US4058654A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for the bulk polymerization of α-olefins
Assignee: Bayer AG
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Filing: 1975-07-14
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Granted: 1977-11-15
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Expires: 1995-07-14
Abstract
Abstract Process for the continuous production of a polymer of an α-olefin monomer. The monomer is polymerized in bulk, employing a screw conveyor as the reactor. The monomer can be in liquid phase when introduced into the conveyor. By the process, the use of diluents is avoided.
Inventors
- 👤 Hubert Sutter
- 👤 Reinhard Peuker
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-08 11:54
CPC Classifications
C; C08; C08F; C08F10/00; B; B01; B01J; B01J19/00; B01J19/18; B01J19/20; C08F210/00; C08F210/04; C08F210/06; C08F210/08
Claims Analysis
Total Claims: 19
Claim 1
Independent Claim
113 words
Process for continuous production of a polymer of an α-olefin monomer by bulk polymerization which comprises continuously introducing the monomer and a catalyst for the polymerization into the feed end portion of a multi-screw conveyor for transport of the monomer and catalyst in admixture through the conveyor and bulk polymerization of the monomer during said transport, the mixture of monomer and catalyst during said transport being under a pressure of 5-200 bars, the temperature of said monomer during said transport following a rising profile with the temperature adjacent the feed end of said multi-screw conveyor being -50° to 30° C and the temperature adjacent the discharge end thereof being 50° to 200° C.
Claim 2
Dependent Claim
113 words
Process for continuous production of a polymer of an α-olefin monomer by bulk polymerization which comprises continuously introducing the monomer and a catalyst for the polymerization into the feed end portion of a multi-screw conveyor for transport of the monomer and catalyst in admixture through the conveyor and bulk polymerization of the monomer during said transport, the mixture of monomer and catalyst during said transport being under a pressure of 5-200 bars, the temperature of said monomer during said transport following a rising profile with the temperature adjacent the feed end of said multi-screw conveyor being -50° to 30° C and the temperature adjacent the discharge end thereof being 50° to 200° C.
Claim 3
Dependent Claim
62 words
Process of claim 1, wherein the catalyst is an organo-metallic mixed catalyst containing a metal compound of an element of sub-groups 4b, 5b, 6b or of group 8 of the periodic table and an organo-metallic compound of an element of groups 1a, 2a or 3a of the periodic table, or a catalyst containing an oxide of sub-group 6b of the periodic table.
Claim 4
Dependent Claim
29 words
Process of claim 1, wherein polymerizable monomer other than said α-olefin monomer is introduced into the feed end portion of the multi-screw conveyor for copolymerization with said α-olefin monomer.
Claim 5
Dependent Claim
16 words
Process of claim 1, wherein the monomer when introduced into the conveyor is in liquid phase.
Claim 6
Dependent Claim
19 words
Process of claim 3, wherein said α-olefin and polymerizable monomer are in liquid phase when introduced into the conveyor.
Claim 7
Dependent Claim
53 words
Process of claim 2, wherein the catalyst is an organo-metallic mixed catalyst, the components of the mixed catalyst are dissolved or dispersed separately from one another in separate portions of monomer and the polymerization is initiated by bringing streams of these portions together, or together with supplementary amounts of monomer in metered ratio.
Claim 8
Dependent Claim
28 words
Process of claim 6, wherein the streams containing the catalyst components are brought together to undergo a pre-reaction and the resulting mixture is fed into the screw reactor.
Claim 9
Dependent Claim
21 words
Process of claim 2, wherein the components of the mixed catalyst are mixed separately from the monomer outside the screw conveyor.
Claim 10
Dependent Claim
9 words
Process of claim 1, wherein the α-olefin is ethylene.
Claim 11
Dependent Claim
8 words
Process of claim 1, wherein α-olefine is propylene.
Claim 12
Dependent Claim
8 words
Process of claim 1, wherein α-olefine is butene-1.
Claim 13
Dependent Claim
9 words
Process of claim 1, wherein the α-olefine is 4-methylpentene-1.
Claim 14
Dependent Claim
18 words
Process of claim 3, wherein the different monomers are fed into the screw reactor at spatially separate positions.
Claim 15
Dependent Claim
18 words
Process of claim 1 wherein the polymerization is effected at a pressure of from 10 to 100 bars.
Claim 16
Dependent Claim
19 words
Process of claim 1, wherein the lower temperature of the rising temperature profile lies between -20° and 30° C.
Claim 17
Dependent Claim
19 words
Process of claim 1, wherein the upper temperature of the rising temperature profile lies between 80° and 180° C.
Claim 18
Dependent Claim
22 words
Process of claim 1, wherein the ratio of the length to diameter of the screws of the conveyor is up to 30.
Claim 19
Dependent Claim
13 words
Process of claim 1, wherein the conveyor is a self-purging, forced feed conveyor.
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) | 1980-11-14 | 1981-05-16 | 1981-11-15 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-11-14 | 1985-05-16 | 1985-11-15 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-11-14 | 1989-05-16 | 1989-11-15 | $7700.00 | Window Closed / Lapsed |