A commercial process was developed to treat a Ca-based Mo-V residue generated in Mo processing plant. Vanadium wasselectively leached using acetic acid and recovered as iron vanadate by hydro process. Process conditio...A commercial process was developed to treat a Ca-based Mo-V residue generated in Mo processing plant. Vanadium wasselectively leached using acetic acid and recovered as iron vanadate by hydro process. Process conditions for selective V leachingand iron vanadate precipitation were investigated. V recovery efficiency of 90.3% was achieved with a V content of 26.5% and an Fecontent of 29% in the iron vanadate cake suitable for ferrovanadium industry. The overall Mo recovery in the whole process was98.6%. The obtained leach residue containing 14.3% Mo with negligible impurities can be used as a feed material for the Moproduction process or ferromolybdenum industry. This simple and economical process generates two product streams from a singleoperation and has the potential to solve a long standing problem of handling such a mixed Mo？V residue.展开更多
The extraction and separation of zinc, manganese, cobalt and nickel from nickel laterite bacteria leach liquor were carried out using sodium salts of TOPS-99 and Cyanex 272 in kerosene. The unwanted metal ions were re...The extraction and separation of zinc, manganese, cobalt and nickel from nickel laterite bacteria leach liquor were carried out using sodium salts of TOPS-99 and Cyanex 272 in kerosene. The unwanted metal ions were removed by precipitation method and solvent extraction was used to extract/separate Zn, Mn, Co and Ni. The nickel laterite leach liquor which was obtained from bioleaching of chromite overburden samples contained 3.72 g/L Fe, 2.08 g/L Al, 0.44 g/L Ni, 0.02 g/L Co, 0.13 g/L Mn, 0.14 g/L Zn and 0.22 g/L Cr. From this leach liquor, 100% Fe, 96.98% Al and 70.42% Cr were removed by precipitation with Ca CO_3 at pH 4.4 followed by precipitation of remaining Al and Cr with 50% ammonia at p H 5.4. After precipitation, the extraction of Zn from the Fe, Al and Cr free leach liquor was carried out with 0.1 mol/L TOPS-99 followed by Mn extraction with 0.04 mol/L Na TOPS-99. The yields of Zn and Mn were 97.77% and 95.63%, respectively. After Mn extraction, cobalt was removed from the leach liquor using 0.0125 mol/L Na Cyanex 272 and finally nickel extraction was carried out using 0.12 mol/L Na TOPS-99 with 99.84% yield. The stripping of loaded organic（LO） phases were achieved with dilute H_2SO_4.展开更多
文摘A commercial process was developed to treat a Ca-based Mo-V residue generated in Mo processing plant. Vanadium wasselectively leached using acetic acid and recovered as iron vanadate by hydro process. Process conditions for selective V leachingand iron vanadate precipitation were investigated. V recovery efficiency of 90.3% was achieved with a V content of 26.5% and an Fecontent of 29% in the iron vanadate cake suitable for ferrovanadium industry. The overall Mo recovery in the whole process was98.6%. The obtained leach residue containing 14.3% Mo with negligible impurities can be used as a feed material for the Moproduction process or ferromolybdenum industry. This simple and economical process generates two product streams from a singleoperation and has the potential to solve a long standing problem of handling such a mixed Mo？V residue.
文摘The extraction and separation of zinc, manganese, cobalt and nickel from nickel laterite bacteria leach liquor were carried out using sodium salts of TOPS-99 and Cyanex 272 in kerosene. The unwanted metal ions were removed by precipitation method and solvent extraction was used to extract/separate Zn, Mn, Co and Ni. The nickel laterite leach liquor which was obtained from bioleaching of chromite overburden samples contained 3.72 g/L Fe, 2.08 g/L Al, 0.44 g/L Ni, 0.02 g/L Co, 0.13 g/L Mn, 0.14 g/L Zn and 0.22 g/L Cr. From this leach liquor, 100% Fe, 96.98% Al and 70.42% Cr were removed by precipitation with Ca CO_3 at pH 4.4 followed by precipitation of remaining Al and Cr with 50% ammonia at p H 5.4. After precipitation, the extraction of Zn from the Fe, Al and Cr free leach liquor was carried out with 0.1 mol/L TOPS-99 followed by Mn extraction with 0.04 mol/L Na TOPS-99. The yields of Zn and Mn were 97.77% and 95.63%, respectively. After Mn extraction, cobalt was removed from the leach liquor using 0.0125 mol/L Na Cyanex 272 and finally nickel extraction was carried out using 0.12 mol/L Na TOPS-99 with 99.84% yield. The stripping of loaded organic（LO） phases were achieved with dilute H_2SO_4.
