2013
DOI: 10.1016/j.cherd.2013.07.014
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The NETmix reactor: Pressure drop measurements and 3D CFD modeling

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Cited by 35 publications
(31 citation statements)
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“…The energy conservation equation, neglecting viscous dissipation, is given by true(ρcPTtrue)t+true(ρcPtrueυTtrue)=true(κTtrue) where T is the temperature, cP is the local fluid heat capacity and κ is the local fluid thermal conductivity. Viscous dissipation is neglected due to NETmix's high energy efficiency demonstrated previously . From the observations made by Fonte et al, in the operational simulation range of this study, an energy dissipation of less than 1 mW is expected, in the chaotic regime.…”
Section: Three‐dimentional Cfd Modelingsupporting
confidence: 52%
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“…The energy conservation equation, neglecting viscous dissipation, is given by true(ρcPTtrue)t+true(ρcPtrueυTtrue)=true(κTtrue) where T is the temperature, cP is the local fluid heat capacity and κ is the local fluid thermal conductivity. Viscous dissipation is neglected due to NETmix's high energy efficiency demonstrated previously . From the observations made by Fonte et al, in the operational simulation range of this study, an energy dissipation of less than 1 mW is expected, in the chaotic regime.…”
Section: Three‐dimentional Cfd Modelingsupporting
confidence: 52%
“…Viscous dissipation is neglected due to NETmix's high energy efficiency demonstrated previously. 15 From the observations made by Fonte et al, 15 in the operational simulation range of this study, an energy dissipation of less than 1 mW is expected, in the chaotic regime. These equations are solved for the following boundary conditions: no-slip condition is assumed in the walls of the domain, t wall 50; simplified uniform velocity profile is applied to the network inlet channels; parallel flow condition is applied at the network's outlet channels by imposing a simplified constant and uniform pressure profile, p out 5p 0 ; periodic boundary conditions are imposed at the symmetry surfaces of the halfchambers of the NUB model; either constant-wall temperature, T wall 5T 0 or constant-wall heat flux, _ q wall 5 _ q 0 , is imposed at both top and bottom surfaces.…”
Section: Governing Equations and Boundary Conditionssupporting
confidence: 49%
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