论文信息 - Conversion model aids scale-up of mobil's fluid-bed MTG process

Conversion model aids scale-up of mobil's fluid-bed MTG process

Abstract Mobil's fluid-bed Methanol-to-Gasoline (MTG) process was successfully scaled-up, from 0.04m diameter reactor, through 0.1m, to 0.6m diameter demonstration plant. Gas tracer responses in cold flow models were interpreted by a one-dimensional axial dispersion model, and combined with reaction kinetics to develop a conversion model.

A. Avidan | M. Edwards | A. Avidan | M. Edwards

[1] S. E. Voltz,et al. Process Variable Effects in the Conversion of Methanol to Gasoline in a Fluid Bed Reactor , 1978 .

[2] M Kwauk,et al. Fluid Beds: At Last, Challenging Two Entrenched Practices , 1985, Science.

[3] C. K. Lee,et al. Predicting fluid‐bed reactor efficiency using adsorbing gas tracers , 1987 .