Recycling process of tin-removing waste liquid
A technology of tin stripping and waste liquid, which is applied in the field of recycling process of tin stripping waste liquid, can solve problems such as entrainment, affecting the quality and stability of the circuit board tin stripping process, and unavoidable chemical components, so as to achieve the process and process The effect of simple equipment, great social environmental health value, and low production cost
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Embodiment 1
[0026] [Example 1] A recycling process for tin stripping waste liquid, comprising the following steps:
[0027] S1. Pass the tin stripping waste liquid into the distillation device, at 65°C, the pressure is 0.5×1.03×10 5 Under Pa, carry out underpressure distillation and reclaim nitric acid;
[0028] S2. The above-mentioned distilled residual liquid is passed into an electrolytic cell provided with an ion exchange membrane for electrolysis, and the copper in the residual liquid is electrolyzed and recovered by controlling the current density and the cathode potential, and tin dioxide is obtained at the anode of the electrolytic cell, and metallic copper is obtained at the negative electrode;
[0029] S3. After the metal copper is recovered, the current density is controlled to remain unchanged, and the cathode potential is changed to electrolytically recover tin, and during the electrolysis process, sulfuric acid solution needs to be continuously added to the cathode chamber u...
Embodiment 2
[0035] [Example 2] A recycling process for tin stripping waste liquid, comprising the following steps:
[0036] S1. Pass the tin stripping waste liquid into the distillation device, at 70°C, the pressure is 0.4×1.03×10 5 Under Pa, carry out underpressure distillation and reclaim nitric acid;
[0037] S2. The above-mentioned distilled residual liquid is passed into an electrolytic cell provided with an ion exchange membrane for electrolysis, and the copper in the residual liquid is electrolyzed and recovered by controlling the current density and the cathode potential, and tin dioxide is obtained at the anode of the electrolytic cell, and metallic copper is obtained at the negative electrode;
[0038] S3. After the metal copper is recovered, the current density is controlled to remain unchanged, and the cathode potential is changed to electrolytically recover tin, and during the electrolysis process, sulfuric acid solution needs to be continuously added to the cathode chamber u...
Embodiment 3
[0044] [Example 3] A recycling process for tin stripping waste liquid, comprising the following steps:
[0045] S1. Pass the tin stripping waste liquid into the distillation device, at 75°C, the pressure is 0.3×1.03×10 5 Under Pa, carry out underpressure distillation and reclaim nitric acid;
[0046] S2. The above-mentioned distilled residual liquid is passed into an electrolytic cell provided with an ion exchange membrane for electrolysis, and the copper in the residual liquid is electrolyzed and recovered by controlling the current density and the cathode potential, and tin dioxide is obtained at the anode of the electrolytic cell, and metallic copper is obtained at the negative electrode;
[0047] S3. After the metal copper is recovered, the current density is controlled to remain unchanged, and the cathode potential is changed to electrolytically recover tin, and during the electrolysis process, sulfuric acid solution needs to be continuously added to the cathode chamber u...
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