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
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Filing: 1974-10-02
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Granted: 1976-09-21
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Expires: 1994-10-02
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.
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 |