| dc.contributor.author |
Parija, C. |
|
| dc.contributor.author |
Sarma, P.V.R.B. |
|
| dc.date.accessioned |
2018-10-01T12:21:46Z |
|
| dc.date.available |
2018-10-01T12:21:46Z |
|
| dc.date.issued |
2000 |
|
| dc.identifier.citation |
Hydrometallurgy, 54(2-3), 2000: 195-204 |
|
| dc.identifier.issn |
0304-386X |
|
| dc.identifier.uri |
http://ore.immt.res.in/handle/2018/876 |
|
| dc.description.abstract |
Ammoniacal-sulphate leach liquors obtained from a copper-nickel-iron concentrate were processed through solvent extraction for nickel-copper separation. Using the extractant LIX84 (40 vol.% diluted with kerosene, mainly aliphatic), 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 prior 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, nickel 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 was nearly quantitative. The spent organic retained similar to 20 g/m(3) of nickel. There was some copper co-stripping (similar to 68 g/m(3)) which is reported in the nickel-pregnant electrolyte, This copper concentration was reduced to 2.3 g/m(3) in a single stage extraction using the same solvent (40 vol.% LIX84) at an A/O ratio of 5 and the loaded organic was combined with the primary loaded organic for copper stripping, From the ammonia depleted and Ni-free loaded organic phase, copper was stripped in three counter-current stages at equal phase ratio using the spent copper electrolyte containing 30 kg/m(3) Cu and 180 kg/m(3) H2SO4. Although the spent organic retained 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-sheet is suggested for the treatment of the leach liquor based on the above results. (C) 2000 Elsevier Science B.V. All rights reserved. |
|
| dc.language |
en |
|
| dc.publisher |
Elsevier |
|
| dc.relation.isreferencedby |
SCI |
|
| dc.rights |
Copyright [2000]. All efforts have been made to respect the copyright to the best of our knowledge. Inadvertent omissions, if brought to our notice, stand for correction and withdrawal of document from this repository. |
|
| dc.subject |
Materials Sciences |
|
| dc.subject |
Materials Sciences |
|
| dc.title |
Separation of nickel and copper from ammoniacal solutions through co-extraction and selective stripping using LIX84 as the extractant |
|
| dc.type |
Journal Article |
|
| dc.affiliation.author |
CSIR-IMMT, Bhubaneswar 751013, Odisha, India |
|