807 - 807 |
Special topic issue - Process design Shah N |
809 - 822 |
Mixed integer optimization in the chemical process industry -Experience, potential and future perspectives Kallrath J |
823 - 839 |
Intelligent modelling interface for dynamic process simulators Clark G, Rossiter D, Chung PWH |
840 - 844 |
Flowsheeting packages: Reliable or fictitious process models? Benyahia F |
845 - 848 |
Taboo search algorithm for continuous function optimization Rajesh J, Jayaraman VK, Kulkarni BD |
849 - 859 |
Optimization of plate fin heat exchangers - A continuous formulation Reneaume JM, Pingaud H, Niclout N |
860 - 865 |
Flow structures of Geldart a solids in circulating fluidized beds Ocone R, Goodwin JAS, Delebarre A |
866 - 870 |
Design aspects of chemical plant exposed to transient pressure loads Ewan BCR, Moatamedi M |
871 - 880 |
The art of mixing with an admixture of art - Viewing creativity through P. V. Danckwerts's early work Ottino JM |
881 - 888 |
Modelling transport phenomena and performance of direct methanol fuel cell stacks Scott K, Argyropoulos P, Taama WM |
889 - 893 |
Mass transfer and influence of physical properties of solutions in a bubble column Alvarez E, Sanjurjo B, Cancela A, Navaza JM |
894 - 902 |
Mixing effects on product particle characteristics from semi-batch crystal precipitation Zauner R, Jones AG |
903 - 910 |
Hydrodynamic characterization of dispersed two-phase flows by laser Doppler velocimeter Deshpande NS, Prasad CV, Kulkarni AA, Joshi JB |
911 - 920 |
On the axial movement of solids in gas-solid fluidized beds Mostoufi N, Chaouki J |
921 - 924 |
Pyrolysis kinetics of tobacco dust Valverde JL, Curbelo C, Mayo O, Molina CB |
925 - 931 |
Simplified numerical simulation of transients in gas networks Kessal M |