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US3689541A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for isolating acrylic acid from aqueous crude acrylic acid by extraction with a ketone and plural stage distillation

Assignee: Individual
•
Filing: 1971-01-18
•
Granted: 1972-09-05
•
Expires: 1991-01-18
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Abstract

Abstract Pure acrylic acid is isolated from an aqueous crude acid containing acrylic acid together with minor proportions of acetic acid, formaldehyde and high boilers boiling at a temperature higher than 220*C by liquid-liquid extraction with the use of 3,3,5-trimethylcyclohexanone and/or isophorone as the extractant(s). To this end, the aqueous acrylic acid-containing crude acid is subjected in an extraction zone to counterflow extraction with the use of the extractant(s) and with the resultant formation of an organic extract containing acrylic acid, acetic acid, high boilers and minor proportions of water, which are dissolved in the extractant; the extract is introduced approximately into the midsection of a first distilling column, which is operated under reduced pressure; the base product of said first distilling column, containing the high boilers and the extractant(s) is recycled to the extraction zone; distillate containing acrylic acid, acetic acid, water and minor proportions of extractant(s) is delivered approximately to the midsection of a second distilling column, which is operated under reduced pressure; a mixture of water and extractant(s) is distilled off; the base product of said second distilling column, containing acrylic acid and acetic acid is introduced into a third distilling column, which is operated under reduced pressure; and acetic acid is separated therein as a distillate and acrylic acid is separated therein as the base product.

Inventors

  • 👤 Kurt Sennewald
  • 👤 Heinz Erpenbach
  • 👤 Heinz Handte
  • 👤 Winfried Lork

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-08 19:57
CPC Classifications
C; C07; C07C; C07C51/00; C07C51/42; C07C51/48; Y; Y10; Y10S; Y10S203/00; Y10S203/22

Claims Analysis

Total Claims: 6
Claim 1
Independent Claim 49 words
The process as claimed in claim 1, wherein a portion of the base product of the first distilling zone, containing the high boilers and extractant, is removed from the said first distilling zone, distilled and the extractant distillatively freed from the high boilers is recycled to the extraction zone.
Claim 2
Dependent Claim 64 words
The process as claimed in claim 1, wherein aqueous raffinate, which is obtained in the extraction zone and contaiNs dissolved extractant, is delivered approximately to the midsection of a stripping zone, the extractant is recovered by removing an azeotrope of extractant and water overhead, the azeotrope is recycled to the extraction zone, and waste water is discharged through the base of the stripping zone.
Claim 3
Dependent Claim 48 words
The process as claimed in claim 1, wherein the mixture of water and extractant, which is obtained as the distillate of the second distilling zone, is combined with the raffinate coming from the extraction zone, and the combination is introduced approximately into the midsection of the stripping zone.
Claim 4
Dependent Claim 27 words
The process as claimed in claim 1, wherein the first, second and third distilling zones are operated under a pressure of between 5 and 200 mm Hg.
Claim 5
Dependent Claim 45 words
The process as claimed in claim 1, wherein the aqueous crude acid contains between 5 and 40 weight percent acrylic acid, between 0.5 and 8 weight percent acetic acid, between 0.5 and 5 weight percent formaldehyde and between 0.2 and 5 weight percent high boilers.
Claim 6
Dependent Claim 37 words
The process as claimed in claim 1, wherein the aqueous crude acid is extracted with the use of between 1 and 10 parts by weight extractant, per part by weight acrylic acid in the aqueous crude acid.

References Cited (Backward Citations)

US2526508A Cited
US3344178A Cited
GB997324A Cited
US3507915A Cited
US3433831A Cited
US3555082A Cited
US3553261A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1975-09-05 1976-03-06 1976-09-05 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1979-09-05 1980-03-06 1980-09-05 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1983-09-05 1984-03-06 1984-09-05 $7700.00 Window Closed / Lapsed

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