[1]Manglik R M, Zhang J, Muley A. Low Reynolds number forced convection in three dimensional wavyplatefin compact channels: Fin density effects [J]. International Journal of Heat and Mass Transfer, 2005, 48: 14391449. [2]Wang C C, Lin Y T, Lee C J. An airside correlation for plain finandtube heat exchangers in wet conditions [J]. International Journal of Heat and Mass Transfer, 2000, 43: 18691872. [3]Wang C C, Lee W S, Sheu W J, et al. A comparison of the airside performance of the finandtube heat exchangers in wet conditions: With and without hydrophilic coating [J]. Applied Thermal Engineering, 2002, 22: 267278. [4]Comini G, Croce G. Convective heat transfer and mass transfer in tubefinexchangers under dehumidifying conditions [J]. Numerical Heat Transfer, Part A, 2001, 40: 579599. [5]Comini G, Nonino C, Savino S. Convective heat and mass transfer in wavy finnedtube exchangers [J]. International Journal of Numerical Methods for Heat & Fluid Flow, 2002, 12(6): 735755. [6]Comini G, Nonino C, Savino S. Numerical evaluation of fin performance under dehumidifying conditions [J]. Journal of Heat transfer, 2007, 129: 13951402. [7]Yang B, Sekhar S C. Numerical algorithm study of CFD modeling for a compartmented cooling coil under dehumidifying conditions [J]. Numerical Heat Transfer, Part A, 2007, 52: 737755. [8]Viisanen Y, Strey R, Reiss H. Homogeneous nucleation rates for water [J]. Journal of Chemical Physics, 1993, 99 (6): 46804692. [9]Yang M, Dai H L. Heterogeneous nucleation and wetting of water thin films on a metal surface: A study by optical second harmonic generation [J]. Journal of Chemical Physics, 2003, 118(11): 51065114. [10]Pirpmpugd W, Wongwises S, Wang C C. A tubebytube reduction method for simultaneous heat and mass transfer characteristics for plain finandtube heat exchangers in dehumidifying conditions [J]. Heat Mass Transfer, 2005, 41: 756765. [11]Pirpmpugd W, Wang C C, Wongwises S. Finite circular fin method for heat and mass transfer characteristics for plain finandtube heat exchangers under fully and partially wet surface conditions [J]. International Journal of Heat and Mass Transfer, 2007, 50: 552565. [12]Pirpmpugd W, Wang C C, Wongwises S. A fully wet and fully dry tiny circular fin method for heat and mass transfer characteristics for plain finandtube heat exchangers under dehumidifying conditions [J]. Journal of Heat Transfer, 2007, 129: 12561267. [13]Pirpmpugd W, Wang C C, Wongwises S. Heat and mass transfer characteristics for finned tube heat exchangers with humidification [J]. Journal of Thermophysics and Heat Transfer, 2007, 21(2): 361371. |