Biosorption of Copper and Cadmium in Packed Bed Columns with Live Immobilized Fungal Biomass of Phanerochaete chrysosporium

被引:28
作者
Pakshirajan, K. [1 ]
Swaminathan, T. [2 ]
机构
[1] Indian Inst Technol Guwahati, Dept Biotechnol, Gauhati 781039, India
[2] Indian Inst Technol Madras, Dept Chem Engn, Madras 600036, Tamil Nadu, India
关键词
Heavy metals; Copper; Cadmium; Phanerochaete chrysosporium; Packed bed column; Immobilized fungus; Biosorption; Desorption; Breakthrough models; ACTIVATED-CARBON SYSTEMS; HEAVY-METALS; AQUEOUS-SOLUTION; ASPERGILLUS-NIGER; DYNAMIC REMOVAL; IONS; CHROMATOGRAPHY; ADSORPTION; REACTOR; MATRIX;
D O I
10.1007/s12010-008-8283-3
中图分类号
Q5 [生物化学]; Q7 [分子生物学];
学科分类号
071010 ; 081704 ;
摘要
Biosorption of copper (II) and cadmium (II) by live Phanerochaete chrysosporium immobilized by growing onto polyurethane foam material in individual packed bed columns over two successive cycles of sorption-desorption were investigated in this study. Initial pH and concentrations of the metals in their respective solutions were set optimum to each of those: 4.6 and 35 mg center dot l(-1) in case of copper and 5.3 and 11 mg center dot l(-1) for cadmium. The breakthrough curves obtained for the two metals during sorption in both the cycles exhibited a constant pattern at various bed depths in the columns. The maximum yield of the columns in removing these metals were found to be, respectively, 57% and 43% for copper and cadmium indicating that copper biosorption by the immobilized fungus in its column was better than for cadmium. Recovery values of the sorbed copper and cadmium metals from the respective loaded columns by using 0.1 N HCl as eluant was observed to be quite high at more than 65% and 75%, respectively, at the end of desorption in both the cycles. Breakthrough models of bed-depth service time, Adams-Bohart, Wolborska, and Clark were fitted to the experimental data on sorption of copper and cadmium in the columns, and only the Clark model could fit the sorption performance of the columns well over the entire range of ratios of concentrations of effluent to influent, i.e., C/C (0) for both copper and cadmium biosorption. The kinetic coefficients of mass transfer and other suitable parameters in the system were determined by applying the experimental data at C/C (0) ratios lower than 0.5 to the other three models.
引用
收藏
页码:159 / 173
页数:15
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