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e CO conversion versus reactor length for cases of dense PdeAg MR, silica MR and TR at 623 K, H 2 O/CO ¼ 1 and 3 bar pressure. 

e CO conversion versus reactor length for cases of dense PdeAg MR, silica MR and TR at 623 K, H 2 O/CO ¼ 1 and 3 bar pressure. 

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The main purpose of present study is the theoretical analysis and the comparison of inorganic membrane reactor (MR) performances, namely, silica MR performance with respect to dense Pd-Ag MR during water gas shift (WGS) reaction. To this target, a one-dimensional, isothermal numerical model was developed and its validation was realized by literatur...

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... the other hand, Fig. 7 indicates the CO conversion along both MRs length and also versus traditional reactor (TR) length. As corresponding curve for the TR case, in which no membrane is used, it effectively depict the role of membrane in enhancing the conversion. In particular, by using PdeAg membrane, around 10% conversion enhancement was ob- tained with ...

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