Abstract-An improved form of the so-called ‘near-wall ’ k-8 turbulence model is proposed. The damping functions accounting for viscous effects at low Reynolds numbers are modified to yield a turbulent viscosity that properly predicts heat transfer rates over a wide range of Prandtl numbers, using a constant turbulent Prandtl number Pr, = 0.9. These modifications aimed at improving the prediction of wall fluxes, also yield a better description of mean velocity and temperature profiles as well as of mean turbulent properties
Engineering flows are generally characterised by complex strain field and turbulence structure arisi...
The paper summarizes current strategies for computing heat transfer coefficients in complex turbulen...
Engineering flows are generally characterised by complex strain field and turbulence structure arisi...
[[abstract]]An improved low Reynolds number k(theta)-(theta) turbulence model is proposed to model t...
Numerical predictions have been made of heat transfer to low-Prandtl-number fluids in pipes with con...
Numerical predictions have been made of heat transfer to low-Prandtl-number fluids in pipes with con...
Numerical predictions have been made of heat transfer to low-Prandtl-number fluids in pipes with con...
Abstract: In order to make Durbin’s υ2-f model robust and applicable for calculation of complex turb...
A new wall boundary condition for the standard Wilcox’s k ω model (1988) is proposed. The model com...
IIn ordinary fluids with Pr~1 it is well known that a two equation turbulence model with a constant ...
IIn ordinary fluids with Pr~1 it is well known that a two equation turbulence model with a constant ...
IIn ordinary fluids with Pr~1 it is well known that a two equation turbulence model with a constant ...
The Reynolds-averaged computation of turbulent flow with heat transfer most commonly introduces the...
2.42SIGLEAvailable from British Library Lending Division - LD:4371.323(CFD--84/8) / BLDSC - British ...
The modeling of near-wall turbulent heat transfer necessitates appropriate description of near-wall ...
Engineering flows are generally characterised by complex strain field and turbulence structure arisi...
The paper summarizes current strategies for computing heat transfer coefficients in complex turbulen...
Engineering flows are generally characterised by complex strain field and turbulence structure arisi...
[[abstract]]An improved low Reynolds number k(theta)-(theta) turbulence model is proposed to model t...
Numerical predictions have been made of heat transfer to low-Prandtl-number fluids in pipes with con...
Numerical predictions have been made of heat transfer to low-Prandtl-number fluids in pipes with con...
Numerical predictions have been made of heat transfer to low-Prandtl-number fluids in pipes with con...
Abstract: In order to make Durbin’s υ2-f model robust and applicable for calculation of complex turb...
A new wall boundary condition for the standard Wilcox’s k ω model (1988) is proposed. The model com...
IIn ordinary fluids with Pr~1 it is well known that a two equation turbulence model with a constant ...
IIn ordinary fluids with Pr~1 it is well known that a two equation turbulence model with a constant ...
IIn ordinary fluids with Pr~1 it is well known that a two equation turbulence model with a constant ...
The Reynolds-averaged computation of turbulent flow with heat transfer most commonly introduces the...
2.42SIGLEAvailable from British Library Lending Division - LD:4371.323(CFD--84/8) / BLDSC - British ...
The modeling of near-wall turbulent heat transfer necessitates appropriate description of near-wall ...
Engineering flows are generally characterised by complex strain field and turbulence structure arisi...
The paper summarizes current strategies for computing heat transfer coefficients in complex turbulen...
Engineering flows are generally characterised by complex strain field and turbulence structure arisi...