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US2965561A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for upgrading desulfurized naphthas

Assignee: Pure Oil Co
•
Filing: 1956-12-24
•
Granted: 1960-12-20
•
Expires: 1976-12-24
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Abstract

No abstract record available.

Inventors

  • 👤 Norman L Carr
  • 👤 Oral L Beber

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 14:15
CPC Classifications
C; C10; C10G; C10G61/00; C10G61/02; C10G61/06

Claims Analysis

Total Claims: 2
Claim 1
Independent Claim 302 words
A PROCESS FOR PRODUCING A GASOLINE MOTOR FUEL HAVING ENHANCED ROAD PERFORMANCE CHARACTERISTICS WHICH COMPRISES FRACTIONATING A DESULFURIZED, VIRGIN PETROLEUM NAPHTHA BOILING BETWEEN ABOUT 90* AND 400*F. INTO A LOW-BOILING FRACTION CONSISTING ESSENTIALLY OF N-C7 AND LOWER-BOILING HYDROCARBONS PRESENT IN SAID NAPHTHA, AND A CONSECUTIVE HIGH-BOILING FRACTION CONTAINING SUBSTANTIALLY ALL THE HYDROCARBONS PRESENT IN SAID NAPHTHA HAVING A BOILING POINT HIGHER THAN N-C7, SEPARATING THE NORMAL HYDROCARBON CONSTITUENTS FROM THE BRANCHED CHAIN, HYDROCARBON CONSTITUENTS OF SAID LOW-BOILING FRACTION, ISOMERIZING SAID NORMAL HYDROCARBON CONSTITUENTS IN AN ISOMERIZATION ZONE IN THE PRESENCE OF HYDROGEN AND A COMPOSITE CATALYST PREPARED BY IMPREGNATING A REFRACTORY, ACIDIC, MIXED OXIDES BASE WITH A HYDROGENATION AGENT, AND PRECONDITIONED BY REDUCTION, FOLLOWED BY OXIDATION AT 650*-750*F., AND REDUCTION WITH HYDROGEN AT 650*-750* F., EMPLOYING THE FOLLOWING REACTION CONDITIONS: TO PRODUCE AN ISOMERIZATION EFFLUENT RICH IN BRANCHEDCHAIN, SATURATED HYDROCARBONS, AND RECOVERING THE BRANCHED-CHAIN HYDROCARBONS FROM SAID ISOMERIZATION EFFLUENT, CATALYTICALLY REFORMING SAID HIGH-BOILING FRACTION IN A REFORMING ZONE IN THE PRESENCE OF HYDROGEN AND A CATALYST CONSISTING ESSENTIALLY OF A NOBLE METAL SELECTED FROM THE GROUP CONSISTING OF PLATINUM AND PALLADIUM SUPPORTED ON A SUITABLE CARRIER AT A TEMPERATURE OF 900*-920* F., UNDER REFORMING CONDITIONS TO PRODUCE A REFORMED REACTION EFFLUENT, SOLVENT EXTRACTING SAID REFORMED EFFLUENT TO PRODUCE A PARAFFINIC FRACTION AND AN AROMATIC FRACTION, FRACTIONATING SAID PARAFFINIC FRACTION TO PRODUCE A DISTILLATE FRACTION CONSISTING ESSENTIALLY OF N-C7 AND LOWER-BOILING HYDROCARBONS AND RESIDUAL FRACTION CONTAINING HYDROCARBONS BOILING ABOVE N-C7, RECYCLING SAID RESIDUAL FRACTION TO SAID REFORMING ZONE, FRACTIONATING SAID DISTILLATE FRACTION TO SEPARATE THE NORMAL HYDROCABON CONSTITUENTS THEREOF FOR TREATMENT IN SAID ISOMERIZATION ZONE, AND RECOVERING THE BRANCHED-CHAIN HYDROCARBONS CONSTITUENTS FROM SAID DISTILLATE FRACTION, AND BLENDING SAID BRANCHEDCHAIN HYDROCARBON CONSTITUENTS FROM SAID LOW-BOILING FRACTION, SAID ISOMERIZATION EFFLUENT, AND SAID DISTILLATE FRACTION WITH SAID AROMATIVE FRACTION TO PRODUCE A HIGH OCTANE NUMBER GASOLINE.
