A continuum model for gas-liquid flow in packed towers

Chemical Engineering Science

Volumn 56, Issue 21-22, 2001, Pages 5945-5953

  Liu, Shijie ^a  

^a UNIVERSITY OF ALBERTA   (Canada)

Author keywords

Counter current flow; Multiphase flow; Packed tower; Phase hold up; Velocity distribution; Volume and time averaging

Indexed keywords

COLUMNS (STRUCTURAL); COMPUTER SIMULATION; NAVIER STOKES EQUATIONS; POROUS MATERIALS; PRESSURE DROP;

PACKED TOWERS;

TWO PHASE FLOW;

COUNTERCURRENT FLOW; GAS-LIQUID TWO-PHASE FLOW; HOLD-UP; PACKED COLUMN;

EID: 0035941317     PISSN: 00092509     EISSN: None     Source Type: Journal    
DOI: 10.1016/S0009-2509(01)00232-9     Document Type: Article

References (19)

1. Modeling of the hydrodynamics of the cocurrent gas-liquid trickle flow through a trickle-bed reactor
2. Trickle-bed reactors. A review
3. Hydrodynamics and amss transfer in trickle-bed reactors: An overview
4. Liquid and gas flow patterns in random packings
5. Implementation of radial porosity and velocity distribution in a reactor model for heterogeneous catalytic gas phase reactions (Torus-Model)
6. Particle dispersion for suspension suspension flow
7. A continuum approach to multi-phase flow in porous media
8. An experimental study of pressure drop in helical pipes
9. Gas-liquid countercurrent flows through packed towers
10. Single fluid flow in porous media
11. Non-linear flows in porous media
12. Capillary conduction of liquids through porous media
13. Liquid distribution in trickle-bed reactors