869 - 872 |
On the relation between ideal and real mixtures in multicomponent distillation Vogelpohl A |
873 - 877 |
Determination of the power law exponent from magnetic resonance imaging (MRI) flow data Heinen C, Guthausen G, Buggisch H |
877 - 882 |
Effect of heterogenic surfaces on contact angle hysteresis: Dynamic contact angle analysis in material sciences Rupp F, Scheideler L, Geis-Gerstorfer J |
882 - 885 |
Potential of pollutant treatment by combined extraction and oxidation with supercritical carbon dioxide Kruse A, Dahmen N, Dinjus E |
885 - 888 |
Dust redeposition during regeneration of surface filters Schmidt E, Bach B, Xu XY |
888 - 890 |
Prevention of water hammer and cavitational hammer in pipeline systems Dudlik A, Schonfeld SBH, Schluter S, Fahlenkamp H, Prasser HM |
891 - 895 |
Modeling of char holdup and char particle size distributions in circulating fluidized bed combustors Lucke K, Hartge EU, Werther J |
896 - 898 |
Conversion of a wet-process flue-gas desulfurization plant from quicklime (CaO) to chalk (CaCO3) Peschen N |
899 - 904 |
Electrostatic drop formation in liquid/liquid systems Gneist G, Bart HJ |
905 - 910 |
Mass transfer mechanisms in the fixed-bed ion-exchange process for dilute colloidal silica manufacture Falamaki C |
911 - 915 |
The segregation in the binary-solid liquid fluidized bed Hu XH |
917 - 920 |
Formation of zeolite (MFI) layers on gauze wire and arranged packing segment Brehm A, Zanter KD |
921 - 924 |
The potential use of low-grade phosphate rocks as adsorbent Kandah MI |
925 - 928 |
Non-stick droplets Quere D, Aussillous P |