2015
DOI: 10.1016/j.proeng.2015.11.492
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Studies on Heat and Mass Transfer Limitations in Oxidative Dehydrogenation of Ethane Over Cr2O3 /Al2O3 Catalyst

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Cited by 25 publications
(10 citation statements)
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“…The Weisz-Prater criteria were used to confirm that the reaction is not diffusion-limited. [45][46][47][48] The details of calculations are provided in the supporting information. The supported catalysts were used directly for catalytic properties evaluation, without any activation/reduction in hydrogen as the synthesis conditions were maintained to get metallic/bimetallic form of copper and nickel.…”
Section: Experimental Techniquesmentioning
confidence: 99%
“…The Weisz-Prater criteria were used to confirm that the reaction is not diffusion-limited. [45][46][47][48] The details of calculations are provided in the supporting information. The supported catalysts were used directly for catalytic properties evaluation, without any activation/reduction in hydrogen as the synthesis conditions were maintained to get metallic/bimetallic form of copper and nickel.…”
Section: Experimental Techniquesmentioning
confidence: 99%
“…Mass transfer resistance of the heterogeneous catalytic reaction was checked by using the Weisz‐Prater criterion (for external diffusion from the bulk fluid to the external surface of the catalyst) and Mears criterion (for internal diffusion from the external surface into and through its pores). The mentioned internal and external mass transfer mechanisms could act as resistance which affects the rate of reaction 36 …”
Section: Diffusion Effects On Heterogeneous Reactionsmentioning
confidence: 99%
“…The Weisz‐Prater parameter ( C wp ) and Mears parameter ( C M ) were calculated by using Equations (4) and (5) 36 : CnormalWP=rnormalobsρcRP2DnormaleffCS, CM=rnormalobsρbRpnkcCnormalAb,…”
Section: Diffusion Effects On Heterogeneous Reactionsmentioning
confidence: 99%
“…The macroscopic structure of solid catalysts can affect the efficiency of heat and mass transfer in chemical conversions. [1][2][3][4][5] Solid catalysts are typically manufactured by pelleting or extruding composites of pre-catalysts, promoters and binders. [6][7][8][9][10] Although these methods can yield different catalyst shapes like grids, beads, rods or foams, these topologies are not necessarily optimal for all types of reactor and process.…”
Section: Introductionmentioning
confidence: 99%