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Modelling-based Optimisation of the Direct Synthesis of Dimethyl Ether from Syngas in a Commercial Slurry Reactor

Sadegh Papari, Mohammad Kazemeini, Moslem Fattahi   

  1. Department of Chemical and Petroleum Engineering, Sharif University of Technology, Azadi Avenue 11365-9465, Tehran, Iran
  • Received:2011-10-11 Revised:2012-06-09 Online:2013-07-03 Published:2013-06-28
  • Contact: Mohammad Kazemeini

Modelling-based Optimisation of the Direct Synthesis of Dimethyl Ether from Syngas in a Commercial Slurry Reactor

Sadegh Papari, Mohammad Kazemeini, Moslem Fattahi   

  1. Department of Chemical and Petroleum Engineering, Sharif University of Technology, Azadi Avenue 11365-9465, Tehran, Iran
  • 通讯作者: Mohammad Kazemeini

Abstract: In the present study, we developed a multi-component one-dimensional mathematical model for simulation and optimisation of a commercial catalytic slurry reactor for the direct synthesis of dimethyl ether (DME) from syngas and CO2, operating in a churn-turbulent regime. DME productivity and CO conversion were optimised by tuning operating conditions, such as superficial gas velocity, catalyst concentration, catalyst mass over molar gas flow rate (W/F), syngas composition, pressure and temperature. Reactor modelling was accomplished utilising mass balance, global kinetic models and heterogeneous hydrodynamics. In the heterogeneous flow regime, gas was distributed into two bubble phases: small and large. Simulation results were validated using data obtained from a pilot plant. The developed model is also applicable for the design of large-scale slurry reactors.

Key words: modelling, slurry bubble column, optimisation, dimethyl ether synthesis, two-bubble phases

摘要: In the present study, we developed a multi-component one-dimensional mathematical model for simulation and optimisation of a commercial catalytic slurry reactor for the direct synthesis of dimethyl ether (DME) from syngas and CO2, operating in a churn-turbulent regime. DME productivity and CO conversion were optimised by tuning operating conditions, such as superficial gas velocity, catalyst concentration, catalyst mass over molar gas flow rate (W/F), syngas composition, pressure and temperature. Reactor modelling was accomplished utilising mass balance, global kinetic models and heterogeneous hydrodynamics. In the heterogeneous flow regime, gas was distributed into two bubble phases: small and large. Simulation results were validated using data obtained from a pilot plant. The developed model is also applicable for the design of large-scale slurry reactors.

关键词: modelling, slurry bubble column, optimisation, dimethyl ether synthesis, two-bubble phases