Author: William Owen Jones
Publisher:
ISBN:
Category : Mass transfer
Languages : en
Pages : 502
Book Description
Entry Region Mass Transfer in Turbulent Pipe Flow
Author: William Owen Jones
Publisher:
ISBN:
Category : Mass transfer
Languages : en
Pages : 502
Book Description
Publisher:
ISBN:
Category : Mass transfer
Languages : en
Pages : 502
Book Description
Entry Region Gas-phase Mass Transfer in Turbulent Pipe Flow
Author: Anand Shankar Paranjape
Publisher:
ISBN:
Category :
Languages : en
Pages : 73
Book Description
Publisher:
ISBN:
Category :
Languages : en
Pages : 73
Book Description
Solid-liquid Mass Transfer in Turbulent Pipe Flow
Author: Robert Maynard Hamilton
Publisher:
ISBN:
Category : Mass transfer
Languages : en
Pages : 302
Book Description
Publisher:
ISBN:
Category : Mass transfer
Languages : en
Pages : 302
Book Description
Analogy Between Mass and Heat Transfer with Turbulent Flow
Author: Edmund E. Callaghan
Publisher:
ISBN:
Category : Heat
Languages : en
Pages : 724
Book Description
An analysis of combined heat and mass transfer from a flat plate has been made in terms of Prandtl's simpified physical concept of the turbulent boundary layer. The results of the analysis show that tor conditioins of reasonably small heat and mass transfer, the ratio of the mass- and heat-transfer coefficients is dependent on the Reynolds number of the boundary layer, the Prandtl number of the medium of diffusion, and the Schmidt number of the diffusing fluid in the medium of diffusion. For the particular case of water evaporating into air, the ratio of mass-transfer coefficient to heat-transfer coefficient is found to be slightly greater than unity.
Publisher:
ISBN:
Category : Heat
Languages : en
Pages : 724
Book Description
An analysis of combined heat and mass transfer from a flat plate has been made in terms of Prandtl's simpified physical concept of the turbulent boundary layer. The results of the analysis show that tor conditioins of reasonably small heat and mass transfer, the ratio of the mass- and heat-transfer coefficients is dependent on the Reynolds number of the boundary layer, the Prandtl number of the medium of diffusion, and the Schmidt number of the diffusing fluid in the medium of diffusion. For the particular case of water evaporating into air, the ratio of mass-transfer coefficient to heat-transfer coefficient is found to be slightly greater than unity.
VDI Heat Atlas
Author: VDI Gesellschaft
Publisher: Springer Science & Business Media
ISBN: 3540778764
Category : Science
Languages : en
Pages : 1608
Book Description
For more than 50 years, the Springer VDI Heat Atlas has been an indispensable working means for engineers dealing with questions of heat transfer. Featuring 50% more content, this new edition covers most fields of heat transfer in industrial and engineering applications. It presents the interrelationships between basic scientific methods, experimental techniques, model-based analysis and their transfer to technical applications.
Publisher: Springer Science & Business Media
ISBN: 3540778764
Category : Science
Languages : en
Pages : 1608
Book Description
For more than 50 years, the Springer VDI Heat Atlas has been an indispensable working means for engineers dealing with questions of heat transfer. Featuring 50% more content, this new edition covers most fields of heat transfer in industrial and engineering applications. It presents the interrelationships between basic scientific methods, experimental techniques, model-based analysis and their transfer to technical applications.
Mass Transfer in Turbulent Pipe Flow
Author: W. C. Brennan
Publisher:
ISBN:
Category :
Languages : en
Pages :
Book Description
Publisher:
ISBN:
Category :
Languages : en
Pages :
Book Description
Heat Transfer in Turbulent Mixed Convection
Author: B. S. Petukhov
Publisher: Core/Mechanical
ISBN: 9780891166443
Category : Science
Languages : en
Pages : 244
Book Description
Broad coverage of buoyancy effects on convective heat transfer in duct flows. Provides an immense quantity of experimental data deriving from active and excellent research in the USSR. Acidic paper. Annotation copyright Book News Inc. Portland, Or.
Publisher: Core/Mechanical
ISBN: 9780891166443
Category : Science
Languages : en
Pages : 244
Book Description
Broad coverage of buoyancy effects on convective heat transfer in duct flows. Provides an immense quantity of experimental data deriving from active and excellent research in the USSR. Acidic paper. Annotation copyright Book News Inc. Portland, Or.
Rates of turbulent transfer to a pipe wall in the mass transfer entry region
Author: Christian von Alfthan
Publisher:
ISBN: 9789516661196
Category : Mass transfer
Languages : en
Pages : 16
Book Description
Publisher:
ISBN: 9789516661196
Category : Mass transfer
Languages : en
Pages : 16
Book Description
Mass Transfer and Chemical Reaction in Turbulent Pipe Flow
Author: Sarabjit Singh Randhava
Publisher:
ISBN:
Category : Chemical reactions
Languages : en
Pages : 388
Book Description
Publisher:
ISBN:
Category : Chemical reactions
Languages : en
Pages : 388
Book Description
Analysis of Turbulent Heat Transfer, Mass Transfer, and Friction in Smooth Tubes at High Prandtl and Schmidt Numbers
Author: Robert G. Deissler
Publisher:
ISBN:
Category : Aerodynamic heating
Languages : en
Pages : 62
Book Description
The expression for eddy diffusivity from a previous analysis was modified in order to account for the effect of kinematic viscosity in reducing the turbulence in the region close to a wall. By using the modified expression, good agreement was obtained between predicted and experimental results for heat and mass transfer at Prandtl and Schmidt numbers between 0.5 and 3000. The effects of length-to-diameter ratio and of variable viscosity were investigated for a wide range of Prandtl numbers.
Publisher:
ISBN:
Category : Aerodynamic heating
Languages : en
Pages : 62
Book Description
The expression for eddy diffusivity from a previous analysis was modified in order to account for the effect of kinematic viscosity in reducing the turbulence in the region close to a wall. By using the modified expression, good agreement was obtained between predicted and experimental results for heat and mass transfer at Prandtl and Schmidt numbers between 0.5 and 3000. The effects of length-to-diameter ratio and of variable viscosity were investigated for a wide range of Prandtl numbers.