The Backflow-Cell Model for Continuous Two-Phase Nonlinear Mass-Transfer Operations Including Nonlinear Axial Holdup and Mixing Effects
- 1 January 1966
- journal article
- research article
- Published by Taylor & Francis in Separation Science
- Vol. 1 (6) , 677-700
- https://doi.org/10.1080/01496396608049474
Abstract
The backflow-cell model is applied to countercurrent two-phase flow processes with exchange of a single solute. The effects of nonuniform axial holdup of the phases and nonlinear equilibrium are considered. Efficient matrix methods of solving the model equations for the array of cell concentrations in each phase are developed. These profiles are compared to those of the diffusion model for some linear cases, and methods of smoothing them are discussed.Keywords
This publication has 8 references indexed in Scilit:
- The backflow cell model of isothermal first order flow reactors with axial dispersionThe Canadian Journal of Chemical Engineering, 1966
- Mathematical Determination of Concentration Profiles in Two-Phase Continuous Countercurrent ExtractorsIndustrial & Engineering Chemistry Fundamentals, 1964
- Diffusion and Back-Flow Models for Two-Phase Axial DispersionIndustrial & Engineering Chemistry Fundamentals, 1963
- Longitudinal Dispersion in Two-Phase Continuous-Flow OperationsIndustrial & Engineering Chemistry Fundamentals, 1963
- Entrainment and extraction efficiency of mixer‐settlersAIChE Journal, 1960
- Axial mixing and extraction efficiencyAIChE Journal, 1959
- Correction factor for axial mixing in packed bedsThe Canadian Journal of Chemical Engineering, 1958
- An Alternating Direction Method for Solving the Biharmonic EquationMathematical Tables and Other Aids to Computation, 1958