• Title of article

    Intensification principle of a new three-phase catalytic slurry reactor. Part II: Eco-efficiency and techno-economic performances

  • Author/Authors

    Machefer، Stephan نويسنده , , Stephan and Falk، نويسنده , , Laurent and de Panthou، نويسنده , , Fabrice، نويسنده ,

  • Issue Information
    روزنامه با شماره پیاپی سال 2013
  • Pages
    10
  • From page
    267
  • To page
    276
  • Abstract
    In two papers, the concept and the performances of a new continuous intensified reactor named RAPTOR® (French acronym for Reactor with Polyvalent Rectilinear Stirred Reactor with Optimised Transfer) are presented. on flow, heat and mass transfer characterisations and real hydrogenation experiments, Paper I presented a simple analytical model based on characteristic times that enables to explain the intensified performances compared with a semi-batch stirred reactor and to generalise the operability, rapidity and the flexibility of this minireactor. In Paper II (this article), the model is used to evaluate in a comparative study the eco-efficiency and the techno-economical advantages of a continuous process involving a RAPTOR® versus a classical batch process equipped with a stirred reactor. Economical, environmental aspects are considered as well as productivity, safety and process control.
  • Keywords
    economy , Batch to continuous , environment , Productivity , Ortho-cresol , Hydrogenation , Process intensification , eco-efficiency , Minireactor , Multiphase reaction
  • Journal title
    Chemical Engineering and Processing: Process Intensification
  • Serial Year
    2013
  • Journal title
    Chemical Engineering and Processing: Process Intensification
  • Record number

    1611275