559 - 559 |
A showcase for the best in chemical and process engineering Grant C |
561 - 578 |
Modelling and optimization of utility systems Varbanov PS, Doyle S, Smith R |
579 - 586 |
An MILP approach to safe process plant layout Patsiatzis DI, Knight G, Papageorgiou LG |
587 - 590 |
Revisiting the Wen and Yu equations for minimum fluidization velocity prediction Delebarre A |
591 - 598 |
Local and global sensitivity analysis for a reactor design with parameter uncertainty Haaker MPR, Verheijen PJT |
599 - 604 |
Computational studies of the countercurrent multistage extraction-coupled esterification process of oleic acid with methanol using excess methanol as extractant Chen F, Kawasaki J, Naka Y |
605 - 610 |
Efficient expressions for effectiveness factor for a finite cylinder Asif M |
611 - 623 |
Multi-objective optimization of an industrial crude distillation unit using the elitist non-dominated sorting genetic algorithm Inamdar SV, Gupta SK, Saraf DN |
624 - 630 |
Diffusion rate of no gas inside zeolite agglomerate Golman B, Odate K, Shinohara K, Tsuji T, Masuda T |
631 - 636 |
Production of small composite particles by co-grinding in a media mill - Characterization of the granulometric and the mechanical properties Zapata C, Frances C, Le Bolay N, Molina-Boisseau SM |
637 - 641 |
Rheology and heat transfer during mineral residue phosphatation in a rheo-reactor Nzihou A, Bournonville B, Marchal P, Choplin L |
642 - 652 |
Power law fluid flow through beds of spheres at intermediate Reynolds numbers - Pressure in fixed and distended beds Dhole SD, Chhabra RP, Eswaran V |
653 - 658 |
Slug flow hydrodynamics in the presence of catalyst rods Vaitsis E, Chadwick D, Alpay E |
659 - 666 |
Potentials of ceramic membranes as catalytic three-phase reactors Vospernik M, Pintar A, Bercic G, Batista J, Levec J |
667 - 681 |
Adsorption of xylenes on faujasite-type zeolite - Equilibrium and kinetics in batch adsorber Minceva M, Rodrigues AE |