1031 - 1040 |
The use of simulation techniques in developing kinetic models for polymerization Busch M, Muller M, Wulkow M |
1041 - 1044 |
Three-dimensional numerical simulation of flow-induced tube bundle vibration Fischer M |
1044 - 1046 |
Influence of the nozzle geometry on spray-dried particle formation expanding superheated suspensions Monse K, Linnepe T, Groom S, Walzel P |
1047 - 1051 |
Time- and velocity-dependent properties of powders effecting slip-stick oscillations Schulze D |
1051 - 1054 |
Flow tube with mobile sampling orifice: A compact reaction system for toxic and corrosive gases and aerosols Letzel T, Schauer C, Niessner R, Poschl U |
1055 - 1060 |
Influence of the transport properties of the crystal/heat transfer surface interfacial on fouling behavior Bohnet M |
1061 - 1067 |
Mass transfer in trickle-bed reactors with structured packing Battista J, Bohm U |
1068 - 1073 |
Mass transfer in a flat gas/liquid interface using non-Newtonian media Gomez-Diaz D, Navaza JM |
1074 - 1079 |
Comparison of hydrodynamics and mass transfer in airlift and bubble column reactors using CFD van Baten JM, Krishna R |
1080 - 1083 |
Determination of local gas holdup and volumetric mass transfer coefficient in a bubble column by means of an ultrasonic method and neural network Supardan MD, Maezawa A, Uchida S |
1084 - 1087 |
Sol-gel-derived Sb-doped SnO2 nanoparticles controlled in size by Nb2O5 Zhu XL, Geis-Gerstorfer J |