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US4617090A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for producing peracids from aliphatic hydroxy carboxylic acids

Assignee: United States Department of Energy
•
Filing: 1984-12-20
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Granted: 1986-10-14
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Expires: 2004-12-20
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Abstract

Abstract A process for producing peracids from lactic acid-containing solutions derived from biomass processing systems comprising: adjusting the pH of the solution to about 8-9 and removing alkaline residue fractions therefrom to form a solution comprised substantially of lower aliphatic hydroxy acids; oxidizing the solution to produce volatile lower aliphatic aldehydes; removing said aldehydes as they are generated; and converting said aldehydes to peracids.

Inventors

  • 👤 Helena L. Chum
  • 👤 Matthew A. Ratcliff
  • 👤 Peter D. Palasz

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 14:18
CPC Classifications
C; C07; C07C; C07C45/00; C07C45/78; C07C45/783; C07C407/00; C07C409/00; C07C409/24; C07C409/26; C07C45/27; C07C45/29; C07C45/292; C07C45/298; C07C45/30; C07C59/00; C07C59/01; C07C59/06; C07C59/08; C07C59/235; C07C59/245; C07C59/285; C25; C25B; C25B3/00; C25B3/01; C25B3/07; C25B3/20; C25B3/23; Y; Y02; Y02P; Y02P20/00; Y02P20/10; Y02P20/133

Claims Analysis

Total Claims: 7
Claim 1
Independent Claim 250 words
In a wood pulp processing system of the type producing both pulp and a stream of lactic acid-containing black liquor solution, the processor for production of peracid bleaching agents from hydroxy acid contained in the black liquor solution, comprising: adjusting the pH of said black liquor solution to the range of about 8-9 by exposing the solution to CO 2 carbon dioxide to form an alkaline precipitate; separating solids from the black liquor solution to produce a residual solution containing lower aliphatic hydroxy acids selected from the group consisting of lactic acid, glycolic acid, 2-hydroxybutanoic acid, xyloisosaccharinic acid, and glucoisosaccharinic acid; decarboxylating said lower aliphatic hydroxy acids to corresponding gaseous aliphatic aldehydes by admixing a powdered semiconductor with said residual solution to form a slurry, said semiconductor being selected from the group consisting of doped n-TiO 2 , both platinized and unplatinized, n-WO 3 , a-Fe 2 O 3 and other insoluble semiconductors having bandgaps equal to or higher than a-Fe 2 O 3 , and then irradiating said slurry by a means for causing photoelectro-chemical reaction at the site of the semiconductor material resulting in decarboxylation of the carboxylic acid and produuction of CO 2 and corresponding aldehydes; removing said gaseous aldehydes from the residual solution by sweeping gas flow as soon as they are generated to prevent further oxidation to carboxylic acids; reacting said gaseous aldehydes with oxygen to form corresponding peracids; and applying said peracids as bleaching agents to said pulp produced in the pulp processing system.
Claim 2
Dependent Claim 250 words
In a wood pulp processing system of the type producing both pulp and a stream of lactic acid-containing black liquor solution, the processor for production of peracid bleaching agents from hydroxy acid contained in the black liquor solution, comprising: adjusting the pH of said black liquor solution to the range of about 8-9 by exposing the solution to CO 2 carbon dioxide to form an alkaline precipitate; separating solids from the black liquor solution to produce a residual solution containing lower aliphatic hydroxy acids selected from the group consisting of lactic acid, glycolic acid, 2-hydroxybutanoic acid, xyloisosaccharinic acid, and glucoisosaccharinic acid; decarboxylating said lower aliphatic hydroxy acids to corresponding gaseous aliphatic aldehydes by admixing a powdered semiconductor with said residual solution to form a slurry, said semiconductor being selected from the group consisting of doped n-TiO 2 , both platinized and unplatinized, n-WO 3 , a-Fe 2 O 3 and other insoluble semiconductors having bandgaps equal to or higher than a-Fe 2 O 3 , and then irradiating said slurry by a means for causing photoelectro-chemical reaction at the site of the semiconductor material resulting in decarboxylation of the carboxylic acid and produuction of CO 2 and corresponding aldehydes; removing said gaseous aldehydes from the residual solution by sweeping gas flow as soon as they are generated to prevent further oxidation to carboxylic acids; reacting said gaseous aldehydes with oxygen to form corresponding peracids; and applying said peracids as bleaching agents to said pulp produced in the pulp processing system.
Claim 3
Dependent Claim 57 words
The process as described in claim 1, further comprising: cooking said black liquor solution or residual solution in the presence of oxygen for a time and at a temperature sufficient to form lactic acid from other hydroxy acids of the cooked solution, wherein said cooking step is performed prior to the step of decarboxylating the hydroxy acids.
Claim 4
Dependent Claim 28 words
The process as described in claim 2, wherein said cooking step is performed at a temperature in the range 150°-200° C. for a time from approximately 2-4 hours.
Claim 5
Dependent Claim 39 words
The process as described in claim 1, wherein said step of separating solids is performed by filtering any alkaline lignin components and ultrafiltering other residual components so as to separate said lower aliphatic hydroxy acids from higher hydroxy acids.
Claim 6
Dependent Claim 40 words
The process as described in claim 1, wherein said step of separating solids is performed by filtering any alkaline lignin components and membrane separating other residual components so as to separate said lower aliphatic hydroxy acids from higher hydroxy acids.
Claim 7
Dependent Claim 51 words
The process as described in claim 1, wherein said step of separating solids is performed by filtering any alkaline lignin components and then acidifying said solution to a pH of about 3-4 to precipitate any remaining alkaline components so as to leave a solution having predominently said lower aliphatic hydroxy acids.

References Cited (Backward Citations)

US2804473A Cited
US3502715A Cited
US4137256A Cited
US4461691A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1989-10-13 1990-04-14 1990-10-14 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1993-10-13 1994-04-14 1994-10-14 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1997-10-13 1998-04-14 1998-10-14 $7700.00 Window Closed / Lapsed

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