2002
DOI: 10.1016/s0304-386x(01)00221-3
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Effect of potential and ferric ions on lead sulfide dissolution in nitric acid

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Cited by 35 publications
(16 citation statements)
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“…The combination of brine solutions and high-temperature improved leaching but the solution chemistry is undesirable because of extensive corrosion of the steel parts of the reactors. Nitrate-based leaching was found to be more effective than sulfate and chloride leaching because of the high solubility of lead nitrate. However, the possible release of harmful nitrogen oxide gases makes it unfavorable. …”
Section: Introductionmentioning
confidence: 99%
“…The combination of brine solutions and high-temperature improved leaching but the solution chemistry is undesirable because of extensive corrosion of the steel parts of the reactors. Nitrate-based leaching was found to be more effective than sulfate and chloride leaching because of the high solubility of lead nitrate. However, the possible release of harmful nitrogen oxide gases makes it unfavorable. …”
Section: Introductionmentioning
confidence: 99%
“…According to the characterization analysis of the low-nickel matte, in order to comprehensively extract Ni, Cu, and Co from the low-nickel matte, the metal sulfide and ferronickel need to be dissolved by oxidation. Fe 3+ in an acidic solution has a strong oxidizing property and is often used for oxidation leaching of metal sulfides [34]. In addition, considering the high solubility of metal chloride generated in the leaching of metal sulfide in the chloride system, and the porous and loose form of the elemental S 0 generated by the reaction [35], it has little hindrance to the diffusion and mass transfer of the reactant at the initial stage of the reaction, which is conducive to the leaching of metal elements.…”
Section: Chemical Feasibility Of the Leaching Processmentioning
confidence: 99%
“…Hydrometallurgical routes of leaching lead concentrates have been developed progressively by testing a number of solvents to overcome such problems ( Greet and Smart, 2002 ; Aydoğan et al, 2007 ; Long et al, 2009 ; Wu et al, 2014 ). However, the chemical solvents used are reported to have a very low solubility of lead, a high corrosiveness, and very high toxicity, and a significantly high temperature (65–85°C) is required to achieve a high lead recovery as listed in Table 1 ( Warren et al, 1987 ; Pashkov et al, 2002 ; Aydoğan et al, 2007 ; Qin et al, 2009 ; Zárate-Gutiérrez et al, 2010 , 2015 ; Baba and Adekola, 2013 ; Wu et al, 2014 ; Anugrah et al, 2017 ; Allen and Igboayaka, 2019 ).…”
Section: Introductionmentioning
confidence: 99%
“…However, the bioleaching of galena (PbS) has been poorly studied, since the complete oxidation of galena leads to insoluble anglesite (PbSO 4 ) that thus precludes the recovery of lead from bioleaching and ferric sulfate leaching through conventional solvent extraction/electrowinning routes ( Da Silva et al, 2003 ; Da Silva, 2004 ). Moreover, several studies demonstrated that the elevated lead bioleaching/leaching efficiencies were achieved in the presence of NaCl ( Warren et al, 1987 ; Liao and Deng, 2004 ; Ye et al, 2017 ), FeCl 3 ( Dutrizac, 1986 ; Kim et al, 1986 ; Warren et al, 1987 ; Dutrizac and Chen, 1990 ; Long et al, 2009 ), and ferric (Fe 3+ ) ions ( Pashkov et al, 2002 ). Hence, the present study investigated the use of a local mixotrophic bacterium (identified as Citrobacter sp.)…”
Section: Introductionmentioning
confidence: 99%