987 - 990 |
A comparative study of catalytic opening of epoxides by alcohols Garcia R, Martinez M, Aracil J |
991 - 994 |
Regeneration of hydrophobic zeolites with steam Kuntzel J, Ham R, Melin T |
994 - 997 |
Simulation of particle movement on vibrating conveyors Walzel P, Landwehr F |
997 - 1000 |
Polymer modification in a vibratory mill Janke G, Frendel A, Schmidt-Naake G |
1001 - 1006 |
Wet chemical UV oxidation of 2-fluorophenol optimization with chosen reaction parameters Kreisel G, Schmidt M |
1006 - 1009 |
Influence of fluid dynamics on collection and agglomeration of aerosols in a fluidized bed Fleck S, Riebel U |
1010 - 1011 |
The effect of thermal cycling damage on the permeability and structure of transparent gas barrier films Henry BM, Norenberg H, Dinelli F, Grovenor CRM, Briggs GAD, Tsukahara Y, Miyamoto T |
1012 - 1016 |
Flow distribution concepts for new type monolithic co- or countercurrent reactors Frauhammer J, Friedrich G, Kolios G, Klingel T, Eigenberger G, von Hippel L, Arntz D |
1017 - 1027 |
Modeling hydrodynamic cavitation Kumar PS, Pandit AB |
1029 - 1033 |
Feed cycling in dead end filtration Richter U, Kohler W, Cabassud C, Sutter F, Bouaifi M |
1035 - 1038 |
Short stopping of runaway methyl methacrylate polymerizations Platkowski K, Reichert KH |
1039 - 1042 |
Modeling of temperature-programmed surface reactions Hinrichsen O, Hornung A, Muhler M |
1043 - 1049 |
Experimental study on a co-current gas-liquid down flow contactor with gas entrainment by a liquid jet Maalej S, Benadda B, Dabaliz A, Otterbein M |
1051 - 1058 |
Parallel bubble columns with fed-batch technique for microbial process development on a small scale Altenbach-Rehm J, Nell C, Arnold M, Weuster-Botz D |
1059 - 1061 |
Selective hydrogenation of an acetylene process: An example of modeling an industrial reactor process Szukiewicz M, Petrus R |
1063 - 1067 |
Computing homogeneous azeotropes using interval analysis Maier RW, Brennecke JF, Stadtherr MA |