作者: Ali Reza Miroliaei , Farhad Shahraki , Hossein Atashi , Ramin Karimzadeh
DOI: 10.1016/J.JIEC.2012.05.003
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摘要: Abstract Hydrogenation of carbon monoxide in a fixed bed Fischer–Tropsch reactor has been simulated using computational fluid dynamics. The geometry was modeled the discrete packing method. effects reaction temperature, feed flow rate and H 2 /CO ratio on CO conversion product selectivity were investigated. mass fraction products also predicted by CFD model at different ratios. It observed that increased with increasing while decreased rate. temperature ratio.