| 1 |
Reduction in minimum fluidization velocity and minimum bubbling velocity in gas-solid fluidized beds due to vibration
McLaren CP, Metzger JP, Boyce CM, Muller CR
Powder Technology, 382, 566, 2021 |
| 2 |
Mesh size effect on CFD simulation of gas-fluidized Geldart A particles
Sande PC, Ray S
Powder Technology, 264, 43, 2014 |
| 3 |
CFD study of the minimum bubbling velocity of Geldart A particles in gas-fluidized beds
Wang JW, van der Hoef MA, Kuipers JAM
Chemical Engineering Science, 65(12), 3772, 2010 |
| 4 |
A new approach to the identification of transitions in fluidized beds
Davies CE, Krouse D, Carroll A
Powder Technology, 199(1), 107, 2010 |
| 5 |
Hydrodynamics of Geldart group A particles in gas-solid fluidized beds
Leu LP, Tsai FC
Korean Journal of Chemical Engineering, 26(2), 513, 2009 |
| 6 |
The minimum bubbling velocity of fluidized beds operating at high temperature
Girimonte R, Formisani B
Powder Technology, 189(1), 74, 2009 |
| 7 |
Micro fluidized beds: Wall effect and operability
Liu XH, Xu GW, Gao SQ
Chemical Engineering Journal, 137(2), 302, 2008 |
| 8 |
Determination of intrinsic minimum bubbling velocity in fine powder aerations based on experimentally measured elastic deformation coefficients
Wiratni W, Kono HO
Canadian Journal of Chemical Engineering, 83(3), 418, 2005 |
| 9 |
Prediction of minimum bubbling velocity, fluidization index and range of particulate fluidization for gas-solid fluidization in cylindrical and non-cylindrical beds
Singh RK, Roy GK
Powder Technology, 159(3), 168, 2005 |
| 10 |
Minimum bubbling velocity and homogeneous fluidization region under reduced pressure for group-A powders
Mawatari Y, Kawai A, Tatemoto Y, Noda K
Journal of Chemical Engineering of Japan, 37(1), 89, 2004 |
