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Continuous-phase mass-transfer coefficients for liquid extraction in agitated vessels

✍ 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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πŸ“œ SIMILAR VOLUMES


Continuous-phase mass transfer coefficie
✍ Young I. Mok; Robert E. Treybal πŸ“‚ Article πŸ“… 1971 πŸ› American Institute of Chemical Engineers 🌐 English βš– 504 KB

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

Mass transfer coefficients for solids su
✍ James J. Barker; Robert E. Treybal πŸ“‚ Article πŸ“… 1960 πŸ› American Institute of Chemical Engineers 🌐 English βš– 730 KB

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

Mass Transfer Coefficients in Mechanical
✍ J. Markopoulos; C. Christofi; I. Katsinaris πŸ“‚ Article πŸ“… 2007 πŸ› John Wiley and Sons 🌐 English βš– 133 KB πŸ‘ 1 views

## Abstract There are a large number of correlations given in literature for the prediction of volume‐related liquid‐side mass transfer coefficients in mechanically agitated gas‐liquid contactors. Significant disagreement can be observed concerning the proposed correlations, so that no single corre