Oxidation-free thiourea leaching of gold uthig sulphur dioxide

\nThe paper summarizes research on gold recovery by the Carbon in Leach (CIL) process using thiourea by feeding sulphur dioxide by a hydroacoustic emitter. It was found that the use of such a device favors the formation of the radical OH*. The latter is the strongest oxidizing agent. One of the main regulated parameters of the plant is the pressure of pulp supply to the inlet device, which was studied. According to the results of the study, it was found that a high degree of gold recovery is achieved under the following conditions: initial concentration of H2SO4 – 0.5%, thiourea loading – 1.5 kg/t, coal loading 10 g/kg, sulphur dioxide feed –0.13 kg/t*min, ratio L:S – 1:3, slurry supply pressure to the inlet – 1.5 atm, CIL process time – 60 min. Thiourea consumption amounted to 0.57 kg/t, and sulphur dioxide – 8 kg/t. Gold recovery reached 93.5%.\n

Publication Details

Journal
Springer Link (Chiba Institute of Technology)
Published
2024-10-09
DOI
https://doi.org/10.1051/bioconf/202413006007/pdf
Primary Topic
Metal Extraction and Bioleaching
Type
article
Field-Weighted Citation Impact
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article

Oxidation-free thiourea leaching of gold uthig sulphur dioxide

Springer Link (Chiba Institute of Technology)
Metal Extraction and Bioleaching
article

Oxidation-free thiourea leaching of gold uthig sulphur dioxide

article en

Abstract

\nThe paper summarizes research on gold recovery by the Carbon in Leach (CIL) process using thiourea by feeding sulphur dioxide by a hydroacoustic emitter. It was found that the use of such a device favors the formation of the radical OH*. The latter is the strongest oxidizing agent. One of the main regulated parameters of the plant is the pressure of pulp supply to the inlet device, which was studied. According to the results of the study, it was found that a high degree of gold recovery is achieved under the following conditions: initial concentration of H2SO4 – 0.5%, thiourea loading – 1.5 kg/t, coal loading 10 g/kg, sulphur dioxide feed –0.13 kg/t*min, ratio L:S – 1:3, slurry supply pressure to the inlet – 1.5 atm, CIL process time – 60 min. Thiourea consumption amounted to 0.57 kg/t, and sulphur dioxide – 8 kg/t. Gold recovery reached 93.5%.\n

Springer Link (Chiba Institute of Technology)
Clean water and sanitation
Openalex Percentile: Top 73%
Metal Extraction and Bioleaching
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