971 - 971 |
Tribute to Albert Renken Kiwi-Minsker L |
972 - 978 |
Quantitative prediction of flow patterns in liquid-liquid flow in micro-capillaries Kashid M, Kiwi-Minsker L |
979 - 990 |
Villermaux-Dushman protocol for experimental characterization of micromixers Commenge JM, Falk L |
991 - 997 |
Stripping of acetone from isopropanol solution with membrane and mesh gas-liquid contactors Sun XY, Constantinou A, Gavriilidis A |
998 - 1009 |
Measurement and analysis of spatial reactor profiles in high temperature catalysis research Korup O, Mavlyankariev S, Geske M, Goldsmith CF, Horn R |
1010 - 1016 |
Evaporation of hydrogen peroxide with a microstructured falling film Klemm E, Mathivanan G, Schwarz T, Schirrmeister S |
1017 - 1026 |
Scale-up concept for modular microstructured reactors based on mixing, heat transfer, and reactor safety Kockmann N, Roberge DM |
1027 - 1034 |
A conceptual framework for description of complexity in intensive chemical processes Lapkin AA, Voutchkova A, Anastas P |
1035 - 1040 |
Large Eddy Simulation of mixing effects on the course of parallel chemical reactions and comparison with k-epsilon modeling Makowski L, Baldyga J |
1041 - 1053 |
Nanosized catalysts as a basis for intensifications of technologies Sulman EM, Valetsky PM, Sulman MG, Bronstein LM, Sidorov AI, Doluda VY, Matveeva VG |
1054 - 1062 |
Catalytic syngas production from greenhouse gasses: Performance comparison of Ru-Al2O3 and Rh-CeO2 catalysts Djinovic P, Crnivec IGO, Batista J, Levec J, Pintar A |
1063 - 1068 |
Limiting withdrawal rate and maximum film thickness during dip-coating of titania sols onto a Si substrate Rebrov EV, Schouten JC |
1069 - 1075 |
Pressure drop and mixing in single phase microreactors: Simplified designs of micromixers Holvey CP, Roberge DM, Gottsponer M, Kockmann N, Macchi A |
1076 - 1084 |
Revisiting shrinking particle and product layer models for fluid-solid reactions - From ideal surfaces to real surfaces Salmi T, Grenman H, Warna J, Murzin DY |
1085 - 1094 |
A simple device to test biodiesel process intensification Santacesaria E, Di Serio M, Tesser R, Tortorelli M, Turco R, Russo V |
1095 - 1107 |
Effect of rotor-stator distance and rotor radius on the rate of gas-liquid mass transfer in a rotor-stator spinning disc reactor Meeuwse M, Hamming E, van der Schaaf J, Schouten JC |
1108 - 1114 |
Hydrodynamics and mass transfer in carbon-nanofiber/graphite-felt composite under two phase flow conditions Cao YJ, Li P, Zhou JH, Sui ZJ, Zhou XG |