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Volumn 81, Issue 1-3, 2001, Pages 223-230
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A highly elevated mass transfer rate process for three-phase, liquid-continuous fluidized beds
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Author keywords
Gas holdup; Mass transfer; Non Newtonian fluid; Three phase fluidized beds
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Indexed keywords
BUBBLES (IN FLUIDS);
COALESCENCE;
MAGNETIC FIELD EFFECTS;
MASS TRANSFER;
NON NEWTONIAN LIQUIDS;
OXYGEN;
VISCOSITY OF LIQUIDS;
GAS HOLDUP;
MASS TRANSFER COEFFICIENT;
FLUIDIZED BEDS;
FLUIDIZED BED REACTOR;
GAS;
LIQUID;
MASS TRANSFER;
OXYGEN CONCENTRATION;
VELOCITY;
FLUIDIZED BED;
GAS-LIQUID-SOLID FLUIDIZED BED;
HOLD-UP;
MASS TRANSFER;
NON-NEWTONIAN FLUID;
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EID: 0034745826
PISSN: 13858947
EISSN: None
Source Type: Journal
DOI: 10.1016/S1385-8947(00)00196-0 Document Type: Article |
Times cited : (8)
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References (16)
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