| 1 - 10 |
A Conductivity Technique for Gas and Solids Holdup Determination in 3-Phase Reactors
Uribesalas A, Gomez CO, Finch JA |
| 11 - 18 |
Pt-Catalyzed Combustion of CH4-C3H8 Mixtures
Balakrishna A, Schmidt LD, Aris R |
| 19 - 27 |
Modeling of Heat-Transfer in Metallic Monoliths Consisting of Sinusoidal Cells
Cybulski A, Moulijn JA |
| 29 - 39 |
Marangoni Convection Around a Ventilated Air Bubble Under Microgravity Conditions
Hoefsloot HC, Janssen LP, Hoogstraten HW |
| 41 - 50 |
The Application of Continuum Equations to Diffusion and Reaction in Pore Networks
Zhang L, Seaton NA |
| 51 - 60 |
Concentration of a Trace Component by Pressure Swing Adsorption
Ruthven DM, Farooq S |
| 61 - 73 |
Modeling of a Distributed-Parameter Process with a Variable Boundary - Application to Its Control
Toure Y, Biston J, Gilles G |
| 75 - 84 |
Incorporation of a Valve Equation into the Simulation of a Pressure Swing Adsorption Process
Chou CT, Huang WC |
| 85 - 97 |
Optimal Feedback-Control of Batch Reactors with a State Inequality Constraint and Free Terminal Time
Palanki S, Kravaris C, Wang HY |
| 99 - 113 |
A Population Balance Approach for the Description of Particle-Size Distribution in Suspension Polymerization Reactors
Alvarez J, Alvarez J, Hernandez M |
| 115 - 121 |
Antisintering Criteria in the Metal-Spacer Catalytic-System
Sloczynski J |
| 123 - 130 |
Steady-State Multiplicity Analysis of the Heterogeneous Axial-Dispersion Reactor
Juncu G, Bildea S, Floarea O |
| 131 - 137 |
An Example of Type-III Intermittency in Chemical-Engineering
Possio CT, Pellegrini L |
| 139 - 144 |
Particle-Liquid Mass-Transfer in a Bubble-Column with a Draft Tube
Kushalkar KB, Pangarkar VG |
| 145 - 146 |
The Pore-Size Distribution of Model Filters Produced by Random Fragmentation Described in Terms of the Weibull Distribution
Brown RC |
| 147 - 150 |
Non-Newtonian Flow Past a Swarm of Newtonian Droplets
Zhu JT, Deng Q |
