Simulation of an industrial adiabatic multi-bed catalytic reactor for sulfur dioxide oxidation using the Maxwell-Stefan model
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- 作者：Miguel-Á ; ngel Gó ; mez-Garcí ; aa ; magomez@unal.edu.co" class="auth_mail" title="E-mail the corresponding author ; Izabela Dobrosz-Gó ; mezb ; Edison GilPavasc ; Jacek Rynkowskid
- 关键词：SO2 oxidation ; Adiabatic reactor ; Maxwell&ndash ; Stefan diffusion model ; Industrial reactor
- 刊名：Chemical Engineering Journal
- 出版年：2015
- 出版时间：15 December 2015
- 年：2015
- 卷：282
- 期：Complete
- 页码：101-107
- 全文大小：615 K
文摘
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A rigorous model was proposed for the analysis of a SO2 oxidation catalytic reactor.
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The Maxwell–Stefan diffusional model was justified from thermodynamic correction factor matrix.
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The model allowed evaluating the reactor behavior with errors lower than 3%.