Biological metallurgy method and device based on primary battery
A biometallurgy and primary battery technology, applied in the direction of improving process efficiency, can solve the problems of limited concentration, energy loss, limited microbial tolerance, etc., and achieve the effect of reducing operating power consumption, shortening processing cycle, and improving leaching efficiency
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Embodiment 1
[0034] The iron concentration of the leaching agent was 0.5 mol / L, the sulfuric acid concentration was 1.5 mol / L, the leaching aid NaCl was 10 g / L, and the sodium lignosulfonate or calcium lignosulfonate was 2 g / L. The microorganism in the bacterial solution was Thiobacillus ferrooxidans acidophilus, the iron ion concentration was 0.05 mol / L, and the pH was adjusted to 1.5. The raw material to be leached is chalcocite (Cu 2 S), the mass concentration is 5%. The temperature of the leaching tank is 30 degrees, and the temperature of the bacteria liquid tank is 30 degrees. The diaphragm is an anion exchange membrane, the current collector is a copper plate, and the positive and negative plates are made of graphite. The reaction time was 2 days, the leaching rate of copper in chalcocite was 80.5%, the recovered electric energy was 18.4kWh / t, and the microbial metabolism fixed carbon dioxide 27.5kg / t.
[0035] When the galvanic cell biometallurgical device of this embodiment is ...
Embodiment 2
[0044] The iron concentration of the leaching agent was 0.2 mol / L, the leaching aid NaCl was 20 g / L, 5 g / L sodium lignosulfonate or calcium lignosulfonate, and the sulfuric acid concentration was 2 mol / L. The microorganism in the bacterial solution was Leptospira ferrooxidans, the iron ion concentration was 0.1 mol / L, and the pH was adjusted to 1.7. The raw material to be leached is sphalerite (ZnS) with a mass concentration of 10%. The temperature of the leaching tank is 50 degrees, and the temperature of the bacteria liquid tank is 35 degrees. The diaphragm is an anion exchange membrane, the current collector is an aluminum plate, and the positive and negative plates are made of conductive plastic. The reaction time was 2 days, the leaching rate of zinc in sphalerite was 92.3%, the recovered electricity was 15.7kWh / t, and the microbial metabolism fixed carbon dioxide 23.5kg / t.
[0045] When the galvanic cell biometallurgical device of this embodiment is in operation, anion...
Embodiment 3
[0054] The iron concentration of the leaching agent was 0.01 mol / L, the leaching aid was 30 g / L NaCl, 30 g / L sodium lignosulfonate or calcium lignosulfonate, and the sulfuric acid concentration was 5 mol / L. The microorganism in the bacterial liquid was Thiobacillus acidophilus thermophilic, the iron ion concentration was 0.01 mol / L, and the pH was adjusted to 0.5. The raw material to be leached is sphalerite (ZnS) with a mass concentration of 10%. The temperature of the leaching tank is 80 degrees, and the temperature of the bacteria liquid tank is 50 degrees. The diaphragm is an anion exchange membrane, the current collector is an aluminum plate, and the positive and negative plates are made of conductive plastic. The reaction time was 2 days, the leaching rate of zinc in sphalerite was 87.3%, the recovered electrical energy was 13.6 kWh / t, and the microbial metabolism fixed carbon dioxide 20.4 kg / t.
[0055] When the galvanic cell biometallurgical device of this embodiment...
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