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

✍ Scribed by M. Edwards; A. Avidan


Publisher
Elsevier Science
Year
1986
Tongue
English
Weight
400 KB
Volume
41
Category
Article
ISSN
0009-2509

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✦ Synopsis


Mobil's fluid-bed Methanol-to-Gasoline (MTG) process was successfully scaled-up, from 0.04m diameter reactor, through O.lm. 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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