| 391 - 397 |
Simulation and design of membrane plants with AspenPlus
Rautenbach R, Knauf R, Struck A, Vier J |
| 398 - 404 |
Design of affinity membrane bioseparations
Sridhar P |
| 405 - 409 |
Simplified transient model of an upflow cocurrent packed bed bioreactor
Samb FM, Benthack C, Deront M, Adler N, Peringer P |
| 410 - 419 |
General criteria to analyze the role of mass transfer and hydrodynamics in trickle-bed reactors
Cassanello MC, Cukierman AL, Martinez OM |
| 420 - 424 |
A new continuous-flow recycle microwave reactor for homogeneous and heterogeneous chemical reactions
Chemat F, Poux M, diMartino JL, Berlan J |
| 425 - 431 |
Mass transfer studies in pneumatic reactors
Benyahia F, Jones L, Petit S, Plantaz D |
| 432 - 437 |
A new method for the characterisation of the wettability of powders
Link KC, Schlunder EU |
| 438 - 442 |
The use of statistical properties of transmission signals for particle characterization
Wessely B, Altmann J, Ripperger S |
| 443 - 447 |
EXSENSEL - A rule-based approach to selection of sensors for process variables
Barua A, Sengupta S |
| 448 - 455 |
Mathematical modeling and experimental validation of an absorption-driven multiple-effect evaporator
Yanniotis S, Pilavachi PA |
| 456 - 461 |
Performance of a three-phase fluidized bed as a reactive distillation device
Liang WG, Wang ZW, Jin Y, Ya ZQ, Yang S |
| 462 - 466 |
Interfacial tension measurements between alpha-tocopherol and carbon dioxide at high pressures
Moser M, Pietzonka W, Trepp C |
| 467 - 472 |
Natural gas compression factors calculated from relative density, heating value, and diluent compositions
IglesiasSilva GA, Hall KR |
