1 |
Analysis of flexible ribbon particle residence time distribution in a fluidised bed riser using three-dimensional CFD-DEM simulation Wu K, Zhang EQ, Yuan ZL, Li B, Zhu WK, Xu J, Wang L, Luo DS Powder Technology, 369, 184, 2020 |
2 |
Particle residence time measurement in a pressurized drop-tube reactor with radioactive tracer Russig S, Gonzalez V, Schurz M, Krzack S, Kleeberg J, Guhl S, Meyer B Fuel, 252, 37, 2019 |
3 |
Study of single-particle residence time in impulse, symmetric and asymmetric coaxial impinging streams Liu XQ, Yue S, Lu LY, Gao W, Li JL Powder Technology, 342, 118, 2019 |
4 |
Study of particle residence time in a pressurized fluidized bed with in-bed heat exchanger tubes Seguin MA, Hughes RW, Fitzsimmons M, Macchi A, Mehrani P Powder Technology, 355, 201, 2019 |
5 |
Particle exchange in horizontal two-compartment fluidized beds - CFD simulation and experimental validation Lau P, Arlt CR, Potthoff M, Kind M Advanced Powder Technology, 28(2), 543, 2017 |
6 |
The effect of sheath flow rate on the particle trajectory inside an optical cavity with direct flow configuration Lee H, Jeong YS, Choi K, Shin WG Journal of Aerosol Science, 114, 146, 2017 |
7 |
Direct optical observation of coal particle fragmentation behavior in a drop-tube reactor Friedemann J, Wagner A, Heinze A, Krzack S, Meyer B Fuel, 166, 382, 2016 |
8 |
CFD-DEM simulation of solid circulation rate in the cold flow model of chemical looping systems Peng ZB, Doroodchi E, Alghamdi YA, Shah K, Luo CM, Moghtaderi B Chemical Engineering Research & Design, 95, 262, 2015 |
9 |
Numerical study of the particle residence time and flow characters in an Opposed Multi-Burner gasifier Li C, Dai ZH, Xu JL, Yang J, Yu GS, Wang FC Powder Technology, 286, 64, 2015 |
10 |
Development of an axisymmetric population balance model for spray drying and validation against experimental data and CFD simulations Pinto M, Kemp I, Bermingham S, Hartwig T, Bisten A Chemical Engineering Research & Design, 92(4), 619, 2014 |