• Title of article

    Comparative study of two cocurrent downflow three phase catalytic fixed bed reactors: application to the sulphur dioxide catalytic oxidation on active carbon particles

  • Author/Authors

    E. Bezerra Moraes Medeiros، نويسنده , , M. Petrissans، نويسنده , , A. Wehrer، نويسنده , , A. Zoulalian، نويسنده ,

  • Issue Information
    روزنامه با شماره پیاپی سال 2001
  • Pages
    6
  • From page
    153
  • To page
    158
  • Abstract
    Classic three phase catalytic-cocurrent downflow trickle bed reactor was compared, under the same operating conditions, with a three phase cocurrent downflow vector named VERLIFIX. This reactor is an association of a Venturi device set above a fixed bed. The Venturi device allows a good gas–liquid mass transfer and an homogeneous distribution of the gas and liquid flows.The chemical reaction studied, in both reactors, is the catalytic oxidation of sulphur dioxide on active carbon particles. All experiments have been carried out at 25°C. The presence of a Venturi distributor increases the gas–liquid mass transfer, the wetting efficiency of the catalyst and improve the conversion of sulphur dioxide. The Verlifix reactor is particularly adapted for heterogeneous reactions limited by gas–liquid and solid–liquid mass transfer.
  • Keywords
    Three phase reactors , Catalytic oxidation , Sulphur dioxide , Active carbon particles
  • Journal title
    Chemical Engineering and Processing: Process Intensification
  • Serial Year
    2001
  • Journal title
    Chemical Engineering and Processing: Process Intensification
  • Record number

    417737