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Simulation of the oxidation reaction is being carried out for two adiabatic packed-bed reactors using MATLAB. This reaction is an important industrial catalytic reaction for the production of H_2SO_4 ...in the chemical industry. The catalyst is V_2O_5 and it is a heterogeneous system. The reaction rate is complex for this non-elementary exothermic reaction. It is highly important to simulate the performance of the packed-bed reactors where two beds are operated adiabatically with an inter-stage-cooling. In this study, the effects of inlet compositions of reactants, initial pressure, feeding temperature, total inlet flow rate, reactor diameter, and catalyst particle diameter on conversion and pressure drop in both packed-bed reactors were investigated.続きを見る
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Mendeley出力
