| 81 - 89 |
Steady state model of the electrochemical process of brine electrolysis in DeNora amalgam reactors
Oniciu L, Agachi S, Bugan J, ImreLucaci A |
| 91 - 98 |
Secondary flow generated in curved flow
Nemeth J, Bucsky G |
| 99 - 102 |
Studies of ion-exchange purification process of Sm(III) complexes with HEDTA from Ho(III) on anion-exchangers
Hubicka H, Drobek D |
| 103 - 107 |
Thermal deactivation of V2O5/TiO2 catalyst used in selective catalytic reduction of NOx
Tac PC, Egyhazy T, Kovacs J |
| 109 - 114 |
Prediction of crystal size by Nielsen nucleation model
Liszi I, HasznosNezdei M |
| 115 - 125 |
Modelling and dynamic simulation of the stochastic behaviour of bulk solid mixing
Diaz E, Szepvolgyi J, Gyenis J |
| 127 - 135 |
Computer aided designing of heat exchanger networks
Jezowski J, Jezowska A |
| 137 - 145 |
Interaction of kinetics, diffusion and geometric structure of pore networks in catalyst supports - A percolation theoretical approach to hydrodemetallation
Rieckmann C, Duren T, Keil FJ |
| 147 - 152 |
Modelling of diffusion and reaction phenomena in electrolytes: Nitrate reduction on a bimetal catalyst immobilized in poly(vinyl-alcohol)-hydrogel
Fergg F, Keil FJ |
| 153 - 155 |
Skeletal isomerization of n-hexane over platinum-loaded h-mordenite
Hollo A, Hancsok J |
| 157 - 160 |
Chemically activated carbons from sugar cane bagasse fractions
Lavarack BP |
