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US3951901A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for the production of homogeneous polyolefin rubber-oil mixtures

Assignee: Huels AG
•
Filing: 1974-02-21
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Granted: 1976-04-20
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Expires: 1994-02-21
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Abstract

Abstract A process for preparing a homogeneous liquid mixture consisting essentially of a normally solid polyolefin rubber copolymer of at least two different monoolefinically unsaturated hydrocarbons of 2-8 carbon atoms or of at least two different monoolefinically unsaturated hydrocarbons of 2-8 carbon atoms and at least one copolymerizable unconjugated diene hydrocarbon of 6-16 carbon atoms and at least an equal amount by weight of an extending oil having a viscosity of 50-5000 centistokes and a specific gravity of 0.84 - 0.98, which comprises: A. adding the copolymer to said extending oil at a temperature of 80° - 230°C; and B. admixing the copolymer with the hot extending oil at an agitation speed of 1-500 cm/sec and a shear velocity of 0.5 - 100 sec.sup. -1 for a period of time sufficient to form said homogeneous liquid mixture substantially free of particulate copolymer.

Inventors

  • 👤 Harald Bluemel
  • 👤 Georg Schleich

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-26 18:33
CPC Classifications
C; C10; C10M; C10M1/00; C10M1/08; C10M2203/00; C10M2203/06; C10M2205/00; C10N; C10N2020/00; C10N2020/01; Y; Y10; Y10S; Y10S524/00; Y10S524/924

Claims Analysis

Total Claims: 6
Claim 1
Independent Claim 240 words
A process for preparing a homogeneous liquid mixture consisting essentially of i) a normally solid polyolefin rubber copolymer of 30-65% by weight ethylene and correspondingly 70-35% by weight of at least one monoolefinically unsaturated hydrocarbon of 3-8 carbon atoms, optionally further including at least one copolymerizable unconjugated diene hydrocarbon of 6-16 carbon atoms in an amount which provides 0.5- 30 olefinic double bonds per 100 carbon atoms in the copolymer, sad polyolefin rubber copolymer having a molecular weight (M n ) of 25,000-100,000 as determined by the osmometric method and a Mooney viscosity ML 1 +4 at 100° C. of 30-180, dissolved in ii) 3-6 parts by weight, per part by weight of the copolymer, of an extending oil having a viscosity of 50-5000 centistokes at 20° C., a specific gravity of 0.84- 0.98 and a boiling point of 120°-370° C. at 5 Torr, which comprises: a. adding the polyolefin rubber in the form of loose, freely movable crumbs having a density of 0.1-0.4 g/cm 3 to said extending oil at a temperature of 160-210° C; and b. admixing the polyolefin rubber crumbs with the hot extending oil at an agitation speed of 5-100 cm/sec. and a shear velocity of 1-50 sec. - 1 for a period of time less than about 45 minutes but which time is sufficient to form a homogeneous liquid mixture wherein less than 1% by weight of the polyolefin rubber remains in the solid state.
Claim 2
Dependent Claim 240 words
A process for preparing a homogeneous liquid mixture consisting essentially of i) a normally solid polyolefin rubber copolymer of 30-65% by weight ethylene and correspondingly 70-35% by weight of at least one monoolefinically unsaturated hydrocarbon of 3-8 carbon atoms, optionally further including at least one copolymerizable unconjugated diene hydrocarbon of 6-16 carbon atoms in an amount which provides 0.5- 30 olefinic double bonds per 100 carbon atoms in the copolymer, sad polyolefin rubber copolymer having a molecular weight (M n ) of 25,000-100,000 as determined by the osmometric method and a Mooney viscosity ML 1 +4 at 100° C. of 30-180, dissolved in ii) 3-6 parts by weight, per part by weight of the copolymer, of an extending oil having a viscosity of 50-5000 centistokes at 20° C., a specific gravity of 0.84- 0.98 and a boiling point of 120°-370° C. at 5 Torr, which comprises: a. adding the polyolefin rubber in the form of loose, freely movable crumbs having a density of 0.1-0.4 g/cm 3 to said extending oil at a temperature of 160-210° C; and b. admixing the polyolefin rubber crumbs with the hot extending oil at an agitation speed of 5-100 cm/sec. and a shear velocity of 1-50 sec. - 1 for a period of time less than about 45 minutes but which time is sufficient to form a homogeneous liquid mixture wherein less than 1% by weight of the polyolefin rubber remains in the solid state.
Claim 3
Dependent Claim 14 words
A process according to claim 1, wherein the polyolefin rubber is an ethylene-propylene rubber.
Claim 4
Dependent Claim 15 words
A process according to claim 1, wherein the polyolefin rubber is an unconjugated diene rubber.
Claim 5
Dependent Claim 23 words
A process according to claim 3, wherein the unconjugated diene is selected from the group consisting of 1,4-hexadiene, dicyclopentadiene, methylenenorbornene, ethylidenenorbornene and propenylnorbornene.
Claim 6
Dependent Claim 19 words
A process according to claim 1, wherein the extending oil has a viscosity of 200-3000 centistokes at 20° C.

References Cited (Backward Citations)

US3691078A Cited
US3676387A Cited
US3679380A Cited
US3794611A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1979-04-20 1979-10-20 1980-04-20 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1983-04-20 1983-10-20 1984-04-20 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1987-04-20 1987-10-20 1988-04-20 $7700.00 Window Closed / Lapsed

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