The influence of the reactor pressure on the hydrodynamics in a cocurrent gas-liquid trickle-bed reactor

Chemical Engineering Science

Volumn 45, Issue 8, 1990, Pages 2247-2254

  Wammes, W J A ^a   Westerterp, K R ^a  

^a UNIVERSITY OF TWENTE   (Netherlands)

Author keywords

elevated pressures.; flow regime transition; Liquid hold up

Indexed keywords

CATALYSTS; GASES--DENSITY; HELIUM; NITROGEN; WATER;

COCURRENT GAS-LIQUID TRICKLE-BED REACTOR; ETHYLENE GLYCOL; FLOW REGIME TRANSITION; GALILEO NUMBER;

CHEMICAL REACTORS;

EID: 0025626707     PISSN: 00092509     EISSN: None     Source Type: Journal    
DOI: 10.1016/0009-2509(90)80102-K     Document Type: Article

References (9)

1. Etude de la rétention de liquide dans une colonne à garnissage arrosé à co-courant et à contro-courant de gaz-liquide
2. Hydrodynamics and solid-liquid contacting effectiveness in trickle-bed reactors
3. Mass transfer in packed columns
4. Hydrodynamics of two phase downflow through packed beds
5. Performance of packed columns
6. Pressure drop and liquid hold-up for two phase cocurrent flow in packed beds
7. Two phase downflow through catalyst beds
8. The influence of pressure on the liquid hold-up in a cocurrent gas-liquid trickle-bed reactor operating at low gas velocities
9. The transition between trickle-flow and pulse-flow in a cocurrent gas-liquid trickle-bed reactor at elevated pressures