A kind of leaching method of zinc sulfide concentrate
A zinc sulfide concentrate and leaching technology, applied in the field of wastewater treatment, can solve the problems of long processing time, cumbersome steps, and many steps, and achieve the effect of short leaching time, simple process and high leaching rate
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Embodiment 1
[0020] Embodiment 1: the grade of zinc in the zinc sulfide concentrate in this embodiment is 30%, and the mass percentage content of iron is 10%;
[0021] A kind of leaching method of zinc sulfide concentrate, concrete steps are:
[0022] Add water, excess oxidant (oxygen), zinc sulfide concentrate, and sulfur-containing additives (sulfuric acid) into the high-temperature and high-pressure reactor to obtain a reaction system. Under airtight conditions, the temperature and pressure of the reaction system in the high-temperature and high-pressure reactor are The reaction system reached the supercritical state, and reacted for 30 minutes to obtain the reaction product system, cooled to room temperature, and separated the solid-liquid phase to obtain the zinc-containing leaching solution and iron-containing oxide leaching residue; the temperature of the supercritical state was 380°C, the pressure was 40Mpa, and the sulfur-containing The molar ratio of sulfur atoms in additive (sul...
Embodiment 2
[0024] Embodiment 2: the grade of zinc in the zinc sulfide concentrate in this embodiment is 35%, and the mass percentage content of iron is 12%;
[0025] A kind of leaching method of zinc sulfide concentrate, concrete steps are:
[0026] Add water, excess oxidant (ozone), zinc sulfide concentrate, sulfur-containing additive (elemental sulfur) and dispersant (sodium lignosulfonate) into a high-temperature and high-pressure reactor to obtain a reaction system. The reaction system in the high-pressure reactor is heated and pressurized until the reaction system reaches a supercritical state, and reacted for 30 minutes to obtain a reaction product system, cooled to room temperature, and the solid-liquid phase is separated to obtain a zinc-containing leachate and an iron-containing oxide leaching residue; the supercritical state The temperature is 380°C, the pressure is 35Mpa, the molar ratio of sulfur atoms in sulfur-containing additives (elemental sulfur) to zinc atoms in zinc su...
Embodiment 3
[0028] Embodiment 3: the grade of zinc in the zinc sulfide concentrate in this embodiment is 38%, and the mass percentage content of iron is 12%;
[0029] A kind of leaching method of zinc sulfide concentrate, concrete steps are:
[0030] Add water, excess oxidant (hydrogen peroxide), zinc sulfide concentrate, and sulfur-containing additives (sulfur dioxide) into a high-temperature and high-pressure reactor to obtain a reaction system. Under airtight conditions, the temperature and pressure of the reaction system in the high-temperature and high-pressure reactor are The reaction system reaches a supercritical state, and reacts for 60 minutes to obtain a reaction product system, cools to room temperature, and separates the solid-liquid phase to obtain a zinc-containing leaching solution and an iron-containing oxide leaching residue; the temperature of the supercritical state is 460°C, the pressure is 30Mpa, and the sulfur-containing The molar ratio of sulfur atoms in the additi...
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