The method for treating Basic Copper Chloride production wastewater according to claim, wherein in step II, the mixing system is oxidized by a jet aeration device and a blast tower to control the jet aeration The aeration amount of the device is 280m3/h, and the flow rate of the mixed system is 10m3/h.
　　 The method for treating basic copper chloride production wastewater according to claim, wherein the evaporation system is an MVR evaporator.
　　 The method for treating basic copper chloride production wastewater according to claim, wherein the filtrate obtained after the solid-liquid separation treatment in the step IV uses an inflection point chlorine method to remove ammonia nitrogen.
The method for treating Basic Copper Carbonate production wastewater according to claim, wherein the active resin filled in the ion exchange system is a macroporous chelating resin or a macroporous strong acid resin.