765 - 765 |
Special topic issue - Particle technology Wakeman R |
767 - 774 |
More chemistry for finer particle technology Senna M |
775 - 796 |
Particle technology - Reflections and horizons : An engineering perspective Roberts AW |
797 - 802 |
Food particles and the problems of hydration Lillford PJ, Fryer PJ |
803 - 808 |
An interfacial model for the transfer of impurities into the sucrose crystal Lionnet GRE |
809 - 814 |
Morphology of NaCl crystals in drowning-out precipitation operation Takiyama H, Otsuhata T, Matsuoka M |
815 - 822 |
Evaluation of the thin-layer method used for measuring single particle drying kinetics Fyhr C, Kemp IC |
823 - 834 |
Effect of sparger design and height to diameter ratio on fractional gas hold-up in bubble columns Thorat BN, Shevade AV, Bhilegaonkar KN, Aglawe RH, Veera UP, Thakre SS, Pandit AB, Sawant SB, Joshi JB |
835 - 842 |
A novel profiled blade impeller for homogenization of miscible liquids in stirred vessels Fentiman NJ, St Hill N, Lee KC, Paul GR, Yianneskis M |
843 - 848 |
Model for liquid phase flow on sieve trays Mehta B, Chuang KT, Nandakumar K |
849 - 854 |
Output effectiveness and scaling sensitivity for secondary measurement selection Cao Y, Owens DH, Rossiter D |
855 - 863 |
A model for particle collection in a turbulent bed contactor -New packings Gimenes ML, Handley D |
864 - 872 |
Calculation of burnoff distributions of char particles in a bubbling fluidized bed reactor by means of batch combustion experiments Marban G, Fuertes AB, Pis JJ |
873 - 881 |
A dispersion/coalescence model in a turbulent bed contactor Guerriere RA, Fayed ME, Matchett AJ |