| 31 |
Influence of frictional packing limit on hydrodynamics and performance of gas-solid fluidized beds
Sahu AK, Raghavan V, Prasad B
Korean Journal of Chemical Engineering, 37(12), 2368, 2020 |
| 32 |
Sensitivity analysis of the variational model for the particulate expansion of fluidized beds
Duris M, Arsenijevic Z, Radoicic TK
Particulate Science and Technology, 38(1), 95, 2020 |
| 33 |
Identification of regime transition from bubbling to turbulent fluidization through dynamic phase tracking method
Wang HL, Zhu J, Huang WX, Zhang H
Powder Technology, 360, 534, 2020 |
| 34 |
Fluidization characteristics in a vibrated gas-fluidized bed of Geldart D particles based on the collaborative measurement by impact force sensor and high-speed image analysis system
Wang S, Wu WW, Yang XL, Zhao YM
Powder Technology, 360, 872, 2020 |
| 35 |
Measurements of wall-media contact forces and work in a vibratory finisher
Maciel LS, Spelt JK
Powder Technology, 360, 911, 2020 |
| 36 |
Multistep reduction kinetics of Fe3O4 to Fe with CO in a micro fluidized bed reaction analyzer
He K, Zheng Z, Chen ZW
Powder Technology, 360, 1227, 2020 |
| 37 |
EMMS-based solid stress model for the multiphase particle-in-cell method
Jiang Y, Li F, Ge W, Wang W
Powder Technology, 360, 1377, 2020 |
| 38 |
Effect of granular properties on hydrodynamics in coarse-grid riser flow simulation of Geldart A and B particles
Bin Rashid TA, Zhu LT, Luo ZH
Powder Technology, 359, 126, 2020 |
| 39 |
Comparison of velocimetry methods for horizontal air jets in a semicircular fluidized bed of Geldart Group D particles
Fullmer WD, Higham JE, LaMarche CQ, Issangya A, Cocco R, Hrenya CM
Powder Technology, 359, 323, 2020 |
| 40 |
Comparison of DEM predictions and measured wall-media contact forces and work in a vibratory finisher
Maciel LD, Spelt JK
Powder Technology, 366, 434, 2020 |
