US3984387A
Expired / Lapsed
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Preparation of linear α-olefin polymers having ultra high molecular weight
Assignee: Dow Chemical Co
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Filing: 1974-08-07
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Granted: 1976-10-05
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Expires: 1994-08-07
Abstract
Abstract Ultra high molecular weight, linear α-olefin polymers are produced without reactor fouling by polymerizing an α-olefin in the presence of Ziegler catalyst dispersed in an inert diluent and an amount of an inert gas not in excess of that which will dissolve in the inert liquid diluent.
Inventors
- 👤 Gordon Y. T. Liu
- 👤 Donald R. Smith
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-07 18:12
CPC Classifications
C; C08; C08F; C08F10/00; Y; Y10; Y10S; Y10S526/00; Y10S526/905
Claims Analysis
Total Claims: 7
Claim 1
Independent Claim
75 words
A process for polymerization in a polymerization zone α-olefin in the presence of a catalytic amount of a Ziegler catalyst in an inert liquid diluent which comprises the steps ( 1) introducing into the polymerization zone an inert gas in an amount sufficient to effect macromolecular heat transfer in the liquid phase of the polymerization zone but not in excess of the capacity of the diluent to solvate the gas and (2) polymerizing the α-olefin.
Claim 2
Dependent Claim
75 words
A process for polymerization in a polymerization zone α-olefin in the presence of a catalytic amount of a Ziegler catalyst in an inert liquid diluent which comprises the steps ( 1) introducing into the polymerization zone an inert gas in an amount sufficient to effect macromolecular heat transfer in the liquid phase of the polymerization zone but not in excess of the capacity of the diluent to solvate the gas and (2) polymerizing the α-olefin.
Claim 3
Dependent Claim
30 words
The process of claim 1 wherein the inert gas is nitrogen in an amount in the range from about 100 to 10,000 parts per million based on the inert diluent.
Claim 4
Dependent Claim
31 words
The process of claim 1 wherein the inert gas is helium in an amount in the range from about 20 to about 1000 parts per million based on the inert diluent.
Claim 5
Dependent Claim
34 words
The process of claim 2 wherein the α-olefin is ethylene or a mixture of ethylene and another α-olefin and the catalyst contains the reaction product of an alkyl aluminum compound and a titanium halide.
Claim 6
Dependent Claim
32 words
The process of claim 4 wherein the α-olefin is a mixture of ethylene and butene-1 and the catalyst is aluminum triisobutyl and the reaction product of diethyl aluminum chloride and titanium tetrachloride.
Claim 7
Dependent Claim
33 words
The process of claim 1 for polymerizing the α-olefin in a reactor to form a polymer having a melt flow viscosity as determined by ASTM-D-1238-65T(E) less than 0.3 decigram/minute without fouling the reactor.
References Cited (Backward Citations)
GB991397A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1979-10-05 | 1980-04-05 | 1980-10-05 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1983-10-05 | 1984-04-05 | 1984-10-05 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1987-10-05 | 1988-04-05 | 1988-10-05 | $7700.00 | Window Closed / Lapsed |