| 3065 - 3075 |
Design issues for membrane-based, gas phase microchemical systems
Quiram DJ, Hsing IM, Franz AJ, Jensen KF, Schmidt MA |
| 3077 - 3083 |
Intermediate temperature solid oxide fuel cells operated with methanol fuels
Sahibzada M, Steele BCH, Hellgardt K, Barth D, Effendi A, Mantzavinos D, Metcalfe IS |
| 3085 - 3090 |
The rate enhancing effect of ultrasound by inducing supersaturation in a solid-liquid system
Thompson LH, Doraiswamy LK |
| 3091 - 3100 |
Direct sulfation of limestone at elevated pressures
Qiu KR, Lindqvist O |
| 3101 - 3111 |
A model for the coagulation of polyvinyl acetate particles in emulsion
Melis S, Kemmere M, Meuldijk J, Storti G, Morbidelli M |
| 3113 - 3122 |
Flexible operation through optimal tracking in nonlinear processes
Costanza V, Neuman CE |
| 3123 - 3132 |
Modelling temperature distributions in cooling chocolate moulds
Tewkesbury H, Stapley AGF, Fryer PJ |
| 3133 - 3143 |
Drop size distributions in horizontal oil-water dispersed flows
Angeli P, Hewitt GF |
| 3145 - 3159 |
Difference points in extractive and reactive cascades. I -Basic properties and analysis
Hauan S, Ciric AR, Westerberg AW, Lien KM |
| 3161 - 3174 |
Difference points in extractive and reactive cascades. II -Generating design alternatives by the lever rule for reactive systems
Lee JW, Hauan S, Lien KM, Westerberg AW |
| 3175 - 3185 |
Measurements and model prediction of the solid-liquid equilibria of organic binary mixtures
Huang CC, Chen YP |
| 3187 - 3194 |
Batch distillation column low-order models for quality program control
Betlem BHL |
| 3195 - 3208 |
On the measurement of strain rate in an oscillatory baffled column using particle image velocimetry
Ni X, Cosgrove JA, Arnott AD, Greated CA, Cumming RH |
| 3209 - 3221 |
Cascade control for a class of uncertain nonlinear systems: a backstepping approach
Alvarez-Ramirez J, Suarez R, Morales A |
| 3223 - 3235 |
MTG fluidized bed reactor-regenerator unit with catalyst circulation: process simulation and operation of an experimental setup
Gayubo AG, Ortega JM, Aguayo AT, Arandes JM, Bilbao J |
| 3237 - 3259 |
Recent developments in modeling gas-phase catalyzed olefin polymerization fluidized-bed reactors: The effect of bubble size variation on the reactor's performance
Hatzantonis H, Yiannoulakis H, Yiagopoulos A, Kiparissides C |
| 3261 - 3273 |
Three-dimensional simulation of a three-phase draft-tube bubble column
Padial NT, VanderHeyden WB, Rauenzahn RM, Yarbro SL |
| 3275 - 3286 |
Three-phase Eulerian simulations of bubble column reactors operating in the churn-turbulent regime: a scale up strategy
Krishna R, van Baten JM, Urseanu MI |
| 3287 - 3303 |
Turbulent flow in stirred vessels agitated by a single, low-clearance hyperboloid impeller
Pinho FT, Piqueiro FM, Proenca MF, Santos AM |
| 3305 - 3318 |
Fundamental theory for prediction of single-component mass transfer in liquid drops at intermediate Reynolds numbers (10 <= Re <= 250)
Uribe-Ramirez AR, Korchinsky WJ |
| 3319 - 3328 |
Fundamental theory for prediction of multicomponent mass transfer in single-liquid drops at intermediate Reynolds numbers (10 <= Re <= 250)
Uribe-Ramirez AR, Korchinsky WJ |
| 3329 - 3334 |
Steady state solutions for chloride distribution due to wick action in concrete
Puyate YT, Lawrence CJ |
