Recovery and comprehensive utilization process for electroplating wastewater
A technology of electroplating wastewater and process, applied in metallurgical wastewater treatment, multi-stage water treatment, water/sewage treatment and other directions, can solve problems such as teratogenicity, high toxicity and mutagenicity
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Embodiment 1
[0018] A process for recycling and comprehensive utilization of electroplating wastewater, comprising the following steps:
[0019] 1) adjusting the pH value of the electroplating wastewater to 2;
[0020] 2) Add sodium pyrophosphite as a reducing agent to reduce dichromate or chromate in water to trivalent chromium, or add sodium pyrosulfite according to the amount of hexavalent chromium;
[0021] 3) Adjust the pH value of the electroplating wastewater to 9.0 to form a precipitate and filter it;
[0022] 4) the precipitate is dried, and the chromium hydroxide product with a chromium content of 25% is determined by titration;
[0023] 5) Dissolved with sulfuric acid to generate chromium sulfate, concentrated and evaporated to a crude product.
[0024] In said step 3), if there are copper ions and nickel ions, the available percentage of precipitation is 5% ammonia water plus 15% ammonium sulfate by mass, so that the pH value of the solution is 8.5, leaching for 2h, so that c...
Embodiment 2
[0026] A process for recycling and comprehensive utilization of electroplating wastewater, comprising the following steps:
[0027] 1) The electroplating wastewater is adjusted to a pH value of 3;
[0028] 2) Add sodium pyrophosphite as a reducing agent to reduce dichromate or chromate in water to trivalent chromium, or add sodium pyrosulfite according to the amount of hexavalent chromium;
[0029] 3) Adjust the pH value of the electroplating wastewater to 8.5 to form a precipitate and filter it;
[0030] 4) the precipitate is dried, and the chromium hydroxide product with a chromium content of 45% is determined by titration;
[0031] 5) Dissolved with sulfuric acid to generate chromium sulfate, concentrated and evaporated to a crude product.
[0032] In said step 3), if there are copper ions and nickel ions, the available percentage of precipitation is 5% ammonia water plus 15% ammonium sulfate by mass, so that the pH value of the solution is 8.0, leaching for 2h, so that c...
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