• Title of article

    CO2 Adsorption loop experiment with Eulerian–Lagrangian simulation

  • Author/Authors

    Clark، نويسنده , , Samuel and Snider، نويسنده , , Dale M. and Spenik، نويسنده , , James، نويسنده ,

  • Issue Information
    روزنامه با شماره پیاپی سال 2013
  • Pages
    8
  • From page
    100
  • To page
    107
  • Abstract
    A full-loop circulating fluidized bed experimental carbon capture unit was constructed at the US DOE National Energy Technology Laboratory (NETL) to study gas-particle flow behavior and provide data against which math-based simulation tools could be compared. This paper compares cold-flow experimental results with math-based simulation results using the commercially-available Barracuda® software package. The simulation was three-dimensional, and the entire full-loop system was simulated. The gas-particle flow behavior predicted by the simulation matched well with video recordings of the experiment. Pressure drop predictions across several key fluidized bed vessels also showed good agreement between simulation and experiment.
  • Keywords
    Mathematical Modeling , Fluidization , Multiphase flow , Carbon capture , CPFD , Eulerian–Lagrangian
  • Journal title
    Powder Technology
  • Serial Year
    2013
  • Journal title
    Powder Technology
  • Record number

    1703748