Separation of nickel and copper from ammoniacal solutions through co-extraction and selective stripping using LIX84 as the extractant

Ammoniacal-sulphate leach liquors obtained from a copper-nickel-iron concen trate were processed through solvent extraction for nickel-copper separatio n. Using the extractant LIX84 (40 vol.% diluted with kerosene, mainly aliph atic), the two metals were co-extracted quantitatively from a leach liquor containing (in kg/m(3)) 13.8 Cu, 10.7 Ni, 90 (NH4)OH and 45 (NH4)(2)SO4 in two counter-current stages at an aqueous/organic (A/O) phase ratio of 1:2, The ammonia present in the loaded organic phase(1.92 kg/m(3)) was removed p rior to nickel stripping in a single stage scrubbing step using 6.6 kg/m(3) H2SO4 solution. The ammonia removal was similar to 99% and the nickel loss to the scrub raffinate was 26.3 g/m(3). From the NH3-depleted organic, nic kel was selectively stripped in four counter-current stages at an A:O phase ratio of 2:1. By using a spent nickel electrolyte containing 57 kg/m(3) of nickel, 12 kg/m(3) each of H3BO3 and Na2SO4 (pH 1.70), nickel stripping wa s nearly quantitative. The spent organic retained similar to 20 g/m(3) of n ickel. There was some copper co-stripping (similar to 68 g/m(3)) which is r eported in the nickel-pregnant electrolyte, This copper concentration was r educed to 2.3 g/m(3) in a single stage extraction using the same solvent (4 0 vol.% LIX84) at an A/O ratio of 5 and the loaded organic was combined wit h the primary loaded organic for copper stripping, From the ammonia deplete d and Ni-free loaded organic phase, copper was stripped in three counter-cu rrent stages at equal phase ratio using the spent copper electrolyte contai ning 30 kg/m(3) Cu and 180 kg/m(3) H2SO4. Although the spent organic retain ed similar to 0.6 kg/m(3) copper, this value remained constant on recycling the spent organic in the extraction-stripping-extraction loop. A flow-shee t is suggested for the treatment of the leach liquor based on the above res ults. (C) 2000 Elsevier Science B.V. All rights reserved.