Resourceful treatment method of chemical nickel plating waste liquid
A technology of electroless nickel plating and treatment methods, which is applied in the directions of chemical instruments and methods, liquid chemical plating, metallurgical wastewater treatment, etc., which can solve the problems of increased treatment cost, difficult treatment, high cost, etc., to save treatment cost and shorten oxidation The effect of using less technology and medicine
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Embodiment 1
[0037] The electroless nickel plating waste liquid that this embodiment takes, pH is 4.5, and total nickel content is 6700mg / L, and total phosphorus content is 70000mg / L, and COD value is 102000mg / L, and Na + The concentration is 35000mg / L, SO 4 2- The concentration is 71300mg / L.
[0038] S1. Oxidation and decompression: Take 1.0L of electroless nickel plating waste solution, add sodium hydroxide solution to adjust the pH to 6, then add 175g of hydrogen peroxide with a mass concentration of 40%, mix well, and add to the interior filled with heterogeneous Fenton Aerated and oxidized for 5 hours in the oxidation tower of the catalyst to obtain an acidic reaction solution;
[0039] S2. Synchronous precipitation of nickel and phosphorus: detect that the pH of the acidic reaction solution is 4.4, add 10% sodium hydroxide solution to the acidic reaction solution to adjust the pH to 7.5, and slowly add 1.3L with a mass concentration of 30% under stirring at 200rpm The nickel sulfa...
Embodiment 2
[0043] The electroless nickel plating waste liquid that this embodiment takes, pH is 3.7, and total nickel content is 5120mg / L, and total phosphorus content is 41000mg / L, and COD value is 65000mg / L, and Na + The concentration is 25800mg / L, SO 4 2- The concentration is 52300mg / L.
[0044] The difference between this example and Example 1 is: in step S1, the pH is adjusted to 5.5, the mass concentration of hydrogen peroxide is 27.5%, the mass is 150g, and the oxidation reaction time is 3h; in step S2, the pH is 4.2 after the oxidation is complete, Adjust the pH to 7.8, the mass concentration of the nickel sulfate solution is 15%, the volume is 1.7L, and the aging time is 0.5h; in step S3, the volume of the sodium hydroxide solution is 70mL, and the pH is adjusted to 12.03 to obtain the second filtrate 2.6 L; in step S4, take 2.5L of the second filtrate, the conductivity is 90mS / cm, the voltage is 25.0V, the current is 3.4A, the working temperature is 35°C, and the adding volum...
Embodiment 3
[0046] The electroless nickel plating waste liquid that this embodiment takes, pH is 3.2, and total nickel content is 2030mg / L, and total phosphorus content is 25000mg / L, and COD value is 32000mg / L, and Na + The concentration is 21600mg / L, SO 4 2- The concentration is 44500mg / L.
[0047] The difference between this example and Example 1 is: in step S1, the pH is adjusted to 5.5, the mass concentration of hydrogen peroxide is 27.5%, the mass is 108g, and the oxidation reaction time is 2h; in step S2, the pH is 4.8 after the oxidation is complete, The mass concentration of the nickel sulfate solution is 15%, the volume is 0.47L, and the aging time is 0.5h; in step S3, the volume of the sodium hydroxide solution is 80mL, and the pH is adjusted to be 11.85 to obtain the second filtrate 1.5L; in step S4 , take 1.5L of the second filtrate, adjust the pH to 7.8, the current is 4.0A, the working temperature is 35°C, and the volumes added to the salt chamber, acid chamber, and alkali...
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