Mass transfer modelling for GS heavy water plants: Part 1: Point efficiency on GS sieve trays
- 1 August 1982
- journal article
- research article
- Published by Wiley in The Canadian Journal of Chemical Engineering
- Vol. 60 (4) , 504-509
- https://doi.org/10.1002/cjce.5450600410
Abstract
No abstract availableKeywords
This publication has 10 references indexed in Scilit:
- Gas-Liquid Interfacial Area of a Sieve-Plate with Downcomers and 0.6% PerforationIndustrial & Engineering Chemistry Process Design and Development, 1979
- The prediction of distillation plate efficiencies from froth propertiesChemical Engineering Science, 1977
- The measurement of bubble parameters in two-phase dispersions—II: The structure of sieve tray frothsChemical Engineering Science, 1975
- Aires interfaciales et coefficients de transfert de matière dans les divers types d'absorbeurs et de réacteurs gaz—liquideThe Chemical Engineering Journal, 1974
- Bubble Size, Interfacial Area, and Liquid-Phase Mass Transfer Coefficient in Bubble ColumnsIndustrial & Engineering Chemistry Process Design and Development, 1974
- Mathematical models for mass transfer accompanied by reversible chemical reactionAIChE Journal, 1965
- Axial mixing in a rotating disk contactor—I Apparent longitudinal diffusionChemical Engineering Science, 1962
- Simultaneous mass transfer and equilibrium chemical reactionAIChE Journal, 1960
- Mechanism of Mass Transfer on Bubble PlatesIndustrial & Engineering Chemistry, 1952
- Significance of Liquid-Film Coefficients in Gas AbsorptionIndustrial & Engineering Chemistry, 1951