Reactors, Kinetics, and Catalysis
Parametric analysis of Fischer-tropsch synthesis in a catalytic microchannel reactor
Article first published online: 2 MAR 2011
DOI: 10.1002/aic.12558
Copyright © 2011 American Institute of Chemical Engineers (AIChE)
Additional Information
How to Cite
Gumuslu, G. and Avci, A. K. (2012), Parametric analysis of Fischer-tropsch synthesis in a catalytic microchannel reactor. AIChE J., 58: 227–235. doi: 10.1002/aic.12558
Publication History
- Issue published online: 7 DEC 2011
- Article first published online: 2 MAR 2011
- Accepted manuscript online: 18 JAN 2011 12:39PM EST
- Manuscript Revised: 9 JAN 2011
- Manuscript Received: 25 SEP 2010
Funded by
- Bogazici University Research Fund. Grant Number: BAP-09HA507D
- Abstract
- Article
- References
- Cited By
Keywords:
- Fischer-Tropsch synthesis;
- heat-exchange reactor;
- microchannel reactor;
- modeling;
- temperature control
Abstract
Fischer-Tropsch synthesis (FTS) involves highly exothermic conversion of syngas to a wide range of hydrocarbons, but demands isothermal conditions due to the strong dependence of product distribution on temperature. Running FTS in microchannel reactors is promising, as the sub-millimeter dimensions can lead to significant intensification that inherently favors robust temperature control. This study involves computer-based FTS simulations in a heat-exchange integrated microchannel network composed of horizontal groups of square-shaped cooling and wall-coated, catalytic reaction channels. Effects of material type and thickness of the wall separating the channels, side length of the cooling channel, coolant flow rate, and channel wall texture on reaction temperature are investigated. Use of thicker walls with high thermal conductivities and micro-baffles on the catalytic reaction channel wall favor near-isothermal conditions. Response of reaction temperature against coolant flow rate is significant. Using cooling channels with smaller side lengths, however, is shown to be insufficient for temperature control. © 2011 American Institute of Chemical Engineers AIChE J, 2012

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