Precipitation of arsenic as Na3AsS4 from Cu3AsS4-NaHS-NaOH leach solutions

This study investigates the feasibility of a precipitation process for the removal of arsenic from highly alkaline enargite leaching solutions in the Cu3AsS4-NaHS-NaOH system and regeneration of the leaching reagents. The main objective was to reduce elemental sulfur and subsequently oxidize arsenite (As (III)) to arsenate (As (V)) for the formation and precipitation of Na3AsS4. First, solutions with over 35g/L As were prepared with either arsenic trisulfide (As2S3) or enargite (Cu3AsS4) in the NaHS-NaOH system. These solutions were conditioned at 90A degree C followed by addition of elemental sulfur and fast cooling to 30A degree C for precipitate formation. The effect of elemental sulfur addition (sulfur/arsenic ratio), NaHS and NaOH concentrations and times for conditioning and precipitation were evaluated, as well as the recirculation of the mother liquor containing arsenic with leach reagents. The results showed that conditioning solution with high arsenic concentration at 90A degree C in NaHS (100-250g/L) and NaOH (50-100g/L), and sulfur addition at 1/2wt of arsenic in solution for 1-2h followed by fast cooling to 30A degree C and conditioning for 3-5h reduced arsenic concentration in solution by over 60%. Characterization by XRD showed Na3AsS4 as the dominant phase. Starting solutions prepared from As2S3 and Cu3AsS4 produced similar results. The recirculation of process filtrates for re-use in enargite leaching continued to give reproducible leaching results. A general overview about the objective of this work is, as we intend to discuss in our manuscript; a-[ordm(1) the feasibility of developing a precipitation process to partially remove arsenic dissolved in a Cu3AsS4-NaHS-NaOH leaching system as Na3AsS4 precipitate a-[ordm(2) the effect of elemental sulfur on oxidation of As(III) to As (V) and identify optimum conditions to precipitate Na3AsS4 a-[ordm(3) the possibility of circulating final waste water from precipitation to initial leaching stage for re-use constituting regeneration of leach reagents and water resource and containment or control of arsenic within the leaching and precipitation systems.