A dissertation submitted to the Faculty of Engineering and the Built
Environment at the University of Witwatersrand, Johannesburg, in part fulfillment
of the requirements for the degree of Master of Science in
Engineering,
17 May 2018 / Traditionally, copper and cobalt are extracted from oxidised ores via
hydrometallurgical processing route. The ore is leached in sulphuric acid in reducing
conditions. This method co-extracts impurity metal values like iron and manganese,
necessitating downstream solution purification, which causes significant valuable
losses. Pregnant leach solution purification is performed through step-wise oxidation
and acid neutralisation of the leach solution. Cobalt is the most affected component in
this process due to high losses incurred during the precipitation stages. Moreover,
because the lixiviant is not recycled, the method consumes ominously high quantities
of sulphuric acid. As a result, the process must be accompanied by readily available
and cost-effective acid-making plant. In the event of an increase in the price of
sulphuric acid raw materials or a decline in the ore grade, a source of 50% of the
world’s cobalt might be rendered impracticable.
This work investigates the viability of using ammoniacal solution as an alternative
lixiviant to sulphuric acid. Ammoniacal solution forms soluble complexes with copper
and cobalt at pH and potential where iron, manganese and other impurities tend to
form precipitates. Because of the preferential leaching, downstream solution
purification can be circumvented, thereby reducing valuable losses. Furthermore,
because there is no solution altering, multi-step solution purification required, the
leach solution retains its initial pre-leaching properties, making it fully recyclable. The
recyclable nature of the lixiviant thus reduces lixiviant costs. Furthermore, an
advantage of leaching in ammonia is lower equipment costs because ammonia is less
corrosive than acid.
The feed material used in this study was an oxidised copper-cobalt ore sourced from
Katanga Region in the DRC. A size fraction analysis was undertaken in order to
determine the deportation of the copper and cobalt metals in the feed material. In the
leaching tests conducted, the effect of particle size, temperature, concentration of the
reducing agent and concentrations of ammonia and ammonium carbonate were
investigated.
The results showed that a +63-75μm size fraction had the highest grade of copper and
cobalt and was thus used for all the experiments undertaken. The results also indicated
that cobalt and copper extraction was highly influenced by temperature. It was found
that working at ambient temperature results in poor extraction of the value metal
species while raising the temperature to 80°C significantly improves the extraction of
both value metals if premature depressurising of the leach vessel is avoided.
The results also showed that there was no significant extraction advantage gained from
milling finer than -63μm. Moreover, it was found that at 80°C, 2.0M ammonia
solution, 0.4M ammonium carbonate, 300rpm, 0.4M reducing agent and 60 minutes
pre-treatment and leach time, a peak extraction of 90% could be realised for copper.
It was also noted that even better extraction efficiencies could be obtained for copper
in the absence of a reducing agent. Optimum cobalt extraction of 85% was obtained
at 80°C, 2.0M ammonia solution, 2.0M ammonium carbonate solution, 0.4M
ammonium sulphite, 60 minutes pre-treatment time and 60 minutes leaching time.
This compares well to about 40-60% recovery reported when leaching in acid.
These findings point to the conclusion that ammoniacal solution is a viable alternative
to sulphuric acid for hydrometallurgical processing of the copper-cobalt ore. / MT 2018
| Identifer | oai:union.ndltd.org:netd.ac.za/oai:union.ndltd.org:wits/oai:wiredspace.wits.ac.za:10539/26002 |
| Date | January 2018 |
| Creators | Thabane, Seliee |
| Source Sets | South African National ETD Portal |
| Language | English |
| Detected Language | English |
| Type | Thesis |
| Format | Online resource (87 leaves), application/pdf, application/pdf |
Page generated in 0.0018 seconds