In an earlier paper (11), the continuous-phase mass transfer coefficients resulting from the continuous-flow contact of ethyl acetate and water in an agitated vessel, ethyl acetate dispersed, were reported to be substantially larger than might be expected from consideration of the data obtained from
Continuous-phase mass-transfer coefficients for liquid extraction in agitated vessels
β Scribed by Harvey D. Schindler; Robert E. Treybal
- Publisher
- American Institute of Chemical Engineers
- Year
- 1968
- Tongue
- English
- Weight
- 929 KB
- Volume
- 14
- Category
- Article
- ISSN
- 0001-1541
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The mass transfer coefficient in covered, right-cylindrical tanks full of liquid, turbulently agitated at various speeds by turbines with six flat blades, was measured by the rate of solution of suspended solids in water and in 45% sucrose solutions. Screened crystals in the following U. S. mesh si
## Abstract There are a large number of correlations given in literature for the prediction of volumeβrelated liquidβside mass transfer coefficients in mechanically agitated gasβliquid contactors. Significant disagreement can be observed concerning the proposed correlations, so that no single corre