690 - 695 |
Environmental biotechnology: Challenges and opportunities for chemical engineers Chen W, Mulchandani A, Deshusses MA |
696 - 712 |
Three-dimensional simulation of bubble column flows with bubble coalescence and breakup Chen P, Dudukovic MP, Sanyal J |
713 - 724 |
Optimal feeding for tower-type reactors Fu CC, Lu SY, Wu WT |
725 - 739 |
Turbulent mixing in a tubular reactor: Assessment of an FDF/LES approach van Vliet E, Derksen JJ, van den Akker HEA |
740 - 749 |
Studies on strongly swirling flows in the full space of a volute cyclone separator Hu LY, Zhou LX, Zhang J, Shi MX |
750 - 758 |
Flow normal to a flat plate of a viscoplastic fluid with inertia effects Savreux F, Jay P, Magnin A |
759 - 765 |
Concentration of Gengnian'an extract with a vapor-liquid-solid evaporator Liu MY, Yang Y, Li XI, Nie WD, Ling NS, Pan LJ |
766 - 775 |
An investigation of the mechanism of liquid injection into fluidized beds Bruhns S, Werther J |
776 - 790 |
Experimental and numerical study of a rotating wheel air classifier Karunakumari L, Eswaraiah C, Jayanti S, Narayanan SS |
791 - 801 |
Dispersion of particle pulses in fluidized beds measured by positron emission tomography Dechsiri C, Van der Zwan EA, Dehling HG, Hoffmann AC |
802 - 835 |
Experimental investigation of the hydrodynamics in a liquid-solid riser Roy S, Kernoun A, Al-Dahhan MH, Dudukovic MP |
836 - 844 |
Simulation and experiments of mixing and segregation in a tote blender Sudah OS, Arratia PE, Alexander A, Muzzio FJ |
845 - 853 |
Study on suspension catalytic distillation for synthesis of linear alkylbenzene Wang EQ, Li CY, Wen LY, Min E |
854 - 866 |
Influence of mass transfer in distillation: Feasibility and design Baur R, Krishna R, Taylor R |
867 - 877 |
Multiscale models of sweep gas and porous support effects on zeolite membranes Skoulidas AI, Sholl DS |
878 - 894 |
Mass and heat transfer modeling of a physical vapor deposition effusion source Junker ST, Birkmire RW, Doyle FJ |
895 - 908 |
Optimal transition and robust control design for exothermic continuous reactors Flores-Tlacuahuac A, Alvarez J, Saldivar-Guerra E, Oaxaca G |
909 - 921 |
Optimal production and scheduling of a process with decaying catalyst Bizet VM, Grossmann IE, Juhasz NM |
922 - 930 |
Rapid generation of composition profiles for reactive and extractive cascades Chin J, Lee JW |
931 - 945 |
Statistical batch process monitoring using gray models Van Sprang ENM, Ramaker HJ, Westerhuis JA, Smilde AK |
946 - 959 |
Recursive estimation in constrained nonlinear dynamical systems Vachhani P, Rengaswamy R, Gangwal V, Narasimhan S |
960 - 970 |
Modeling and kinetics of allylation of phenol in a triphase-catalytic membrane reactor Wu HS, Lo MH |
971 - 981 |
Kinetics of dibenzylether hydrothermolysis in supercritical water Gonzalez G, Montane D |
982 - 988 |
Design of micro-scale fuel processors assisted by numerical modeling Cao CS, Wang Y, Holladay JD, Jones EO, Palo DR |
989 - 997 |
Electrochemically enhanced biosynthesis of gluconic acid Gros P, Bergel A |
998 - 1008 |
Deactivation dynamics of rough catalytic surfaces Filoche M, Sapoval B |
1009 - 1021 |
Continuous RAFT miniemulsion polymerization of styrene in a train of CSTRs Smulders WW, Jones CW, Schork FJ |
1022 - 1031 |
Flocculation mechanism induced by phenolic resin/PEO and floc properties Negro C, Fuente E, Blanco A, Tijero J |
1032 - 1041 |
Concentration enrichment in confined, gradient energy systems Kosto TJ, Nauman EB |
1042 - 1047 |
Increased biofilm activity in BGAC reactors Herzberg M, Dosoretz CG, Green M |
1048 - 1052 |
Using a stirred cell to evaluate structural changes in proteins adsorbed on particles Yoon JY, Garrell RL, Choi SW, Kim JH, Kim WS |