A new, improved pressure drop correlation for trickle-bed reactors

Chemical Engineering Science

Volumn 43, Issue 8, 1988, Pages 2201-2206

  Ellman, M J ^a   Midoux, N ^a   Laurent, A ^a   Charpentier, J C ^a  

^a UNIVERSITÉ DE LORRAINE   (France)

Author keywords

correlation; data base; dimensional analysis; pressure drop; Trickle bed reactor

Indexed keywords

FLOW OF FLUIDS--TWO PHASE; HYDRODYNAMICS;

PRESSURE DROP CORRELATION; TRICKLE BED REACTORS;

CHEMICAL EQUIPMENT;

EID: 0024122323     PISSN: 00092509     EISSN: None     Source Type: Journal    
DOI: 10.1016/0009-2509(88)87104-5     Document Type: Article

References (13)

1. Recent advances in the analysis and design of trickle-bed reactor
2. Hydrodynamics and transfer processes in trickle-bed reactors
3. Proposed correlation of data for isothermal two-phase, two-component flow in pipes
4. Fluid-flow characteristics of concurrent gas-liquid flow in packed beds
5. Two-phase concurrent flow in packed beds
6. Hydrodynamics of a trickle-bed reactor operating under pressure (0-10MPa): Flow regimes and pressure drop
7. Prediction of pressure drop for two-phase two-component concurrent flow in packed beds
8. Pressure drop and liquid holdup for two-phase concurrent flow in packed beds
9. Two-phase pressure drop in cocurrent downflow in packed beds Air-Silicone oil systems
10. Hydrodynamic parameters for gas-liquid cocurrent flow in packed beds
11. The hydrodynamics of trickling flow in packed beds
12. An investigation into the laws of flow of fluids through beds of granular materials
13. Einflüsse der Porosität und Korngrößenverteilung im Widerstandsgesetz der Porenströmung