Hydrodynamics and heat transfer in packed bed with co current up flow for coalescing and non-coalescing liquids. A simple model

Chemical Engineering Science

Volumn 55, Issue 19, 2000, Pages 4149-4157

  Colli Serrano, M T ^a,c   Midoux, N ^b  

^a INSTITUTO POLITÉCNICO NACIONAL   (Mexico)

^b UNIVERSITÉ DE LORRAINE   (France)

^c University of Bath   (United Kingdom)

Author keywords

Gas liquid solid reactor; Heat transfer; Hydrodynamics; Liquid hold up; Packed bed; Thermal conductivity

Indexed keywords

CHEMICAL REACTORS; COALESCENCE; COMPUTATIONAL FLUID DYNAMICS; CORRELATION METHODS; HYDRODYNAMICS; MATHEMATICAL MODELS; NITROGEN; SOLUTIONS; THERMAL CONDUCTIVITY OF LIQUIDS; TWO PHASE FLOW; WATER;

GAS-LIQUID-SOLID REACTOR; LIQUID HOLD-UP; PENTANOL;

PACKED BEDS;

HEAT TRANSFER; HOLD-UP; HYDRODYNAMICS; PACKED BED;

EID: 0033626727     PISSN: 00092509     EISSN: None     Source Type: Journal    
DOI: 10.1016/S0009-2509(00)00077-4     Document Type: Article

References (18)

1. Hold-up profiles in packed beds
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3. Effective radial thermal conductivity of packing in gas flow. Part I. Convective transport coefficient
4. Performance and design of packed distillation columns
5. The length effect on packed bed effective heat transfer parameters
6. Heat transfer phenomena in packed bed reactors with co current up flow of gas and liquid
7. Hydrodynamics and heat transfer in packed bed with cocurrent upflow
8. Hydrodynamics and heat transfer in packed bed with cocurrent upflow
9. Heat transfer in a packed bed with gas liquid concurrent upflow
10. Thermal conductivity of a stationary granular bed with upward gas-liquid flow
11. Heat transfer in packed bed reactors with one phase flow
12. Heat transfer characteristics of cocurrent gas-liquid flow in packed bed
13. Heat transfer in packed beds through which water is following