Evaluation of a stochastic model of particle dispersion in a turbulent round jet

Evaluation of a stochastic model of particle dispersion in a turbulent round jet by Eq. 19 = turbulent flux of a passive additive = characteristic veloci,ty appearing : the turbulent model for (ulc’); 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., “The Effect of Sample Probe Size on Sublayer Period in Turbulent Boundary Layers,” Chem. Eng. Comm., 5,337 (1980). Blackwelder, R. F., “The Bursting Process in Turbulent Boundary Layers,” 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, “A New Theory for Turbulent Mass Transfer at a Solid Boundary,” submitted to A.Z.Ch.E.J. (1981). Cantwell, B. J., “Organized http://www.deepdyve.com/assets/images/DeepDyve-Logo-lg.png Aiche Journal Wiley

Evaluation of a stochastic model of particle dispersion in a turbulent round jet

Aiche Journal, Volume 29 (1) – Jan 1, 1983

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Publisher
Wiley
Copyright
Copyright © 1983 American Institute of Chemical Engineers
ISSN
0001-1541
eISSN
1547-5905
DOI
10.1002/aic.690290127
Publisher site
See Article on Publisher Site

Abstract

by Eq. 19 = turbulent flux of a passive additive = characteristic veloci,ty appearing : the turbulent model for (ulc’); 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., “The Effect of Sample Probe Size on Sublayer Period in Turbulent Boundary Layers,” Chem. Eng. Comm., 5,337 (1980). Blackwelder, R. F., “The Bursting Process in Turbulent Boundary Layers,” 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, “A New Theory for Turbulent Mass Transfer at a Solid Boundary,” submitted to A.Z.Ch.E.J. (1981). Cantwell, B. J., “Organized

Journal

Aiche JournalWiley

Published: Jan 1, 1983

References

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