Internal flow of pure vapor experiencing film condensation on the walls of a straight horizontal duct is studied. The commonly occurring annular case of turbulent (or laminar) vapor flow in the core and laminar flow of the liquid condensate—with or without waves on the interface—is emphasized. We propose and implement a new methodology which models interfacial shear with the help of first-principles based theory, computations, and reliable experimental data on hear transfer rates. Other details of the flow are predicted with the help of this model. These predictions are shown to be in agreement with relevant experimental data. Correlations for film thickness, heat transfer rats, and pressure drops are given
The flow of pure saturated vapor between parallel plates, with film condensation on the bottom plate...
In this study, a computational model has been developed to predict condensation heat transfer betwee...
The paper presents accurate numerical solutions of the full 2D governing equations for steady and un...
Internal flow of pure vapor experiencing film condesation on the walls of a straight duct is studied...
Internal flow of pure vapor experiencing film condensation on the walls of a straight horizontal duc...
Internal flows of pure vapor experiencing film condensation on the bottom wall of an inclined (horiz...
Condensation of a vapor flow inside a horizontal rectangular duct, using the bottom plate as the onl...
A mathematical model was developed for the study of external turbulent film condensation of pure vap...
Interfacial waves on condensate films inside ducts increase heat transfer rates and lead to changes ...
This article presents accurate numerical solutions of the full 2D governing equations for steady and...
A mathematical model is developed for the study of external turbulent film condensation of pure vap...
The analysis of heat transfer design methods in condensing inside plain tubes under existing influen...
Condensation heat transfer in an annular flow regime with and without interfacial waves was experime...
The flow or pure saturated vapor between horizontal parallel plates, with film condensation on the b...
The flow or pure saturated vapor between horizontal parallel plates, with film condensation on the b...
The flow of pure saturated vapor between parallel plates, with film condensation on the bottom plate...
In this study, a computational model has been developed to predict condensation heat transfer betwee...
The paper presents accurate numerical solutions of the full 2D governing equations for steady and un...
Internal flow of pure vapor experiencing film condesation on the walls of a straight duct is studied...
Internal flow of pure vapor experiencing film condensation on the walls of a straight horizontal duc...
Internal flows of pure vapor experiencing film condensation on the bottom wall of an inclined (horiz...
Condensation of a vapor flow inside a horizontal rectangular duct, using the bottom plate as the onl...
A mathematical model was developed for the study of external turbulent film condensation of pure vap...
Interfacial waves on condensate films inside ducts increase heat transfer rates and lead to changes ...
This article presents accurate numerical solutions of the full 2D governing equations for steady and...
A mathematical model is developed for the study of external turbulent film condensation of pure vap...
The analysis of heat transfer design methods in condensing inside plain tubes under existing influen...
Condensation heat transfer in an annular flow regime with and without interfacial waves was experime...
The flow or pure saturated vapor between horizontal parallel plates, with film condensation on the b...
The flow or pure saturated vapor between horizontal parallel plates, with film condensation on the b...
The flow of pure saturated vapor between parallel plates, with film condensation on the bottom plate...
In this study, a computational model has been developed to predict condensation heat transfer betwee...
The paper presents accurate numerical solutions of the full 2D governing equations for steady and un...