ES255288A1 - Improvements in or relating to the production of hydrogen peroxide - Google Patents
Improvements in or relating to the production of hydrogen peroxideInfo
- Publication number
- ES255288A1 ES255288A1 ES0255288A ES255288A ES255288A1 ES 255288 A1 ES255288 A1 ES 255288A1 ES 0255288 A ES0255288 A ES 0255288A ES 255288 A ES255288 A ES 255288A ES 255288 A1 ES255288 A1 ES 255288A1
- Authority
- ES
- Spain
- Prior art keywords
- solution
- regeneration
- metal silicate
- working
- regenerated
- 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
Abstract
At least a portion of a working solution comprising an anthraquinone dissolved in a solvent therefor which has become degraded by use in the cyclic anthraquinone/anthrahydroquinone process for the production of hydrogen peroxide is regenerated by contact with a Group II metal silicate after a hydrogenation stage and before the next hydrogenation stage to which it is submitted. The metal silicate is preferably one of calcium, magnesium or zinc, or a mixture, especially magnesium trisilicate, in a pelleted or granulated form, and may be used in amount 5-10% based on the weight of the solution to be treated. The degraded solution is regenerated at at least 75 DEG C., e.g. 85 DEG -140 DEG C. Regeneration of the solution may be effected at any stage in the cyclic process, preferably of the oxidized solution. As a continuous process regeneration may be effected by removing a portion, e.g. 10% by volume of the working solution after oxidation and H2O2 extraction, contacting it with a bed of metal silicate and returning it to the main bulk of working solution cycling in the process prior to entry into the hydrogenator. The degree of regeneration is related to the mesh size of the silicate, the precise formula relationship being given in the Specification. For practical purposes a particle size of not less than 360 microns is employed. Working solutions may combine 2-ethyl, methyl, propyl, isopropyl or butyl anthraquinones in solvents such as mixtures of xylene and methyl cyclohexanol acetate. Specifications 465,070, 798,237 and 838,939 are referred to.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB243159A GB928784A (en) | 1959-01-22 | 1959-01-22 | Improvements in or relating to the production of hydrogen peroxide |
Publications (1)
Publication Number | Publication Date |
---|---|
ES255288A1 true ES255288A1 (en) | 1960-05-01 |
Family
ID=9739464
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
ES0255288A Expired ES255288A1 (en) | 1959-01-22 | 1960-01-26 | Improvements in or relating to the production of hydrogen peroxide |
Country Status (2)
Country | Link |
---|---|
ES (1) | ES255288A1 (en) |
GB (1) | GB928784A (en) |
-
1959
- 1959-01-22 GB GB243159A patent/GB928784A/en not_active Expired
-
1960
- 1960-01-26 ES ES0255288A patent/ES255288A1/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
GB928784A (en) | 1963-06-12 |
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