scholarly journals HEAT AND MASS TRANSFER IN SOLID – LIQUID SYSTEM WITH SUPERFICIAL HEAT SOURCE

2017 ◽  
Vol 27 (9) ◽  
pp. 133-136
Author(s):  
D. M. Simak ◽  
Yа. M. Gumnytsky ◽  
V. M. Atamanyuk
2010 ◽  
Vol 65 (15) ◽  
pp. 4460-4471 ◽  
Author(s):  
Tapio Salmi ◽  
Henrik Grénman ◽  
Heidi Bernas ◽  
Johan Wärnå ◽  
Dmitry Yu. Murzin

2018 ◽  
Vol 178 ◽  
pp. 222-237 ◽  
Author(s):  
Carlos L. Bassani ◽  
Fausto A.A. Barbuto ◽  
Amadeu K. Sum ◽  
Rigoberto E.M. Morales

2017 ◽  
Vol 377 ◽  
pp. 111-126 ◽  
Author(s):  
C. Sulochana ◽  
G.P Ashwinkumar ◽  
Naramgari Sandeep

In this study, we investigated the 2D MHD flow of a dissipative Maxwell nanofluid past an elongated sheet with uneven heat source/sink, Brownian moment and thermophoresis effects. The flow governing PDEs are transmuted into nonlinear ODEs adopting the suitable similarity transmissions. Further, the RK-4 technique is employed to acquire the numerical solutions. The impact of pertinent parameters such as thermal radiation, frictional heating, irregular heat source/sink, biot number, Brownian moment and thermophoresis on the flow quantities such as velocity, thermal and concentration fields likewise friction factor, heat and mass transfer rates are bestowed with the succour of graphs and tables. Dual nature is witnessed for Newtonian and non-Newtonian fluid cases. It is noticed that the heat and mass transfer rate in Newtonian fluid larger as compared with non-Newtonian fluid.


Author(s):  
You-Rong Li ◽  
Dan-Ling Zeng

Based on non-equilibrium thermodynamic theory and combined with the conservation laws, a comprehensive theoretical model was established to describe heat and mass transfer during convective drying process, and numerical calculation was performed. The results show that: (a) the external convective heat and mass transfer may be treated as the conductive heat transfer with internal heat source and the molecular mass diffusion with internal mass source, respectively, and the ability of heat and mass transfer mainly depends on the strength of the heat source and mass source; the higher the temperature of the drying media, the lower the strength of the internal heat source, but the higher that of the internal mass sources; (b) the evaporation of internal water takes place inside the whole material, and the molecular mass diffusion of the internal vapor is in the direction of decreasing mass transfer potential, not along the decreasing partial pressure of vapor.


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