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Volumn 36, Issue 6, 1997, Pages 489-495

Experimental study of a cocurrent upflow packed bed bubble column reactor: Pressure drop, holdup and interfacial area

Author keywords

Bed bubble column; Interfacial area; Pressure drop

Indexed keywords

ABSORPTION; BUBBLE COLUMNS; CARBON DIOXIDE; FLOW OF FLUIDS; GASES; INTERFACES (MATERIALS); LIQUIDS; PRESSURE; PRESSURE DROP; VELOCITY;

EID: 0031375682     PISSN: 02552701     EISSN: None     Source Type: Journal    
DOI: 10.1016/S0255-2701(97)00026-3     Document Type: Article
Times cited : (28)

References (10)
  • 1
    • 0031105248 scopus 로고    scopus 로고
    • Gas-liquid interfacial area and holdup in a cocurrent upflow packed bed bubble column reactor up to elevated pressures
    • E. Molga, K.R. Westerterp, Gas-liquid interfacial area and holdup in a cocurrent upflow packed bed bubble column reactor up to elevated pressures, Ind. Eng. Chem. Res. 36 (1997) 622-631.
    • (1997) Ind. Eng. Chem. Res. , vol.36 , pp. 622-631
    • Molga, E.1    Westerterp, K.R.2
  • 2
    • 84984082547 scopus 로고
    • Prediction of pressure drop for two-phase, twocomponent cocurrent flow i packed beds
    • J.L. Turpin, R.L. Huntington, Prediction of pressure drop for two-phase, twocomponent cocurrent flow i packed beds, AIChE J 13 (1967) 1196-1202.
    • (1967) AIChE J , vol.13 , pp. 1196-1202
    • Turpin, J.L.1    Huntington, R.L.2
  • 3
    • 0018505975 scopus 로고
    • Gas-liquid mass transfer and hydrodynamic flow region in packed columns with cocurrent upward flow
    • S. Fukushima, K. Kusaka, Gas-liquid mass transfer and hydrodynamic flow region in packed columns with cocurrent upward flow, J. Chem. Eng. Jap. 12 (1979) 296-301.
    • (1979) J. Chem. Eng. Jap. , vol.12 , pp. 296-301
    • Fukushima, S.1    Kusaka, K.2
  • 5
    • 0028400964 scopus 로고
    • Influence of gas density on the hydrodynamics of cocurrent gas-liquid upflow fixed bed reactors
    • F. Larachi, G. Wild, A. Laurent, N. Midoux, Influence of gas density on the hydrodynamics of cocurrent gas-liquid upflow fixed bed reactors, Ind. Eng. Chem. Res. 33 (1994) 519-525.
    • (1994) Ind. Eng. Chem. Res. , vol.33 , pp. 519-525
    • Larachi, F.1    Wild, G.2    Laurent, A.3    Midoux, N.4
  • 6
    • 0025750324 scopus 로고
    • Experimental study of a trickle bed reactor operating at high pressure: Two-phase pressure drop and liquid saturation
    • F. Larachi, A. Laurent, N. Midoux, G. Wild, Experimental study of a trickle bed reactor operating at high pressure: two-phase pressure drop and liquid saturation, Chem. Eng. Sci. 46 (1991) 1233-1246.
    • (1991) Chem. Eng. Sci. , vol.46 , pp. 1233-1246
    • Larachi, F.1    Laurent, A.2    Midoux, N.3    Wild, G.4
  • 7
    • 0021225558 scopus 로고
    • Interfacial area and liquid-side mass transfer co-efficient in trickle bed reactors operating with organic liquids
    • N. Midoux, B.I. Morsi, M. Purwasasmita, A. Laurent, J.C. Charpentier, Interfacial area and liquid-side mass transfer co-efficient in trickle bed reactors operating with organic liquids, Chem. Eng. Sci. 39 (1984) 781-794.
    • (1984) Chem. Eng. Sci. , vol.39 , pp. 781-794
    • Midoux, N.1    Morsi, B.I.2    Purwasasmita, M.3    Laurent, A.4    Charpentier, J.C.5
  • 8
    • 0026918496 scopus 로고
    • Mass transfer characteristics of fixed beds with cocurrent upflow and downflow. a special reference to the effect of pressure
    • A. Lara Marquez, F. Larachi, G. Wild, A. Laurent, Mass transfer characteristics of fixed beds with cocurrent upflow and downflow. A special reference to the effect of pressure, Chem. Eng. Sci. 47 (1992) 3485-3492.
    • (1992) Chem. Eng. Sci. , vol.47 , pp. 3485-3492
    • Lara Marquez, A.1    Larachi, F.2    Wild, G.3    Laurent, A.4
  • 9
    • 0017680097 scopus 로고
    • Dynamic gas disengagement: A new technique for assessing the behaviour of bubble columns
    • K. Sriram, R. Mann, Dynamic gas disengagement: a new technique for assessing the behaviour of bubble columns, Chem. Eng. Sci. 32 (1977) 571-580.
    • (1977) Chem. Eng. Sci. , vol.32 , pp. 571-580
    • Sriram, K.1    Mann, R.2


* 이 정보는 Elsevier사의 SCOPUS DB에서 KISTI가 분석하여 추출한 것입니다.