US3965205A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Conversion of low octane hydrocarbons to high octane gasoline
Assignee: Mobil Oil AS
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Filing: 1974-06-10
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Granted: 1976-06-22
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Expires: 1994-06-10
Abstract
Abstract It is known to convert methanol and/or other relatively low molecular weight organic compounds containing at least one oxygen, sulfur, nitrogen or halogen hetero atom to high octane gasoline by contacting such with a particular group of crystalline aluminosilicate zeolites at conversion conditions. The instant disclosure shows improvements in total gasoline production from such process by inclusion of natural gas liquid or other light hydrocarbons having low octane numbers, preferably paraffinic, in the feed to said process thereby converting at least a portion of these lighter materials as well to high octane gasoline boiling range components.
Inventors
- 👤 William E. Garwood
- 👤 John A. Manzoni
- 👤 Thaddeus F. Whyte, Jr.
- 👤 John J. Wise
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-25 23:12
CPC Classifications
C; C10; C10G; C10G3/00; C10G3/42; C10G3/44; C10G3/45; C10G3/48; C10G3/49; C10G35/00; C10G35/04; C10G35/06; C10G35/095; C10G2300/00; C10G2300/10; C10G2300/1037; C10G2300/20; C10G2300/30; C10G2300/305; C10G2300/40; C10G2300/4018; C10G2400/00; C10G2400/02; C10G2400/06; Y; Y02; Y02P; Y02P30/00; Y02P30/20; Y10; Y10S; Y10S585/00; Y10S585/929; Y10S585/943
Claims Analysis
Total Claims: 13
Claim 1
Independent Claim
162 words
A process for producing high octane gasoline which comprises forming a feed by admixing at least one lower aliphatic oxygenated organic alcohol, ether or ketone compound having up to about 8 carbon atoms in its longest hydrocarbon chain with an effective amount up to about 95 volume percent based on the volume of lower aliphatic organic component, of a hydrocarbon fraction having a clear research octane number up to about 85; contacting at about 400° to 1000°F said feed with an aluminosilicate zeolite catalyst having a silica to alumina ratio of at least about 12, a constraint index of about 1 to 12 and a crystal density of not substantially below about 1.6 grams per cubic centimeter; and recovering a product comprising a liquid fraction having a boiling range in the normal gasoline boiling range, a clear research octane number higher than that of the hydrocarbon portion of the feed and containing a major proportion of the carbon content of said feed.
Claim 2
Dependent Claim
162 words
A process for producing high octane gasoline which comprises forming a feed by admixing at least one lower aliphatic oxygenated organic alcohol, ether or ketone compound having up to about 8 carbon atoms in its longest hydrocarbon chain with an effective amount up to about 95 volume percent based on the volume of lower aliphatic organic component, of a hydrocarbon fraction having a clear research octane number up to about 85; contacting at about 400° to 1000°F said feed with an aluminosilicate zeolite catalyst having a silica to alumina ratio of at least about 12, a constraint index of about 1 to 12 and a crystal density of not substantially below about 1.6 grams per cubic centimeter; and recovering a product comprising a liquid fraction having a boiling range in the normal gasoline boiling range, a clear research octane number higher than that of the hydrocarbon portion of the feed and containing a major proportion of the carbon content of said feed.
Claim 3
Dependent Claim
21 words
A process as claimed in claim 1 wherein said organic compound comprises methanol, dimethyl ether or a mixture of the two.
Claim 4
Dependent Claim
16 words
A process as claimed in claim 1 wherein said hydrocarbon fraction is a natural gas liquid.
Claim 5
Dependent Claim
17 words
A process as claimed in claim 1 wherein said hydrocarbon fraction is in the gasoline boiling range.
Claim 6
Dependent Claim
22 words
A process as claimed in claim 1 wherein said catalyst is selected from the group consisting of ZSM-5, ZSM-11, ZSM-12 and ZSM-21.
Claim 7
Dependent Claim
12 words
A process as claimed in claim 1 wherein said catalyst is ZSM-5.
Claim 8
Dependent Claim
15 words
A process as claimed in claim 6 wherein said catalyst consisting essentially of nickel ZSM-5.
Claim 9
Dependent Claim
15 words
A process as claimed in claim 6 wherein said catalyst consisting essentially of zinc ZSM-5.
Claim 10
Dependent Claim
21 words
A process as claimed in claim 1 wherein said product has a clear research octane number of at least about 85.
Claim 11
Dependent Claim
14 words
A process as claimed in claim 1 wherein said hydrocarbon fraction is light reformate.
Claim 12
Dependent Claim
18 words
A process as claimed in claim 1 wherein said hydrocarbon fraction is in the gas oil boiling range.
Claim 13
Dependent Claim
19 words
A process as claimed in claim 1 carried out at a space velocity of about 0.5 to 40 LHSV.
References Cited (Backward Citations)
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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) | 1979-06-22 | 1979-12-22 | 1980-06-22 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1983-06-22 | 1983-12-22 | 1984-06-22 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1987-06-22 | 1987-12-22 | 1988-06-22 | $7700.00 | Window Closed / Lapsed |