The Third Pacific Chemical Engineering Congress: Fluid mechanics, fluid-solid interactions, fluid operations, mass transfer1983 - Chemical engineering - 1717 pages |
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Page 125
... holdup on the height and the voidage of the fluidized beds ; The liquid holdup on the height and the voidage of the beds was shown in Fig . 2 . v , ( m / s ) 0.0243 0.0796 ( msec ) 0.00020 0.000975 1 ( 1 ) 11 , ( m1 ) 0.0.50 0.400 0.050 ...
... holdup on the height and the voidage of the fluidized beds ; The liquid holdup on the height and the voidage of the beds was shown in Fig . 2 . v , ( m / s ) 0.0243 0.0796 ( msec ) 0.00020 0.000975 1 ( 1 ) 11 , ( m1 ) 0.0.50 0.400 0.050 ...
Page 306
... holdup in the present ex- periment , upon the gas holdup is very little for each type of column . The gas holdup in the gas - slurry reactors were reported to decrease generally with increas- ( Vpc / V ) observed [ - ] Fig . 4 ...
... holdup in the present ex- periment , upon the gas holdup is very little for each type of column . The gas holdup in the gas - slurry reactors were reported to decrease generally with increas- ( Vpc / V ) observed [ - ] Fig . 4 ...
Page 413
... hold - up at Q - 10 ( 1 / hr ) Fig . 2 . was used to measure dispersed phase hold - up to study the effect of packing dimensions and shapes on mass transfer rate . Fig.3 shows the plots of ød as a function of Ps / Ds at Qd of about 10 1 ...
... hold - up at Q - 10 ( 1 / hr ) Fig . 2 . was used to measure dispersed phase hold - up to study the effect of packing dimensions and shapes on mass transfer rate . Fig.3 shows the plots of ød as a function of Ps / Ds at Qd of about 10 1 ...
Contents
Flow Characteristics in Channel with Symmetric Wavy Wall for Steady Flow | 5 |
Method of Multiinterval Expansion for a Boundary Layer Flow Problem | 11 |
Effect of the Wound Thread Around a Vertical Tube on Flowing Down of the Liquid Film | 24 |
91 other sections not shown
Common terms and phrases
acid adsorbed adsorption aqueous average axial mixing Baker's map benzene bubble column calcium hydroxide calculated Chem Chemical cm/s component concentration constant continuous phase correlation curves cyclohexane decrease density desorption diameter diffusion dimensionless disk dispersed phase distillation distribution effect efficiency emulsion equation equilibrium experiments extraction feed Figure film theory filter filtration flow pattern fluid fluidized bed flux fraction function gas velocity gas-liquid Glycerine granulator growth rate height hexane holdup increase interface interfacial area liquid film liquid phase mass transfer coefficient measured membrane methanol method Newtonian fluids non-Newtonian non-Newtonian fluids obtained operation oxygen packed bed packing parameters plate plot pressure drop Raschig ring ratio reaction region resin Reynolds number rotating shear stress shown in Fig shows slurry solution solvent spacers spouted vessel surface tank temperature theoretical tion tower tracer tube turbulent urea volume