US2656302A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Catalytic desulfurization of petroleum hydrocarbons
Assignee: Anglo Iranian Oil Co Ltd
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Filing: 1950-09-20
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Granted: 1953-10-20
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Expires: 1970-09-20
Abstract
No abstract record available.
Inventors
- 👤 Porter Frederick Willi Bertram
- 👤 Haresnape John Norman
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-27 19:08
CPC Classifications
C; C10; C10G; C10G45/00; C10G45/02; C10G45/24; C10G45/28; C10G45/30; B; B01; B01J; B01J23/00; B01J23/70; B01J23/76; B01J23/84; B01J23/85; B01J23/88; B01J23/882; B01J37/00; B01J37/20
Claims Analysis
Total Claims: 2
Claim 1
Independent Claim
344 words
IN A CONTINOUS PROCESS FOR THE HYDROCATALYTIC DESULPHURIZATION OF A SULPHUR-AND-NAPHTHENE-CONTAINING HYDROCARBON OIL WHEREIN THE OIL IS CONTACTED IN A REACTION ZONE AT AN ELEVATED TEMPERATURE AND PRESSURE IN THE PRESENCE OF HYDROGEN WITH A DEHYDROGENATON-HYDROGENATION CATALYST WHICH HAS EEN PRETREATED WITH HYDROGEN SULPHIDE AND WHICH IS IMMUNE TO SULPHUR POISONING AND COMBINING ACTIVITY FOR THE DEHYDROGENATIN OF NAPHTHENES IN SAID OIL TO AROMATICS WITH ACTIVITY FOR THE HYDROGENATION OF ORGANICALLY COMBINED SULPHUR IN THE OIL TO HYDRO GEN SULPHIDE, THE METHOD OF OPERATING THE PROCESS SO THAT IT WILL BE SELF-SUPPORTING WITH RESPECT TO THE AMOUNT OF HYDROGEN NEEDED AND GIVE INCREASED DEHYDROENATION AND DESULPHURIZATION DURING THE EARLY HOURS ON STREAM AND CONSUME CONSIDERABLY LESS HYDROGEN THAN HEREFORE REQUIRED FOR THE PURPOSE OF PRETREATING THE CATALYST AND PRODUCE A DESULPHURIZED OIL; COMPRISSING THE STEPS OF PASSING THE HYDROCARBON OIL TO BE TREATED THROUGH SAID REACTION ZONE AND CONTACTING THE OIL THEREIN WITH HYDROGEN DERIVED SOLELY FROM THE OIL AND WITH SAID CATALYST WHICH HAS BEEN PRETREATED WITH HYDROGEN SULPHIDE DERIVED SOLELY FROM THE OIL, SAID CONDITIONS OF ELEVATED TEMPERATURE AND PRESSURE BEING SUCH THAT SUFFICIENT HYDROGEN IS PRODUCED BY DEHYDROGENATION OF NAPHTHENE HYDROCARBONS CONTAINED IN THE OIL TO EFFECT THE CONVERSIN OF SULPHUR COMPOUNDS CONTAINED I THE OIL HYDROGEN SULPHIDE AND TO PROVIDE A HYDROGEN-RICH GASEOUS MIXTURE WHICH IS RECYCLED TO THE CATALYTIC DESULPHURIZATION ZONE IN ORDER TO MAINTAIN THE NECESSARY PARTIAL PRESSURE OF HDROGEN THEREIN, PASSING THE DESULPHURIZED OIL TO A GAS SEPARATION STAGE MAINTAINED UNDER THE DESULPHURIZATIN PRESSURE BUT REDUCED TEMPERATURE, SEPARATING A HYDROGEN-RICH GAS MIXTURE, AND LEAVING A LIQUID PRODUCT CONTAINING THE BULK OF THE HYDROGEN-SULPHDE OBTAINED FROM THE REACTION IN SOLUTION, RECYCLING SAID HYDROGEN-RICH GAS MIXTURE TO THE REACTION ZONE TO CONSTITUTE THE WHOLE OF THE HYDROGEN SUPPLIED TO SAID ZONE, PASSING SAID HYDROGEN-SULPHIDE-CONTAINING LUQUID PRODUCT TO A STABILIZING STAGE FOR THE SEPARATION OF A HYDROGEN-SULPHIDE-RICH GAS, SEPARATELY REGENERATING CATALYST FOR USE IN SAID PROCESS, AND PASSING SAID HYDROGEN-SULPHIDE-RICH GAS BACK TO THE REGENERATION SYSTEM FOR TREATING THE CATALYST IN SAID REGENERATION SYSTEM JUST AFTER IT HAS BEEN REGENERATED.
