← Back to Patent Explorer
US2920115A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for the production of naphthalene from a petroleum oil

Assignee: Sinclair Refining Co
•
Filing: 1955-09-09
•
Granted: 1960-01-05
•
Expires: 1975-09-09
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

No abstract record available.

Inventors

  • 👤 Bernard S Friedman

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-28 13:09
CPC Classifications
C; C10; C10G; C10G61/00; C10G61/02; C10G61/06

Claims Analysis

Total Claims: 2
Claim 1
Independent Claim 136 words
THE METHOD OR PRODUCING NAPHTHALENE WHICH COMPRISES EXTRACTING WITH A MATERIAL SELECTIVE FOR AROMATICS A LIGHT CATALYTIC CYCLE OIL DERIVED BY CRACKING A PETROLEUM HYDROCABON OIL IN THE PRESENCE OF AN ACIDIC EATALYST, SAID LIGHT CYCLE OIL HAVING A BOILING RANGE WITHIN ABOYT 400* TO 600*F., SAID EXTRACTING BEING UNDER CONDITIONS TO PRODUCE AN AROMATIC RICH EXTRACT OF ND25 OF ABOUT 1.55 TO 1.61 AND A SPECIFIC DISPERSION OF ABOUT 200 TO 270, HYDROCONVERSION OF THE EXTRACTED OIL BY CONTACTING THE EXTRACTED OIL IN THE PRESENCE OF HYDROGEN AND A HYDROFORMING CATALYST HAVING A NON-COMBUSTIBLE BASE AT REACTION CONDITIONS OF SEVERITY DEFINED BY TEMPERATURE AND SPACE VELOCITY OF FORM ABOUT 1050* TO 1150*F. AT 0.5 LHSV AND AT A PRESSURE OF AT LEAST ABOUT ATMOSPHERIC TO FORM NAPHTHALENE, AND SEPARATING THE NAPTHALENE FROM THE HYDROCONVERSION PRODUCT.
Claim 2
Independent Claim 136 words
THE METHOD OR PRODUCING NAPHTHALENE WHICH COMPRISES EXTRACTING WITH A MATERIAL SELECTIVE FOR AROMATICS A LIGHT CATALYTIC CYCLE OIL DERIVED BY CRACKING A PETROLEUM HYDROCABON OIL IN THE PRESENCE OF AN ACIDIC EATALYST, SAID LIGHT CYCLE OIL HAVING A BOILING RANGE WITHIN ABOYT 400* TO 600*F., SAID EXTRACTING BEING UNDER CONDITIONS TO PRODUCE AN AROMATIC RICH EXTRACT OF ND25 OF ABOUT 1.55 TO 1.61 AND A SPECIFIC DISPERSION OF ABOUT 200 TO 270, HYDROCONVERSION OF THE EXTRACTED OIL BY CONTACTING THE EXTRACTED OIL IN THE PRESENCE OF HYDROGEN AND A HYDROFORMING CATALYST HAVING A NON-COMBUSTIBLE BASE AT REACTION CONDITIONS OF SEVERITY DEFINED BY TEMPERATURE AND SPACE VELOCITY OF FORM ABOUT 1050* TO 1150*F. AT 0.5 LHSV AND AT A PRESSURE OF AT LEAST ABOUT ATMOSPHERIC TO FORM NAPHTHALENE, AND SEPARATING THE NAPTHALENE FROM THE HYDROCONVERSION PRODUCT.

References Cited (Backward Citations)

US2304289A Cited
US2547221A Cited
US2686818A Cited
US2700638A Cited
US2727854A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1963-01-04 1963-07-06 1964-01-05 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1967-01-04 1967-07-06 1968-01-05 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1971-01-04 1971-07-06 1972-01-05 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag