Mass transfer in structured corrugated packing
- 1 December 1991
- journal article
- research article
- Published by Wiley in The Canadian Journal of Chemical Engineering
- Vol. 69 (6), 1336-1343
- https://doi.org/10.1002/cjce.5450690614
Abstract
The performance of structured corrugated packing has been simulated by establishing mechanistic models for liquid distribution, liquid flow on the packing surface and mass transfer. The models were used to investigate the effect of packing height, liquid load, initial maldistribution as well as differing initial distribution and solid‐liquid contact angle on the packed column performance.Wetted surface area is the primary value of interest and the simulated results compare very well with those predicted by Onda (1968). The results clearly demonstrate that the wetted surface area is a strong function of the solid‐liquid contact angle. Other predicted values such as mass transfer coefficients and overall height of a transfer unit show reasonable agreement with published data.This publication has 3 references indexed in Scilit:
- Performance of packings for water distillationThe Canadian Journal of Chemical Engineering, 1988
- Radial liquid spread and maldistribution in packed columns under different wetting conditionsChemical Engineering Science, 1978
- MASS TRANSFER COEFFICIENTS BETWEEN GAS AND LIQUID PHASES IN PACKED COLUMNSJOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 1968