Patent US4049741A successfully refreshed from Google Patents.
US4049741A
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Method for upgrading Fischer-Tropsch synthesis products
Assignee: Mobil Oil AS
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Filing: 1975-09-18
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Granted: 1977-09-20
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Expires: 1995-09-18
Abstract
Abstract The products of Fischer-Tropsch synthesis boiling below a separated decant oil fraction are subjected to cooling to a temperature of about 100 DEG F and separation of the cooled product to recover Fischer-Tropsch produced water comprising oxygenates, a normally liquid hydrocarbon phase comprising absorbed oxygenates and a gaseous phase normally comprising a substantial amount of C5 hydrocarbons in combination with lower boiling materials including unreacted synthesis gas and carbon dioxide. Each of said gaseous phase and said normally liquid hydrocarbon phase are thereafter contacted with a selected crystalline zeolite catalyst particularly selective for the formation of gasoline boiling material of high octane.
Inventors
- 👤 James C. Kuo
- 👤 Charles D. Prater
- 👤 John J. Wise
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-02 10:30
CPC Classifications
C; C10; C10G; C10G35/00; C10G35/04; C10G35/06; C10G35/095; C10G3/00; C10G3/42; C10G3/44; C10G3/48; C10G3/49; C10G50/00; C10L; C10L1/00; C10L1/04; C10L1/06; C10G2300/00; C10G2300/10; C10G2300/1022; C10G2300/20; C10G2300/30; C10G2300/301; C10G2400/00; C10G2400/02; Y; Y02; Y02P; Y02P30/00; Y02P30/20; Y10; Y10S; Y10S208/00; Y10S208/95; Y10S585/00; Y10S585/929; Y10S585/943
Claims Analysis
Total Claims: 7
Claim 1
Independent Claim
291 words
A method for upgrading products of Fischer-Tropsch synthesis which comprises, separating the product effluent of Fischer-Tropsch after cooling to recover a synthetic water phase comprising oxygenates, a normally liquid hydrocarbon light oil phase boiling below about 560° F. comprising oxygenates and a normally gaseous phase rich in C 5 hydrocarbons in combination with lower boiling gaseous materials, passing the normally liquid hydrocarbon light oil phase boiling below about 560° F without further water washing in contact with a selective crystalline aluminosilicate zeolite that has a pore diameter greater than about 5 Angstroms; a silica-to-alumina ratio of at least 12; a constraint index within the range of 1 to 12; under conversion conditions selected to increase the octane rating of a gasoline product separated therefrom in combination with gaseous components suitable for alkylation, passing the products obtained from said normally liquid hydrocarbon light oil conversion operation to product separation, passing the total synthesis gaseous phase rich in C 5 hydrocarbons and comprising a mixture of carbon monoxide, methane, paraffins, olefins and oxygenates in contact with a selective crystalline aluminosilicate zeolite that has a pore diameter greater than about 5 Angstrom units; a silica-to-alumina ratio of at least 12; and a constraint index within the range of 1 to 12 under conversion conditions selected for upgrading hydrocarbon components of said gaseous phase to gasoline boiling compounds and gaseous hydrocarbons suitable for alkylation, passing the products obtained from said gaseous phase conversion operation to product separation, separating the products of said catalytic conversion operations to recover gasoline boiling product of improved octane rating, a light fuel oil product higher boiling than said gasoline fraction, a C 3 -C 4 net fraction suitable for alkylation and a stream comprising C 2 and lower boiling hydrocarbons.
Claim 2
Independent Claim
291 words
A method for upgrading products of Fischer-Tropsch synthesis which comprises, separating the product effluent of Fischer-Tropsch after cooling to recover a synthetic water phase comprising oxygenates, a normally liquid hydrocarbon light oil phase boiling below about 560° F. comprising oxygenates and a normally gaseous phase rich in C 5 hydrocarbons in combination with lower boiling gaseous materials, passing the normally liquid hydrocarbon light oil phase boiling below about 560° F without further water washing in contact with a selective crystalline aluminosilicate zeolite that has a pore diameter greater than about 5 Angstroms; a silica-to-alumina ratio of at least 12; a constraint index within the range of 1 to 12; under conversion conditions selected to increase the octane rating of a gasoline product separated therefrom in combination with gaseous components suitable for alkylation, passing the products obtained from said normally liquid hydrocarbon light oil conversion operation to product separation, passing the total synthesis gaseous phase rich in C 5 hydrocarbons and comprising a mixture of carbon monoxide, methane, paraffins, olefins and oxygenates in contact with a selective crystalline aluminosilicate zeolite that has a pore diameter greater than about 5 Angstrom units; a silica-to-alumina ratio of at least 12; and a constraint index within the range of 1 to 12 under conversion conditions selected for upgrading hydrocarbon components of said gaseous phase to gasoline boiling compounds and gaseous hydrocarbons suitable for alkylation, passing the products obtained from said gaseous phase conversion operation to product separation, separating the products of said catalytic conversion operations to recover gasoline boiling product of improved octane rating, a light fuel oil product higher boiling than said gasoline fraction, a C 3 -C 4 net fraction suitable for alkylation and a stream comprising C 2 and lower boiling hydrocarbons.
Claim 3
Dependent Claim
35 words
The method of claim 1 wherein oxygenates in the water phase are recovered to separate lower alcohols therefrom and separated lower alcohols are passed in contact with said special crystalline zeolite catalyst to form aromatics.
Claim 4
Dependent Claim
29 words
The method of claim 1 wherein a product shown rich in C 3 -C 4 hydrocarbons is passed to either one or both of said crystalline zeolite conversion operations.
Claim 5
Dependent Claim
25 words
The method of claim 1 wherein oxygenates retained in the light oil phase are converted to hydrocarbons during contact with said crystalline zeolite conversion catalyst.
Claim 6
Dependent Claim
36 words
The method of claim 1 wherein C 5 minus gaseous material separated from the synthesis product effluent is recombined with the light oil phase and processed as a combined stream over said crystalline zeolite conversion catalyst.
Claim 7
Dependent Claim
33 words
The method of claim 1 wherein the light oil phase separated from the cooling zone is heated to a temperature above 500° F. before passing in contact with said crystalline zeolite conversion catalyst.
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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) | 1980-09-19 | 1981-03-21 | 1981-09-20 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-09-19 | 1985-03-21 | 1985-09-20 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-09-19 | 1989-03-21 | 1989-09-20 | $7700.00 | Window Closed / Lapsed |