US4052477A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method for upgrading a fischer-tropsch light oil
Assignee: Mobil Oil AS
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Filing: 1976-05-07
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Granted: 1977-10-04
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Expires: 1996-05-07
Abstract
Abstract The product of Fischer-Tropsch Synthesis is separated to recover a C 5 -400° F liquid fraction which is thereafter hydrogenated in order to saturate diolefins and contacted with a ZSM-5 type zeolite under conditions of elevated temperature and pressure so as to obtain gasoline of a higher octane rating. The contact with the ZSM-5 zeolite is preferably in the presence of added hydrogen.
Inventors
- 👤 Henry R. Ireland
- 👤 Alan W. Peters
- 👤 Thomas R. Stein
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-30 03:39
CPC Classifications
C; C10; C10G; C10G45/00; C10G45/32; C10G45/34; C10G45/40; C10G35/00; C10G35/04; C10G35/06; C10G35/095; Y; Y10; Y10S; Y10S208/00; Y10S208/95; Y10S585/00; Y10S585/929; Y10S585/943
Claims Analysis
Total Claims: 14
Claim 1
Independent Claim
137 words
A method for upgrading the C 5 + liquid product of a Fischer-Tropsch synthesis having an end point from about 340°-400° F which comprises hydrogenating said liquid in the presence of a hydrogenation catalyst component at conditions of temperature and pressure so as the selectively hydrogenate substantially only the diolefins contained therein and thereafter contacting said liquid at a temperature within the range of about 575° to about 850° F and at a pressure within the range of from about atmospheric to 700 psig with a crystalline aluminosilicate catalyst component characterized by a pore dimension greater than about 5 Angstroms, a silica to alumina ratio of at least 12, and a constraint index within the range of 1:12 said catalyst being presulfided prior to use, and recovering a gasoline boiling range product having an enhanced octane number.
Claim 2
Independent Claim
137 words
A method for upgrading the C 5 + liquid product of a Fischer-Tropsch synthesis having an end point from about 340°-400° F which comprises hydrogenating said liquid in the presence of a hydrogenation catalyst component at conditions of temperature and pressure so as the selectively hydrogenate substantially only the diolefins contained therein and thereafter contacting said liquid at a temperature within the range of about 575° to about 850° F and at a pressure within the range of from about atmospheric to 700 psig with a crystalline aluminosilicate catalyst component characterized by a pore dimension greater than about 5 Angstroms, a silica to alumina ratio of at least 12, and a constraint index within the range of 1:12 said catalyst being presulfided prior to use, and recovering a gasoline boiling range product having an enhanced octane number.
Claim 3
Dependent Claim
13 words
The process of claim 1, wherein the hydrogenation component comprises platinum or palladium.
Claim 4
Dependent Claim
20 words
The process of claim 2, wherein the hydrogenation is carried out at a temperature of from 100° to 400° F.
Claim 5
Dependent Claim
19 words
The process of claim 1, wherein the crystalline aluminosilicate zeolite has been exchanged with hydrogen ions or ammonium ions.
Claim 6
Dependent Claim
25 words
The process of claim 4, wherein a hydrogenation/dehydrogenation component is associated with the crystalline aluminosilicate and contact therewith is in the presence of added hydrogen.
Claim 7
Dependent Claim
11 words
The process of claim 5, wherein the hydrogenation/dehydrogenation component is nickel.
Claim 8
Independent Claim
123 words
A method for upgrading the C 5 + liquid fraction of a Fischer-Tropsch synthesis comprising sulfur having an end point of from about 340°-400° F, which comprises hydrogenating said C 5 + liquid by contact with a presulfided hydrogenation catalyst comprising platinum or palladium at a temperature of 100° to 400° F and a pressure of 50 to 800 psig so as to selectively hydrogenate only the diolefins contained therein and thereafter contacting said selectively hydrogenated liquid at a temperature of 575°-850° F and a pressure of from about atmospheric to 700 psig with a crystalline aluminosilicate zeolite selected from the group consisting of ZSM-5, ZSM-11, ZSM-12, ZSM-21, ZSM-35, and ZSM-38 and recovering a gasoline boiling range product having an enhanced octane number.
Claim 9
Independent Claim
123 words
A method for upgrading the C 5 + liquid fraction of a Fischer-Tropsch synthesis comprising sulfur having an end point of from about 340°-400° F, which comprises hydrogenating said C 5 + liquid by contact with a presulfided hydrogenation catalyst comprising platinum or palladium at a temperature of 100° to 400° F and a pressure of 50 to 800 psig so as to selectively hydrogenate only the diolefins contained therein and thereafter contacting said selectively hydrogenated liquid at a temperature of 575°-850° F and a pressure of from about atmospheric to 700 psig with a crystalline aluminosilicate zeolite selected from the group consisting of ZSM-5, ZSM-11, ZSM-12, ZSM-21, ZSM-35, and ZSM-38 and recovering a gasoline boiling range product having an enhanced octane number.
Claim 10
Dependent Claim
20 words
A process of claim 7, wherein the crystalline aluminosilicate zeolite has been base exchanged with hydrogen ions or ammonium ions.
Claim 11
Dependent Claim
28 words
The process of claim 8, wherein the crystalline aluminosilicate has a hydrogenation/dehydrogenation component associated therewith in sulfided condition and contact therewith is in the presence of added hydrogen.
Claim 12
Dependent Claim
10 words
The process of claim 7, wherein the zeolite is ZSM-5.
Claim 13
Dependent Claim
23 words
The process of claim 9, wherein the zeolite is ZSM-5 which has nickel associated therewith and is composited with an inorganic oxide binder.
Claim 14
Dependent Claim
10 words
The process of claim 11, wherein the binder is alumina.
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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) | 1980-10-03 | 1981-04-04 | 1981-10-04 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-10-03 | 1985-04-04 | 1985-10-04 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-10-03 | 1989-04-04 | 1989-10-04 | $7700.00 | Window Closed / Lapsed |