 100°C.; the maximum amount of butene-1 present in the solvent mixture is not greater than 10 molar percent and the maximum amount of propylene is not greater than 5 molar percent at a polymerization temperature of 50 to 70°C.; and the maximum amount of butene-1 present in the solvent mixture is not greater than 20 molar percent and the maximum amount of propylene is not greater than 15 molar percent at a polymerization temperature of 20°to 50°C.
Claim 3
Dependent Claim 50 words
A process according to claim 1 wherein said solvent consists essentially of, per 100 parts of weight of solvent, 30 - 60 parts propane and/or butane; 25 - 50 parts trans-butene-2, 10 - 30 parts cis-butene-2; 0.1 - 20 parts combined propylene and butene-1; and 0.01 - 2 parts isobutene.
Claim 4
Dependent Claim 51 words
A process according to claim 1 wherein said solvent is a C 4 hydrocarbon mixture consisting essentially of, per 100 parts by weight of solvent, 30 - 60 parts butane; 25 - 50 parts trans-butene-2; 10 - 20 parts cis-butene-2; 0.1 - 20 parts butene-1; and 0.01 - 2 parts isobutene.
Claim 5
Dependent Claim 22 words
A process according to claim 3 wherein said solvent is the distillation residue obtained from the sump of a butene-1 concentration process.
Claim 6
Dependent Claim 40 words
A process according to claim 1 wherein said solvent consists essentially of, per 100 parts by weight of solvent, about 20 parts propane; about 3 parts propylene; about 30 parts butane; about 42 parts butene-2; and about 5 parts butene-1.
Claim 7
Dependent Claim 16 words
A process according to claim 1 wherein said solvent contains 0.1 - 20 molar percent butene-1.
Claim 8
Dependent Claim 16 words
A process according to claim 1 wherein said solvent contains 0.1 - 15 molar percent propylene.
Claim 9
Dependent Claim 20 words
A process according to claim 1, further comprising conducting the polymerization reaction in the presence of a molecular weight regulator.
Claim 10
Dependent Claim 14 words
A process according to claim 8, wherein the molecular weight regulator is gaseous hydrogen.
Claim 11
Dependent Claim 22 words
A process according to claim 1 further comprising adiabatically expanding unreacted monomers and residual solvent at the completion of the polymerization reaction.
Claim 12
Dependent Claim 25 words
A process according to claim 1 wherein said catalyst component (b) is selected from the group consisting of triethylaluminum, tripropylaluminum, tri-n-butylaluminum, triisobutylaluminum and diisolbutylaluminum hydride.
Claim 13
Dependent Claim 31 words
A process according to claim 11 wherein said catalyst component (a) is a crystalline titanium trichloride of the formula TiCl 3 .sup.. n AlCl 3 wherein n = 0.2 - 0.6.

References Cited (Backward Citations)

GB932658A Cited
GB967788A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1979-09-21 1980-03-22 1980-09-21 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1983-09-21 1984-03-22 1984-09-21 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1987-09-21 1988-03-22 1988-09-21 $7700.00 Window Closed / Lapsed

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