Hydrometallurgical processing of complex copper–lead–zinc ore from the Chehel-Kureh mine

The Chehel-Kureh copper–zinc–lead deposit poses processing challenges due to complex sulphide inter-growths and unwanted lead/zinc in copper concentrate. This study evaluates roasting followed by leaching to recover metals from run-of mine (ROM) ore and bulk flotation concentrate. Key parameters including temperature, time, acid molarity, liquid-to-solid ratio, and oxidant type were optimised. Roasting ROM at 600 °C for 1 h, followed by 2 M H 2 SO 4 leaching, achieved 94.08% Cu and 94.92% Zn dissolution. For flotation concentrate, optimal conditions were 800 °C roasting and 3.5 M H 2 SO 4 leaching, yielding 86.61% Cu and 92.33% Zn recovery. Although ROM showed higher metal extraction, processing the concentrate proved more economically viable because flotation reduced feed mass by ∼88%, lowering acid consumption and energy costs.

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Publication Details

Journal
Mineral Processing and Extractive Metallurgy Transactions of the Institutions of Mining and Metallurgy
Published
2026-07-27
DOI
https://doi.org/10.1177/25726641261455501
Primary Topic
Metal Extraction and Bioleaching
Type
article
Field-Weighted Citation Impact
0.00
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article

Hydrometallurgical processing of complex copper–lead–zinc ore from the Chehel-Kureh mine

Kianoush Barani, Alireza Zare
Mineral Processing and Extractive Metallurgy Transactions of the Institutions of Mining and Metallurgy
Metal Extraction and Bioleaching
article

Hydrometallurgical processing of complex copper–lead–zinc ore from the Chehel-Kureh mine

Kianoush Barani, Alireza Zare
article en

Abstract

The Chehel-Kureh copper–zinc–lead deposit poses processing challenges due to complex sulphide inter-growths and unwanted lead/zinc in copper concentrate. This study evaluates roasting followed by leaching to recover metals from run-of mine (ROM) ore and bulk flotation concentrate. Key parameters including temperature, time, acid molarity, liquid-to-solid ratio, and oxidant type were optimised. Roasting ROM at 600 °C for 1 h, followed by 2 M H 2 SO 4 leaching, achieved 94.08% Cu and 94.92% Zn dissolution. For flotation concentrate, optimal conditions were 800 °C roasting and 3.5 M H 2 SO 4 leaching, yielding 86.61% Cu and 92.33% Zn recovery. Although ROM showed higher metal extraction, processing the concentrate proved more economically viable because flotation reduced feed mass by ∼88%, lowering acid consumption and energy costs.

Mineral Processing and Extractive Metallurgy Transactions of the Institutions of Mining and Metallurgy
Lorestan University (IR)
Affordable and clean energy
Openalex Percentile: Top 17%
Metal Extraction and Bioleaching
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