화학공학소재연구정보센터
검색결과 : 11건
No. Article
1 Mesh size effect on CFD simulation of gas-fluidized Geldart A particles
Sande PC, Ray S
Powder Technology, 264, 43, 2014
2 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
3 A new approach to the identification of transitions in fluidized beds
Davies CE, Krouse D, Carroll A
Powder Technology, 199(1), 107, 2010
4 Hydrodynamics of Geldart group A particles in gas-solid fluidized beds
Leu LP, Tsai FC
Korean Journal of Chemical Engineering, 26(2), 513, 2009
5 The minimum bubbling velocity of fluidized beds operating at high temperature
Girimonte R, Formisani B
Powder Technology, 189(1), 74, 2009
6 Micro fluidized beds: Wall effect and operability
Liu XH, Xu GW, Gao SQ
Chemical Engineering Journal, 137(2), 302, 2008
7 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
8 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
9 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
10 Use of angle of repose and bulk densities for powder characterization and the prediction of minimum fluidization and minimum bubbling velocities
Wong ACY
Chemical Engineering Science, 57(14), 2635, 2002