Hydrodynamics of trickle-flow reactors: Updated slip functions for the slit models

Chemical Engineering Research and Design

Volumn 80, Issue 2, 2002, Pages 195-200

  Iliuta, I ^a   Grandjean, B P A ^a   Larachi, F ^a  

^a UNIVERSITÉ LAVAL   (Canada)

Author keywords

Gas liquid interfacial area; Liquid hold up; Pressure drop; Trickle bed reactor; Wetting efficiency

Indexed keywords

DATABASE SYSTEMS; PRESSURE DROP; SURFACE CHEMISTRY; VELOCITY; WETTING;

TRICKLE-FLOW REACTORS;

HYDRODYNAMICS;

HOLD-UP; HYDRODYNAMICS; PRESSURE DROP; TRICKLE BED REACTOR; WETTING;

EID: 0036496682     PISSN: 02638762     EISSN: None     Source Type: Journal    
DOI: 10.1205/026387602753501924     Document Type: Article

References (14)

1. A phenomenological model of pressure drop, liquid holdup and flow regime transition in gas-liquid trickle flow
2. Prediction of pressure drop and liquid hold-up in high-pressure trickle-bed reactors
3. Double-slit model for partially wetted trickle flow hydrodynamics
4. Hydrodynamic parameters for gas-liquid co-current flow in packed-beds
5. Modelling of the hydrodynamics of the co-current gas-liquid trickle flow through a trickle-bed reactor
6. Pressure drop and liquid hold-up in trickle flow reactors: Improved Ergun constants and slip correlations for the slit model
7. Gas-liquid interfacial mass transfer in trickle-bed reactors: State-of-the-art correlations
8. Prediction of liquid-solid wetting efficiency in trickle flow reactors
9. Liquid-solid wetting factor in trickled-bed reactors: Its determination by a physical method
10. Trickle-bed reactor diluted with fine particles and coiled tubular flow-type reactor for kinetic measurements without external effects
11. A trickle bed reactor model for hydrogenation of 2.4-dinitrotoluene: Experimental verification