ON THE CONJUGATED HEAT TRANSFER PROBLEMS INVOLVING FILM CONDENSATION IN THE PRESENCE OF A NONCONDENSABLE GAS

Author(s):  
Karoline da Costa Rocha Fernandes Ferreira ◽  
Kleber Marques Lisbôa
Author(s):  
Géssica R. Silva ◽  
Diego C. Knupp ◽  
Carolina P. Naveira-Cotta ◽  
Renato M. Cotta ◽  
Antônio J. Silva Neto

Author(s):  
Huijun Li ◽  
Wenping Peng ◽  
Yingguang Liu ◽  
Chao Ma

Based on the double boundary layer theory, a generalized mathematical model was developed to study the distributions of gas film, liquid film, and heat transfer coefficient along the tube surface with different geometries and curvatures for film condensation in the presence of a noncondensable gas. The results show that: (i) for tubes with the same geometry, gas film thickness, and liquid film thickness near the top of the tube decrease with the increasing of curvature and the heat transfer rate increases with it. (ii) For tubes with different geometries, one need to take into account all factors to compare their overall heat transfer rate including gas film thickness, liquid film thickness and the separating area. Besides, the mechanism of the drainage and separation of gas film and liquid film was analyzed in detail. One can make a conclusion that for free convection, gas film never separate since parameter A is always positive, whereas liquid film can separate if parameter B becomes negative. The separating angle of liquid film decreases with the increasing of curvature.


Author(s):  
Diego C. Knupp ◽  
Carolina P. Naveira Cotta ◽  
Renato M. Cotta

The present work is an extension of a novel methodology recently proposed by the authors for the analytical solution of conjugated heat transfer problems in channel flow, here taking into account the axial diffusion effects which are often of relevance in micro-channels. This methodology is based on a single domain formulation, which is proposed for modeling the heat transfer phenomena at both the fluid stream and the channel walls regions. By making use of coefficients represented as space variable functions, with abrupt transitions occurring at the fluid-wall interface, the mathematical model is fed with the information concerning the transition of the two domains, unifying the model into a single domain formulation with space variable coefficients. The Generalized Integral Transform Technique (GITT) is then employed in the hybrid numerical-analytical solution of the resulting convection-diffusion problem with variable coefficients. When the axial conduction term is included into the formulation, a non-classical eigenvalue problem must be employed in the solution procedure, which is itself handled with the GITT. In order to covalidate the results obtained by means of this solution path, we have also proposed an alternative solution, including a pseudo-transient term, with the aid of a classical Sturm-Liouville eigenvalue problem. The remarkable results demonstrate the feasibility of this single domain approach in handling conjugated heat transfer problems in micro-channels, as well as when fluid axial conduction cannot be neglected.


1942 ◽  
Vol 148 (1) ◽  
pp. 81-112 ◽  
Author(s):  
C. H. Lander

The state of knowledge of heat transfer in relation to mechanical engineering problems was summarized by Professor Dalby in a paper before the Institution in 1909. The present paper discusses the growth of knowledge during the past thirty years, and the ever-expanding fields of application. Complete rationalization is still not possible, but dimensional methods similar to those used in ship and aircraft design are being applied more and more generally to heat transfer problems. By their aid the practical range of any set of data may be greatly widened. For example, experiments made under pressure on surfaces only a few inches high may be used to deduce the heat transfer for surfaces several feet high at atmospheric pressure; or experiments made in gases may be used to predict the heat transfer in liquids. Selected cases dealt with in the paper are: forced convection for banks of tubes and beds of broken solids, and the relation between heat transfer and friction; natural convection from vertical and horizontal surfaces and across fluid layers; heat transfer in the drop and film condensation of steam, and in film and nucleate boiling; evaporation and its relation to convection; emissive powers of surfaces for radiation; and radiation from non-luminous gases.


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