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US2676903A Expired / Lapsed US ⏱️ 0.0 years remaining

Fractional liquid extraction of vitamins

Assignee: F Hoffmann La Roche AG
•
Filing: 1950-02-15
•
Granted: 1954-04-27
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Expires: 1970-02-15
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Abstract

No abstract record available.

Inventors

  • 👤 Scheibel Edward George
  • 👤 Andrew E Karr

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-30 14:48
CPC Classifications
A; A61; A61K; A61K31/00; A61K31/59

Claims Analysis

Total Claims: 2
Claim 1
Independent Claim 283 words
A PROCESS FOR PURIFYING A MIXTURE OF A VITAMIN A ACTIVE MATERIAL SELECTED FROM THE GROUP CONSISTING OF VITAMIN A ALCOHOL AND ITS ESTERS AND NON-ACTIVE IMPURITIES ASSOCIATED THEREWITH WHICH COMPRISES (1) CONTACTING SAID MIXTURE IN A FIRST MULTI-STAGE EXTRACTION ZONE WITH TWO SUBSTANTIALLY IMMISCIBLE COUNTERCURRENTLY FLOWING LIQUID ORGANIC SOLVENTS WHICH HAVE DIFFERENT SPECIFIC GRAVITIES AND BETWEEN WHICH THE VITAMIN A ACTIVE MATERIAL AND THE NON-ACTIVE IMPURITIES HAVE DIFFERENT DISTRIBUTION COEFFICIENTS, SAID MIXTURE BEING INTRODUCED INTO THE SOLVENT STREAMS AT A POINT APPROXIMATELY MIDWAY BETWEEN THE POINTS OF INTRODUCTION OF TWO SOLVENTS, THE EXTRACTION FACTOR OF SAID VITAMIN A ACTIVE MATERIAL WITH RESPECT TO SAID SOLVENT PAIR IN SAID FIRST EXTRACTION ZONE BEING LESS THAN ONE; (2) WITHDRAWING A FIRST EXTRACT STREAM COMPRISING VITAMIN A ACTIVE MATERIAL IN THE HEAVY SOLVENT AND SEPARATELY WITHDRAWING A SECOND EXTRACT STREAM COMPRISING THE LIGHT SOLVENT AND IMPURITIES; (3) SEPARATING THE HEAVY SOLVENT FROM THE FIRST EXTRACT STREAM TO OBTAIN A FIRST VITAMIN A CONCENTRATE; (4) CONTACTING SAID CONCENTRATE IN A SECOND MULTI-STAGE EXTRACTION ZONE WITH THE SAME TWO SOLVENTS IN COUNTERCURRENT FLOW, SAID CONCENTRATE BEING INTRODUCED INTO THE SOVENT STREAMS AT A POINT APPROXIMATELY MIDWAY BETWEEN THE POINTS OF INTRODUCTION OF THE TWO SOLVENTS, THE EXTRACTION FACTOR OF THE VITAMIN A ACTIVE MATERIAL WITH RESPECT TO THE SOLVENT PAIR IN THE SECOND EXTRACTION ZONE BEING GREATER THAN ONE; (5) WITHDRAWING A THIRD EXTRACT STREAM WHICH COMPRISES VITAMIN A ACTIVE, MATERIAL STREAM WHICH COMPRISES AND A SEPARATE EXTRACT STREAM WHICH COMPRISES THE SAID HEAVY SOLVENT AND IMPURITIES; (6) SEPARATING THE LIGHT SOLVENT FROM SAID THIRD EXTRACT STREAM TO OBTAIN A VITAMIN A CONCENTRATE HAVING A GREATER PERCENTAGE CONTENT OF VITAMIN A ACTIVE MATERIAL THAN THE ORIGINAL FEED.
Claim 2
Dependent Claim 283 words
A PROCESS FOR PURIFYING A MIXTURE OF A VITAMIN A ACTIVE MATERIAL SELECTED FROM THE GROUP CONSISTING OF VITAMIN A ALCOHOL AND ITS ESTERS AND NON-ACTIVE IMPURITIES ASSOCIATED THEREWITH WHICH COMPRISES (1) CONTACTING SAID MIXTURE IN A FIRST MULTI-STAGE EXTRACTION ZONE WITH TWO SUBSTANTIALLY IMMISCIBLE COUNTERCURRENTLY FLOWING LIQUID ORGANIC SOLVENTS WHICH HAVE DIFFERENT SPECIFIC GRAVITIES AND BETWEEN WHICH THE VITAMIN A ACTIVE MATERIAL AND THE NON-ACTIVE IMPURITIES HAVE DIFFERENT DISTRIBUTION COEFFICIENTS, SAID MIXTURE BEING INTRODUCED INTO THE SOLVENT STREAMS AT A POINT APPROXIMATELY MIDWAY BETWEEN THE POINTS OF INTRODUCTION OF TWO SOLVENTS, THE EXTRACTION FACTOR OF SAID VITAMIN A ACTIVE MATERIAL WITH RESPECT TO SAID SOLVENT PAIR IN SAID FIRST EXTRACTION ZONE BEING LESS THAN ONE; (2) WITHDRAWING A FIRST EXTRACT STREAM COMPRISING VITAMIN A ACTIVE MATERIAL IN THE HEAVY SOLVENT AND SEPARATELY WITHDRAWING A SECOND EXTRACT STREAM COMPRISING THE LIGHT SOLVENT AND IMPURITIES; (3) SEPARATING THE HEAVY SOLVENT FROM THE FIRST EXTRACT STREAM TO OBTAIN A FIRST VITAMIN A CONCENTRATE; (4) CONTACTING SAID CONCENTRATE IN A SECOND MULTI-STAGE EXTRACTION ZONE WITH THE SAME TWO SOLVENTS IN COUNTERCURRENT FLOW, SAID CONCENTRATE BEING INTRODUCED INTO THE SOVENT STREAMS AT A POINT APPROXIMATELY MIDWAY BETWEEN THE POINTS OF INTRODUCTION OF THE TWO SOLVENTS, THE EXTRACTION FACTOR OF THE VITAMIN A ACTIVE MATERIAL WITH RESPECT TO THE SOLVENT PAIR IN THE SECOND EXTRACTION ZONE BEING GREATER THAN ONE; (5) WITHDRAWING A THIRD EXTRACT STREAM WHICH COMPRISES VITAMIN A ACTIVE, MATERIAL STREAM WHICH COMPRISES AND A SEPARATE EXTRACT STREAM WHICH COMPRISES THE SAID HEAVY SOLVENT AND IMPURITIES; (6) SEPARATING THE LIGHT SOLVENT FROM SAID THIRD EXTRACT STREAM TO OBTAIN A VITAMIN A CONCENTRATE HAVING A GREATER PERCENTAGE CONTENT OF VITAMIN A ACTIVE MATERIAL THAN THE ORIGINAL FEED.

References Cited (Backward Citations)

US2355605A Cited
US2111360A Cited
US2090738A Cited
US2154713A Cited
US2200391A Cited
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US2278309A Cited
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USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1957-04-26 1957-10-26 1958-04-27 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1961-04-26 1961-10-26 1962-04-27 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1965-04-26 1965-10-26 1966-04-27 $7700.00 Window Closed / Lapsed

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