| 305 - 305 |
Transactions - A Time for Growth
Hewitt G |
| 307 - 320 |
Long-Term Maintenance Policy Optimization in Multipurpose Process Plants
Dedopoulos IT, Shah N |
| 321 - 328 |
Matrix-Methods for Pipe Network Analysis - Observations on Partitioning and Cut Methods
Houache O, Khezzar L, Benhamza MH |
| 329 - 339 |
Modification of Sialon Microfilters by Pressureless Sintering, Pyrolysis of Organometallic Precursors and Nitridation of Thin-Films
Wakeman RJ, Henshall JL, Ng SG |
| 340 - 348 |
Joint Use of Calorimetry, Densimetry and Mathematical-Modeling for Multiple Component Polymerization
Mckenna TF, Fevotte G, Graillat C, Guillot J |
| 349 - 356 |
Micellar-Catalyzed Oximation of Cyclohexanone by Sodium Dodecyl-Sulfate
Asai S, Nakamura H, Yamaguchi H, Shimizu H |
| 357 - 362 |
Design of Optimal Thermally-Coupled Distillation Systems Using a Dynamic-Model
Hernandez S, Jimenez A |
| 363 - 368 |
Alternate Eddy Shedding Set-Up by the Non Axisymmetrical Recirculation Zone at the Exhaust of a Cyclone Dust Separator
Yazdabadi PA, Griffiths AJ |
| 369 - 378 |
The Influence of Rushton Impeller Blade and Disk Thickness on the Mixing Characteristics of Stirred Vessels
Rutherford K, Mahmoudi SM, Lee KC, Yianneskis M |
| 379 - 389 |
Distribution of Energy Between Convective and Turbulent-Flow for 3 Frequently Used Impellers
Zhou G, Kresta SM |
| 390 - 396 |
A New Theory Improves the Correlation of Blend Time Data from Turbulent Jet Mixed Vessels
Grenville RK, Tilton JN |
| 397 - 405 |
Gas Holdup and Interfacial Area Distributions in a Mechanically Agitated Gas-Liquid Contactor
Barigou M, Greaves M |
| 406 - 414 |
Influence of the Gas Sparger on the Hydrodynamic Behavior of Bubble-Columns
Hebrard G, Bastoul D, Roustan M |
| 415 - 415 |
First International-Symposium on Mixing in Industrial-Processes
Smith JM |
