2 - 8 |
Protein and peptide biomimicry: Gold-mining inspiration from nature's ingenuity Czyzewski AM, Barron AE |
9 - 19 |
Derivation, simulation and validation of a cohesive particle flow CFD model van Wachem B, Sasic S |
20 - 31 |
Stability analysis of core-annular flow and neutral stability wave number Rodriguez OMH, Bannwart AC |
32 - 41 |
"Mixing Rules" for estimating the hydraulic permeability of fiber mixtures Mattern KJ, Deen WM |
42 - 55 |
CFD modeling of pump-mix action in continuous flow stirred tank Singh KK, Mahajani SM, Shenoy KT, Ghosh SK |
56 - 73 |
Generalized scaling on forecasting heating patterns for microwave processing Bhattacharya M, Basak T |
74 - 85 |
Free surface flow in the mixing zone of an annular centrifugal contactor Wardle KE, Allen TR, Anderson MH, Swaney RE |
86 - 103 |
Fluidization of fine and ultrafine particles using nitrogen and neon as fluidizing gases Valverde JM, Quintanilla MAS, Castellanos A, Lepek D, Quevedo J, Dave RN, Pfeffer R |
104 - 121 |
Fluidization of coated group C powders Chen YH, Yang J, Dave RN, Pfeffer R |
122 - 131 |
Hollow fiber membrane contactor for hydrogen sulfide odor control Bouci N, Favre E, Roizard D, Belloul M |
132 - 137 |
Flocculation analysis and control system by laser diffractometry at industrial scale Bizi M, Gaboriau H |
138 - 142 |
Recovery of transition metal complex by reverse flow adsorption Dunnewijk J, Bosch H, de Haan AB |
143 - 149 |
Concentration and temperature dependence on diffusivities of CO2 and N-2 for poly(dimethyl, methylphenyl siloxane) Jha P, Way JD |
150 - 162 |
Control structure design for optimal operation of heat exchanger networks Lersbamrungsuk V, Srinophakun T, Narasimhan S, Skogestad S |
163 - 182 |
Lagrangean heuristic for the scheduling and control of polymerization reactors Terrazas-Moreno S, Flores-Tlacuahuac A, Grossmann IE |
183 - 193 |
Simultaneous batching and scheduling of single stage batch plants with parallel units Castro PM, Erdirik-Dogan M, Grossmann IE |
194 - 208 |
'Cycle to cycle' optimizing control of simulated moving beds Grossmann C, Erdem G, Morari M, Amanullah M, Mazzotti M, Morbidelli M |
209 - 222 |
Morphological population balance for modeling crystal growth in face directions Ma CY, Wang XZ, Roberts KJ |
223 - 241 |
Enhancing data-based fault isolation through nonlinear control Ohran BJ, Munoz de la Pena D, Davis JF, Christofides PD |
242 - 248 |
Performance study of heptane reforming in the dense ceramic membrane reactors Zhu WL, Han W, Xiong GX, Yang WS |
249 - 257 |
Effect of hydrodynamic multiplicity on trickle bed reactor performance van der Merwe W, Nicol W, Al-Dahhan MH |
258 - 268 |
A pore-flow-through membrane reactor for partial hydrogenation of 1,5-cyclooctadiene Schmidt A, Wolf A, Warsitz R, Dittmeyer R, Urbanczyk D, Voigt I, Fischer G, Schomacker R |
269 - 279 |
Hydrogen storage in metal-organic and covalent-organic frameworks by spillover Li YW, Yang RT |
280 - 288 |
Simple and safe synthesis of microporous aluminophosphate molecular sieves by inothermal approach Han LJ, Wang YB, Li CX, Zhang SJ, Lu XM, Cao MJ |
289 - 297 |
Miniemulsification in high-pressure homogenizers Manea M, Chemtob A, Paulis M, de la Cal JC, Barandiaran MJ, Asua JM |
298 - 309 |
Micrometer-sized monodispersed silica spheres with advanced adsorption properties Chen Y, Wang YJ, Yang LA, Luo GS |
310 - 320 |
Experimental validation of perfumery ternary diagram (R) methodology Gomes PB, Mata VG, Rodrigues AE |
321 - 326 |
Kinetics of carbon dioxide absorption into aqueous glucosamine solutions Gomez-Diaz D, Navaza JM |
327 - 336 |
A heterogeneous acid-catalyzed process for biodiesel production from enzyme hydrolyzed fatty acids Su CH, Fu CC, Gomes J, Chu IM, Wu WT |
337 - 342 |
Separation of p-xylene from the multicomponent xylene system by stripping crystallization Shiau LD, Wen CC, Lin BS |