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• W2892579802 abstract "By increasing industrial development and social welfare growth, demand for industrial chemicals is increasing. Over the past few decades, there has been significant advances in meeting the chemical needs of the growing population, while the adverse effects on our environment have been minimized. In the present research on reactor structure modeling, a shell and tube reactor, including two Steam Reforming of Methane (SRM) and Oxidative Coupling of Methane (OCM) processes, was investigated. In this reactor, catalysts of the OCM process were placed on the tube side and the catalysts of the SRM are in the shell side. Regarding that the reactions of the SRM process are endothermic and the reactions of the OCM process are exothermic, the heat transfer was carried out through the wall of the pipe and the required heat for the SRM process was provided from the heat generated by the OCM process. Investigating the effects of the total heat transfer coefficient on performance of each of the two reactors showed that with an increase in the total heat transfer coefficient, the C2 yield in the OCM reactor would decrease in high ratios of methane to oxygen and this ratio increased to 6 times. In addition, by increasing the overall heat transfer coefficient, the output hydrogen yield of the SRM process increases up to 50 percent. In fact, increasing the overall heat transfer coefficient significantly affects the yield of the desired products including that of the ethylene at the output of the OCM reactor for up to 5%." @default.
• W2892579802 created "2018-10-05" @default.
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• W2892579802 date "2018-11-01" @default.
• W2892579802 modified "2023-10-16" @default.
• W2892579802 title "The effect of heat transfer on products of a thermally coupled shell and tube reactor consisting of two processes: Steam reforming of methane and oxidative coupling of methane" @default.
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• W2892579802 doi "https://doi.org/10.1016/j.cep.2018.09.008" @default.
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