789 - 802 |
Improvements of a hollow fiber reverse osmosis desalination model: Analysis of numerical results Marcovecchio MG, Scenna NJ, Aguirre PA |
803 - 808 |
On the effect of phase fraction on drop size distribution of liquid-liquid dispersions in agitated vessels Razzaghi K, Shahraki F |
809 - 818 |
Mixing studies of non-Newtonian fluids in an anchor agitated vessel Triveni B, Vishwanadham B, Madhavi T, Venkateshwar S |
819 - 826 |
Experimental studies on phase inversion in a small diameter horizontal pipe De B, Mandal TK, Das G |
827 - 843 |
Turbulent flow of shear-thinning liquids in stirred tanks-The effects of Reynolds number and flow index Venneker BCH, Derksen JJ, Van den Akker HEA |
844 - 860 |
An overall thermodynamic view of processes: Comparison of fuel producing processes Patel B, Hildebrandt D, Glasser D |
861 - 874 |
Control of proton exchange membrane fuel cells using data driven state space models Methekar RN, Patwardhan SC, Rengaswamy R, Gudi RD, Prasad V |
875 - 880 |
Design of Controllers for a Fluidized Catalytic Cracking Process Pandimadevi G, Indumathi P, Selvakumar V |
881 - 892 |
Treatment of oily wastewater using low cost ceramic membrane: Comparative assessment of pore blocking and artificial neural network models Nandi BK, Moparthi A, Uppaluri R, Purkait MK |
893 - 898 |
Prediction of solute solubility in supercritical carbon dioxide: A novel semi-empirical model Nejad SJ, Abolghasemi H, Moosavian MA, Maragheh MG |
899 - 910 |
Air flow patterns in an industrial milk powder spray dryer Gabites JR, Abrahamson J, Winchester JA |
911 - 917 |
Application of CFD and breakage modelling for predicting the size reduction of protein precipitates during transport Zumaeta N, Byrne EP, Fitzpatrick JJ |