Patent US3239453A successfully refreshed from Google Patents.
US3239453A
Expired / Lapsed
US
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Selective hydrogenation of hydrocarbons
Assignee: ExxonMobil Oil Corp
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Filing: 1962-11-19
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Granted: 1966-03-08
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Expires: 1982-11-19
Abstract
No abstract record available.
Inventors
- 👤 Raymond R Halik
- 👤 Fritz A Smith
- 👤 Carl W Streed
- 👤 Richard G Graven
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-27 13:23
CPC Classifications
C; C10; C10G; C10G65/00; C10G65/02; C10G65/04; C10G65/06; Y; Y10; Y10S; Y10S585/00; Y10S585/949; Y10S585/956
Claims Analysis
Total Claims: 2
Claim 1
Independent Claim
294 words
A PROCESS FOR THE SELECTIVE NONDESTRUCTIVE HYDROGENATION OF A LIQUID HYDROCARBON FEED BOILING BELOW ABOUT 500*F. AND CONTAINING AROMATIC HYDROCARBONS, OLEFINS, DIOLEFINS AND SULFUR COMPOUNDS WHICH COMPRISES PASSING SAID FEED SUBSTANTIALLY IN THE LIQUID PHASE AND HYDROGEN THROUGH AN INITIAL HYDROGENATION ZONE IN CONTACT WITH A POROUS SOLID HYDROGENATION CATALYST OFHIGH HYDROGENATION ACTIVITY AND LOW POLYMERIZATION ACTIVITY WHILE CONTROLLING HYDROGENATING CONDITIONS INAID ZONE INCLUDING HYDROGEN PARTIAL PRESSURE WITHIN THE RANGE OF ABOUT 200-800 P.S.I.A., HOURLY SPACE VELOCITY WITHIN THE RANGE OF ABOUT 0.2-15.0 BASED ON THE VOLUME OF LIQUID FEED, THE HYDROGEN CHARGE WITHINTHE RANGE OF ABOUT 5005000 S.C.F./B. OF LIQUID FEED AND FEED TEMPERATURE WITHIN THE BROAD RANGE OF ABOUT 75-300*F., SAID HYDROGENATING CONDITIONS BEING REGULATED TO PROVIDE A HYDROGENATION EFFLUENT FROM SAID ZONE IN WHICH AT LEAST ABOUT 35% OF THE DIOLEFINS HAVE BEEN AT LEAST PARTIALLY SATURATED AND IN WHICH A SUBSTANTIAL AMOUNT OF SAID EFFLUENT IS IN THE LIQUID PHASE,EFFECTING CONTROLED VAPORIZATION OF A PORTION OF THE LIQUID PHASE OF SAID HYDROGENATION EFFLUENT, PASSING HYDROGEN TOGETHER WITH GASEOUS MATERIAL DERIVED FROM VAPORIZATION STEP THROUGH A SUBSEQUENT CONVERSION ZONE IN CONTACT WITH A POROUS SOLID CONVERSION CATALYST OF AT LEAST MODERATE HYDROGENATION ACTIVITY AND HIGH DESULFURIZATION ACTIVITY AT A SUBSTANTIALLY HIGHER AVERAGE TEMPERATURE THAN IN SAID INITIAL ZONE WHILE CONTROLLING CONVERSION CONDITIONS IN SAID CONVERSION ZONE INCLUDING HYDROGEN PARTIAL PRESSURE WITHIN THE RANGE OF ABOUT 200-800 P.S.I.A., HOURLY SPACE VELOCITY WITHIN THE RANGE OF ABOUT 0.2-6.0 BASED ON THE VOLUME OF SAID LIQUID FEED, THE TOTAL HYDROGEN CHARGE WITHIN THE RANGE OF ABOUT 50010,000 S.C.F./B. OF SAID LIQUID FEED AND INLET TEMPERATURE WITHIN THE WIDE RANGE OF ABOUT 350-700*F., SAID CONVERSION CONDITIONS BEING REGULATED TO PRODUCE A SUBSTANTIALLY DESULFURIZED CONVERSION EFFLUENT HAVING A SUBSTANTIALLY LOWER BROMINE NUMBER THAN SAID LIQUID FEED.
