Mass transfer in foam and froth regimes in distillation with sieve tray column

Journal of Chemical Engineering of Japan

Volumn 34, Issue 4, 2001, Pages 493-500

  Mortaheb, H R ^a   Kosuge, H ^a   Asano, K ^a  

^a TOKYO INSTITUTE OF TECHNOLOGY   (Japan)

Author keywords

Diffusion flux; Flow regime; Foam; Liquid holdup; Sieve tray column

Indexed keywords

DIFFUSION; DISTILLATION; MASS TRANSFER; REYNOLDS NUMBER;

SIEVE TRAY COLUMN;

DISTILLATION COLUMNS;

DISTILLATION; FOAM; HOLD-UP; MASS TRANSFER; SIEVED DISTILLATION COLUMN;

EID: 0035300413     PISSN: 00219592     EISSN: None     Source Type: Journal    
DOI: 10.1252/jcej.34.493     Document Type: Article

References (20)

1. The hydrodynamics of bubbler processes
2. Prediction of point efficiencies on sieve trays. 1. Binary systems
3. Prediction of point efficiency for sieve trays in distillation
4. Clear liquid height and froth density on sieve trays
5. Surface tension effects on a large rectangular tray with small diameter holes
6. The effect of surface tension characteristics on plate efficiencies
7. Flow-pattern and gas-holdup conditions in gas-sparged contactors
8. Foaming and frothing related to system physical properties in a small perforated plate distillation column
9. Surface tension effects in binary and multicomponent distillation
10. Prediction of multicomponent distillation efficiencies
11. Ternary component efficiencies
12. Mass transfer in ternary distillation with sieve tray column
13. Dimensionierung des Gas/Flussigkeit-Kontaktapparates Bodenkolonne
14. Theoretical consideration of gas void fraction and froth height on a perforated plate, low clear liquid height under liquid stagnant flow
15. Sieve trays, a view on the state of the art
16. Marangoni effect in distillation of alcohol-water mixtures
17. The influence of surface phenomena on the performance of distillation columns