US4188470A
Expired / Lapsed
US
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Process for polymerizing ethylene in a gaseous phase
Assignee: Montedison SpA
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Filing: 1978-01-11
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Granted: 1980-02-12
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Expires: 1998-01-11
Abstract
Abstract Ethylene is polymerized in a gaseous phase and in contact with a Ziegler/Natta type solid catalyst capable of producing polyethylene in the form of granules having an easily controllable and homogeneous granulometric size, the polymerization being conducted in a tubular reactor in which the catalyst and the polymer granules which are formed are carried along the reactor by the flow of the gas.
Inventors
- 👤 Amilcare Collina
- 👤 Arrigo Soverini
- 👤 Francesco Rosati
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-23 22:05
CPC Classifications
C; C08; C08F; C08F110/00; C08F110/02; Y; Y10; Y10S; Y10S526/00; Y10S526/901; Y10S526/904
Claims Analysis
Total Claims: 7
Claim 1
Independent Claim
146 words
Process for the polymerization of ethylene in a gaseous phase, in a tubular reactor in which the flow of the gas consisting of ethylene or a mixture of ethylene with other gases, and having a flow rate comprised between 2 and 5 m/sec., carries the catalyst and the polymer particles that are formed at a mean velocity about equal for all the particles, the polymerization being conducted in the presence of a catalyst obtained by mixing at least one compound of a transition metal selected from the group consisting of titanium, vanadium, zirconium and chromium, with an organometallic compound or hydride of a metal belonging to Groups I to III of the Mendelyeev Periodic System, and having a starting polymerization speed such that a yield of at least 100,000 g of polymer/g of transition metal is obtained within the first 15 minutes of the polymerization reaction.
Claim 2
Dependent Claim
146 words
Process for the polymerization of ethylene in a gaseous phase, in a tubular reactor in which the flow of the gas consisting of ethylene or a mixture of ethylene with other gases, and having a flow rate comprised between 2 and 5 m/sec., carries the catalyst and the polymer particles that are formed at a mean velocity about equal for all the particles, the polymerization being conducted in the presence of a catalyst obtained by mixing at least one compound of a transition metal selected from the group consisting of titanium, vanadium, zirconium and chromium, with an organometallic compound or hydride of a metal belonging to Groups I to III of the Mendelyeev Periodic System, and having a starting polymerization speed such that a yield of at least 100,000 g of polymer/g of transition metal is obtained within the first 15 minutes of the polymerization reaction.
Claim 3
Dependent Claim
24 words
The process of claim 1, in which the concentration of the solid particles in the gas flow is comprised between 2 and 20 kg/cu.mt.
Claim 4
Dependent Claim
21 words
The process of claim 1, in which the catalyst introduced into the reactor is supported on granules of a preformed polymer.
Claim 5
Dependent Claim
22 words
The process of claim 3, in which the granules of preformed polymer have a particle size comprised between 100 and 500 microns.
Claim 6
Dependent Claim
19 words
The process of claim 1, in which part of the polymer produced is recycled back into the tubular reactor.
Claim 7
Dependent Claim
26 words
The process of claim 1, in which the gaseous mixture separated from the polymerization product is recycled back, in whole or in part, to the reactor.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1983-02-11 | 1983-08-13 | 1984-02-12 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1987-02-11 | 1987-08-13 | 1988-02-12 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1991-02-11 | 1991-08-13 | 1992-02-12 | $7700.00 | Window Closed / Lapsed |