719 - 727 |
New granular material for hot gas filtration: Use of the "Lapilli" Macias-Machin A, Socorro M, Verona JM, Macias M |
728 - 733 |
Concepts of phase separation in supercritical processing Zacchi P, Pietsch A, Voges S, Ambrogi A, Eggers R, Jaeger P |
734 - 746 |
Flow pattern and transition of rectangular spout-fluid bed Zhong WQ, Zhang MY, Jin BS, Chen XP |
747 - 754 |
Experiment and prediction of breakthrough curves for packed bed adsorption of water vapor on cornmeal Chang H, Yuan XG, Tian H, Zeng AW |
755 - 763 |
Influence of diluent on amine extraction of pyruvic acid using Alamine system Senol A |
764 - 772 |
Effect of surface-active agents on the phase holdups of three-phase fluidized beds Dargar P, Macchi A |
773 - 782 |
Coupling activity coefficient models, Henry constant equations, and equations of state to calculate vapor-liquid and solid-liquid equilibrium data Ferrando N, Lugo R, Mougin P |
783 - 791 |
Influence of controlled nucleation by ultrasounds on ice morphology of frozen formulations for pharmaceutical proteins freeze-drying Nakagawa K, Hottot A, Vessot S, Andrieu J |
792 - 797 |
Optimal rotating speed in a rotated wired thermal diffusion column with transverse sampling streams Yeh HM |
798 - 805 |
Flow stability in a downer mixing chamber McMillan J, Briens C, Berruti F |
806 - 811 |
A simple treatment of mass transfer data in continuous dialyzer Palaty Z, Zakova A, Petrik P |