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US2859207A Expired / Lapsed US ⏱️ 0.0 years remaining

Process of purification of polyvinyl acetals

Assignee: Celanese Corp
•
Filing: 1955-05-24
•
Granted: 1958-11-04
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Expires: 1975-05-24
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Abstract

Abstract A polyvinyl acetal resin is purified by adding a non-solvent liquid to a solution of an impure polyvinyl acetal resin, the amount and temperature of the non-solvent being such that a gel of said resin and liquor, containing solvent and non-solvent, are produced and then separating the liquor from the gel. Specified acetals are those produced by the reaction of formaldehyde, acetaldehyde, propionaldehyde, butyraldehyde or valeraldehyde with polyvinyl alcohol or polyvinyl esters in the presence of acidic catalysts, e.g. sulphuric acid, in a liquid medium. Specified solvents are methanol, ethanol, propanol and acetic acid while water or water-solvent mixtures are used as the non-solvent. The separated gel may be further dissolved in a polyvinyl acetal solvent and the purification repeated. The amount and temperature of the non-solvent may be such that there are dissolved in the liquor the major proportion of polymers of such molecular weight as to be soluble in methanol-water mixtures of specific gravity 0.84 or alternatively at least 0.93. The separated gel may be heated to liquefy it and/or sprayed in particle form into a zone where the solvent and non-solvent are removed therefrom, e.g. by evaporation.

Inventors

  • 👤 Dahle Joseph

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-25 22:15
CPC Classifications
C; C08; C08F; C08F8/00; C08F8/28

Claims Analysis

Total Claims: 2
Claim 1
Independent Claim 106 words
IN THE PROCESS FOR THE PRODUCTION OF POLYVINYL ACETAL RESINS, THE STEPS WHICH COMPRISE ADDING AN AQUEOUS NONSOLVENT LIQUID TO A SOLUTION OF AN IMPURE POLYVINYL ACETAL RESIN IN A SOLVENT THEREFOR, THE AMOUNT AND TEMPERATURE OF THE AQUEOUS NON-SOLVENT BEING SUCH THAT A GEL PHASE OF SAID RESIN AND A LIQUOR PHASE, COMPRISING AN AQUEOUS MIXTURE OF THE SOLVENT AND NON-SOLVENT, ARE PRODUCED, AND SEPARATING SAID LIQUOD PHASE FROM SAID GEL PHASE, AND GEL BEING CHARACTERIZED BY THE PROPERTY OF SETTLING ON STANDING TO FORM A LOWER DISTINCT FROM SAID LQUOR WHICH LOWER LAYER MAY BE BROKEN INTO SMALL PARTICLES AGGLOMERATION WHEN THE AGITATION CEASES.
Claim 2
Dependent Claim 106 words
IN THE PROCESS FOR THE PRODUCTION OF POLYVINYL ACETAL RESINS, THE STEPS WHICH COMPRISE ADDING AN AQUEOUS NONSOLVENT LIQUID TO A SOLUTION OF AN IMPURE POLYVINYL ACETAL RESIN IN A SOLVENT THEREFOR, THE AMOUNT AND TEMPERATURE OF THE AQUEOUS NON-SOLVENT BEING SUCH THAT A GEL PHASE OF SAID RESIN AND A LIQUOR PHASE, COMPRISING AN AQUEOUS MIXTURE OF THE SOLVENT AND NON-SOLVENT, ARE PRODUCED, AND SEPARATING SAID LIQUOD PHASE FROM SAID GEL PHASE, AND GEL BEING CHARACTERIZED BY THE PROPERTY OF SETTLING ON STANDING TO FORM A LOWER DISTINCT FROM SAID LQUOR WHICH LOWER LAYER MAY BE BROKEN INTO SMALL PARTICLES AGGLOMERATION WHEN THE AGITATION CEASES.

References Cited (Backward Citations)

US2194613A Cited
US2356896A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1961-11-03 1962-05-05 1962-11-04 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1965-11-03 1966-05-05 1966-11-04 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1969-11-03 1970-05-05 1970-11-04 $7700.00 Window Closed / Lapsed

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