177 - 183 |
Importance of Using the Correct Impeller Boundary-Conditions for Cfd Simulations of Stirred Tanks Fokema MD, Kresta SM, Wood PE |
184 - 193 |
Modeling of the 3D Hydrodynamics of 2-Blade Impellers in Stirred Tanks Filled with a Highly Viscous-Fluid Abid M, Xuereb C, Bertrand J |
194 - 200 |
A Correlation to the Solution of the 2-Phase Dispersion Model Qabazard H, Johnson MM, Meier PF |
201 - 206 |
Drag on Individual Cubic Assemblies of Spheres in Non-Newtonian Tube Flow Subramaniam G, Zuritz CA |
207 - 211 |
Non-Newtonian Liquid Flow-Through Globe and Gate Valves Banerjee TK, Das M, Das SK |
212 - 221 |
Changes in Liquid Hold-Up in Foam and Size of Foam by Perforated Plates and Contribution to Mechanical Foam-Breaking Kunii M, Hosokai K, Yamagiwa K, Onodera M, Ohkawa A |
222 - 228 |
Dispersed Phase Characteristics in 3-Phase (Liquid-Liquid Solid) Fluidized-Beds Kim SD, Kim DY, Han JH |
229 - 234 |
Measurements of Voidage Profiles in Spouted Beds He YL, Lim CJ, Grace JR, Zhu JX, Qin SZ |
235 - 239 |
Minimum Spouting Velocity in Multiple Spouted Beds Murthy DV, Singh PN |
240 - 248 |
The Movement of Solids Through Flighted Rotating Drums .2. Solids Gas Interaction and Model Validation Sherritt RG, Caple R, Behie LA, Mehrotra AK |
249 - 255 |
Transient Forced-Convection in the Entrance Region of a Porous Tube Alnimr MA, Aldoss T, Naji MI |
256 - 261 |
Simulation of SO2 Absorption by Falling Water Drops Hsu CT, Shih SM, Chang CY |
262 - 271 |
Diffusion in Liquid-Filled Pores of Activated Carbon .1. Pore Volume Diffusion Leyvaramos R, Geankoplis CJ |
272 - 278 |
Residual Oil Cracking Combined with Hydrogen-Production by Steam-Iron Reaction Fukase S, Suzuka T |
279 - 288 |
Kinetics of Hydrogen Reduction of Sodium-Sulfate Mixed with Sodium Titanate Zou X, Avedesian MM, Vanheiningen AR |
289 - 295 |
Kinetic-Study of the Reaction Between Molybdenum Trioxide and Gaseous Carbon-Tetrachloride Ruiz MD, Rivarola JB, Quiroga OD |
296 - 303 |
Preparation, Characterization and Activity of Wet-Proofed Pt/Silicalite Catalysts Rangwala HA, Wanke SE, Otto FD |
304 - 313 |
Development of an Absorber Using a Wet-Dry Method with High-Energy Venturi Kholi N, Benachour M, Zoulalian A |
314 - 320 |
Thermodynamics and Kinetics of the Kraft Causticizing Reaction Wang L, Tessier PJ, Englezos P |
321 - 329 |
Identification and Control of an Industrial Steam-Reforming Plant Meziou AM, Alatiqi IM |
330 - 341 |
Multicomponent Ion-Exchange Column Dynamics Tan HK, Spinner IH |
342 - 351 |
Evaluation of Capital-Cost Data .8. Liquid Waste-Disposal with Emphasis on Biological Treatment Wright DG, Woods DR |
352 - 353 |
Pressure-Drop for the Slow Flow of Dilatant Fluids Through a Fixed-Bed of Spherical-Particles Jaiswal AK, Sundararajan T, Chhabra RP |
354 - 357 |
Heat-Transfer Mechanism Due to Particle Convection in Circulating Fluidized-Bed Qi CM, Farag IH |
358 - 364 |
Synthesis of Entrainers in Heteroazeotropic Distillation Systems Furzer IA |
365 - 369 |
A Proposed Method for the Calculation of Theoretical Plates in Liquid-Liquid-Solid 3-Phase Extraction Columns - Methanol, Hexane and Rapeseed Meal System Shi MR, Shen SQ, Liu J |
370 - 374 |
Experimental Evaluation of Molten Caustic Leaching of an Oil Sand Coke Residue Ityokumbul MT |
375 - 379 |
Modified Oil Agglomeration Process for Coal Beneficiation .3. Grinding and Agglomeration Using Different Szego Mill Designs Mccracken TW, Trass O |
380 - 384 |
Characteristics of Heavy-Oil-in-Water Emulsions Containing Produced Sand Jamaluddin AK, Bowen CT, Gillies R, Small M, Nazarko TW |