1 - 6 |
Numerical calculation of particle transport in turbulent wall bounded flows Sommerfeld M, Ho CA |
7 - 14 |
Effect of particle characteristics on particle pickup velocity Hayden KS, Park K, Curtis JS |
15 - 22 |
Effect of temperature on slug properties in a gas fluidized bed Choi JH, Kim TW, Moon YS, Kim SD, Son JE |
23 - 39 |
Slow and intermediate flow of a frictional bulk powder in the Couette geometry Tardos GI, McNamara S, Talu I |
40 - 47 |
Evaluation of apparent viscosity of liquid-containing porous particles by the intrusion method using a conical rotor Iwasaki T, Satoh M, Okui M, Kobayashi M, Sugawara T, Tsuchiya R |
48 - 55 |
Radial gas mixing in a fluidized bed using response surface methodology Lin YC, Chyang CS |
56 - 65 |
Hydrodynamics of a spouted bed with a porous draft tube containing a small amount of finer particles Ishikura T, Nagashima H, Ide M |
66 - 70 |
Prediction of minimum fluidization velocity for vibrated fluidized bed Mawatari Y, Tatemoto Y, Noda K |
71 - 79 |
Classification of ultra fine powder by a new pneumatic type classifier Morimoto H, Shakouchi T |
80 - 92 |
Study on the stress distribution and modeling of the stand pipe in a circulating moving bed Xu C, Han MH, Chen S, Wang DZ, Jin Y |
93 - 98 |
A multifractal comminution approach for drilling scaling laws Carpinteri A, Pugno N |
99 - 104 |
Improved particle plug valve for Geldart-D powders Jing S, Hu QY, Bian Y, Mei F, Wang JF, Jin Y |