Antimony sulfide concentrate smelting process
A technology for antimony sulfide concentrate and antimony sulfide, which is applied in the field of metallurgy and chemical industry, can solve the problems of high energy consumption and environmental pollution by arsenic-alkali slag, and achieve the effects of clean and efficient separation, improved reduction effect, and efficient extraction.
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Embodiment 1
[0056] The main components of antimony concentrate provided by a company in Hunan are: Sb 54.68%, Fe 8.76%, SiO 2 11.36%, As0.35%, Pb 0.22%, S 15.66%, Au 87g t -1 .
[0057] Take 100g of the above-mentioned antimony concentrate powder, at a shear strength of 8000 rpm, a leaching temperature of 85°C, chlorine gas as an oxidant, an oxidation potential of 460mV, a solution volume (ml): concentrate mass (g) = 5:1, and a hydrochloric acid concentration of 5mol ·L -1 And sodium lignosulfonate 0.1g / L under the condition of leaching for 90min, the leaching reaction was completed. Then add an appropriate amount of antimony sulfide concentrate to the leached pulp for reduction, the amount of antimony sulfide concentrate will be leaching the Fe in the pulp 3+ and Sb 5+ reduced to Fe 2+ and Sb 3+ 1.2 times the required theoretical amount, continue to react for 60 minutes. After the reaction is finished, the solution is filtered while it is hot to obtain leaching residue and reduced...
Embodiment 2
[0059] Take 100 g of the antimony concentrate powder in the above-mentioned embodiment 1, at a shear strength of 4000 rpm, a leaching temperature of 65° C., chlorine gas as an oxidant, an oxidation potential of 480 mV, solution volume (ml): concentrate mass (g)=4: 1. The concentration of hydrochloric acid is 7mol L -1 and calcium lignosulfonate 1.8g / L under the condition of antimony sulfide concentrate controlled potential shear enhanced leaching (wherein, the chlorine gas used is the dechlorinated back liquid membrane obtained by repeatedly carrying out repeated experiments according to the conditions in the above-mentioned embodiment 1) Chlorine produced by electrolysis). After leaching for 120min, the leaching reaction was ended. Then add an appropriate amount of antimony powder to the leached pulp for reduction. The amount of antimony powder added is the amount of Fe in the leached pulp. 3+ and Sb 5+ reduced to Fe 2+ and Sb 3+ 1.8 times the required theoretical amount...
Embodiment 3
[0061] The main components of antimony concentrate provided by a company in Hunan are: Sb 32.5%, Fe 16.9%, SiO 2 13.7%, As 1.3%, S 32.4%.
[0062]Take 1000g of the above-mentioned antimony concentrate powder, at a shear strength of 10000 rpm, a leaching temperature of 90°C, chlorine gas as an oxidant, an oxidation potential of 490mV, a solution volume (ml): concentrate mass (g) = 7:1, and a hydrochloric acid concentration of 7mol ·L -1 and sodium lignosulfonate 2g / L, after leaching for 200min, the leaching reaction was completed. Then add an appropriate amount of antimony sulfide concentrate and antimony powder (the mass ratio of antimony sulfide concentrate and antimony powder is 1:1) to the leached pulp for reduction, the addition of antimony sulfide concentrate and antimony powder is the Fe 3+ and Sb 5+ reduced to Fe 2+ and Sb 3+ 1.8 times the required theoretical amount, continue to react for 80min. After the reaction is finished, the solution is filtered while it is...
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