Claim 2
Dependent Claim
344 words
IN A CONTINOUS PROCESS FOR THE HYDROCATALYTIC DESULPHURIZATION OF A SULPHUR-AND-NAPHTHENE-CONTAINING HYDROCARBON OIL WHEREIN THE OIL IS CONTACTED IN A REACTION ZONE AT AN ELEVATED TEMPERATURE AND PRESSURE IN THE PRESENCE OF HYDROGEN WITH A DEHYDROGENATON-HYDROGENATION CATALYST WHICH HAS EEN PRETREATED WITH HYDROGEN SULPHIDE AND WHICH IS IMMUNE TO SULPHUR POISONING AND COMBINING ACTIVITY FOR THE DEHYDROGENATIN OF NAPHTHENES IN SAID OIL TO AROMATICS WITH ACTIVITY FOR THE HYDROGENATION OF ORGANICALLY COMBINED SULPHUR IN THE OIL TO HYDRO GEN SULPHIDE, THE METHOD OF OPERATING THE PROCESS SO THAT IT WILL BE SELF-SUPPORTING WITH RESPECT TO THE AMOUNT OF HYDROGEN NEEDED AND GIVE INCREASED DEHYDROENATION AND DESULPHURIZATION DURING THE EARLY HOURS ON STREAM AND CONSUME CONSIDERABLY LESS HYDROGEN THAN HEREFORE REQUIRED FOR THE PURPOSE OF PRETREATING THE CATALYST AND PRODUCE A DESULPHURIZED OIL; COMPRISSING THE STEPS OF PASSING THE HYDROCARBON OIL TO BE TREATED THROUGH SAID REACTION ZONE AND CONTACTING THE OIL THEREIN WITH HYDROGEN DERIVED SOLELY FROM THE OIL AND WITH SAID CATALYST WHICH HAS BEEN PRETREATED WITH HYDROGEN SULPHIDE DERIVED SOLELY FROM THE OIL, SAID CONDITIONS OF ELEVATED TEMPERATURE AND PRESSURE BEING SUCH THAT SUFFICIENT HYDROGEN IS PRODUCED BY DEHYDROGENATION OF NAPHTHENE HYDROCARBONS CONTAINED IN THE OIL TO EFFECT THE CONVERSIN OF SULPHUR COMPOUNDS CONTAINED I THE OIL HYDROGEN SULPHIDE AND TO PROVIDE A HYDROGEN-RICH GASEOUS MIXTURE WHICH IS RECYCLED TO THE CATALYTIC DESULPHURIZATION ZONE IN ORDER TO MAINTAIN THE NECESSARY PARTIAL PRESSURE OF HDROGEN THEREIN, PASSING THE DESULPHURIZED OIL TO A GAS SEPARATION STAGE MAINTAINED UNDER THE DESULPHURIZATIN PRESSURE BUT REDUCED TEMPERATURE, SEPARATING A HYDROGEN-RICH GAS MIXTURE, AND LEAVING A LIQUID PRODUCT CONTAINING THE BULK OF THE HYDROGEN-SULPHDE OBTAINED FROM THE REACTION IN SOLUTION, RECYCLING SAID HYDROGEN-RICH GAS MIXTURE TO THE REACTION ZONE TO CONSTITUTE THE WHOLE OF THE HYDROGEN SUPPLIED TO SAID ZONE, PASSING SAID HYDROGEN-SULPHIDE-CONTAINING LUQUID PRODUCT TO A STABILIZING STAGE FOR THE SEPARATION OF A HYDROGEN-SULPHIDE-RICH GAS, SEPARATELY REGENERATING CATALYST FOR USE IN SAID PROCESS, AND PASSING SAID HYDROGEN-SULPHIDE-RICH GAS BACK TO THE REGENERATION SYSTEM FOR TREATING THE CATALYST IN SAID REGENERATION SYSTEM JUST AFTER IT HAS BEEN REGENERATED.
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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) | 1956-10-19 | 1957-04-20 | 1957-10-20 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1960-10-19 | 1961-04-20 | 1961-10-20 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1964-10-19 | 1965-04-20 | 1965-10-20 | $7700.00 | Window Closed / Lapsed |