Separation and recovery of cobalt and aluminium from spent gas-to-liquid catalysts using CYANEX® 272

In the field of Fischer-Tropsch synthesis catalysts, cobalt, platinum, and aluminium are the primary metal constituents of the conventionally used cobalt catalyst. While platinum recovery remains a focal point in this field, a recent endeavour by a South African company emerged, which aimed to recover cobalt and aluminium from spent Fischer-Tropsch synthesis catalysts for potential use in the agricultural sector. This study aimed to optimally separate cobalt and aluminium from spent Fischer-Tropsch synthesis catalyst for this purpose. It further leverages the OLI® database to predict metal speciation during solvent extraction to aid with experimental planning. Shake-out tests were conducted to determine optimal separation conditions, which were validated using three distinct methods: (i) evaluating the experimental error, (ii) comparing results with similar research, and (iii) validating results against the OLI® database. The investigation revealed the pivotal role of the aqueous pH yielding effective separation at pH 3.13 ([H2SO4] = 2.5 x 10-4 M) when using 20 vol.% CYANEX® 272 and 50 mol.% pre-neutralisation. Effective cobalt scrubbing was achieved with 50 g/L Al at pH 2.8, while successful stripping required 1 M H2SO4. Competitive interactions between complexing aluminium and cobalt species were observed when contacting with CYANEX® 272 at a pH < 4. Equipment design analysis for a targeted separation efficiency of 87% dictated the necessity of two mixer stages and a settler measuring 1.5 m x 1.5 m x 6.0 m (height x width x length). This settler would ensure sufficient residence time for gravity separation at a flow rate of 10 m3/h.

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Publication Details

Journal
Journal of the Southern African Institute of Mining and Metallurgy
Published
2025-06-06
DOI
https://doi.org/10.17159/2411-9717/713/2025
Primary Topic
Extraction and Separation Processes
Type
article
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article

Separation and recovery of cobalt and aluminium from spent gas-to-liquid catalysts using CYANEX® 272

D.J. van der Westhuizen, Henning M. Krieg, Martin Krüger
Journal of the Southern African Institute of Mining and Metallurgy
Extraction and Separation Processes
article

Separation and recovery of cobalt and aluminium from spent gas-to-liquid catalysts using CYANEX® 272

D.J. van der Westhuizen, Henning M. Krieg, Martin Krüger
article en

Abstract

In the field of Fischer-Tropsch synthesis catalysts, cobalt, platinum, and aluminium are the primary metal constituents of the conventionally used cobalt catalyst. While platinum recovery remains a focal point in this field, a recent endeavour by a South African company emerged, which aimed to recover cobalt and aluminium from spent Fischer-Tropsch synthesis catalysts for potential use in the agricultural sector. This study aimed to optimally separate cobalt and aluminium from spent Fischer-Tropsch synthesis catalyst for this purpose. It further leverages the OLI® database to predict metal speciation during solvent extraction to aid with experimental planning. Shake-out tests were conducted to determine optimal separation conditions, which were validated using three distinct methods: (i) evaluating the experimental error, (ii) comparing results with similar research, and (iii) validating results against the OLI® database. The investigation revealed the pivotal role of the aqueous pH yielding effective separation at pH 3.13 ([H2SO4] = 2.5 x 10-4 M) when using 20 vol.% CYANEX® 272 and 50 mol.% pre-neutralisation. Effective cobalt scrubbing was achieved with 50 g/L Al at pH 2.8, while successful stripping required 1 M H2SO4. Competitive interactions between complexing aluminium and cobalt species were observed when contacting with CYANEX® 272 at a pH < 4. Equipment design analysis for a targeted separation efficiency of 87% dictated the necessity of two mixer stages and a settler measuring 1.5 m x 1.5 m x 6.0 m (height x width x length). This settler would ensure sufficient residence time for gravity separation at a flow rate of 10 m3/h.

Journal of the Southern African Institute of Mining and MetallurgyVol. 125(5)
North-West University (ZA)
Openalex Percentile: Top 87%
Extraction and Separation Processes
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Separation and recovery of cobalt and aluminium from spent gas-to-liquid catalysts using CYANEX® 272 — D.J. van der Westhuizen, Henning M. Krieg, et al. · Journal of the Southern African Institute of Mining and Metallurgy (2025) | TGRS Research Map | TGRS