Method for purifying waste water and recovering waste materials on line in electroplating and chemical plating processes
A technology for recycling waste and chemical plating, which is applied in the fields of metallurgical wastewater treatment, magnetic field/electric field water/sewage treatment, etc. It can solve the problems of high resource consumption, secondary pollution, no wastewater analysis and elaboration, and achieve simplified washing process. The effect of saving water resources and electric energy and ensuring the quality of plated products
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Embodiment 1
[0047] The electrode area of the electrode pair of the capacitive deionization device is 5000 square centimeters, which is used to treat the wastewater generated by the nickel-plating washing water. The metal ion content in the wastewater generated by the nickel-plating washing water is 100ppm, the COD value is 930, and the water inflow is controlled. (Influent volume is 120 liters) The flow rate is 4 liters / minute. Divided into three test groups, the working voltages were 2 volts, 10 volts and 20 volts.
[0048] The test results are as follows:
[0049] Working Voltage (Volts)
[0050] In this embodiment, the electrodes saturated with electrosorption at a voltage of 20 volts are short-circuited, so that the ions are discharged and desorbed in the water sample in the electrode channel. The influent water is 120 liters. After adsorption and desorption, about 100 liters of effluent water fully meet the reuse requirements, and about 20 liters are enriched and recover...
Embodiment 2
[0052] The electrode area of the activated carbon fiber electrode pair of the capacitive deionization device is 20,000 square centimeters, which is used to treat the wastewater generated by the tinning washing water. The metal ion content in the wastewater generated by the tinning washing water is 790ppm, and the COD value is 1340. The flow rate of water (inlet volume 300 liters) is 4 liters / minute, and the metal ion concentration and chemical oxygen demand (COD) of the water are detected by atomic absorption spectrometry and potassium dichromate oxidation method, respectively. Divided into three test groups, the working voltages were 2 volts, 10 volts and 20 volts.
[0053] The test results are as follows:
[0054] Working Voltage (Volts)
[0055] In this embodiment, the electrodes with saturated electro-adsorption are short-circuited to discharge and desorb the ions. Quantitative analysis with an atomic absorption spectrometer shows that the discharge resolution ...
Embodiment 3
[0057] The electric adsorption capacity of the CDI device used in Example 1 and Example 2 was calibrated with 2000 mg / L sodium chloride solution. The residence time of the influent water was controlled for 30 minutes. When the operating voltage was 20 volts, the measured electric adsorption capacities in terms of monovalent cations (sodium ions) were 0.8 mmol / g carbon and 0.7 mmol / g carbon respectively.
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