GB798237A - Improvements in or relating to the production of hydrogen peroxide - Google Patents
Improvements in or relating to the production of hydrogen peroxideInfo
- Publication number
- GB798237A GB798237A GB281356A GB281356A GB798237A GB 798237 A GB798237 A GB 798237A GB 281356 A GB281356 A GB 281356A GB 281356 A GB281356 A GB 281356A GB 798237 A GB798237 A GB 798237A
- Authority
- GB
- United Kingdom
- Prior art keywords
- alumina
- magnesia
- solution
- regeneration
- per cent
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B15/00—Peroxides; Peroxyhydrates; Peroxyacids or salts thereof; Superoxides; Ozonides
- C01B15/01—Hydrogen peroxide
- C01B15/022—Preparation from organic compounds
- C01B15/023—Preparation from organic compounds by the alkyl-anthraquinone process
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Treatment Of Liquids With Adsorbents In General (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
A degraded solution of an alkyl anthraquinone in a solvent, which has become degraded in the process for synthesizing hydrogen peroxide involving alternately hydrogenating the alkyl anthraquinone and oxygenating the resulting alky anthrahydroquinone which is recycled after separation of the simultaneously formed hydrogen peroxide, is regenerated by heating the degraded solution at at least 55 DEG C. in the presence of activated alumina or active magnesia. Activated alumina is microporous alumina of extensive surface area obtained by heating, e.g. at 300-800 DEG C., natural or synthetic hydrated alumina, which may or may not contain a minor proportion of silica, to convert it to a less-hydrated form, e.g. a -alumina monohydrate, or g -alumina. Active magnesia is anhydrous microporous magnesia of extensive surface area obtained by decomposing magnesium hydroxide, carbonate, or nitrate. The alumina or magnesia adsorbs the organic degradation products and catalyses the regeneration, and is preferably granular, e.g. 4-100 mesh. The adsorption may be effected at 55-300 DEG C., preferably 90-150 DEG C., and the adsorbent may be in amount at least 0.5 per cent, usually 5-10 per cent. The spent adsorbent may be revivified by extracting with an organic solvent. Preferred revivification is by successive treatments with heptane, methanol, hydrochloric acid solution in aqueous methanol, water, dilute aqueous alkali, e.g. 0.1N caustic soda, and water. The adsorbent is finally dried at 100-110 DEG C. Alkyl anthraquinones may be ethyl-, methyl-, propyl-, or isopropyl-anthraquinones, and solvents may be mixtures of benzene and higher alcohols, but exemplified is a solution of 2-t-butylanthraquinone in a mixture of 1-methyl naphthalene and diisobutyl carbinol. The alumina or magnesia contact may be batch or continuous in a column. It is preferred to treat continuously a portion, e.g. 10 per cent, of the recycle from the extractor to the hydrogenator. When the solvent contains both an alcohol constituent and a hydrocarbon constituent, the regeneration is effected on a solution from which the alcohol has been distilled, and the alcohol constituent is added after treatment. The activated alumina may have palladium deposited thereon. It is stated that silica gel, glass beads, corundum, magnesia obtained by burning magnesium in air, synthetic zeolite, and bone black are not effective in the regeneration.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB281356A GB798237A (en) | 1956-01-27 | 1956-01-27 | Improvements in or relating to the production of hydrogen peroxide |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB281356A GB798237A (en) | 1956-01-27 | 1956-01-27 | Improvements in or relating to the production of hydrogen peroxide |
Publications (1)
Publication Number | Publication Date |
---|---|
GB798237A true GB798237A (en) | 1958-07-16 |
Family
ID=9746406
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB281356A Expired GB798237A (en) | 1956-01-27 | 1956-01-27 | Improvements in or relating to the production of hydrogen peroxide |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB798237A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3247228A (en) * | 1961-02-27 | 1966-04-19 | Kali Chemie Ag | Regeneration of degraded anthraquinone working solution by treatment with an ion exchange resin |
FR2755121A1 (en) * | 1996-10-25 | 1998-04-30 | Rhodia Chimie Sa | METHOD FOR REGENERATING ANTHRAQUINONE DERIVATIVES IN THE PROCESS OF SYNTHESIZING OXYGENATED WATER |
US5985235A (en) * | 1995-12-04 | 1999-11-16 | Eka Chemicals Ab | Method of treating a catalyst |
US6180804B1 (en) | 1998-09-10 | 2001-01-30 | Fmc Corporation | Reversion of expoxide in the production of Hydrogen peroxide |
EP2766300B1 (en) | 2011-10-11 | 2020-05-20 | Solvay SA | Process for producing hydrogen peroxide |
-
1956
- 1956-01-27 GB GB281356A patent/GB798237A/en not_active Expired
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3247228A (en) * | 1961-02-27 | 1966-04-19 | Kali Chemie Ag | Regeneration of degraded anthraquinone working solution by treatment with an ion exchange resin |
US5985235A (en) * | 1995-12-04 | 1999-11-16 | Eka Chemicals Ab | Method of treating a catalyst |
FR2755121A1 (en) * | 1996-10-25 | 1998-04-30 | Rhodia Chimie Sa | METHOD FOR REGENERATING ANTHRAQUINONE DERIVATIVES IN THE PROCESS OF SYNTHESIZING OXYGENATED WATER |
WO1998018715A1 (en) * | 1996-10-25 | 1998-05-07 | Procatalyse | Method for regenerating anthraquinone derivatives during a synthesis process of hydrogen peroxide 30 % |
CZ297842B6 (en) * | 1996-10-25 | 2007-04-11 | Procatalyse S. A. | Regeneration process of anthraquinone derivatives during synthesis of hydrogen peroxide |
US6180804B1 (en) | 1998-09-10 | 2001-01-30 | Fmc Corporation | Reversion of expoxide in the production of Hydrogen peroxide |
EP2766300B1 (en) | 2011-10-11 | 2020-05-20 | Solvay SA | Process for producing hydrogen peroxide |
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