SEPARATION OF NICKEL AND COBALT IN SOLUTION FROM MIXED HYDROXIDE PRECIPITATE (MHP) LEACHING BY SOLVENT EXTRACTION USING VERSATIC 10 FOLLOWED BY CYANEX 272
lithium ion batteries, nickel and cobalt from nickel laterite ores are commonly prepared in the form of nickel sulfate and cobalt sulfate through leaching, purification of the pregnant leach solution, separation of nickel and cobalt and crystallization of both metals in the form of nickel sulfate...
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Format: | Final Project |
Language: | Indonesia |
Online Access: | https://digilib.itb.ac.id/gdl/view/55991 |
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Institution: | Institut Teknologi Bandung |
Language: | Indonesia |
Summary: | lithium ion batteries, nickel and cobalt from nickel laterite ores are commonly
prepared in the form of nickel sulfate and cobalt sulfate through leaching,
purification of the pregnant leach solution, separation of nickel and cobalt and
crystallization of both metals in the form of nickel sulfate and cobalt sulfate
hexahydrate. The separation of nickel and cobalt is usually carried out by the
solvent extraction (SX) method in a mixed hydroxide precipitate (MHP) or mixed
sulfide precipitate (MSP) solution. In this study, the separation of nickel and cobalt
in the solution produced by MHP leaching was carried out by SX using Versatic 10
followed by Cyanex 272 and studied the effect of various SX process variables on
the extraction of nickel and cobalt and the separation factor between the two (????Co-
Ni) and the separation factor with metals. impurities (Mg and Ca).
The pregnant leach solution was prepared by atmospheric agitation leaching of
limonite ore followed by iron precipitation, MHP precipitation, MHP re-leaching,
and SX. The SX experiment was designed with 4 variables, each of which was
varied at a certain level. A series of SX experiments were conducted to study the
effects of SX time, initial pH, ratio of organic volume to aqueous (O/A ratio), and
concentration of extractant to extraction percentage of nickel and cobalt as well as
separation factor between nickel and cobalt and separation factor of the two metals
with impurities (Mg and Ca). The concentration of nickel and cobalt in aqueous
solution was measured using Atomic Absorption Spectroscopy (AAS).
The results of experiment of the extraction stage of SX using Versatic 10 show that
The results of the SX experiment using Versatic 10 show that the effect of
increasing the processing time tends to increase the extraction percentages of nickel
and cobalt up to a certain level, which then decreases if it exceeds this time limit,
while the effect of increasing the initial pH, O/A ratio, and extractant concentration
tends to increase the extraction percentages of nickel and cobalt. The best
conditions for SX using Versatic 10 were obtained with a time of 10 minutes, initial
pH 7.0, O/A ratio 0.50, and an extractant concentration of 20% with ????Ni-Mg and ????Co-
Mg of 2526.02 and 647.93 respectively, and ????Ni-Ca and ????Co-Ca of 66.90 and 17.19,
respectively. The results of the SX experiment using Cyanex 272 showed that
increasing time tends to increase the extraction percentage of cobalt until a certain
value and decrease if it exceeds this time limit, while increasing the initial pH, O/A
ratio, and extractant concentration tends to increase the extraction percentage of
cobalt. The best condition of SX using Cyanex 272 was obtained at a time of 10
minutes, initial pH 5.5, O/A ratio 0.75, and extractant concentration of 15% with
????Co-Ni of 3871.29. |
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