US3933934A
Expired / Lapsed
US
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Fabrication of atactic waxes of polyolefin
Assignee: Naphtachimie SA
•
Filing: 1973-01-18
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Granted: 1976-01-20
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Expires: 1993-01-18
Abstract
Abstract Atactic waxes and method for preparing same by polymerization of polyolefin alone or in combination with other monoolefins of the formula CH 2 = CHR in which R is hydrogen or an alkyl radical having from 2 to 8 carbon atoms in which the polymerization is carried out at low pressure and in a hydrocarbon solvent in the presence of a catalyst formed of the product of the reaction of magnesium or a compound thereof, a compound of a transition metal selected from the sub-groups IVa, Va and VIa of the periodic classification of elements and an alkyl halide, and a co-catalyst in the form of an organometallic compound of a metal selected of groups II and III of the periodic classification of elements.
Inventors
- 👤 Jean Claude Bailly
- 👤 Daniel Durand
- 👤 Pierre Mangin
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-01 01:04
CPC Classifications
C; C08; C08F; C08F10/00; C08F10/04; C08F10/06; Y; Y10; Y10S; Y10S585/00; Y10S585/929; Y10S585/946
Claims Analysis
Total Claims: 10
Claim 1
Independent Claim
252 words
A process for the manufacture of atactic waxes which are substantially completely soluble in boiling n-heptane by polymerizing propylene alone or with the addition of not more than 30% by weight monoolefins having the general formula CH 2 = CHR in which R is hydrogen or an alkyl radical containing 2 to 8 carbon atoms in which the polymerization is carried out at low pressure and in a hydrocarbon solvent in the presence of a catalytic system formed of (a) a catalyst prepared in a one step reaction between magnesium, an alkyl halide and a titanium compound having the general formula TiX 4 -m (OR') m in which Ti represents titanium, X represents a halogen atom, R' represents an alkyl radical having from 2 to 8 carbon atoms and m is a number within the range of 1 to 4, in which the titanium compound is present in an amount to provide 0.5 to 2 milligram-atoms of titanium per liter of solvent, and (b) a co-catalyst in the form of an organo aluminum compound having the formula AlR" n X 3 -n , in which R" represents an alkyl radical having from 1 to 12 carbon atoms, some of which may be replaced by hydrogen atoms, X is a halogen atom and n is a number within the range of 1 to 3, the organo aluminum compound being present in an amount such that the atomic ratio of aluminum to titanium in the catalyst is within the range of 2 to 10.
Claim 2
Dependent Claim
252 words
A process for the manufacture of atactic waxes which are substantially completely soluble in boiling n-heptane by polymerizing propylene alone or with the addition of not more than 30% by weight monoolefins having the general formula CH 2 = CHR in which R is hydrogen or an alkyl radical containing 2 to 8 carbon atoms in which the polymerization is carried out at low pressure and in a hydrocarbon solvent in the presence of a catalytic system formed of (a) a catalyst prepared in a one step reaction between magnesium, an alkyl halide and a titanium compound having the general formula TiX 4 -m (OR') m in which Ti represents titanium, X represents a halogen atom, R' represents an alkyl radical having from 2 to 8 carbon atoms and m is a number within the range of 1 to 4, in which the titanium compound is present in an amount to provide 0.5 to 2 milligram-atoms of titanium per liter of solvent, and (b) a co-catalyst in the form of an organo aluminum compound having the formula AlR" n X 3 -n , in which R" represents an alkyl radical having from 1 to 12 carbon atoms, some of which may be replaced by hydrogen atoms, X is a halogen atom and n is a number within the range of 1 to 3, the organo aluminum compound being present in an amount such that the atomic ratio of aluminum to titanium in the catalyst is within the range of 2 to 10.
Claim 3
Dependent Claim
24 words
The process as claimed in claim 1 in which the monoolefin is present in an amount less than 10% by weight of the propylene.
Claim 4
Dependent Claim
14 words
The process as claimed in claim 1 in which the halogen atom is chlorine.
Claim 5
Dependent Claim
17 words
The process as claimed in claim 1 in which m is a value between 1.5 and 2.5.
Claim 6
Dependent Claim
13 words
The process as claimed in claim 1 in which the halogen is chlorine.
Claim 7
Dependent Claim
37 words
The process as claimed in claim 1 in which the amount of co-catalyst is such that the atomic ratio of aluminum in the co-catalyst to titanium in the catalyst is within the range of 3 to 5.
Claim 8
Dependent Claim
39 words
The process as claimed in claim 1 in which the polymerization is carried out at a pressure below 20 bars at a temperature within the range of 40° to 150°C and in which the solvent is a paraffinic hydrocarbon.
Claim 9
Dependent Claim
35 words
The process as claimed in claim 7 in which the paraffinic hydrocarbon is selected from the group consisting of n-heptane and a petroleum fraction consisting essentially of paraffin having from 6 to 8 carbon atoms.
Claim 10
Dependent Claim
22 words
The process as claimed in claim 1 which includes the step of separating the formed waxes from the hydrocarbon solvent after polymerization.
References Cited (Backward Citations)
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Cited
US2956993A
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US3121063A
Cited
US3065216A
Cited
US3179601A
Cited
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Cited
US3801558A
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1979-01-19 | 1979-07-21 | 1980-01-20 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1983-01-19 | 1983-07-21 | 1984-01-20 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1987-01-19 | 1987-07-21 | 1988-01-20 | $7700.00 | Window Closed / Lapsed |