Thermal entrance lengths for non-newtonian fluids in turbulent pipe flow

Letters in Heat and Mass Transfer - Tập 2 - Trang 189-197 - 1975
S.S. Yoo1, J.P. Hartnett1
1University of Illinois, Chicago, Illinois 60680, USA

Tài liệu tham khảo

Sleicher, 1961 Sparrow, 1957, Turbulent Heat Transfer in the Thermal Entrance Region of a Pipe with Uniform Heat Flux, Appl. Sci. Res. A, 7, 37, 10.1007/BF03184700 Hartnett, 1955, Experimental Determination of the Thermal Entrance Length for the Flow of Water and of Oil in Circular Pipes, Trans. ASME, 77, 1211 Allen, 1964, Friction and Heat Transfer Measurements to Turbulent Pipe Flow of Water (Pr=7 and 8) at Uniform Wall Heat Flux, ASME, J. of Heat Transfer, 86, 301, 10.1115/1.3688680 Gupta, 1967, Turbulent Heat Transfer Characteristics of Viscoelastic Fluids, Int. J. Heat and Mass Trans., 10, 1211, 10.1016/0017-9310(67)90085-3 Kays, 1966 Yoo, 1974, Heat Transfer and Friction Factors for Non-Newtonian Fluids in Turbulent Pipe Flow, 10.1615/IHTC5.2090 Metzner, 1965, Heat Transfer in Non-Newtonian Fluids, Vol. 2 Bogue, 1963, Velocity Profiles in Turbulent Pipe Flow, Ind. Eng. Ch. Fundamentals, 2, 143, 10.1021/i160006a010 Eissenberg, 1964, Velocity Profiles of Thoria Suspensions in Turbulent Pipe Flow, A.I.Ch.E. Journal, 10, 723, 10.1002/aic.690100528 Seyer, 1959, Turbulence Phenomena in Drag Reducing Systems Khabakhpasheva, 1970, Heat Transfer in Viscoelstic Fluids, Vol. IV, Rh2 Virk, 1971, An Elastic Sublayer Model for Drag Reduction by Dilute Solutions of Linear Macromolecules, J. Fluid Mech., 45, 417, 10.1017/S0022112071000120