by Eq. 19 = turbulent flux of a passive additive = characteristic veloci,ty appearing : the turbulent model for (ulcâ); uc = fT(x1) = coordinate vector with compont. .s ~ 1 . ~ xg , 2 = superscript denoting a quantity made dimensionless using the wall parameters u* and v Greek Letters a 6, = defined by Eq. 23 = characteristic size of the concentration layer near the mass transfer interface (Eq. 7) = kinematic viscosity = characteristic relaxation time for the velocity TH autocorrelation in a frame of reference moving with the average velocity = mean period between burst = semi-infinite spatial domain LITERATURE CITED Abromowitz, M., and I. A. Stegun, Handbook of Mathematical Functbns, NBS, App. Math Series, 55 (1964). Berman, N. S., âThe Effect of Sample Probe Size on Sublayer Period in Turbulent Boundary Layers,â Chem. Eng. Comm., 5,337 (1980). Blackwelder, R. F., âThe Bursting Process in Turbulent Boundary Layers,â Coherent Structure of Turbulent Boundory Layers, eds., C. R. Smith and D. E. Abbott, AFOSR, Lehigh Univ., 211 (1978). Campbell, J. A. and T J. Hanratty, âA New Theory for Turbulent Mass Transfer at a Solid Boundary,â submitted to A.Z.Ch.E.J. (1981). Cantwell, B. J., âOrganized
Aiche Journal – Wiley
Published: Jan 1, 1983
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