← Back to Patent Explorer
US2906676A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for purifying crude acetone

Assignee: Hercules Powder Co
•
Filing: 1957-01-23
•
Granted: 1959-09-29
•
Expires: 1977-01-23
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

No abstract record available.

Inventors

  • 👤 Bewley Thomas
  • 👤 Cooke Maurice Dudley

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-01 17:11
CPC Classifications
C; C07; C07C; C07C45/00; C07C45/78; C07C45/81; C07C45/82

Claims Analysis

Total Claims: 2
Claim 1
Independent Claim 177 words
THE PROCESS FOR THE PURIFICATION OF THE CRUDE ACETONE OBTAINED BY THE DECOMPOSITION OF CUMENE HYDROPEROXIDE AND CONTAINING ALDEHYDES, ESTER, ACETALS, MESITYL OXIDE AND SULPHUR COMPOUNDS AS IMPURITIES WHICH COMPRISES CONTINUOUSLY INTRODUCING SAID ACETONE AT A RATE IN THE RANGE OF ABOUT 5 TO ABOUT 10 GALLONS PER MINUTE INTO AN ALDEHYDIC STRIPPING COLUMN WHEREIN THE MAJOR PART OF THE ALDEHYDIC IMPURITIES IS REMOVED, ALSO CONTINUOUSLY INTRODUCING INTO SAID COLUMN AN AQUEOUS SOLUTION OF ABOUT 5 TO ABOUT 25% CONCENTRATION OF AN ALKALI METAL HYDROXIDE SELECTED FROM THE GROUP CONSISTING OF SODIUM HYDROXIDE AND POTASSIUM HYDROXIDE, THE AQUEOUS HYDROXIDE SOLUTION BEING INTRODUCED AT A RATE VARYING BETWEEN ABOUT 5 GALLONS PER HOUR WHEN THE CONCENTRATION IS ABOUT 5% AND ABOUT 1 GALLON PER HOUR WHEN THE CONCENTRATION IS ABOUT 25%, CONTINUOUSLY WITHDRAWING FROM THE BASE OF SAID COLUMN A MIXTURE OF CRUDE ACETONE AND ALKALI METAL HYDROXIDE SOLUTION, CONTINUOUSLY FEEDING SAID MIXTURE INTO A FRACTIONAL DISTILLATION COLUMN AT AN INTERMEDIATE POINT IN SAID COLUMN, AND REMOVING PURE ACETONE AS AN OVERHEAD STREAM FROM SAID FRACTIONAL DISTILLATION COLUMN.
Claim 2
Dependent Claim 177 words
THE PROCESS FOR THE PURIFICATION OF THE CRUDE ACETONE OBTAINED BY THE DECOMPOSITION OF CUMENE HYDROPEROXIDE AND CONTAINING ALDEHYDES, ESTER, ACETALS, MESITYL OXIDE AND SULPHUR COMPOUNDS AS IMPURITIES WHICH COMPRISES CONTINUOUSLY INTRODUCING SAID ACETONE AT A RATE IN THE RANGE OF ABOUT 5 TO ABOUT 10 GALLONS PER MINUTE INTO AN ALDEHYDIC STRIPPING COLUMN WHEREIN THE MAJOR PART OF THE ALDEHYDIC IMPURITIES IS REMOVED, ALSO CONTINUOUSLY INTRODUCING INTO SAID COLUMN AN AQUEOUS SOLUTION OF ABOUT 5 TO ABOUT 25% CONCENTRATION OF AN ALKALI METAL HYDROXIDE SELECTED FROM THE GROUP CONSISTING OF SODIUM HYDROXIDE AND POTASSIUM HYDROXIDE, THE AQUEOUS HYDROXIDE SOLUTION BEING INTRODUCED AT A RATE VARYING BETWEEN ABOUT 5 GALLONS PER HOUR WHEN THE CONCENTRATION IS ABOUT 5% AND ABOUT 1 GALLON PER HOUR WHEN THE CONCENTRATION IS ABOUT 25%, CONTINUOUSLY WITHDRAWING FROM THE BASE OF SAID COLUMN A MIXTURE OF CRUDE ACETONE AND ALKALI METAL HYDROXIDE SOLUTION, CONTINUOUSLY FEEDING SAID MIXTURE INTO A FRACTIONAL DISTILLATION COLUMN AT AN INTERMEDIATE POINT IN SAID COLUMN, AND REMOVING PURE ACETONE AS AN OVERHEAD STREAM FROM SAID FRACTIONAL DISTILLATION COLUMN.

References Cited (Backward Citations)

US2662848A Cited
US2555185A Cited
US2624699A Cited
US2737480A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1962-09-28 1963-03-30 1963-09-29 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1966-09-28 1967-03-30 1967-09-29 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1970-09-28 1971-03-30 1971-09-29 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag