Convective Heat and Mass Transfer

By H. Oertel. 2010

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Exergetic performance evaluation and parametric studies of solar air heater (2008, background): “The following correlation for air, for fully developed turbulent flow (if the length to equivalent diameter ratio exceeds 30) with one side heated and the other side insulated [23], is appropriate:”
Tomography based determination of permeability, Dupuit–Forchheimer coefficient, and interfacial heat transfer coefficient in reticulate porous ceramics (2008, neutral): “Also plotted is the local Nusselt number for laminar flow in a circular tube with constant wall temperature and diameter dnom at Re =1 , 10 and 100, and for Pr =1 ( Kays and Crawford, 1993 ).”
Recent Trends in Computation of Turbulent Jet Impingement Heat Transfer (2012, neutral): “[46].”
Heat transfer from multiple row arrays of low aspect ratio pin fins (2011, methodology): “The Nusselt number augmentation is the ratio of the measured endwall Nusselt number (Nu) to the correlation for a smooth duct Nusselt number (Nuo) at the same duct Reynolds number [2].”