103 - 103 |
Special Issue: ICMF 2001 - Foreword Michaelides E |
104 - 110 |
High-resolution simulations of particle-eddy interactions Burton TM, Eaton JK |
111 - 121 |
Numerical simulation of gas-particle two-phase mixing layer by vortex method Uchiyama T, Naruse M |
122 - 130 |
Linear stability analysis of particle-laden mixing layers using Lagrangian particle tracking Narayanan C, Lakehal D, Yadigaroglu G |
131 - 139 |
Equilibrium expansion for the Eulerian velocity of small particles Ferry J, Balachandar S |
140 - 148 |
Shear and gravity effects on particle motion in turbulent boundary layers Ziskind G, Gutfinger C |
149 - 157 |
Numerical study of the near-wall behaviour of particles in turbulent pipe flows Portela LM, Cota P, Oliemans RVA |
158 - 167 |
Turbulence modification by the clusters of settling particles in turbulent water flow in a horizontal duct Hagiwara Y, Murata T, Tanaka M, Fukawa T |
168 - 178 |
Dispersion of a particle-laden air jet in a confined rectangular crossflow Yi J, Plesniak MW |
179 - 186 |
How many particles for my Lagrangian simulations? Graham DI, Moyeed RA |
187 - 191 |
Electrophoresis of an insulating particle near a plane boundary Sellier A |
192 - 198 |
Fluid dynamics of a sphere in an arbitrary electric field Feng ZG, Michaelides EE |
199 - 205 |
On the behavior of charged particles in the near wall region of a channel flow Rambaud P, Taniere A, Oesterle B, Buchlin JM |
206 - 216 |
Numerical calculation of electrostatic powder painting using the Euler/Lagrange approach Bottner CU, Sommerfeld M |
217 - 225 |
Scaling and guidelines for erosion in fluidized beds Lyczkowski RW, Bouillard JX |
226 - 233 |
Simulation of 3-D gas-particle flows and coal combustion in a tangentially fired furnace using a two-fluid-trajectory model Zhou LX, Li L, Li RX, Zhang J |
234 - 241 |
Improving the efficiency of fluid cokers by altering two-phase feed characteristics Tafreshi ZM, Kirpalani D, Bennett A, McCracken TW |
242 - 250 |
Experimental and numerical investigation of particle erosion caused by pulverised fuel in channels and pipework of coal-fired power plant Schade KP, Erdmann HJ, Hadrich T, Schneider H, Frank T, Bernert K |
251 - 259 |
Computational simulation of controllable structure formation among particle additives in a continuous-flow chaotic mixer Danescu RI, Zumbrunnen DA |
260 - 265 |
On the design of miniature cyclones for the collection of bioaerosols Pant K, Crowe CT, Irving P |
266 - 278 |
Investigation of powder dispersion inside a SPIROS (R) dry dry powder inhaler using particle image velocimetry Han R, Papadopoulos G, Greenspan BJ |
279 - 291 |
Investigations of flow instabilities within the dense pneumatic conveying system Jaworski AJ, Dyakowski T |
292 - 297 |
Flow frictional resistance in pneumatic conveying of solid particles through inclined lines Carpinlioglu MO, Ozbelge TA, Oruc V |
298 - 305 |
Modeling of the gas-particle flow in industrial classification chambers for design optimization Kolaitis DI, Founti MA |
306 - 312 |
Hydrodynamic study of sedimentation flows and avalanches Bounhoure C, Brunet Y, Merlen A |