| 823 - 827 |
Interactivity and automated process design
Fraga ES, Wang KF, Salhi A |
| 828 - 832 |
Plant-wide integration of information and decision support systems: Present tools and limitations
Espuna A, Nougues JM, Puigjaner L |
| 832 - 835 |
Solution crystallization - Developments and new trends
Ulrich J |
| 835 - 840 |
Catalytic and multiphase reactors for the future
Keurentjes JTF, Goetheer ELV, Gielens FC, Kuijpers MWA, Heijnen JHM, van den Broeke LJP, Kemmere MF, Vorstman MAG |
| 840 - 845 |
Particle design using supercritical fluids
Reverchon E, Della Porta G |
| 845 - 852 |
Spouted bed reactors
Olazar M, Alvarez S, Aguado R, Jose MJS |
| 852 - 857 |
Microporous solid characterization: Use of classical and "new" techniques
Lozano-Castello D, Cazorla-Amoros D, Linares-Solano A |
| 857 - 862 |
Fuel cells, advanced reactors and smart catalysis: The exploitation of ceramic ion-conducting membranes
Metcalfe IS |
| 862 - 868 |
Two-phase flow with mass transfer in bubble columns
Mewes D, Wiemann D |
| 868 - 874 |
Sustainable growth and chemical engineering
Venselaar J |
| 874 - 879 |
Influence of reaction kinetics on the performance of a chromatographic reactor
Herbsthofer R, Bart HM |
| 881 - 889 |
Monitoring crystallization kinetics of azelaic acid by in situ FTIR spectroscopy in three-phase systems
Nattkemper A, Schleiden T, Migliavacca JM, Melin T |
| 890 - 901 |
Nonstationary simulation model of absorber with falling film of suspension
Gerbec M, Stergarsek A, Kocjancic R |
| 902 - 907 |
Theoretical investigation of a Pd-membrane reactor for methanol synthesis
Rahimpour MR, Ghader S |
| 908 - 911 |
Performance of a new mixed down pumping impeller
Ascanio G, Foucault W, Tanguy PA |
