Method for processing acidic etching waste solution of printed circuit board
A technology for acid etching waste liquid and printed circuit board, which is applied in the field of acid etching waste liquid treatment, can solve the problems of waste of resources, low copper extraction efficiency, pollution, etc., so as to save resources, improve copper extraction efficiency, and avoid environmental pollution. Effect
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Embodiment 1
[0037] Take 100ml acidic etching waste solution (the acidic etching solution system is "hydrochloric acid + sodium chlorate" system), and the relevant parameters are Cu 2+ =143.6g / L, Cl - =225.7g / L, the acid equivalent is 1.28N, neutralize it with 25% ammonia water, adjust the pH to be 8 (±0.2), the adjusted solution volume is 196ml, Cu 2+ =73.2g / L, Cl - =92.3g / L, pH value=8.01. Carry out extraction with oxime extractant, di-tert-butylmethylphenol or methylphenol are antioxidant, wherein, oxime content is 98wt%, antioxidant content is 2wt%, volume ratio (V / V) 25%, oil-liquid ratio ( After O / A) 2 / 1 carries out three extractions, raffinate is clear and transparent (copper ion concentration is below 0.5g / L). Then the raffinate is adjusted to a pH value of 6.5 to 7.0, and the solid content in the raffinate is analyzed to be 30g. The extract is placed in a distiller for negative pressure distillation, and the pressure is set to make it boil at 75 to 85°C. When the solution was ...
Embodiment 2
[0041] The implementation conditions are basically the same as in Example 1, except that the acidic etching solution is firstly pretreated by pressurized distillation, and then distilled under reduced pressure at 75°C to 85°C. The volume of the distilled liquid is 60ml, the acid equivalent is 1.1mol / L, and the remaining The solution is 40ml, neutralized with 25% ammonia water, and the pH is adjusted to be 8 (±0.2), and the adjusted solution volume is 96ml, Cu 2+ =149.6g / L, Cl - =235g / L, pH value=8.01. Carry out extraction with oxime extractant, di-tert-butylmethylphenol or methylphenol are antioxidant, wherein, oxime content is 98wt%, antioxidant content is 2wt%, volume ratio (V / V) 30%, oil-liquid ratio ( After O / A) 3 / 1 carried out four extractions, the raffinate was clear and transparent (copper ion concentration is below 0.5g / L).
Embodiment 3
[0043] The implementation conditions are basically the same as in Example 1, the difference is: extract with β-diketone extractant, without adding antioxidant, volume ratio (V / V) 30%, oil-liquid ratio (O / A) 2 / 1 After carrying out three extractions, the raffinate is clear and transparent (copper ion concentration is below 0.5g / L).
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