• Title of article

    Modeling of adsorption isotherms and kinetics of a tannery dye onto an activated carbon prepared from an agricultural by-product

  • Author/Authors

    Baccar، نويسنده , , R. and Blلnquez، نويسنده , , P. and Bouzid، نويسنده , , J. and Feki، نويسنده , , M. and Attiya، نويسنده , , H. and Sarrà، نويسنده , , M.، نويسنده ,

  • Issue Information
    روزنامه با شماره پیاپی سال 2013
  • Pages
    8
  • From page
    408
  • To page
    415
  • Abstract
    The potential of an activated carbon prepared from an agricultural by-product for the removal of a tannery dye from aqueous solution was investigated. The effects of contact time, solution pH and temperature were evaluated. The results indicated that the equilibrium data were perfectly represented using a Langmuir isotherm. The maximum monolayer adsorption capacity was found to be 146.31 mg g− 1 at 25 °C. The kinetic studies indicated that the adsorption process followed a pseudo-second-order model. The application of an intra-particle diffusion model revealed that the adsorption mechanism of the concerned dye is a rather complex process and that diffusion is involved in the overall rate of the adsorption process, but it is not the only rate-controlling step. The calculated thermodynamics parameters revealed the spontaneous and endothermic nature of the adsorption process. The activation energy, Ea = 9.50 kJ mol− 1, could indicate a physical adsorption process. Despite the presence of other components in the real effluent, the adsorbent was able to remove the target dye. The present study indicates that activated carbon prepared from olive-waste cakes is a promising candidate as a low cost adsorbent for the removal of a tannery dye from industrial wastewater.
  • Keywords
    Olive-waste cakes , Tannery dye , Isotherm , Thermodynamics , Real effluent
  • Journal title
    Fuel Processing Technology
  • Serial Year
    2013
  • Journal title
    Fuel Processing Technology
  • Record number

    1509490