3569 - 3578 |
Pressure fluctuations in bubbling gas-fluidized beds Croxford AJ, Gilbertson MA |
3579 - 3591 |
An analytical method for selecting the optimal nozzle external geometry for fluid dynamic gauging Peralta JM, Chew YMJ, Wilson DI |
3592 - 3604 |
Incorporating particle flow information from discrete element simulations in population balance models of mixer-coaters Freireich B, Li JF, Litster J, Wassgren C |
3605 - 3616 |
Derivation and validation of a binary multi-fluid Eulerian model for fluidized beds Chao ZX, Wang YF, Jakobsen JP, Fernandino M, Jakobsen HA |
3617 - 3627 |
CFD simulation of a chemical-looping fuel reactor utilizing solid fuel Mahalatkar K, Kuhlman J, Huckaby ED, O'Brien T |
3628 - 3640 |
Limitations of quadrature-based moment methods for modeling inhomogeneous polydisperse fluidized powders Mazzei L |
3641 - 3647 |
A mesoporous SiO2 intermediate layer for improving light propagation in a bundled tube photoreactor Denny F, McCaffrey P, Scott J, Peng GD, Amal R |
3648 - 3655 |
Bed height and material density effects on fluidized bed hydrodynamics Escudero D, Heindel TJ |
3656 - 3665 |
Numerical simulation of polypropylene foaming process assisted by carbon dioxide: Bubble growth dynamics and stability Li Y, Yao Z, Chen ZH, Cao K, Qiu SL, Zhu FJ, Zeng CC, Huang ZM |
3666 - 3674 |
A two-scale model for discrete cell gravure roll coating Hewson RW, Kapur N, Gaskell PH |
3675 - 3686 |
The effect of dispersed elastomer particle size on heterogeneous nucleation of TPO with N-2 foaming Kim SG, Leung SN, Park CB, Sain M |
3687 - 3691 |
Role of inertial lift in elutriating particles according to their density Galvin KP, Liu H |
3692 - 3700 |
LES/FDF simulation of a gas-particle backward-facing step flow Jin HH, Chen Y, Fan JR, Luo K |
3701 - 3709 |
Porometry, porosimetry, image analysis and void network modelling in the study of the pore-level properties of filters Gribble CM, Matthews GP, Laudone GM, Turner A, Ridgway CJ, Schoelkopf J, Gane PAC |