A kind of steel pickling wastewater recovery and treatment method
A technology for steel pickling and waste water recovery, which is applied to the improvement of instruments, optics, and process efficiency, can solve the problems that have not been seen in the report, and achieve the effect of realizing full utilization, increasing hydrogen evolution overpotential, and reducing environmental pollution.
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Embodiment 1
[0028] (1) Add dodecyltrimethylammonium chloride (cationic surfactant) to iron and steel sulfate pickling wastewater to obtain an electrolytic mixture. Fe in the electrolyte mixture 2+ The concentration is 160g / L, the concentration of the cationic surfactant is 2g / L, and the pH of the electrolytic mixture is 1-2.
[0029] (2) Put the electrolytic mixture solution into the diaphragm electrolyzer for electrolysis. The anode is a rolled lead plate (inert electrode), the highly polished stainless steel plate is a cathode, the cell voltage is controlled to 0.9V, and the current density is controlled to 300A / m 2 , The electrolysis temperature is controlled at 30°C to 40°C, and the electrolysis cycle is 72h. The cathode of the diaphragm electrolyzer precipitates high-purity iron, and the anode waste acid is regenerated. The current efficiency of the electrolysis process is 94%, and the power consumption is 920t / KW.h. Fe in solution after electrolysis 2+ The concentration of the ...
Embodiment 2
[0033] (1) Add dodecyltrimethylammonium chloride to iron and steel sulfate pickling wastewater to obtain an electrolytic mixture. Fe in the electrolyte mixture 2+ The concentration is 140g / L, the cationic surfactant concentration is 4g / L, and the pH=1 of the mixed solution.
[0034] (2) Put the electrolytic mixture solution into the diaphragm electrolyzer for electrolysis. The anode is a rolled lead plate, the highly polished stainless steel plate is a cathode, the cell voltage is controlled at 1.1V-1.2V, and the current density is controlled at 400A / m 2 , The electrolysis temperature is controlled at 30°C to 40°C, and the electrolysis cycle is 72h. The cathode of the diaphragm electrolyzer precipitates high-purity iron, and the anode waste acid is regenerated. The current efficiency of the electrolysis process is 95%, and the power consumption is 900t / KW.h. Fe in solution after electrolysis 2+The concentration of the iron was 26.1g / L, and the recovery rate of iron was 81...
Embodiment 3
[0038] (1) Add dodecyltrimethylammonium chloride to hydrofluoric acid and nitric acid steel pickling waste water (which contains 10% hydrofluoric acid and 40% nitric acid by mass fraction) to obtain an electrolytic mixture. Fe in the electrolyte mixture 2+ The concentration is 100g / L, the cationic surfactant concentration is 6g / L, and the pH of the mixed solution is 0.5-1.
[0039] (2) Put the electrolytic mixture solution into the diaphragm electrolyzer for electrolysis. The anode is a graphite electrode (inert electrode), the highly polished stainless steel plate is a cathode, the cell voltage is controlled at 1.2V, and the current density is controlled at 450A / m 2 , The electrolysis temperature is controlled at 30°C to 40°C, and the electrolysis cycle is 72h. The cathode of the diaphragm electrolyzer precipitates high-purity iron, and the anode waste acid is regenerated. The current efficiency of the electrolysis process is 98%, and the power consumption is 980t / KW.h. F...
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