Claim 2
Dependent Claim 302 words
A PROCESS FOR PRODUCING A GASOLINE MOTOR FUEL HAVING ENHANCED ROAD PERFORMANCE CHARACTERISTICS WHICH COMPRISES FRACTIONATING A DESULFURIZED, VIRGIN PETROLEUM NAPHTHA BOILING BETWEEN ABOUT 90* AND 400*F. INTO A LOW-BOILING FRACTION CONSISTING ESSENTIALLY OF N-C7 AND LOWER-BOILING HYDROCARBONS PRESENT IN SAID NAPHTHA, AND A CONSECUTIVE HIGH-BOILING FRACTION CONTAINING SUBSTANTIALLY ALL THE HYDROCARBONS PRESENT IN SAID NAPHTHA HAVING A BOILING POINT HIGHER THAN N-C7, SEPARATING THE NORMAL HYDROCARBON CONSTITUENTS FROM THE BRANCHED CHAIN, HYDROCARBON CONSTITUENTS OF SAID LOW-BOILING FRACTION, ISOMERIZING SAID NORMAL HYDROCARBON CONSTITUENTS IN AN ISOMERIZATION ZONE IN THE PRESENCE OF HYDROGEN AND A COMPOSITE CATALYST PREPARED BY IMPREGNATING A REFRACTORY, ACIDIC, MIXED OXIDES BASE WITH A HYDROGENATION AGENT, AND PRECONDITIONED BY REDUCTION, FOLLOWED BY OXIDATION AT 650*-750*F., AND REDUCTION WITH HYDROGEN AT 650*-750* F., EMPLOYING THE FOLLOWING REACTION CONDITIONS: TO PRODUCE AN ISOMERIZATION EFFLUENT RICH IN BRANCHEDCHAIN, SATURATED HYDROCARBONS, AND RECOVERING THE BRANCHED-CHAIN HYDROCARBONS FROM SAID ISOMERIZATION EFFLUENT, CATALYTICALLY REFORMING SAID HIGH-BOILING FRACTION IN A REFORMING ZONE IN THE PRESENCE OF HYDROGEN AND A CATALYST CONSISTING ESSENTIALLY OF A NOBLE METAL SELECTED FROM THE GROUP CONSISTING OF PLATINUM AND PALLADIUM SUPPORTED ON A SUITABLE CARRIER AT A TEMPERATURE OF 900*-920* F., UNDER REFORMING CONDITIONS TO PRODUCE A REFORMED REACTION EFFLUENT, SOLVENT EXTRACTING SAID REFORMED EFFLUENT TO PRODUCE A PARAFFINIC FRACTION AND AN AROMATIC FRACTION, FRACTIONATING SAID PARAFFINIC FRACTION TO PRODUCE A DISTILLATE FRACTION CONSISTING ESSENTIALLY OF N-C7 AND LOWER-BOILING HYDROCARBONS AND RESIDUAL FRACTION CONTAINING HYDROCARBONS BOILING ABOVE N-C7, RECYCLING SAID RESIDUAL FRACTION TO SAID REFORMING ZONE, FRACTIONATING SAID DISTILLATE FRACTION TO SEPARATE THE NORMAL HYDROCABON CONSTITUENTS THEREOF FOR TREATMENT IN SAID ISOMERIZATION ZONE, AND RECOVERING THE BRANCHED-CHAIN HYDROCARBONS CONSTITUENTS FROM SAID DISTILLATE FRACTION, AND BLENDING SAID BRANCHEDCHAIN HYDROCARBON CONSTITUENTS FROM SAID LOW-BOILING FRACTION, SAID ISOMERIZATION EFFLUENT, AND SAID DISTILLATE FRACTION WITH SAID AROMATIVE FRACTION TO PRODUCE A HIGH OCTANE NUMBER GASOLINE.

References Cited (Backward Citations)

CA487392A Cited
US2443607A Cited
US2650906A Cited
US2691623A Cited
US2697684A Cited
US2718535A Cited
US2762854A Cited
US2687307A Cited
US2799627A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1963-12-20 1964-06-20 1964-12-20 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1967-12-20 1968-06-20 1968-12-20 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1971-12-20 1972-06-20 1972-12-20 $7700.00 Window Closed / Lapsed

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