535 - 546 |
State multiplicity in CSTR-separator-recycle polymerisation systems Kiss AA, Bildea CS, Dimian AC, Iedema PD |
547 - 553 |
Hydrogen solubility in straight run gasoil Ronze D, Fongarland P, Pitault I, Forissier M |
555 - 564 |
Two-way coupled bubble laden mixing layer Yang X, Thomas NH, Guo LJ, Hou Y |
565 - 573 |
The control of bubble size in carbonated beverages Barker GS, Jefferson B, Judd SJ |
575 - 593 |
Advances in simultaneous strategies for dynamic process optimization Biegler LT, Cervantes AM, Wachter A |
595 - 606 |
Population balance modeling. Promise for the future Ramkrishna D, Mahoney AW |
607 - 615 |
Solids motion in flowing froths Neethling SJ, Cilliers JJ |
617 - 629 |
Characterization of an ultrasonic system using wavelet transforms Moholkar VS, Huitema M, Rekveld S, Warmoeskerken MMCG |
631 - 641 |
Modelling the SO2-limestone reaction under periodically changing oxidizing/reducing conditions: the influence of cycle time on reaction rate Barletta D, Marzocchella A, Salatino P |
643 - 650 |
A model describing the two-dimensional calendering of finite width sheets Levine L, Corvalan CM, Campanella OH, Okos MR |
651 - 661 |
Integrated design of coupled separation processes with independent solvent circulation loops El-Rifai MA, Ettouney RS |
663 - 675 |
Dynamic behaviour of drops in oil/water/oil dispersions Sajjadi S, Zerfa M, Brooks BW |
677 - 692 |
A two-dimensional study of the rupture of funicular liquid bridges Urso MED, Lawrence CJ, Adams MJ |
693 - 703 |
Concentration and desalination of protein solutions by ultrafiltration Noordman TR, Ketelaar TH, Donkers F, Wesselingh JA |