1958
DOI: 10.1002/aic.690040213
|View full text |Cite
|
Sign up to set email alerts
|

Momentum and mass transfer by eddy diffusioin in a wetted‐wall channel

Abstract: The role of eddy diffusion of mass (water vapor) and momentum was investigated in a specially devised wetted-wall channel in which the rippling of the liquid film was eliminated.The experimental measurements of the turbulent exchange coefficients for mass and momentum transport were carried out in a fully developed turbulent flow of air within the range of Reynolds numbers of 8,000 to 160,000. A correlation with Reynolds number revealed an approximately linear relationship of the eddy diffusivities to Reynolds… Show more

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
1
1
1

Citation Types

1
2
0

Year Published

1960
1960
1993
1993

Publication Types

Select...
4
1
1

Relationship

0
6

Authors

Journals

citations
Cited by 8 publications
(3 citation statements)
references
References 7 publications
1
2
0
Order By: Relevance
“…The theory of Mothes and Loffler (1988), which divides the cyclone into three distinct regions (a fourth region is possible if reentrainment is occurring) coupled with the concept of a finite diffusivity provides the best fit with the experimental data. The fitted particle turbulent diffusivities Dp are in the range obtained experimentally by Leonard et al (1982), Self et al (1987) and Erlich and Melcher (1987) for turbulent flows, and generally much larger than predicted from available theories or empirical formulae (Taylor, 1954;Dhanak, 1958;Becker et al, 1966). Order of magnitude agreement for the fitted diffusivity is obtained with the experimental grade collection in a standard type sampling cyclone collecting a fine alumina dust (Salcedo, 1981).…”
Section: Discussionsupporting
confidence: 72%
See 1 more Smart Citation
“…The theory of Mothes and Loffler (1988), which divides the cyclone into three distinct regions (a fourth region is possible if reentrainment is occurring) coupled with the concept of a finite diffusivity provides the best fit with the experimental data. The fitted particle turbulent diffusivities Dp are in the range obtained experimentally by Leonard et al (1982), Self et al (1987) and Erlich and Melcher (1987) for turbulent flows, and generally much larger than predicted from available theories or empirical formulae (Taylor, 1954;Dhanak, 1958;Becker et al, 1966). Order of magnitude agreement for the fitted diffusivity is obtained with the experimental grade collection in a standard type sampling cyclone collecting a fine alumina dust (Salcedo, 1981).…”
Section: Discussionsupporting
confidence: 72%
“…The diffusivities are roughly one order of magnitude larger for the Mothes and Loffler model, and for cyclones B and C they are in the range obtained experimentally for turbulent flows (Leonard et al, 1982;Self et al, 1987;Erlich and Melcher, 1987). However, if the effective diffusivity is estimated from Equation (12) or from empirical relations developed for turbulent flows (see for example Dhanak, 1958;Becker et al, 1966), then much smaller values for Dp (between lop5 and m2/s) are obtained. The discrepancy between the fitted turbulent diffusivities as compared to those obtained from empirical relations developed for turbulent flows may also be due to non-uniformity particle distribution at the cyclone inlets or to axially non-uniform radial gas velocity at the vortex finder.…”
Section: Resultsmentioning
confidence: 99%
“…Dhanak (9) DorWeiler' (10) illustrated the interaction between molecular ~nd ed.dy dif:tusi vi ties by extending the mass transfer data for packed beds to low floW rates including the "transition" and "laminar" regions.…”
Section: ··mentioning
confidence: 99%