Method for separating sulfur from zinc sulfide concentrate
A technology for zinc sulfide concentrate and sulfur, applied in the field of metallurgy, can solve the problems of low sulfur grade and high energy consumption
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Embodiment 1
[0023] The zinc sulfide concentrate is subjected to pressure leaching treatment, and the liquid-solid ratio of sulfuric acid and zinc sulfide concentrate in the leaching process is controlled to be 5mL:1g to ensure that the pressure leaching process has an effective evaporation; the temperature of the pressure leaching process is controlled to be 125 ° C, The sulfur in the zinc sulfate concentrate leaching solution is distilled at a pressure of 10Mpa and an end-point acidity of 25g / L to ensure that sulfur exists in the form of elemental sulfur during the pressure leaching process and prevent the sulfur produced from being oxidized to SO 4 2- ;Use a closed device to collect the distilled sulfur-containing water vapor, and control the temperature in the closed device to 25°C and the pressure within the range of 0.1-0.5MPa, so as to condense the sulfur and water vapor in the sulfur-containing water vapor; when the airtight When the internal pressure of the device exceeds 0.55MPa,...
Embodiment 2
[0025] The zinc sulfide concentrate is subjected to pressure leaching treatment, and the liquid-solid ratio of sulfuric acid and zinc sulfide concentrate is controlled to be 10mL:1g during the leaching process, so as to ensure that the pressure leaching process has an effective evaporation; the temperature of the pressure leaching process is controlled to be 300°C, The sulfur in the zinc sulfate concentrate leaching solution is distilled at a pressure of 25Mpa and an end-point acidity of 65g / L to ensure that sulfur exists in the form of elemental sulfur during the pressure leaching process and prevent the sulfur produced from being oxidized to SO 4 2- ; Use a closed device to collect the distilled sulfur-containing water vapor, and control the temperature in the closed device to 65°C and the pressure within the range of 0.1-0.5 MPa, so as to condense the sulfur and water vapor in the sulfur-containing water vapor; when the airtight When the internal pressure of the device exce...
Embodiment 3
[0027]The zinc sulfide concentrate is subjected to pressure leaching treatment, and the liquid-solid ratio of sulfuric acid and zinc sulfide concentrate during the leaching process is controlled to be 6.5mL:1g to ensure effective evaporation during the pressure leaching process; the temperature during the pressure leaching process is controlled to be 175°C , the pressure is 15Mpa and the final acidity is 40g / L, the sulfur in the zinc sulfate concentrate leaching solution is distilled to ensure that the sulfur exists in the form of elemental sulfur during the pressure leaching process, and the sulfur produced is not oxidized to SO 4 2- ;Use a closed device to collect the distilled sulfur-containing water vapor, and control the temperature in the closed device to 35°C and the pressure within the range of 0.1-0.5MPa, so as to condense the sulfur and water vapor in the sulfur-containing water vapor; when the airtight When the internal pressure of the device exceeds 0.55MPa, it sha...
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