Gas-liquid mass transfer in co-current three-phase fluidized beds with non-Newtonian fluids: Theoretical models based on the energy dissipation rate

Chemical Engineering Journal

Volumn 185-186, Issue , 2012, Pages 337-346

  Miura, Hideki ^a   Katoh, Takashi ^a   Kawase, Yoshinori ^a  

^a TOYO UNIVERSITY   (Japan)

Author keywords

Co current three phase fluidized bed; Gas hold up; Gas liquid mass transfer; Non Newtonian liquid

Indexed keywords

A-COEFFICIENT; ENERGY DISSIPATION RATE; EXPERIMENTAL DATA; GAS HOLD-UP; GAS HOLD-UPS; GAS-LIQUID MASS TRANSFER; GASPHASE; GLASS BEAD; LIQUID VELOCITIES; NON-IDEAL MIXING; NON-NEWTONIAN FLUIDS; TANKS-IN-SERIES MODEL; THEORETICAL MODELS; THREE PHASE FLUIDIZED BED;

BUBBLE COLUMNS; FLOCCULATION; FLOW MEASUREMENT; FLUIDIZATION; FLUIDIZED BEDS; MASS TRANSFER; NON NEWTONIAN FLOW; NON NEWTONIAN LIQUIDS; RHEOLOGY; VISCOUS FLOW;

GASES;

EID: 84857365824     PISSN: 13858947     EISSN: None     Source Type: Journal    
DOI: 10.1016/j.cej.2012.01.065     Document Type: Article

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