Simulation of activity loss of fixed bed catalytic reactor of MTO conversion using percolation theory

This publication has 23 references indexed in Scilit:

• Conceptual Reactor Design for the Methanol-to-Olefins Process on SAPO-34
  Industrial & Engineering Chemistry Research, 2004
• Pore network model of deactivation of immobilized glucose isomerase in packed-bed reactors II: three-dimensional simulation at the particle level
  Chemical Engineering Science, 2002
• Modeling of catalyst deactivation
  Applied Catalysis A: General, 2001
• Methanol conversion to light olefins over SAPO-34: kinetic modeling of coke formation
  Microporous and Mesoporous Materials, 2000
• Diffusion and deactivation during methanol conversion over SAPO-34: a percolation approach
  Chemical Engineering Science, 1999
• On the Reaction Mechanism for Hydrocarbon Formation from Methanol over SAPO-34
  Journal of Catalysis, 1996
• Conversion of Methanol to Lower Olefins. Kinetic Modeling, Reactor Simulation, and Selection
  Industrial & Engineering Chemistry Research, 1995
• On the Reaction Mechanism for Hydrocarbon Formation from Methanol over SAPO-34
  Journal of Catalysis, 1994
• Concentration dependence of surface diffusion and zeolitic diffusion
  AIChE Journal, 1991
• A percolation approach for the modeling of deactivation of zeolite catalysts by coke formation
  Chemical Engineering Science, 1990