2682 - 2686 |
Proteomics: An exciting new science, but where are the chemical engineers? Lee KH, Reardon KF |
2687 - 2699 |
Fundamental approach to the design and optimization of static mixers Szalai ES, Muzzio FJ |
2700 - 2714 |
Numerical simulation of solids suspension in a stirred tank Derksen JJ |
2715 - 2727 |
Three-dimensional wave dynamics on a failing film and associated mass transfer Park CD, Nosoko T |
2728 - 2748 |
Unified model for NOX absorption in aqueous alkaline and dilute acidic solutions Patwardhan JA, Joshi JB |
2749 - 2758 |
Chaotic advection in a three-dimensional stokes flow Rodrigo AJS, Mota JPB, Lefevre A, Leprevost JC, Saatdjian E |
2759 - 2767 |
Transient method for the liquid laminar flow friction factor in microtubes Brutin D, Topin F, Tadrist L |
2768 - 2772 |
Mixing of pseudoplastic fluids using helical ribbon impellers Shekhar SM, Jayanti S |
2773 - 2782 |
Microstreaming effects on particle concentration in an ultrasonic standing wave Spengler JF, Coakley WT, Christensen KT |
2783 - 2792 |
Analysis of boundary layer and solute transport in osmotic evaporation Romero J, Rios GM, Sanchez J, Saavedra A |
2793 - 2801 |
Fluid dynamic simulation of O-3 decomposition in a bubbling fluidized bed Syamlal M, O'Brien TJ |
2802 - 2809 |
Observations and process parameter sensitivities in fluid-bed granulation Cryer SA, Scherer PN |
2810 - 2821 |
Scaling and intensification procedures for simulated moving-bed systems Kim JK, Wankat PC |
2822 - 2841 |
Graphical and stage-to-stage methods for reactive distillation column design Daza OS, Perez-Cisneros ES, Bek-Pedersen E, Gani R |
2842 - 2849 |
Flow-induced particulate separations Roberts BW, Olbricht WL |
2850 - 2863 |
Design of SMB for a nonlinear amino acid system with mass-transfer effects Xie Y, Farrenburg CA, Chin CY, Mun S, Wang NHL |
2864 - 2884 |
Thermodynamically equivalent configurations for thermally coupled distillation Caballero JA, Grossmann IE |
2885 - 2899 |
Target linearization and model predictive control of polymerization processes Bindlish R, Rawlings JB |
2900 - 2917 |
Mixed-logic dynamic optimization applied to batch distillation process design Oldenburg J, Marquardt W, Heinz D, Leineweber DB |
2918 - 2932 |
Integrated approach to optimization of an ultrasonic processor Moholkar VS, Warmoeskerken MMCG |
2933 - 2936 |
Glucose hydrogenation in a membrane trickle-bed reactor Diakov V, Varma A |
2937 - 2947 |
Novel solar reactor for studying ultrafast gas-solid reactions above 2,000 K Steiner E, Ganz J, Meier A, Sturzenegger M |
2948 - 2956 |
Regular solution model for asphaltene precipitation from bitumens and solvents Alboudwarej H, Akbarzadeh K, Beck J, Svrcek WY, Yarranton HW |
2957 - 2965 |
New solid equation of state combining excess energy mixing rule for solid-liquid equilibria Twu CH, Tassone V, Sim WD |
2966 - 2973 |
Multilamellar vesicles in a commercial surfactant system Liaw MS, Mackley MR, Bridgwater J, Moggridge GD, Bayly AE |
2974 - 2979 |
Analytical breakthrough curves for inert core adsorbent with sorption kinetics Li P, Xiu GH, Rodrigues AE |
2980 - 2983 |
Real-time optimization in nonlinear chemical processes: Need for global optimizer Lacks DJ |
2984 - 2987 |
Microfiber assisted fabrication of microfluidic channels using poly(dimethylsiloxane) Huang TT, Chang WJ, Akin D, Gomez R, Bashir R, Mosier N, Ladisch MR |