Environmental Engineering Research

  • 제21권2호
  • /
  • Pages.152-163
  • /
  • 2016
  • /
  • 1226-1025(pISSN)
  • /
  • 2005-968X(eISSN)
대한환경공학회 (Korean Society of Environmental Engineers)
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Mass transfer kinetics using two-site interface model for removal of Cr(VI) from aqueous solution with cassava peel and rubber tree bark as adsorbents

  • Vasudevan, M. (Civil Engineering Department, Bannari Amman Institute of Technology) ;
  • Ajithkumar, P.S. (Support In Sports (ME) LLC) ;
  • Singh, R.P. (Civil Engineering Department, Motilal Nehru National Institute of Technology) ;
  • Natarajan, N. (Civil Engineering Department, Maharaja Vijayaram Gajapathi Raj College of Engineering)
  • 투고 : 2015.12.22
  • 심사 : 2016.02.18
  • 발행 : 2016.06.30
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초록

Present study investigates the potential of cassava peel and rubber tree bark for the removal of Cr (VI) from aqueous solution. Removal efficiency of more than 99% was obtained during the kinetic adsorption experiments with dosage of 3.5 g/L for cassava peel and 8 g/L for rubber tree bark. By comparing popular isotherm models and kinetic models for evaluating the kinetics of mass transfer, it was observed that Redlich-Peterson model and Langmuir model fitted well ($R^2$ > 0.99) resulting in maximum adsorption capacity as 79.37 mg/g and 43.86 mg/g for cassava peel and rubber tree bark respectively. Validation of pseudo-second order model and Elovich model indicated the possibility of chemisorption being the rate limiting step. The multi-linearity in the diffusion model was further addressed using multi-sites models (two-site series interface (TSSI) and two-site parallel interface (TSPI) models). Considering the influence of interface properties on the kinetic nature of sorption, TSSI model resulted in low mass transfer rate (5% for cassava peel and 10% for rubber tree bark) compared to TSPI model. The study highlights the employability of two-site sorption model for simultaneous representation of different stages of kinetic sorption for finding the rate-limiting process, compared to the separate equilibrium and kinetic modeling attempts.

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