1996
DOI: 10.1016/0043-1354(96)00118-2
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Strategies to maximize the microbial leaching of lead from metal-contaminated aquatic sediments

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Cited by 29 publications
(17 citation statements)
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“…Chen and Lin (2004) and Chartier and Couillard (1997) have also reported a similar trend for lead while working on bioleaching heavy metals from contaminated sediments by sulfur oxidizing bacteria and A. ferrooxidans, respectively. The reason for low solubility of lead during bioleaching is attributed to its tendency to form a less soluble compound (lead sulfate) with sulfate produced during oxidation of elemental sulfur (Mercier et al 1996). Figure 5 shows zinc solubilization from soil during bioleaching.…”
Section: Heavy Metal Solubilization During Bioleachingmentioning
confidence: 98%
“…Chen and Lin (2004) and Chartier and Couillard (1997) have also reported a similar trend for lead while working on bioleaching heavy metals from contaminated sediments by sulfur oxidizing bacteria and A. ferrooxidans, respectively. The reason for low solubility of lead during bioleaching is attributed to its tendency to form a less soluble compound (lead sulfate) with sulfate produced during oxidation of elemental sulfur (Mercier et al 1996). Figure 5 shows zinc solubilization from soil during bioleaching.…”
Section: Heavy Metal Solubilization During Bioleachingmentioning
confidence: 98%
“…Both Wong and Henry (1983) and Blais et al (1992b) reported significantly higher cadmium solubilization (80%) than Ni solubilization from the same sludge samples. Mercier et al (1996) reported that microbial leaching processes were capable of solubilizing 80% Cd, 73% Cu, and 90% Cu from heavily contaminated sediments.…”
Section: Comparison Between Bioleaching and Acid Leachingmentioning
confidence: 99%
“…To avoid nutrient limitations, the leaching reactors also contained the following nutrient concentrations: (NH 4 ) 2 SO 4 , 3 g/L -1 ; KH 2 PO 4 , 0.5 g/L -1 ; MgSO 4 , 0.5 g/L -1 ; Ca(NO 3 ) 2 , 0.01 g/L -1 ; KCl, 0.1 g/L -1 ; FeCl 2 , 37.0 g/L -1 ). Ferrous chloride (FeCl 2 ) as a substrate was used to avoid the generation of jarosite with yellow precipitates due to sulfate (Mercier et al 1996). Oxygen and carbon dioxide were supplied by aeration at a rate of 50-100 cm 3 /L of medium/ min and the contents of each reactor were mixed with a magnetic stirrer at 100 rpm.…”
Section: Solubilizationmentioning
confidence: 99%
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“…The bacterial population adapted well to the FeCl, but not to the substitution of HCl for H 2 SO 4 in initial acidification of the system, due to either chloride intolerance or to a sulfate requirement. Further research is needed to optimize lead solublization by these methods, but the leaching technique for the other metals appears ready for implementation (Mercier et al 1996).…”
Section: Microbial Leachingmentioning
confidence: 99%