Abstrac-Expenments conducted In a stirred cell on evaporation of pure bqulds Into various tamer gases yield that the gas-wde NaSS transfer coefficient, 4, IS proportIonal to the bmary dfiusmty, D, ramed to the power 0 684 t-2/3) Ih'TRODUCTION The obJectrve of the present study IS to detemme the expo
The effect of concentration dependent diffusivities on mass transfer coefficients
β Scribed by D.P. Rao; G.H. Rao
- Publisher
- Elsevier Science
- Year
- 1980
- Weight
- 278 KB
- Volume
- 7
- Category
- Article
- ISSN
- 0094-4548
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π SIMILAR VOLUMES
The effect of diffusivity on gas-side mass transfer coefficient was studied in an experimental bubble column. A fourteen-fold variation of diffusivity was obtained by using a variety of solutes and carrier gases. Both absorption and vaporization experiments were car&d ou< some&es for the same solute
A and B fall to zero witlung the film, I e mstantaneous reactrons Tlus range of behavlour has been discussed frequently at some length (e g Danckwerts[2], Astar&@]) It Is therefore clear that the react~oon may proceed supnticantly either m the bulk of the liquid (Fig la-c) or m the liquid tilm (Fg l
## Abstract The freeβvolume theory of diffusion is used to predict the effect of the glass transition on the concentration dependence of the solvent selfβdiffusion coefficient at constant temperature. The theoretical prediction is in agreement with experimental data. Β© 2003 Wiley Periodicals, Inc.