Patent US831766A successfully refreshed from Google Patents.
US4046831A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method for upgrading products of Fischer-Tropsch synthesis
Assignee: Mobil Oil AS
•
Filing: 1975-09-18
•
Granted: 1977-09-06
•
Expires: 1995-09-18
Abstract
Abstract The product effluent of a Fischer-Tropsch synthesis is subjected to cooling sufficient to separate a high boiling product fraction boiling above about 400 DEG F from lower boiling product effluent material and comprising water product with formed oxygenates. The total lower boiling product effluent thus obtained is passed in contact with a special class of selective crystalline zeolite catalyst maintained under conditions to improve upon the hydrocarbon products contacted and convert oxygenates for hydrocarbons.
Inventors
- 👤 James C. Kuo
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-02 08:20
CPC Classifications
C; C10; C10L; C10L1/00; C10L1/04; C10L1/06; C10G; C10G3/00; C10G3/42; C10G3/44; C10G3/48; C10G3/49; C10G35/00; C10G35/04; C10G35/06; C10G35/095; C10G50/00; C10G2300/00; C10G2300/10; C10G2300/1022; C10G2300/40; C10G2300/4006; C10G2400/00; C10G2400/02; C10G2400/28; Y; Y02; Y02P; Y02P30/00; Y02P30/20; Y10; Y10S; Y10S208/00; Y10S208/95
Claims Analysis
Total Claims: 7
Claim 1
Independent Claim
174 words
A method for upgrading the product effluent of a Fischer-Tropsch synthesis gas operation comprising gaseous hydrocarbons, liquid hydrocarbons and oxygenates which comprises, cooling the product effluent of Fischer-Tropsch synthesis sufficient to separate a decant oil phase comprising the higher boiling hydrocarbon components of the Fischer-Tropsch effluent from a lower boiling phase comprising gaseous and liquid hydrocarbons and a water phase, heating the lower boiling phase to a temperature of at least about 500° F. and passing the thus heated material in contact with a selective crystalline zeolite conversion catalyst selected from the class of crystalline zeolites represented by ZSM-5 maintained at a temperature within the range of 500° to 850° F., separating a product effluent of said crystalline zeolite conversion operation under conditions to recover a gaseous phase comprising C 5 and lower boiling material, a water phase and a hydrocarbon phase boiling above said gaseous phase and separating the hydrocarbon phase obtained from said zeolite conversion operation under conditions to recover LPG gaseous materials, a gasoline product and a light fuel oil product.
Claim 2
Independent Claim
174 words
A method for upgrading the product effluent of a Fischer-Tropsch synthesis gas operation comprising gaseous hydrocarbons, liquid hydrocarbons and oxygenates which comprises, cooling the product effluent of Fischer-Tropsch synthesis sufficient to separate a decant oil phase comprising the higher boiling hydrocarbon components of the Fischer-Tropsch effluent from a lower boiling phase comprising gaseous and liquid hydrocarbons and a water phase, heating the lower boiling phase to a temperature of at least about 500° F. and passing the thus heated material in contact with a selective crystalline zeolite conversion catalyst selected from the class of crystalline zeolites represented by ZSM-5 maintained at a temperature within the range of 500° to 850° F., separating a product effluent of said crystalline zeolite conversion operation under conditions to recover a gaseous phase comprising C 5 and lower boiling material, a water phase and a hydrocarbon phase boiling above said gaseous phase and separating the hydrocarbon phase obtained from said zeolite conversion operation under conditions to recover LPG gaseous materials, a gasoline product and a light fuel oil product.
Claim 3
Dependent Claim
24 words
The method of claim 1 wherein the decant oil phase is separated to recover a waxy oil phase from a light fuel oil product.
Claim 4
Dependent Claim
40 words
The method of claim 1 wherein a C 3 to C 4 rich hydrocarbon fraction is recovered from the product of the crystalline zeolite conversion operation and are thereafter converted to gasoline boiling components by either catalytic polymerization or alkylation.
Claim 5
Dependent Claim
33 words
The method of claim 1 wherein a portion of the gaseous phase separated from the product effluent of the crystalline zeolite conversion operation is processed to produce LPG gaseous components and gasoline components.
Claim 6
Dependent Claim
25 words
The method of claim 4 wherein a portion of the materials comprising C 3 and C 4 hydrocarbon are catalytically converted to gasoline boiling components.
Claim 7
Dependent Claim
30 words
The method of claim 1 wherein oxygenates retained in the lower boiling phase processed over the crystalline zeolite conversion catalyst are converted to hydrocarbons boiling in the gasoline boiling range.
References Cited (Backward Citations)
US3172842A
Cited
US2740804A
Cited
US2752382A
Cited
US3700585A
Cited
US3729409A
Cited
US3843510A
Cited
US3928483A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1980-09-05 | 1981-03-07 | 1981-09-06 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-09-05 | 1985-03-07 | 1985-09-06 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-09-05 | 1989-03-07 | 1989-09-06 | $7700.00 | Window Closed / Lapsed |