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• W2044951034 abstract "A model is developed for industrial steam reformers for both top fired and side fired furnaces. The catalyst tube model is a one-dimensional heterogeneous model with intra-particle diffusional resistances. The two point boundary value differential equations of the catalyst pellets are solved using a modified novel orthogonal collocation technique to obtain the effectiveness factor variation along the length of the reactor. The side fired furnace equations are algebraic equations, the top fired furnace equations are two-point boundary value differential equations which are solved using the orthogonal collocation technique. A recently developed more general rate expression is used. The model performance is checked against industrial steam reformers. The model is used to investigate the effect of various parameters on the behaviour of the catalyst tubes and the furnace. The effectiveness factor variation along the length of the catalyst tube is also analysed." @default.
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• W2044951034 date "1988-01-01" @default.
• W2044951034 modified "2023-10-18" @default.
• W2044951034 title "Simulation of steam reformers for methane" @default.
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• W2044951034 doi "https://doi.org/10.1016/0009-2509(88)87044-1" @default.
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