567 - 582 |
The performance of structured packings in trickle-bed reactors Frank HJW, Kuipers JAM, Versteeg GF, Van Swaaij WPM |
583 - 587 |
Development of a new generation of structured packings for distillation Billingham JF, Lockett MJ |
588 - 596 |
Optimization of batch extractive distillation processes for separating close boiling and azeotropic mixtures Mujtaba IM |
597 - 608 |
Interaction between design and control of a heat-integrated distillation system with prefractionator Bildea CS, Dimian AC |
609 - 612 |
Influence of hydraulic conditions on separation efficiency of optiflow Spiegel L, Knoche M |
613 - 618 |
Reactive azeotropes in kinetically controlled reactive distillation Frey T, Stichlmair J |
619 - 626 |
A new, ultracapacity tray for distillation columns Fair JR, Trutna WR, Seibert AF |
627 - 632 |
Hydrodynamics and mass transfer of textile vibrating-valve trays Mustafa H, Bekassy-Molnar E, Elhamouz A |
633 - 638 |
Dynamic modelling of reactive absorption with the Maxwell-Stefan approach Schneider R, Kenig EY, Gorak A |
639 - 646 |
CFD simulations of sieve tray hydrodynamics Krishna R, Van Baten JM, Ellenberger J, Higler AP, Taylor R |
647 - 655 |
Multicomponent effects in liquid-liquid extraction Haeberl M, Blass E |
656 - 662 |
Development of an improved method to quantify maldistribution and its effect on structured packing column performance Edwards DP, Krishnamurthy KR, Potthoff RW |
663 - 668 |
The coupling of an absorption-refrigerator with a co-generation system Le Goff P, Hornut JM |