A method for extracting Pb, In, Ag from indium-containing lead silver slag
A lead-silver slag, sponge lead technology, applied in the improvement of process efficiency, photography technology, instruments and other directions, can solve the problems of waste of resources, large equipment investment, indium can not be recovered, etc., to achieve full recovery, improve production efficiency, The effect of improving filtration performance
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0020] A batch of raw materials containing zinc 11.28%, Pb3.51%, Fe12.47%, Si15.83%, In652g / t, Ag273g / t are reduced, oxidized, roasted and volatilized in a rotary kiln to obtain cloth bag powder, which is leached twice with sulfuric acid The indium-containing lead silver slag obtained after separating and extracting Zn and In has the following chemical composition: Pb45.04%, In356g / t, Ag279g / t, Zn 2.15%, Fe 1.14%, Si4.36%. Alkaline leaching of Pb from silver slag: take 200g of indium-containing lead silver slag, carry out alkaline leaching once according to liquid-solid ratio L / S=4, leaching solution NaOH (=250g / L, temperature 85°C, stirring time 2h; once leaching slag Then according to L / S=8, leaching solution NaOH (=250g / L, temperature 85°C, stirring time 3h, carry out leaching twice. The content of primary leaching solution (1000mL) is: Pb58.7g / L, Zn2.65g / L, In content; secondary leaching liquid (800mL) content: Pb14.3g / L, Zn1.04g / L; secondary leaching residue (81.5g) conte...
Embodiment 2
[0022] Adopt one-time alkaline immersion solution (1000mL) in embodiment 1 to carry out electrolysis Pb, electrolysis condition is: with stainless steel plate as cathode and anode plate, pole distance L=80cm, cell voltage is 1.2V, and current density is 150A / m 2 , electrolysis temperature 35 ℃, electrolysis time 8h; electrolysis sponge lead 43.2g, electrolysis raffinate containing Pb16.4g / L.
Embodiment 3
[0024] Adopt the indium-containing lead-silver slag to carry out NH earlier in the embodiment one 4 F solution is washed, and the slag is alkaline leached Pb by the condition of example 1 again, NH 4 F solution washing conditions are: liquid-solid ratio L / S=6, NH 4 The amount of F added is 10g / L, the temperature is 70°C, the stirring time is 1h, and the washing liquid contains H 2 SO 4 8.54g / L, Zn1.34g / L, In 9.6mg / L; secondary alkaline leaching residue (71.4g) content: Pb12.17%, In914g / t, Ag703g / t, Zn 1.05%; leaching rate ( Slag meter): Pb90.35%; twice alkaline leaching filtration speed is faster.
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More 
