| 2767 - 2775 |
Separation of binary mixtures by dense membrane processes: influence of inert gas entrance under variable downstream pressure conditions
Vallieres C, Favre E, Arnold X, Roizard D |
| 2777 - 2784 |
TEOM analysis of the equilibria and kinetics of n-hexane and n-heptane adsorption on FCC catalyst/silicalite
Alpay E, Chadwick D, Kershenbaum LS, Barrie PJ, Sivadinarayana C, Gladden LF |
| 2785 - 2795 |
A critical comparison between the wave model and the standard dispersion model
Iordanidis AA, Annaland MV, Kronberg AE, Kuipers JAM |
| 2797 - 2803 |
Permeation behavior during the catalytic oxidation of CO in a Pt-loaded Y-type zeolite membrane
Hasegawa Y, Sotowa KI, Kusakabe K |
| 2805 - 2821 |
The bifurcation behavior of continuous free-radical solution loop polymerization reactors
Melo PA, Biscaia EC, Pinto JC |
| 2823 - 2834 |
Asymptotic analysis of a complex reaction scheme in solid-liquid system
Haario H, Kalachev L |
| 2835 - 2855 |
Method for inferring contact angle and for correlating static liquid hold-up in packed beds
Ortiz-Arroyo A, Larachi F, Iliuta I |
| 2857 - 2874 |
Powder flowability and density ratios: the impact of granules packing
Santomaso A, Lazzaro P, Canu P |
| 2875 - 2882 |
A parametric study of direct gravure coating
Kapur N |
| 2883 - 2891 |
Derivation of supersaturation and nucleation flux during precipitation from the mixing pattern of an inert tracer in the same device: case of unmixed feed streams
David R, Fall A, Lecoq O |
| 2893 - 2902 |
Particle size distributions and viscosity of suspensions undergoing shear-induced coagulation and fragmentation
Barthelmes G, Pratsinis SE, Buggisch H |
| 2903 - 2909 |
Continuous distribution theory for Ostwald ripening: comparison with the LSW approach
Madras G, McCoy BJ |
| 2911 - 2919 |
Enzymatic degradation of poly (epsilon-caprolactone), poly (vinyl acetate) and their blends by lipases
Sivalingam G, Chattopadhyay S, Madras G |
| 2921 - 2930 |
Simulation and thermodynamic analysis of conventional and oxygen permeable CPO reactors
Ji PJ, van der Kooi HJ, Arons JD |
| 2931 - 2936 |
Molecular thermodynamics approach for liquid-liquid equilibria of the symmetric polymer blend systems
Chang BH, Bae YC |
| 2937 - 2949 |
On the origin, frequency and magnitude of macro-instabilities of the flows in stirred vessels
Nikiforaki L, Montante G, Lee KC, Yianneskis M |
| 2951 - 2962 |
The role of convection and turbulent dispersion in blending
Patwardhan AW, Pandit AB, Joshi JB |
| 2963 - 2972 |
Modeling the protein partitioning in aqueous polymer two-phase systems: influence of polymer concentration and molecular weight
Lin DQ, Wu YT, Mel LH, Zhu ZQ, Yao SJ |
| 2973 - 2984 |
State multiplicity in PFR-separator-recycle polymerization systems
Kiss AA, Bildea CS, Dimian AC, Iedema PD |
| 2985 - 2993 |
A new approach to modelling of single droplet drying
Farid M |
| 2995 - 3004 |
Bubble flow in trickle beds: investigations using resistive sensors
Rode S, Benkrid K, Gillier T, Midoux N |
| 3005 - 3023 |
Nearly irreversible, fast heterogeneous reactions in premixed flow
Mchedlov-Petrossyan PO, Khomenko GA, Zimmerman WB |
| 3025 - 3047 |
Bounded robust control of constrained multivariable nonlinear processes
El-Farra NH, Christofides PD |
| 3049 - 3051 |
Analytical solution for a population balance equation with aggregation and fragmentation
McCoy BJ, Madras G |
| 3053 - 3057 |
Comparison among attrition-reaction models of SO2 capture by uncalcined limestone under pressurized fluidized bed combustion conditions
Shimizu T, Peglow M, Yamagiwa K, Tanaka M |
