769 - 779 |
Liquid jet-array cooling modules for high heat fluxes Oh CH, Lienhard JH, Younis HF, Dahbura RS, Michels D |
780 - 790 |
Imaging stirred-vessel macromixing using electrical resistance tomography Holden PJ, Wang M, Mann R, Dickin FJ, Edwards RB |
791 - 798 |
Drying kinetics of polymer films Guerrier B, Bouchard C, Allain C, Benard C |
799 - 809 |
Olefin/paraffin separations by adsorption : pi-complexation vs. kinetic separation Rege SU, Padin J, Yang RT |
810 - 822 |
Feasibility of extractive distillation in a batch rectifier Lelkes Z, Lang P, Benadda B, Moszkowicz P |
823 - 830 |
Improved direct and indirect systems of columns for ternary distillation Agrawal R, Fidkowski ZT |
831 - 835 |
Effects of Marangoni surface tension forces on modern distillation packings Proctor SJ, Biddulph MW, Krishnamurthy KR |
836 - 848 |
Lumen mass transfer in hollow-fiber membrane processes with nonlinear boundary conditions Qin YJ, Cabral JMS |
849 - 858 |
Internally staged permeator prepared from annular hollow fibers for gas separation Li K, Wang DL, Li DF, Teo WK |
859 - 863 |
Back mixing in a reciprocating plate column with stable density gradients Rao NVR, Baird MHI |
864 - 875 |
Synchronization of batch trajectories using dynamic time warping Kassidas A, MacGregor JF, Taylor PA |
876 - 887 |
Product and process development using artificial neural-network model and information analysis Chen JH, Wong DSH, Jang SS, Yang SL |
888 - 895 |
Analysis of instability in an industrial ammonia reactor Morud JC, Skogestad S |
896 - 911 |
Design of single-product campaign batch plants under demand uncertainty Petkov SB, Maranas CD |
912 - 920 |
Investigation of a complex reaction network : I. Experiments in a high-pressure trickle-bed reactor Khadilkar MR, Jiang Y, Al-Dahhan M, Dudukovic MP, Chou SK, Ahmed G, Kahney R |
921 - 926 |
Investigation of a complex reaction network : II. Kinetics, mechanism and parameter estimation Jiang Y, Khadilkar MR, Al-Dahhan M, Dudukovic MP, Chou SK, Ahmed G, Kahney R |
927 - 936 |
Steam reforming of naphthalene on Ni-Cr/Al2O3 catalysts doped with MgO, TiO2, and La2O3 Bangala DN, Abatzoglou N, Chornet E |
937 - 942 |
Structural stability of kinetic models : Anomalies due to irreversible adsorption Nibbelke RH, Hoebink JHBJ, de Croon MHJM, Marin GB |
943 - 950 |
Study of the morphological hysteresis in immiscible polymer blends Minale M, Mewis J, Moldenaers P |
951 - 958 |
Droplet size evolution during coalescence in semiconcentrated model blends Vinckier I, Moldenaers P, Terracciano AM, Grizzuti N |
959 - 971 |
Modeling and simulation of shell and tube heat exchangers under milk fouling Georgiadis MC, Rotstein GE, Macchietto S |
972 - 977 |
Numerical investigation of mixing efficiency of helical ribbons de la Villeon J, Bertrand F, Tanguy PA, Labrie R, Bousquet J, Lebouvier D |
978 - 981 |
Existence of a critical particle concentration in plugging of a packed bed Pandya VB, Bhuniya S, Khilar KC |
982 - 988 |
Fluoroptic solids holdup measurement in slurry systems Huizenga P, Meijer R, Kuipers JAM, van Swaaij WPM |
989 - 992 |
Effect of CO2 on expansion and supersaturation of saturated solutions Tai CY, Cheng CS |
993 - 998 |
Robust nonlinear control of chemical reactors Dainson BE, Lewin DR |
999 - 1002 |
Synthesis of multipass heat exchanger networks Reddy KA, Rao CDP, Davies GS |