← Back to Patent Explorer
US2789134A Expired / Lapsed US ⏱️ 0.0 years remaining

Recovery of naphthenic acids

Assignee: ExxonMobil Technology and Engineering Co
•
Filing: 1953-06-19
•
Granted: 1957-04-16
•
Expires: 1973-06-19
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

No abstract record available.

Inventors

  • 👤 Joseph F Nelson
  • 👤 James H Mcateer

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-27 10:43
CPC Classifications
C; C10; C10G; C10G19/00; C10G19/02; C07; C07C; C07C51/00; C07C51/42; C07C51/48; C10G17/00; C10G17/02; C10G17/04

Claims Analysis

Total Claims: 2
Claim 1
Independent Claim 174 words
A CONTINUOUS PROCESS FOR RECOVERING NAPHTHENIC ACIDS FROM A NAPHTHENIC ACID-CONTAINING PETROLEUM DIESEL OIL DISTILLATE FRACTION HAVING AN END POINT OF ABOUT 625* F. WHICH COMPRISES THE STEPS OF EXTRACTING THE DIESEL OIL FRACTION WITH AN AQUEOUS SOLUTION OF A SODIUM SALT SELECTED FROM THE GROUP CONSISTING OF SOLIUM CARBONATE, SODIUM BICARBONATE, AND THEIR MIXTURES; SEPARATING THE RESULTING MIXTURE INTO AN ORGANIC PHASE AND AN AQUEOUS SODIUM NAPHTHENATE-CONTAINING PHASES; SEPARATING THE AQUEOUS PHASE FROM THE ORGANIC PHASE; CONTACTING THE SEPARATED AQUEOUS PHASES WITH CARBON DIOXIDE AT A PRESSURE IN EXCESS OF 100 P.S.I.G. IN A PRESSURE ZONE TO CONVERT THE NAPHTHENATES TO NAPHTHENIC ACIDS; SEPARATING THIS RESULTING MIXTURE AT THE AFORESAID CARBON DIOXIDE PRESSURE INTO AN AQUEOUS PHASE CONTAINING DISSOLVED SODIUM BICARBONATE AND A NAPHTHENIC ACID ORGANIC PHASE; CONVERTING THE AQUEOUS SODIUM BICARBONATE TO AQUEOUS SODIUM CARBONATE AND CARBON DIOXIDE; RECYCLING THE LIBERATED CARBON DIOXIDE TO THE AFOREMENTIONED PRESSURE ZONE; RECYLING THE AQUEOUS SODIUM CARBONATE PHASE TO THE EXTRACTION STEP; AND FREEING THE NAPHTHENIC ACIDS OF CARBON DIOXIDE TO OBTAIN THE NAPHTHENIC ACID PRODUCT.
Claim 2
Dependent Claim 174 words
A CONTINUOUS PROCESS FOR RECOVERING NAPHTHENIC ACIDS FROM A NAPHTHENIC ACID-CONTAINING PETROLEUM DIESEL OIL DISTILLATE FRACTION HAVING AN END POINT OF ABOUT 625* F. WHICH COMPRISES THE STEPS OF EXTRACTING THE DIESEL OIL FRACTION WITH AN AQUEOUS SOLUTION OF A SODIUM SALT SELECTED FROM THE GROUP CONSISTING OF SOLIUM CARBONATE, SODIUM BICARBONATE, AND THEIR MIXTURES; SEPARATING THE RESULTING MIXTURE INTO AN ORGANIC PHASE AND AN AQUEOUS SODIUM NAPHTHENATE-CONTAINING PHASES; SEPARATING THE AQUEOUS PHASE FROM THE ORGANIC PHASE; CONTACTING THE SEPARATED AQUEOUS PHASES WITH CARBON DIOXIDE AT A PRESSURE IN EXCESS OF 100 P.S.I.G. IN A PRESSURE ZONE TO CONVERT THE NAPHTHENATES TO NAPHTHENIC ACIDS; SEPARATING THIS RESULTING MIXTURE AT THE AFORESAID CARBON DIOXIDE PRESSURE INTO AN AQUEOUS PHASE CONTAINING DISSOLVED SODIUM BICARBONATE AND A NAPHTHENIC ACID ORGANIC PHASE; CONVERTING THE AQUEOUS SODIUM BICARBONATE TO AQUEOUS SODIUM CARBONATE AND CARBON DIOXIDE; RECYCLING THE LIBERATED CARBON DIOXIDE TO THE AFOREMENTIONED PRESSURE ZONE; RECYLING THE AQUEOUS SODIUM CARBONATE PHASE TO THE EXTRACTION STEP; AND FREEING THE NAPHTHENIC ACIDS OF CARBON DIOXIDE TO OBTAIN THE NAPHTHENIC ACID PRODUCT.

References Cited (Backward Citations)

DE341654C Cited
US2581139A Cited
US2424158A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1960-04-15 1960-10-15 1961-04-16 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1964-04-15 1964-10-15 1965-04-16 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1968-04-15 1968-10-15 1969-04-16 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag