Conversion model aids scale-up of mobil's fluid-bed MTG process
1986; Elsevier BV; Volume: 41; Issue: 4 Linguagem: Inglês
10.1016/0009-2509(86)87164-0
ISSN1873-4405
AutoresMichaël Edwards, Assaf Avidan,
Tópico(s)Petroleum Processing and Analysis
ResumoMobil'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.
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