Solvent system for producing fully acidic hydrogen peroxide working solution by anthraquinone method
A technology of working liquid and anthraquinone method, which is applied in the fields of peroxide/peroxy hydrate/peroxyacid/superoxide/ozonide, chemical instruments and methods, inorganic chemistry, etc., which can solve the problems of heavy workload and solubility Large size, complex synthesis process and other problems, to achieve the effect of reducing the economic cost of solvents, increasing production capacity, and improving solubility
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Embodiment 1
[0020] In the production of hydrogen peroxide by anthraquinone method, heavy aromatics (C 9 ~C 10 ): dioctyl phosphate: tetrabutyl urea=80:10:10 (volume ratio) is the solvent system of working fluid, and alkylanthraquinone solubility is 162g / L. The hydrogenation temperature is 45°C, the hydrogenation pressure is 0.25MPa, and the space velocity is 18h -1 , the ratio of hydrogen to liquid is 5:1. The oxidation temperature is 51°C, and the oxidation pressure is 0.16MPa. The hydrogenation efficiency was 9.3g / L.
Embodiment 2
[0027] With heavy aromatics (C 9 ~C 10 ): dioctyl phosphate: tetrabutyl urea=80:5:15 (volume ratio) is the solvent system of working fluid, and 2 alkyl anthraquinone solubility is 171g / L. The hydrogenation temperature is 48°C, the hydrogenation pressure is 0.28MPa, and the space velocity is 24h -1 , the ratio of hydrogen to liquid is 6.5:1. The oxidation temperature is 53°C and the oxidation pressure is 0.20MPa. The hydrogenation efficiency was 10.2 g / L.
Embodiment 3
[0032] With heavy aromatics (C 9 ~C 10 ): dioctyl phosphate: tetrabutyl urea=75:7:18 (volume ratio) is the solvent system of working fluid, and alkylanthraquinone solubility is 178g / L. The hydrogenation temperature is 50°C, the hydrogenation pressure is 0.33MPa, and the space velocity is 28h -1 , the ratio of hydrogen to liquid is 7:1. The oxidation temperature is 54°C and the oxidation pressure is 0.24MPa. The hydrogenation efficiency was 10.8g / L.
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