655 - 655 |
Special topic issue - Process design Shah N |
657 - 668 |
On establishing the credibility of a model for a system Singh S |
669 - 676 |
Modelling of continuous synthesis process of TiO2 particles using slug flow tubular reactor Kubo M, Kawakatsu T, Yonemoto T |
677 - 684 |
Some efficient formulations for the simultaneous solution of trim-loss and scheduling problems in the paper-converting industry Westerlund T, Isaksson J |
685 - 699 |
Heat integration for batch processes - Part 1 : Process scheduling based on cascade analysis Zhao XG, O'Neill BK, Roach JR, Wood RM |
700 - 710 |
Heat integration for batch processes - Part 2 : Heat exchanger network design Zhao XG, O'Neill BK, Roach JR, Wood RM |
711 - 722 |
Learning to control the performance of batch processes Martinez EC, Pulley RA, Wilson JA |
723 - 727 |
The rising velocity of Taylor bubbles in an annulus Hills JH, Chety P |
728 - 736 |
Turbulent jet reactors : Mixing time scales Forney LJ, Nafia N |
737 - 747 |
Assessment of sliding mesh CFD predictions and LDA measurements of the flow in a tank stirred by a Rushton impeller Ng K, Fentiman NJ, Lee KC, Yianneskis M |
748 - 752 |
Local solid concentration measurement by fibre optics : Application to circulating fluidized beds Saberi B, Shakourzadeh K, Guigon P |
753 - 760 |
Role of liquid bridge forces in cohesive fluidization Wright PC, Raper JA |
761 - 763 |
Solids circulation rate prediction in a pressurized loop-seal Cheng L, Basu P, Cen K |