Abstract
In a flow system for vapor/solid catalytic reactions, there is a concentration distribution along the external catalyst surface, observed in the vicinity of the surface. Change in the reaction rate constant is followed for the case where the concentration distribution varies by flow. A 2-dimensional numerical model in which flow field and property conditions are simplified is used to analyze the change on the assumption that high-activity and low-activity sites are regularly distributed over the external catalyst surface. The transport equations for the reactants are numerically solved for given flow fields. It is found that the concentration distribution shape and equivalent reaction rate constant are almost the same as those in a stationary system at Pecret number of around 10 or lower, the concentration distribution gradually becomes uniform whereas equivalent rate constant increases as flow rate increases at Pecret number in a range from around 10 to 10{sup 6}, and they are almost constant at Pecret number beyond around 10{sup 6}. 3 refs., 11 figs., 1 tab.
Konno, J
[1]
- National Institute for Resources and Environment, Tsukuba (Japan)
Citation Formats
Konno, J.
Change in concentration distribution and equivalent rate constant with flow velocity in a boundary layer around a catalyst of non-uniform surface activity; Kotai shokubai taihyomen no kassei no fukin`itsusei ni motozuku kankyo sonai nodo bunpu oyobi toka hanno sokudo teisu no ryusoku ni yoru henka.
Japan: N. p.,
1997.
Web.
Konno, J.
Change in concentration distribution and equivalent rate constant with flow velocity in a boundary layer around a catalyst of non-uniform surface activity; Kotai shokubai taihyomen no kassei no fukin`itsusei ni motozuku kankyo sonai nodo bunpu oyobi toka hanno sokudo teisu no ryusoku ni yoru henka.
Japan.
Konno, J.
1997.
"Change in concentration distribution and equivalent rate constant with flow velocity in a boundary layer around a catalyst of non-uniform surface activity; Kotai shokubai taihyomen no kassei no fukin`itsusei ni motozuku kankyo sonai nodo bunpu oyobi toka hanno sokudo teisu no ryusoku ni yoru henka."
Japan.
@misc{etde_605073,
title = {Change in concentration distribution and equivalent rate constant with flow velocity in a boundary layer around a catalyst of non-uniform surface activity; Kotai shokubai taihyomen no kassei no fukin`itsusei ni motozuku kankyo sonai nodo bunpu oyobi toka hanno sokudo teisu no ryusoku ni yoru henka}
author = {Konno, J}
abstractNote = {In a flow system for vapor/solid catalytic reactions, there is a concentration distribution along the external catalyst surface, observed in the vicinity of the surface. Change in the reaction rate constant is followed for the case where the concentration distribution varies by flow. A 2-dimensional numerical model in which flow field and property conditions are simplified is used to analyze the change on the assumption that high-activity and low-activity sites are regularly distributed over the external catalyst surface. The transport equations for the reactants are numerically solved for given flow fields. It is found that the concentration distribution shape and equivalent reaction rate constant are almost the same as those in a stationary system at Pecret number of around 10 or lower, the concentration distribution gradually becomes uniform whereas equivalent rate constant increases as flow rate increases at Pecret number in a range from around 10 to 10{sup 6}, and they are almost constant at Pecret number beyond around 10{sup 6}. 3 refs., 11 figs., 1 tab.}
journal = []
issue = {4}
volume = {6}
journal type = {AC}
place = {Japan}
year = {1997}
month = {Sep}
}
title = {Change in concentration distribution and equivalent rate constant with flow velocity in a boundary layer around a catalyst of non-uniform surface activity; Kotai shokubai taihyomen no kassei no fukin`itsusei ni motozuku kankyo sonai nodo bunpu oyobi toka hanno sokudo teisu no ryusoku ni yoru henka}
author = {Konno, J}
abstractNote = {In a flow system for vapor/solid catalytic reactions, there is a concentration distribution along the external catalyst surface, observed in the vicinity of the surface. Change in the reaction rate constant is followed for the case where the concentration distribution varies by flow. A 2-dimensional numerical model in which flow field and property conditions are simplified is used to analyze the change on the assumption that high-activity and low-activity sites are regularly distributed over the external catalyst surface. The transport equations for the reactants are numerically solved for given flow fields. It is found that the concentration distribution shape and equivalent reaction rate constant are almost the same as those in a stationary system at Pecret number of around 10 or lower, the concentration distribution gradually becomes uniform whereas equivalent rate constant increases as flow rate increases at Pecret number in a range from around 10 to 10{sup 6}, and they are almost constant at Pecret number beyond around 10{sup 6}. 3 refs., 11 figs., 1 tab.}
journal = []
issue = {4}
volume = {6}
journal type = {AC}
place = {Japan}
year = {1997}
month = {Sep}
}