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Preparation of monoperoxyphthalic acid

Assignee: PPG Industries Inc
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Filing: 1976-11-24
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Granted: 1978-04-18
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Expires: 1996-11-24
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Abstract

Abstract Stable monoperoxyphthalic acid is prepared by reacting phthalic anhydride with a stoichiometric excess of concentrated hydrogen peroxide in the absence of basic catalyst in liquid halogenated hydrocarbon medium in which the monoperoxyphthalic acid product is insoluble.

Inventors

  • 👤 Robert G. Briody

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-27 15:52
CPC Classifications
C; C07; C07C; C07C407/00; C07C407/003; C08; C08G; C08G2120/00

Claims Analysis

Total Claims: 5
Claim 1
Independent Claim 135 words
A process for preparing thermally stable, solid monoperoxyphthalic acid comprising reacting, in a liquid halogenated hydrocarbon reaction medium, phthalic anhydride with an aqueous hydrogen peroxide solution having a hydrogen peroxide content of at least 65 percent by weight at a molar ratio of hydrogen peroxide to phthalic anhydride of at least 1.2 to 1, said liquid halogenated hydrocarbon being a solvent for the phthalic anhydride and a non-solvent for the monoperoxyphthalic acid, precipitating monoperoxyphthalic acid and recovering a solid monoperoxyphthalic acid having a decomposition rate of less than 3.0 weight percent per day at 60° C., said reaction being conducted with agitation at a temperature of between 35° C. and 70° C., in the absence of a basic catalyst and in the absence of the addition of acids or bases after completion of the reaction.
Claim 2
Dependent Claim 135 words
A process for preparing thermally stable, solid monoperoxyphthalic acid comprising reacting, in a liquid halogenated hydrocarbon reaction medium, phthalic anhydride with an aqueous hydrogen peroxide solution having a hydrogen peroxide content of at least 65 percent by weight at a molar ratio of hydrogen peroxide to phthalic anhydride of at least 1.2 to 1, said liquid halogenated hydrocarbon being a solvent for the phthalic anhydride and a non-solvent for the monoperoxyphthalic acid, precipitating monoperoxyphthalic acid and recovering a solid monoperoxyphthalic acid having a decomposition rate of less than 3.0 weight percent per day at 60° C., said reaction being conducted with agitation at a temperature of between 35° C. and 70° C., in the absence of a basic catalyst and in the absence of the addition of acids or bases after completion of the reaction.
Claim 3
Dependent Claim 12 words
The process of claim 1 wherein the halogenated hydrocarbon is ethylene dichloride.
Claim 4
Dependent Claim 21 words
The process of claim 1 wherein the molar ratio of hydrogen peroxide to phthalic anhydride is at least 1.6 to 1.
Claim 5
Dependent Claim 20 words
The process of claim 1 wherein the hydrogen peroxide solution has a hydrogen peroxide content of over 85 weight percent.

References Cited (Backward Citations)

US2273744A Cited
US3284491A Cited
US3510512A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1981-04-17 1981-10-17 1982-04-18 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1985-04-17 1985-10-17 1986-04-18 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1989-04-17 1989-10-17 1990-04-18 $7700.00 Window Closed / Lapsed

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