Environmental Biotechnology

Electronic Journal of Biotechnology ISSN: 0717-3458 Vol. 8 No. 1, Issue of April 15, 2005
© 2005 by Pontificia Universidad Católica de Valparaíso -- Chile Received July 8, 2004 / Accepted January 20, 2005
RESEARCH ARTICLE

Removal of heavy metal from industrial wastewater using chitosan coated oil palm shell charcoal

Saifuddin M. Nomanbhay*
Chemistry Unit, Department of Engineering Sciences
College of Engineering
Universiti of Tenaga Nasional
43900 Kajang Selangor, Malaysia
Tel: 60389287285
Fax: 60389212116
E-mail: saifuddin@uniten.edu.my

Kumaran Palanisamy
Mechanical Engineering Department
College of Engineering
Universiti of Tenaga Nasional
43900 Kajang Selangor, Malaysia
Tel: 60389282296
Fax: 60389212116
E-mail: kumaran@uniten.edu.my



*Corresponding author

Financial support: Uniten Research Seed Fund – J 5100 10215.

Keywords:
chitosan bioabsorbent, chromium (III), chromium (IV), heavy metal adsorption, oil palm shell charcoal.

Abbreviations:

AOPSC: acid treated oil palm shell charcoal;
CAC: commercial activated carbon;
OPSC: Oil palm shell charcoal;
CCB: chitosan coated beads;
CCAB: chitosan coated acid treated beads.

 

 


Abstract
Full Text

This research focuses on understanding biosorption process and developing a cost effective technology for treatment of heavy metals-contaminated industrial wastewater. A new composite biosorbent has been prepared by coating chitosan onto acid treated oil palm shell charcoal (AOPSC). Chitosan loading on the AOPSC support is about 21% by weight. The shape of the adsorbent is nearly spherical with particle diameter ranging 100~150 µm. The adsorption capacity of the composite biosorbent was evaluated by measuring the extent of adsorption of chromium metal ions from water under equilibrium conditions at 25ºC. Using Langmuir isotherm model, the equilibrium data yielded the following ultimate capacity values for the coated biosorbent on a per gram basis of chitosan: 154 mg Cr/g. Bioconversion of Cr (VI) to Cr (III) by chitosan was also observed and had been shown previously in other studies using plant tissues and mineral surfaces. After the biosorbent was saturated with the metal ions, the adsorbent was regenerated with 0.1 M sodium hydroxide. Maximum desorption of the metal takes place within 5 bed volumes while complete desorption occurs within 10 bed volumes. Details of preparation of the biosorbent, characterization, and adsorption studies are presented. Dominant sorption mechanisms are ionic interactions and complexation.


Supported by UNESCO / MIRCEN network
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