US4045508A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method of making alpha-olefin oligomers
Assignee: Chevron USA Inc
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Filing: 1975-11-20
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Granted: 1977-08-30
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Expires: 1995-11-20
Abstract
Abstract The trimer to tetramer ratio of an alpha-olefin oligomer is varied over a significant range in a continuous, multi-stage alpha-olefin oligomerization process including a first stage tank reactor and a final tube reactor by controlling the amount of conversion taking place in each stage. The multi-stage process is used to prepare various poly(l-decene) oligomer mixtures having different oligomer proportions for use as synthetic lubricants.
Inventors
- 👤 Barrett L. Cupples
- 👤 William J. Heilman
- 👤 A. Norman Kresge
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-26 16:36
CPC Classifications
C; C07; C07C; C07C2/00; C07C2/02; C07C2/04; C07C2/06; C07C2/08; C07C2/14; C07C2/20; C07C2527/00; C07C2527/06; C07C2527/08; C07C2527/12; C07C2527/1213; Y; Y10; Y10S; Y10S585/00; Y10S585/919; Y10S585/921; Y10S585/924; Y10S585/925; Y10S585/926
Claims Analysis
Total Claims: 12
Claim 1
Independent Claim
148 words
The continuous process for polymerizing a 1-olefin to an oligomer mixture including trimer and tetramer which comprises continuously introducing a 1-olefin having from about five to about 14 carbon atoms or a mixture thereof into the first of a series of one or more tank reactors with mixing therein to provide a substantially homogeneous reaction mixture in the presence of a catalytic amount of boron trifluoride and a co-catalyst that complexes with boron trifluoride and continuously removing a partially oligomerized product stream from said series of one or more tank reactors and flowing said product stream through a tube reactor for further conversion of said 1-olefin to oligomer product, the length to diameter ratio of said tube reactor being at least about 15 to one and said series of tank reactors and said tube reactor being maintained at a same or different temperature suitable for the oligomerization reaction.
Claim 2
Dependent Claim
148 words
The continuous process for polymerizing a 1-olefin to an oligomer mixture including trimer and tetramer which comprises continuously introducing a 1-olefin having from about five to about 14 carbon atoms or a mixture thereof into the first of a series of one or more tank reactors with mixing therein to provide a substantially homogeneous reaction mixture in the presence of a catalytic amount of boron trifluoride and a co-catalyst that complexes with boron trifluoride and continuously removing a partially oligomerized product stream from said series of one or more tank reactors and flowing said product stream through a tube reactor for further conversion of said 1-olefin to oligomer product, the length to diameter ratio of said tube reactor being at least about 15 to one and said series of tank reactors and said tube reactor being maintained at a same or different temperature suitable for the oligomerization reaction.
Claim 3
Dependent Claim
44 words
The continuous process for polymerizing a 1-olefin in accordance with claim 1 in which there is one tank reactor and the 1-olefin is 1-decene or a mixture containing 1-decene and up to about 50 mol percent of 1-octene or 1-dodecene or a mixture thereof.
Claim 4
Dependent Claim
47 words
The continuous process for polymerizing a 1-olefin in accordance with claim 2 in which the ratio of the percent conversion of 1-olefin to oligomer in the tank reactor to the percent conversion of 1-olefin to oligomer in the tube reactor is between about 90:10 and about 15:85.
Claim 5
Dependent Claim
23 words
The continuous process for polymerizing a 1-olefin in accordance with claim 3 in which said ratio is between about 80:20 and about 30:70.
Claim 6
Dependent Claim
47 words
The continuous process for polymerizing a 1-olefin in accordance with claim 2 in which the total combined conversion of 1-olefin to oligomer in the tank reactor and the tube reactor is between about 50 percent and about 100 percent of the 1-olefin fed to said tank reactor.
Claim 7
Dependent Claim
28 words
The continuous process for polymerizing a 1-olefin in accordance with claim 2 in which said catalyst is an aliphatic mono-alcohol having from one to about 10 carbon atoms.
Claim 8
Dependent Claim
23 words
The continuous process for polymerizing a 1-olefin in accordance with claim 6 in which said tank reactor is pressured with boron trifluoride gas.
Claim 9
Dependent Claim
33 words
The continuous process for polymerizing a 1-olefin in accordance with claim 2 in which the ratio of the length to the diameter of said tube reactor is at least about 100 to one.
Claim 10
Dependent Claim
33 words
The continuous process for polymerizing a 1-olefin in accordance with claim 8 in which the ratio of the length to the diameter of said tube reactor is at least about 1,000 to one.
Claim 11
Dependent Claim
93 words
The continuous process for polymerizing 1-decene to an oligomer mixture including trimer and tetramer which comprises continuously introducing 1-decene into a tank reactor with mixing to provide a substantially homogeneous reaction mixture in the presence of a catalytic amount of boron trifluoride complex and free boron trifluoride and continuously removing a partially oligomerized product stream from said tank reactor and flowing said product stream through a tube reactor for further conversion at a temperature suitable for oligomerization, the length to diameter ratio of said tube reactor being at least about 15 to one.
Claim 12
Dependent Claim
93 words
The continuous process for polymerizing 1-decene to an oligomer mixture including trimer and tetramer which comprises continuously introducing 1-decene into a tank reactor with mixing to provide a substantially homogeneous reaction mixture in the presence of a catalytic amount of boron trifluoride complex and free boron trifluoride and continuously removing a partially oligomerized product stream from said tank reactor and flowing said product stream through a tube reactor for further conversion at a temperature suitable for oligomerization, the length to diameter ratio of said tube reactor being at least about 15 to one.
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) | 1980-08-29 | 1981-02-28 | 1981-08-30 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-08-29 | 1985-02-28 | 1985-08-30 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-08-29 | 1989-02-28 | 1989-08-30 | $7700.00 | Window Closed / Lapsed |