Recovery method for mother liquor after copper chloride hydroxide production by etching waste liquor
A technology of etching waste liquid and recovery method, applied in copper chloride, chemical instruments and methods, copper halide and other directions, can solve problems such as direct discharge of water resources, achieve zero discharge of waste, simple maintenance, and reduce production costs.
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Embodiment 1
[0036] (1) Put the mother liquor into the neutralization precipitation reaction kettle, under the condition of sufficient stirring, adjust the pH value of the mother liquor to 6.2 with ammonia water, neutralize for 30 minutes, put the mother liquor into the filter press, and the filtrate flows into the mother liquor transfer tank , the copper content is 1g / L.
[0037] (2) Wait for the mother liquor to accumulate to 40m 3 , turn on the mother liquor transfer pump, pour the mother liquor into the two first-stage ion exchange columns connected in series filled with D403 macroporous chelating resin to obtain the first exchange liquid, and the flow rate is controlled at 8m 3 / h, the copper content in the first exchange solution is <1mg / L; the saturated ion exchange column is eluted with hydrochloric acid solution, and the eluent is used to produce basic copper chloride.
[0038] (3) Put the first exchange liquid into the second ion exchanger of the strong acid ion exchange fiber f...
Embodiment 2
[0042] (1) The mother liquor is poured into the neutralization precipitation reaction kettle. Under the condition of sufficient stirring, the pH value of the mother liquor is adjusted to 3.9 with ammonia water, and the precipitation reaction takes 20 minutes. The mother liquor is poured into the filter press, and the filtrate flows into the mother liquor transfer tank, and the The content is 1.1g / L.
[0043] (2) Wait for the mother liquor to accumulate to 40m 3 At this time, the mother liquor transfer pump is turned on, and the mother liquor is poured into the two first-stage ion exchange columns connected in series filled with D403 macroporous chelating resin in turn, and the flow rate is controlled at 9m 3 / h, the copper content in the first exchange solution is <5mg / L; the saturated ion exchange column is eluted with hydrochloric acid solution, and the eluent is used to produce basic copper chloride.
[0044] (3) Put the first exchange liquid into the second ion exchanger f...
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