THESE_EL HAMMAMI.pdf - Toubkal

BIBLIOGRAPHIE 112[23] R. H. Pletcher. Prediction of transpired turbulent boundary layers. J Heat Transfer,94 :89–94, 1974.[24] Y. El Hammami M. Feddaoui T. Mediouni A. Mir. Numerical study in condensinga liquid refrigerant (r134a) film along a vertical channel. International symposiumon convective heat and mass transfer in sustainable energy Hammamet Tunisia.,2 :426–429, 2009.[25] Y. Mori K.Hijikata et P. Wei. Noncondensable gas effect on high parformance verticalcondensing surface with parallel low fins. ASME.JSME Thermal Eng. Joint Conf,3 :297–303, 1983.[26] P. Kaiping et U. Renz. Thermal diffusion in turbulent partial condensation. Int. J.Heat Mass Transfer, 34(10) :2639, 1991.[27] H. Louahlia P. K. Panday. Transfert thermique pour la condensation du r123, r134aet de leurs mélanges en écoulement force entre deux plaques planes horizontales,etude numérique. Rev Gen Therm, 35, 1996.[28] H. A. Hasanein M. S. Kazimi M. W. Golay. orced convection in-tube steam condensationin the presence of non-condensable gases. Int J Heat Mass Transf, 39 :2625–2639, 1996.[29] Z. Lan H. T. Chen S. Chang. Effect on noncondensable gas on laminar film condensationalong a vertical plate fin. Int J of Heat and Fluid Flow, 19(4) :374–381, 1998.[30] E. C. Siow S. J. Ormiston H. M. Soliman. Fully coupled solution of a two-phasemodel for laminar film condensation of vapor-gas mixtures in horizontal channels.Int J Heat and Mass Tran, 45 :3689–3702, 2002.[31] E. C. Siow S. J. Ormiston H. M. Soliman. A two-phase model for laminar filmcondensation from steam-air mixtures in vertical parallel-plate channels. Heat andMass Tran, 40, 2004.[32] S. T. Revankar D. Pollock. Laminar film condensation in a vertical tube in thepresence of noncondensable gas. Applied Mathematical Modelling, 29, 2005.