Electrolysis recovery method of nickel in waste water
A technology for electrolytic recovery and waste water, which is applied in chemical instruments and methods, water/sewage treatment, water/sludge/sewage treatment, etc., and can solve the problems of nickel-containing wastewater whose water quality cannot be kept stable, complex impurity content, and nickel recovery and treatment difficulties To achieve the effect of accelerating the escape of hydrogen, reducing energy consumption and improving electrolysis efficiency
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Embodiment 1
[0018] (1) Take 1000 g of nickel-containing wastewater and adjust the pH value to 2.0 with flake sodium hydroxide;
[0019] (2) Add 0.01g polyethylene glycol, 0.03g thiourea, 0.005g sodium dodecylsulfonate and 0.005g saccharin, maintain the system temperature at 70 ℃, and control the current at 1.0 A under stirring at 700 r / min to start electrolysis , measure the pH value of the system every half an hour, maintain the pH value of the system at 2.0 by adding flake sodium hydroxide, and control the electrolysis time at 12 h. During electrolysis, the titanium plate is used as the cathode plate, and the iridium-plated titanium plate is used as the anode plate;
[0020] (3) Then use flake sodium hydroxide to adjust the pH value of the system to 6.0, add 0.1g sodium hypophosphite and 0.05g gelatin, continue to maintain the system temperature, control the current at 1.0 A for electrolysis under stirring at 900 r / min, and the electrolysis time For 8 h, during electrolysis, the titaniu...
Embodiment 2
[0022] (1) Take 1300 g of nickel-containing wastewater and adjust the pH value to 3.0 with flake sodium hydroxide;
[0023] (2) Add 0.04 g polyethylene glycol, 0.05 g thiourea, 0.01 g chloral hydrate and 0.005 g saccharin, maintain the system temperature at 50 °C, and control the current at 3.0 A under stirring at 800 r / min to start electrolysis. Measure the pH value of the system once half an hour, maintain the pH value of the system at 3.0 by adding flake sodium hydroxide, and control the electrolysis time at 20 h. During electrolysis, the titanium plate is used as the cathode plate, and the titanium iridium-plated plate is used as the anode plate;
[0024] (3) Then use flake sodium hydroxide to adjust the pH value of the system to 9.0, add 0.2g sodium hypophosphite, continue to maintain the system temperature, control the current at 2.5 A for electrolysis under stirring at 1000 r / min, and the electrolysis time is 10 h. During electrolysis, the titanium plate is used as the ...
Embodiment 3
[0026] (1) Take 1500 g of nickel-containing wastewater and adjust the pH value to 5.5 with flake sodium hydroxide;
[0027] (2) Add 0.05 g polyethylene glycol, 0.06 g thiourea, 0.007 g p-toluenesulfonamide and 0.005 g saccharin, maintain the system temperature at 80 °C, and control the current at 5.0 A under stirring at 900 r / min to start electrolysis. The pH value of the system was measured once an hour, and the pH value of the system was maintained at 5.5 by adding flake sodium hydroxide, and the electrolysis time was controlled at 24 h. During electrolysis, the titanium plate was used as the cathode plate, and the titanium iridium-plated plate was used as the anode plate;
[0028] (3) Then use flake sodium hydroxide to adjust the pH value of the system to 10.0, add 0.15g sodium hypophosphite and 0.15g gelatin, continue to maintain the system temperature, control the current at 5.0 A for electrolysis under stirring at 1100 r / min, and the electrolysis time For 16 h, during el...
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