AIChE Symposium Series, Issue 318 |
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Page 21
... PROCEDURE FOR THE DETERMINATION OF THE LATERAL SOLIDS DISPERSION COEFFICIENT The simulation to determine the lateral solids dispersion coefficient is initialized by selecting a particle diameter . The particle diameter is taken from a ...
... PROCEDURE FOR THE DETERMINATION OF THE LATERAL SOLIDS DISPERSION COEFFICIENT The simulation to determine the lateral solids dispersion coefficient is initialized by selecting a particle diameter . The particle diameter is taken from a ...
Page 63
... procedure of Parzen [ 10 ] ; the resultant set of differential equations is a more general , spatially and temporally nonhomogeneous process . An empirical expression for the time - dependent rate parameter in their model was eventually ...
... procedure of Parzen [ 10 ] ; the resultant set of differential equations is a more general , spatially and temporally nonhomogeneous process . An empirical expression for the time - dependent rate parameter in their model was eventually ...
Page 78
... procedure of ball milling which leads to the calculation of the Hardgrove Grindability Index ( HGI ) . On the HGI scale , the greater is the HGI value the greater is the grindability . The results of similar experiments to those ...
... procedure of ball milling which leads to the calculation of the Hardgrove Grindability Index ( HGI ) . On the HGI scale , the greater is the HGI value the greater is the grindability . The results of similar experiments to those ...
Contents
Foreword | 1 |
RESEARCH AND DEVELOPMENT PAPERS | 15 |
Motion of Individual FCC Particles and Swarms in a Circulating Fluidized Bed Riser Analyzed | 31 |
Copyright | |
1 other sections not shown
Common terms and phrases
acoustic agglomerates analysis approach average axial base behavior bubble calculated changes Chem Circulating Fluidized Bed coefficient collisions column compared Comparison cross decrease dense density described determined developed diameter dilute discharge discrete discussed dispersion distribution dynamics eddy effect equal Equation experimental experiments Figure flow rate fluctuations fluid flux force fraction function gas velocity given gives grains granular heap height higher images increasing individual injection interaction linear liquid lower magnetic field mass transfer materials mean measured method normal observed obtained operating particle diameter particle swarms phase position Powder predicted present pressure waves propagation pulse range region relative represents riser sand scheme secondary air shape shown shows simulation solid solid flow stress structure Superbee surface suspension transition University of Surrey upper vertical voidage wall