| 1 - 14 |
Measurement of Boundary Fractal Dimensions - Review of Current Techniques
Allen M, Brown GJ, Miles NJ |
| 15 - 22 |
Effect of Chemisorbed Water on Bed Voidage of High-Temperature Fluidized-Bed
Yamazaki R, Han NS, Sun ZF, Jimbo G |
| 23 - 34 |
Quantitative Predictions of Gas-Particle Flow in a Vertical Pipe with Particle-Particle Interactions
Yasuna JA, Moyer HR, Elliott S, Sinclair JL |
| 35 - 38 |
Production of Fine Tin and Lead Powders and Porous Filters
Styrkas AD, Styrkas D |
| 39 - 47 |
A Phenomenological Model Predicting the Attrition and the Reduction of Attrition Due to the Addition of Solid Lubricants in Slugging Beds
Kokkoris A, Turton R |
| 49 - 56 |
Effect of Particle Diameter, Particle Density and Loading Ratio on the Effective Drag Coefficient in Steady Turbulent Gas-Solids Transport
Littman H, Morgan MH, Jovanovic SD, Paccione JD, Grbavcic ZB, Vukovic DV |
| 57 - 64 |
Water-Only Performance of Proportioning Jet Pumps for Hydraulic Transportation of Solids
Wang D, Wypych PW |
| 65 - 74 |
Hydrodynamic Modeling of Vertical Non-Accelerating Gas-Solids Flow
Garic RV, Grbavcic ZB, Jovanovic SD |
| 75 - 81 |
Distinction Between Upward and Downward Flows in Circulating Fluidized-Beds
Bai D, Shibuya E, Masuda Y, Nishio K, Nakagawa N, Kato K |
| 83 - 90 |
Effect of Exit Geometry on the Vertical-Distribution of Solids in Circulating Fluidized-Beds .1. Solution of Fundamental Equations .2. Analysis of Reported Data and Prediction
Kunii D, Levenspiel O |
| 91 - 98 |
Investigations into Wall-Pressure During Slug-Flow Pneumatic Conveying
Mi B, Wypych PW |
