Continuous adsorption of lead ions in a column packed with palm shell activated carbon.

The continuous adsorption of lead ions from aqueous solution on commercial, granular, unpretreated palm shell activated carbon (PSAC) was studied. Effect of pH, flow rates and presence of complexing agents (malonic and boric acids) were examined. The breakthrough period was longer at pH 5 indicating higher adsorption capacity of lead ions at higher pH. Increase of the flow rate, expectedly, resulted in the faster saturation of the carbon bed. Presence of complexing agents did not improve adsorption uptake of lead ions. However, presence of malonic acid resulted in smoother pH stabilization of solution compared to single lead and lead with boric acid systems. The results on continuous adsorption of lead were applied to the model proposed by Wang et al. [Y.-H. Wang, S.-H. Lin, R.-S. Juang, Removal of heavy metals ions from aqueous solutions using various low-cost adsorbents, J. Hazard. Mater. B 102 (2003) 291-302]. The agreement between experimental and modelled breakthrough curves was satisfactory at both pHs.

[1]  Wan Mohd Ashri Wan Daud,et al.  Comparison on pore development of activated carbon produced from palm shell and coconut shell. , 2004, Bioresource technology.

[2]  J. Chen,et al.  Equilibrium and kinetics of metal ion adsorption onto a commercial H-type granular activated carbon: experimental and modeling studies. , 2001, Water research.

[3]  Mohamed Kheireddine Aroua,et al.  Removal of lead from aqueous solutions on palm shell activated carbon. , 2006, Bioresource technology.

[4]  M. Aroua,et al.  Electrodeposition of copper and lead on palm shell activated carbon in a flow-through electrolytic cell , 2006 .

[5]  J. Chen,et al.  Surface modification of a granular activated carbon by citric acid for enhancement of copper adsorption , 2003 .

[6]  Xiaoyuan Wang,et al.  Removing copper, zinc, and lead ion by granular activated carbon in pretreated fixed-bed columns , 2000 .

[7]  C. Huang,et al.  The adsorption of heavy metals onto hydrous activated carbon , 1987 .

[8]  C. Moreno-Castilla,et al.  Adsorption of Humic Substances on Activated Carbon from Aqueous Solutions and Their Effect on the Removal of Cr(III) Ions , 1998 .

[9]  W. Daud,et al.  Effect of activation temperature on pore development in activated carbon produced from palm shell , 2003 .

[10]  Su Lin,et al.  Removal of heavy metal ions from aqueous solutions using various low-cost adsorbents. , 2003, Journal of hazardous materials.

[11]  J.S.J. van Deventer,et al.  The influence of pH, dissolved oxygen and organics on the adsorption of metal cyanides on activated carbon , 1991 .

[12]  M. Hashim,et al.  Adsorption and desorption characteristics of zinc on ash particles derived from oil palm waste , 2002 .

[13]  S. Dimitrova Use of granular slag columns for lead removal. , 2002, Water research.

[14]  K. H. Chu,et al.  Improved fixed bed models for metal biosorption , 2004 .

[15]  K. Kadirvelu,et al.  Removal of lead(II) by adsorption using treated granular activated carbon: batch and column studies. , 2005, Journal of hazardous materials.

[16]  G. Guo The effects of local hydrodynamics on mass transfer in disordered porous media , 2002 .

[17]  Mohd Zobir Hussein,et al.  Preparation and characterization of active carbons from oil palm shells , 1996 .

[18]  F. Monteil-Rivera,et al.  Acid/base and Cu(II) binding properties of natural organic matter extracted from wheat bran: modeling by the surface complexation model. , 2000 .

[19]  A. Lua,et al.  Adsorption of sulfur dioxide onto activated carbons prepared from oil-palm shells impregnated with potassium hydroxide , 2000 .

[20]  A. Lua,et al.  Textural and chemical properties of adsorbent prepared from palm shell by phosphoric acid activation , 2003 .

[21]  L. Hong,et al.  Elucidation of Interactions between Metal Ions and Ca Alginate-Based Ion-Exchange Resin by Spectroscopic Analysis and Modeling Simulation , 2002 .