US4309276A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Hydrocarbon conversion with low-sodium silicalite
Assignee: Chevron USA Inc
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Filing: 1980-04-28
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Granted: 1982-01-05
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Expires: 2000-04-28
Abstract
Abstract Hydrocarbon conversion in the presence of a low-sodium form crystalline silicate converts normal and slightly branched paraffins, at least in part, to olefins.
Inventors
- 👤 Stephen J. Miller
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-28 18:19
CPC Classifications
C; C10; C10G; C10G35/00; C10G35/04; C10G35/06; B; B01; B01J; B01J29/00; B01J29/03; B01J29/035; B01J29/04; B01J29/06; B01J29/40; C10G29/00; C10G29/16; B01J2229/00; B01J2229/30; B01J2229/42; C10G2300/00; C10G2300/70; C10G2400/00; C10G2400/02
Claims Analysis
Total Claims: 14
Claim 1
Independent Claim
43 words
A process for producing olefins from normal paraffins, slightly branched paraffins, and mixtures thereof, comprising contacting a feed which comprises said paraffins with silicalite containing less than about 0.1 weight percent sodium, and producing an effluent of greater olefin content than said feed.
Claim 2
Dependent Claim
43 words
A process for producing olefins from normal paraffins, slightly branched paraffins, and mixtures thereof, comprising contacting a feed which comprises said paraffins with silicalite containing less than about 0.1 weight percent sodium, and producing an effluent of greater olefin content than said feed.
Claim 3
Dependent Claim
42 words
The process of claim 1 wherein said silicalite is composited with an inorganic matrix wherein the matrix is substantially free of cracking activity, said silicalite being present in the resulting composite in an amount from about 5 to about 95 weight percent.
Claim 4
Dependent Claim
18 words
The process of claim 1 wherein said olefin content is at least 10 weight percent of converted feed.
Claim 5
Dependent Claim
19 words
The process of claim 1 wherein said feed contains at least 5 weight percent normal and slightly branched paraffins.
Claim 6
Dependent Claim
19 words
The process of claim 4 wherein said feed has a nitrogen content less than about 25 ppm by weight.
Claim 7
Dependent Claim
15 words
The process of claim 1 wherein said silicalite contains less than 0.03 weight percent sodium.
Claim 8
Dependent Claim
16 words
The process of claim 6 wherein said silicalite contains less than about 0.01 weight percent sodium.
Claim 9
Dependent Claim
43 words
The process of claim 1 wherein said contacting is carried out at a temperature of from about 285° C. to about 595° C., a pressure from subatmospheric to about 205 bar, and a liquid hourly space velocity from about 0.1 to about 50.
Claim 10
Dependent Claim
27 words
The process of claim 8 wherein said temperature is from about 340° to about 485° C., and said pressure is from about atmospheric to about 140 bar.
Claim 11
Dependent Claim
30 words
The process of claim wherein said contacting is conducted in the presence of hydrogen at a hydrogen to hydrocarbon ratio of from about 350 to about 3650 liters hydrogen/liter hydrocarbon.
Claim 12
Dependent Claim
16 words
The process of claim 10 wherein said ratio is from 890 to 2140 liters hydrogen/liter hydrocarbon.
Claim 13
Dependent Claim
113 words
A process for producing olefins from normal paraffins, slightly branched paraffins, and mixtures thereof, comprising contacting a feed which comprises said paraffins with a composition substantially free of hydrogenation activity comprising silicalite containing less than about 0.1 weight percent sodium composited in a matrix which is substantially free of cracking activity, said contacting occurring at a temperature from about 285° to about 595° C., a pressure from about 14 to about 205 bar, and a hydrogen to hydrocarbon volume ratio from about 350 to about 3650 liters hydrogen/liter hydrocarbon; and producing an effluent of greater olefin content than said feed, wherein said olefin content is at least 10 weight percent of converted feed.
Claim 14
Dependent Claim
113 words
A process for producing olefins from normal paraffins, slightly branched paraffins, and mixtures thereof, comprising contacting a feed which comprises said paraffins with a composition substantially free of hydrogenation activity comprising silicalite containing less than about 0.1 weight percent sodium composited in a matrix which is substantially free of cracking activity, said contacting occurring at a temperature from about 285° to about 595° C., a pressure from about 14 to about 205 bar, and a hydrogen to hydrocarbon volume ratio from about 350 to about 3650 liters hydrogen/liter hydrocarbon; and producing an effluent of greater olefin content than said feed, wherein said olefin content is at least 10 weight percent of converted feed.
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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) | 1985-01-04 | 1985-07-06 | 1986-01-05 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1989-01-04 | 1989-07-06 | 1990-01-05 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1993-01-04 | 1993-07-06 | 1994-01-05 | $7700.00 | Window Closed / Lapsed |