2016
DOI: 10.1016/j.cej.2015.12.018
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Acetophenone hydrogenation on Rh/Al2O3 catalyst: Intrinsic reaction kinetics and effects of internal diffusion

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Cited by 22 publications
(13 citation statements)
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“…46 The adsorption of HKUST–Fe 3 O 4 for RhB was also controlled by external diffusion (i.e., surface adsorption and liquid film diffusion). 46 In addition, Langmuir and Freundlich isotherm models were employed to analyze the adsorption mechanism of HKUST–Fe 3 O 4 for RhB of different concentrations. 47 Compared with the correlation coefficients ( R 2 ) in Table 2, it was found that the Freundlich model gave a better fitting than the Langmuir model, suggesting that the binding sites were heterogeneous with multiple binding interactions.…”
Section: Resultsmentioning
confidence: 99%
“…46 The adsorption of HKUST–Fe 3 O 4 for RhB was also controlled by external diffusion (i.e., surface adsorption and liquid film diffusion). 46 In addition, Langmuir and Freundlich isotherm models were employed to analyze the adsorption mechanism of HKUST–Fe 3 O 4 for RhB of different concentrations. 47 Compared with the correlation coefficients ( R 2 ) in Table 2, it was found that the Freundlich model gave a better fitting than the Langmuir model, suggesting that the binding sites were heterogeneous with multiple binding interactions.…”
Section: Resultsmentioning
confidence: 99%
“…It is assumed that only the target product PE is generated to simplify the calculation. The hydrogenation of AP using the Ni–B–P/SiO 2 catalyst can be described by the L–H‐type rate mechanism . It is assumed that the adsorption of AP on the Ni–B–P/SiO 2 catalyst is stronger than that of hydrogen while the product is not adsorbed.…”
Section: Resultsmentioning
confidence: 99%
“…[12][13][14][15][16] However, these traditional reactors possess a few intrinsic problems: (i) the diffusion of reactants and/or products is hindered by limited diffusion channels within the catalytic zone, which result in decreased reaction rates and poor product selectivity. [17][18][19][20] (ii) poor thermal conductivity and mechanical strength in catalyst supports can lead to catalyst sintering and structural degradation during these reactions. [21][22][23] (iii) the post-reaction, separation of the catalyst from the products increases the operational cost.…”
Section: Introductionmentioning
confidence: 99%