Dynamics of pulsing flow in trickle beds
Authors:
- 1 April 1990
- journal article
- research article
- Published by Wiley in AIChE Journal
- Vol. 36 (4) , 605-621
Abstract
A macroscopic model of two‐phase flow in packed beds, based on the volume‐averaged equations of motion for the gas and liquid phases, was analyzed in an attempt to understand the onset and evolution of fully‐developed pulsing flow in trickle beds. By assuming that solutions take the form of waves travelling at constant speed, periodic solutions to these equations are found which can be associated with long‐time, asymptotic behavior of pulses in a very long bed. Families of one‐dimensional waves which exist at a particular set of mass fluxes can be characterized by infinite period bifurcations in the travelling wave frame. We numerically follow these bifurcations as the fluxes are changed, generating bifurcation diagrams for the original model. The results predict that properties of one‐dimensional pulses should correlate with the total superficial velocity through the bed. A hysteresis in the trickling‐pulsing transition is also predicted.Keywords
This publication has 14 references indexed in Scilit:
- A macroscopic model for countercurrent gas‐liquid flow in packed columnsAIChE Journal, 1989
- Onset of pulsing in two‐phase cocurrent downflow through a packed bedAIChE Journal, 1988
- A numerical study of global bifurcations in chemical dynamicsAIChE Journal, 1987
- Mathematical modeling of pulsing flow in large trickle bedsAIChE Journal, 1987
- Cocurrent downflow of air and water in a two‐dimensional packed columnAIChE Journal, 1986
- A model for flow regime transitions in cocurrent down‐flow trickle‐bed reactorsAIChE Journal, 1986
- Pressure drop and hydrodynamic properties of pulses in two‐phase gas‐liquid downflow through packed columnsThe Canadian Journal of Chemical Engineering, 1983
- Trickle‐bed reactorsAIChE Journal, 1975
- FLOW PATTERN AND PULSATION PROPERTIES OF COCURRENT GAS-LIQUID DOWNFLOW IN PACKED BEDSJOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 1973
- Fluid‐flow characteristics of concurrent gas‐liquid flow in packed bedsAIChE Journal, 1964