Claim 2
Dependent Claim
294 words
A PROCESS FOR THE SELECTIVE NONDESTRUCTIVE HYDROGENATION OF A LIQUID HYDROCARBON FEED BOILING BELOW ABOUT 500*F. AND CONTAINING AROMATIC HYDROCARBONS, OLEFINS, DIOLEFINS AND SULFUR COMPOUNDS WHICH COMPRISES PASSING SAID FEED SUBSTANTIALLY IN THE LIQUID PHASE AND HYDROGEN THROUGH AN INITIAL HYDROGENATION ZONE IN CONTACT WITH A POROUS SOLID HYDROGENATION CATALYST OFHIGH HYDROGENATION ACTIVITY AND LOW POLYMERIZATION ACTIVITY WHILE CONTROLLING HYDROGENATING CONDITIONS INAID ZONE INCLUDING HYDROGEN PARTIAL PRESSURE WITHIN THE RANGE OF ABOUT 200-800 P.S.I.A., HOURLY SPACE VELOCITY WITHIN THE RANGE OF ABOUT 0.2-15.0 BASED ON THE VOLUME OF LIQUID FEED, THE HYDROGEN CHARGE WITHINTHE RANGE OF ABOUT 5005000 S.C.F./B. OF LIQUID FEED AND FEED TEMPERATURE WITHIN THE BROAD RANGE OF ABOUT 75-300*F., SAID HYDROGENATING CONDITIONS BEING REGULATED TO PROVIDE A HYDROGENATION EFFLUENT FROM SAID ZONE IN WHICH AT LEAST ABOUT 35% OF THE DIOLEFINS HAVE BEEN AT LEAST PARTIALLY SATURATED AND IN WHICH A SUBSTANTIAL AMOUNT OF SAID EFFLUENT IS IN THE LIQUID PHASE,EFFECTING CONTROLED VAPORIZATION OF A PORTION OF THE LIQUID PHASE OF SAID HYDROGENATION EFFLUENT, PASSING HYDROGEN TOGETHER WITH GASEOUS MATERIAL DERIVED FROM VAPORIZATION STEP THROUGH A SUBSEQUENT CONVERSION ZONE IN CONTACT WITH A POROUS SOLID CONVERSION CATALYST OF AT LEAST MODERATE HYDROGENATION ACTIVITY AND HIGH DESULFURIZATION ACTIVITY AT A SUBSTANTIALLY HIGHER AVERAGE TEMPERATURE THAN IN SAID INITIAL ZONE WHILE CONTROLLING CONVERSION CONDITIONS IN SAID CONVERSION ZONE INCLUDING HYDROGEN PARTIAL PRESSURE WITHIN THE RANGE OF ABOUT 200-800 P.S.I.A., HOURLY SPACE VELOCITY WITHIN THE RANGE OF ABOUT 0.2-6.0 BASED ON THE VOLUME OF SAID LIQUID FEED, THE TOTAL HYDROGEN CHARGE WITHIN THE RANGE OF ABOUT 50010,000 S.C.F./B. OF SAID LIQUID FEED AND INLET TEMPERATURE WITHIN THE WIDE RANGE OF ABOUT 350-700*F., SAID CONVERSION CONDITIONS BEING REGULATED TO PRODUCE A SUBSTANTIALLY DESULFURIZED CONVERSION EFFLUENT HAVING A SUBSTANTIALLY LOWER BROMINE NUMBER THAN SAID LIQUID FEED.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1969-03-07 | 1969-09-06 | 1970-03-08 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1973-03-07 | 1973-09-06 | 1974-03-08 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1977-03-07 | 1977-09-06 | 1978-03-08 | $7700.00 | Window Closed / Lapsed |