Method for preparing organic acid by electrolyzing organic acid salt on basis of chlor-alkali perfluor ion exchange membrane
A technology of organic acid salts and perfluorinated ions, which is applied in the direction of electrolysis process, electrolysis components, electrolysis organic production, etc., can solve the problems of long production cycle, low total yield, cumbersome operation process, etc., and achieve strong electrochemical corrosion resistance , Improve the electrolytic current density, the effect of no pollution to the environment
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Embodiment 1
[0051] A method for electrolytic preparation of organic acid salts, by using an electrolytic cell with a perfluorinated ion exchange membrane 3 between electrodes and mainly composed of an anode chamber 4, an anode 1, a perfluorinated ion exchange membrane 3, a cathode 2, and a cathode chamber 5, Follow these steps:
[0052] Use 20% mass concentration of sodium tartrate aqueous solution as anolyte, 20% mass concentration of sodium hydroxide aqueous solution as catholyte; figure 1 In the ion-exchange membrane electrolyzer shown, it is supplied to the anode chamber and the cathode chamber of the electrolyzer respectively, wherein the perfluorinated ion-exchange membrane 3 is a domestic DF988 chlor-alkali ion-exchange membrane; with a current density of 3kA / m 2 Conduct electrolysis with direct current and control the mass concentration of the lye out of the tank to 24%; collect the anolyte out of the tank, concentrate and crystallize to obtain tartaric acid crystals with a purity...
Embodiment 2
[0054] Use 30% mass concentration of sodium fumarate (sodium fumarate) aqueous solution as anolyte, and 29% mass concentration of sodium hydroxide aqueous solution as catholyte; after preheating to 60°C, use a pump to figure 1 In the ion-exchange membrane electrolyzer shown, it is supplied to the anode chamber and the cathode chamber of the electrolyzer respectively, wherein the perfluorinated ion-exchange membrane 3 is a domestic DF988 chlor-alkali ion-exchange membrane; at a current density of 4.5kA / m 2 Conduct electrolysis with direct current and control the mass concentration of the lye out of the tank to about 31%; collect the anolyte out of the tank, and process it through concentration and crystallization to obtain fumaric acid crystals with a purity of 99.96%. The current efficiency η was calculated to be 97.4%.
Embodiment 3
[0056] As described in Example 1, the difference is that the anolyte is potassium malate with a mass concentration of 25%, and the catholyte is potassium hydroxide with a mass concentration of 20%. The purity of malic acid crystals obtained was 99.95%; the current efficiency η was calculated to be 97.4%.
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