Method for recycling and treating electroplating wastewater
A technology for the recycling and treatment of electroplating wastewater, which is applied in metallurgical wastewater treatment, water/sewage multi-stage treatment, water/sludge/sewage treatment, etc., and can solve problems such as secondary pollution, resource waste, and non-recyclable metal ions
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Embodiment 1
[0020] (1) Filter 1L of industrial electroplating wastewater with a chromium content of 55ppm, a nickel content of 48ppm, a copper content of 37ppm, a zinc content of 74ppm, and a pH of 6.0, and the filtrate enters the next step.
[0021] (2) the filtrate in step (1) is first passed through an acidic cation exchange column to remove Ni in the waste water 2+ 、Cu 2+ and Zn 2+ At this time, the wastewater mainly contains chromium ions, and then passes through the basic anion exchange column to further remove Cr 2 o 7 2- , at this time the wastewater contains Ni 2+ 0.54ppm, containing Cu 2+ 0.36ppm, including Zn 2+ It is 0.63ppm and contains 0.22ppm Cr(Ⅵ), which can be used as reused water or discharged.
[0022] (3) The anion exchange column recovers 0.21g of chromate through elution; the eluent of the cation exchange column mainly contains Ni 2+ 、Cu 2+ and Zn 2+ , metered into ammonium chloride and phosphoric acid, adjust the pH to 6.0, react for 30min, wherein the mol...
Embodiment 2
[0025] (1) 2L chromium content is 80ppm, nickel content is 64ppm, copper content is 61ppm, zinc content is 93ppm, pH is 3.0 industrial electroplating waste water is filtered, and filtrate enters next step process.
[0026] (2) The filtrate in step (1) is first passed through a strongly acidic cation exchange column to remove Ni in the waste water 2+ 、Cu 2+ and Zn 2+ At this time, the wastewater mainly contains chromium ions, and then passes through the basic anion exchange column to further remove Cr 2 o 7 2- , at this time the wastewater contains Ni 2+ 0.63ppm, containing Cu 2+ 0.52ppm, containing Zn 2+ 0.71ppm, containing 0.35ppm Cr(Ⅵ), which can be used as reused water or discharged.
[0027] (3) The anion exchange column can recover 0.54g of chromate after elution. The eluent of the cation exchange column mainly contains Ni 2+ 、Cu 2+ and Zn 2+ , metering ammonium sulfate and sodium dihydrogen phosphate, adjusting the pH to 8.0, reacting for 60min, wherein the mo...
Embodiment 3
[0030] (1) 5L chromium content is 68ppm, nickel content is 56ppm, copper content is 54ppm, zinc content is 81ppm, and pH is 4.5 industrial electroplating waste water is filtered, and filtrate enters next step process.
[0031] (2) the filtrate in step (1) is first passed through an acidic cation exchange column to remove Ni in the waste water 2+ 、Cu 2+ and Zn 2+ At this time, the wastewater mainly contains chromium ions, and then passes through the basic anion exchange column to further remove Cr 2 o 7 2- , at this time the wastewater contains Ni 2+ 0.59ppm, containing Cu 2+ 0.47ppm, containing Zn 2+ It is 0.66ppm and contains 0.28ppm Cr(Ⅵ), which can be used as reused water or discharged.
[0032] (3) The anion exchange column can recover 1.18g of chromate after elution. The eluent of the cation exchange column mainly contains Ni 2+ 、Cu 2+ and Zn 2+ , metered into ammonia workshop wastewater and pretreated phosphorus-containing wastewater, adjust the pH to 7.0, react...
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