화학공학소재연구정보센터
검색결과 : 10건
No. Article
1 Effect of bed geometry on operating pressure drop and minimum fluidizing velocity in a draft tube spout-fluid bed
Zhang TT, Huang GQ, Su GL, Liu SF, Zhou YM
Canadian Journal of Chemical Engineering, 97(8), 2318, 2019
2 A review of different solvents, mass transfer, and hydrodynamics for postcombustion CO2 capture
Mirzaei S, Shamiri A, Aroua MK
Reviews in Chemical Engineering, 31(6), 521, 2015
3 Experimental study of counter-current gas-droplet flow limitation in a 30 cm pipe
Miwa S, Liu Y, Hibiki T, Ishii M, Kondoh Y, Ukai N, Tanimoto K
Chemical Engineering Science, 92, 167, 2013
4 Calculation of the hydrogen production rate by a palladium membrane separator: Theoretical approaches
Xie DL, Lu NN, Wang F, Fan SS
International Journal of Hydrogen Energy, 38(25), 10802, 2013
5 Fluid bed gas RTD: Effect of fines and intemals
Lorences MJ, Laviolette JP, Patience GS, Alonso M, Diez FV
Powder Technology, 168(1), 1, 2006
6 Gas-liquid mass transfer in pulp retention towers
Rewatkar VB, Bennington CPJ
Canadian Journal of Chemical Engineering, 82(3), 465, 2004
7 Significance of core diameter variation in the lateral solid transfer model for the upper dilute region of circulating fluidized beds
Horio M, Lei HW
Advanced Powder Technology, 9(2), 107, 1998
8 Liquid hold-up and backmixing in cocurrent upflow three-phase fixed-bed reactors
Cassanello M, Martinez O, Cukierman AL
Chemical Engineering Science, 53(5), 1015, 1998
9 Loop Venturi reactor - A feasible alternative to stirred tank reactors?
van Dierendonck LL, Zahradnik J, Linek V
Industrial & Engineering Chemistry Research, 37(3), 734, 1998
10 Pressure drop and liquid holdup in trickle flow reactors: Improved Ergun constants and slip correlations for the slit model
Iliuta I, Larachi F, Grandjean BPA
Industrial & Engineering Chemistry Research, 37(12), 4542, 1998