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Titlebook: Gas Transfer at Water Surfaces; Wilfried Brutsaert,Gerhard H. Jirka Book 1984 Springer Science+Business Media Dordrecht 1984 Entrainment.a

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https://doi.org/10.1007/978-3-642-56171-9terms of the local energy dissipation rate e, then is found to have a similar form to that in other ‘shear-free’ boundary layers such as in thermal convection boundary layers. Since the impinging turbulence controls the viscous surface layer, it also controls the diffusion layer very close to the su
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Arbeitsleistung und Arbeitsgütethe surface fluctuated rapidly from 0.3 to 16 cm sec.. The mean speeds were ca. 5 cm sec. and the turbulent intensities (ratio of rms speed to mean speed) were greater than 0.4. There was a graded shift from high frequency, high amplitude fluctuations at the surface to lower frequency, smaller ampli
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Book 1984ales. As a consequence, scientists and engineers from diverse disciplines and problem areas, have approached the problem, often with greatly differing analytical and experimental techniques and methodologies.
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Physical-Chemical Phenomena and Molecular Propertiescussed. The various exchange mechanisms of diffusion (volatilization or absorption), deposition in association with particles both dry and wet, dissolution in rainfall, spray transfer and bubble transfer are reviewed briefly. It is shown that the physical chemical properties of the exchanging chemic
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The Ratio of Gas-Phase to Liquid-Phase Mass Transfer Coefficients in Gas-Liquid Contacting Processesss transfer rate constants to the two-resistance model with appropriate corrections for molecular diffusivities. We show that the ratio of mass transfer coefficients (k./k.) is significantly smaller than the suggested value of k./k. = 150 customarily used to model surface aeration, bubble aeration,
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