Method for extracting bromine by industrial wastewater rich in Br-
A technology of industrial waste water and bromine, applied in chemical instruments and methods, bromine/hydrogen bromide, water/sewage treatment, etc., can solve problems such as high cost and unfriendly environment, achieve good economic and social benefits, reduce Production cost, cost reduction effect
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Embodiment 1
[0017] This embodiment makes electrolyzer with plexiglass, separates into cathode chamber and anode chamber with cation exchange membrane, and anode and cathode all adopt graphite electrode, and the effective area of cathode and anode is respectively 200cm 2 , the distance between cathode and anode is 1.5cm.
[0018] Get the fumaric acid waste water 2000mL that pH value is 2.5-3.5, contain in the fumaric acid waste water: fumaric acid 3.4g / L, maleic acid 0.7g / L, sodium bromide 2.7g / L and a small amount of ammonium sulfate; Fumaric acid wastewater is filtered to remove suspended matter and transferred to the anode chamber; add 2000mL of maleic acid solution with a mass percentage concentration of 36% in the cathode chamber, keep stirring, control the temperature at 30°C, and control the current density at 0.03A / cm 2 Carry out electrolysis, and use turbidimetry to test Br in the anolyte during the electrolysis process - Concentration, when Br - When the concentration of the ...
Embodiment 2
[0020] The initial composition of the electrolytic cell and electrolyte of this embodiment is the same as that of Example 1. The temperature is controlled to be 40°C under constant stirring, and the constant voltage is controlled to be 5.0V for electrolysis. - When the concentration is no longer reduced, the electrolysis is stopped. After the anolyte was removed, 3.2 g of bromine was obtained through air blowing, condensation, gas-liquid separation, and water-bromine separation, with a recovery rate of 77.0%. The catholyte was removed, concentrated, cooled, and solid-liquid separated to obtain 2.9 g of succinic acid.
[0021] For fumaric acid wastewater, the recovery rate of bromine is slightly higher than the constant voltage method in Example 2 by the constant current method in Example 1.
Embodiment 3
[0023] The industrial wastewater in this example is the industrial wastewater from the production of the upland herbicide—metrimetrione, and the content of sodium bromide is 0.87 mol / L after methanol is removed by rectification. The amount and pH value of the electrolytic cell and the initial electrolyte are as in Example 1, the temperature is controlled at 40°C under constant stirring, and the constant voltage is controlled to be 5.0V for electrolysis. During the electrolysis, the Br in the anolyte is tested by turbidimetry. - When the concentration is no longer reduced, the electrolysis is stopped. After the anolyte was removed, 110.1 g of bromine was obtained through air blowing, condensation, gas-liquid separation, and water-bromine separation, with a recovery rate of 79.1%. After the catholyte was removed, 71.2 g of succinic acid was obtained by concentration, cooling, and solid-liquid separation.
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