The High Temperature Co-Processing of Nickel Sulfide and Nickel Laterite Sources

The pressure oxidation of low-grade nickel sulfide concentrate with high iron sulfides content generates significant amounts of sulfuric acid that must be neutralized. This acid can be utilized to leach metal values from ores such as nickel laterites. The present study demonstrates the use of a low-...

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Main Authors: Robbie G. McDonald, Jian Li
Format: Article
Language:English
Published: MDPI AG 2020-04-01
Series:Minerals
Subjects:
Online Access:https://www.mdpi.com/2075-163X/10/4/351
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spelling doaj-6ba605dab0f04e18b53281268a90e5422020-11-25T02:28:54ZengMDPI AGMinerals2075-163X2020-04-011035135110.3390/min10040351The High Temperature Co-Processing of Nickel Sulfide and Nickel Laterite SourcesRobbie G. McDonald0Jian Li1CSIRO Mineral Resources, PO Box 7229, Karawara, WA 6152, AustraliaCSIRO Mineral Resources, PO Box 7229, Karawara, WA 6152, AustraliaThe pressure oxidation of low-grade nickel sulfide concentrate with high iron sulfides content generates significant amounts of sulfuric acid that must be neutralized. This acid can be utilized to leach metal values from ores such as nickel laterites. The present study demonstrates the use of a low-grade nickel concentrate generated from Poseidon Nickel Mt Windarra ore to enable additional nickel and cobalt extraction from a Bulong Nickel Operation nickel laterite blend. The co-processing of these materials at 250 °C, with oxygen overpressure, using total pulp densities of 30% or 40% w/w, and a range of nickel concentrate to nickel laterite mass ratios between 0.30–0.53, yielded base metal extractions of 95% or greater. The final free acid range was between 21.5–58.5 g/L, which indicates that enough in situ sulfuric acid was generated during co-processing. The acid was shown from mineralogical analysis to be efficiently utilized to dissolve the laterite ore, which indicates that the primary iron hydrolysis product was hematite, while the aluminum-rich sodium alunite/jarosite phase that formed hosts approximately 5% of the hydrolyzed iron.https://www.mdpi.com/2075-163X/10/4/351nickel lateritenickel sulfidehigh pressure acid leachingco-processingpressure oxidationQXRD analysis
collection DOAJ
language English
format Article
sources DOAJ
author Robbie G. McDonald
Jian Li
spellingShingle Robbie G. McDonald
Jian Li
The High Temperature Co-Processing of Nickel Sulfide and Nickel Laterite Sources
Minerals
nickel laterite
nickel sulfide
high pressure acid leaching
co-processing
pressure oxidation
QXRD analysis
author_facet Robbie G. McDonald
Jian Li
author_sort Robbie G. McDonald
title The High Temperature Co-Processing of Nickel Sulfide and Nickel Laterite Sources
title_short The High Temperature Co-Processing of Nickel Sulfide and Nickel Laterite Sources
title_full The High Temperature Co-Processing of Nickel Sulfide and Nickel Laterite Sources
title_fullStr The High Temperature Co-Processing of Nickel Sulfide and Nickel Laterite Sources
title_full_unstemmed The High Temperature Co-Processing of Nickel Sulfide and Nickel Laterite Sources
title_sort high temperature co-processing of nickel sulfide and nickel laterite sources
publisher MDPI AG
series Minerals
issn 2075-163X
publishDate 2020-04-01
description The pressure oxidation of low-grade nickel sulfide concentrate with high iron sulfides content generates significant amounts of sulfuric acid that must be neutralized. This acid can be utilized to leach metal values from ores such as nickel laterites. The present study demonstrates the use of a low-grade nickel concentrate generated from Poseidon Nickel Mt Windarra ore to enable additional nickel and cobalt extraction from a Bulong Nickel Operation nickel laterite blend. The co-processing of these materials at 250 °C, with oxygen overpressure, using total pulp densities of 30% or 40% w/w, and a range of nickel concentrate to nickel laterite mass ratios between 0.30–0.53, yielded base metal extractions of 95% or greater. The final free acid range was between 21.5–58.5 g/L, which indicates that enough in situ sulfuric acid was generated during co-processing. The acid was shown from mineralogical analysis to be efficiently utilized to dissolve the laterite ore, which indicates that the primary iron hydrolysis product was hematite, while the aluminum-rich sodium alunite/jarosite phase that formed hosts approximately 5% of the hydrolyzed iron.
topic nickel laterite
nickel sulfide
high pressure acid leaching
co-processing
pressure oxidation
QXRD analysis
url https://www.mdpi.com/2075-163X/10/4/351
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