ANNA UNIVERSITY QUESTION BANK FOR HEAT AND MASS TRANSFER

Rudy, T. M., and Webb, R. L. (1981). Condensate Retention on Horizontal Integral-Fin Tubing,in Advances in Enhanced Heat Transfer, 20th National Heat Transfer Conference, ASME-HTD-18, ASME, New York, pp. 35–41.Saunders, E. A. D. (1988). Heat Exchangers Selection, Design and Construction, Wiley, NewY[r]

and width ∆x of the grid. The constitutive relations for obtaining conductance terms for conductance (U’s) matrix are calculated over discretised control areas in y-z plane for conduction heat flow, radiation and convection heat exchange. Whilst, heat transport conductance terms are calculated from[r]

đúng bằng các phơng pháp số (Husain A., Chen C.S., Clayton J. T, Whitney L.F, 1972). 4. Kết luận Quá trình trao đổi nhiệt ẩm trong vùng chứa trứng đợc mô tả bằng hệ phơng trình vi phân riêng (phơngtrình 41) cho biết mối quan hệ giữa các thông số trong vùng công nghệ làm cơ sở cho việc nghiên cứu và[r]

Galbiati, L., and Andreini, P. (1992). The Transition between Stratified and Annular Regimesfor Horizontal Two-Phase Flow in Small Diameter Tubes, Int. Commun. Heat Mass Trans-fer, 19(2), 185–190.Gidwani, A., Molki, M., Ohadi, M., Dessiatoun, S. V., and Da Silva, L. W. (1998). EHD-Enhanced Condensati[r]

Africa, where his thesis topic covered in-tube condensation of refrigerants in the intermittent flow regime.His current research is on falling film flow visualization, as well as falling film evaporation and condensation heat transfer on bundles of enhanced tubes.Mathieu Habert[r]

transfer at the same time of cylinder form in conditional freeze – drying. Result research willapply for preserving fishery foods crustacean group (PENAEUS MONODON, PENAEUSMERGUIENSIS, PENAEUS VANNAMEI) has economy value.TÀI LIỆU THAM KHẢO [1]. Nguyễn Tấn Dũng – Trịnh Văn Dũng – Trần Đức Ba, Nghiên[r]

1 and 2, Int. J. Heat Mass Transfer, 40, 1753–1793.Baker, O. (1954). Design of Pipe Lines for Simultaneous Flow of Oil and Gas, Oil Gas J., July,p. 26.Barnea, D., and Taitel, Y. (1986). Flow Pattern Transition in Two-Phase Gas–Liquid Flows, inEncyclopedia of Fluid Mechanics, Gulf Publishing, Houston[r]

. For more details on transition boiling,refer to Witte and Lienhard (1982) or Dhir and Liaw (1987).9.6 INTRODUCTION TO FLOW BOILINGFor evaporation under forced-flow conditions, heat transfer includes both a convectivecontribution and a nucleate boiling contribution, whose relative importance depends[r]

Devpura, A., Phelan, P. E., and Prasher, R. S. (2000). Percolation Theory Applied to theAnalysis of Thermal Interface Materials in Flip-Chip Technology, Proc. Itherm, May 23–26, Vol. 1, pp. 21–29.Dunn, P. D., and Reay, D. A. (1994). Heat Pipes, 4th ed., Elsevier Science, Oxford.Eckert, E. R. G., and[r]

when a thick slab of meat is to be cooled, or when sunlight strikeson a roof and heats the surface. When this happens, some of theheat changes the temperature of the first layer of the solid, and theremaining heat passes on to the next layer, and so on. Calculationsfor heating or cooling times of th[r]

Contact Phase Change Heat Transfer between Refrigerant and PCM in an Enclosure, Trans.Jpn. Soc. Mech. Eng., 62(12), 3757–3762.Utaka, Y., Saito, A., and Seki, T. (1998). Gas Hydrate Cold Storage Using Direct-Contact HeatTransfer of Liquid–Vapor Phase Change and Natural Circulation of Refrigerant in C[r]

ceutical, and agricultural products; refrigerant evaporation and condensation in airconditioning and refrigeration; gas flow heating in manufacturing and waste-heat re-covery; air and liquid cooling of engine and turbomachinery systems; and cooling ofelectrical machines and electronic devices. Improv[r]