| 885 - 900 |
Microwave and ultrasonic processing: Now a realistic option for industry
Leonelli C, Mason TJ |
| 901 - 911 |
Surfactant-free emulsion polymerisation of methyl methacrylate and methyl acrylate using intensified processing methods
Dobie CG, Boodhoo KVK |
| 912 - 922 |
Design principles of microwave applicators for small-scale process equipment
Sturm GSJ, Stefanidis GD, Verweij MD, Van Gerven TDT, Stankiewicz AI |
| 923 - 929 |
Gas-liquid mass transfer in periodically operated trickle-bed reactors: Influence of the liquid-phase physical properties and flow modulation
Borren B, Zeitler O, Schmaus C, Agar DW |
| 930 - 935 |
Intensification of organic reactions with hybrid flow reactors
Cravotto G, Bonrath W, Tagliapietra S, Speranza C, Gaudino EC, Barge A |
| 936 - 942 |
Intensification of heat transfer process: Improvement of shell-and-tube heat exchanger performances by means of ultrasound
Gondrexon N, Rousselet Y, Legay M, Boldo P, Le Person S, Bontemps A |
| 943 - 952 |
Sequence of monolithic converters DOC-CDPF-NSRC for lean exhaust gas detoxification: A simulation study
Schejbal M, Stepanek J, Koci P, Marek M, Kubicek M |
| 953 - 957 |
Falling liquid film stability in microgas/liquid absorption
Monnier H, Mhiri N, Falk L |
| 958 - 964 |
Fischer-Tropsch synthesis in milli-structured fixed-bed reactors: Experimental study and scale-up considerations
Knochen J, Guttel R, Knobloch C, Turek T |
| 965 - 972 |
Pilot plant synthesis of n-propyl propionate via reactive distillation with decanter separator for reactant recovery. Experimental model validation and simulation studies
Altman E, Kreis P, van Gerven T, Stefanidis GD, Stankiewicz A, Gorak A |
| 973 - 978 |
Structured catalytic wall microreactor for efficient performance of exothermic reactions
Kiwi-Minsker L, Ruta M, Eslanloo-Pereira T, Bromley B |
| 979 - 991 |
Application of generic principles of process intensification to solution crystallization enabled by a task-based design approach
Lakerveld R, Kramer HJM, Stankiewicz AI, Grievink J |
