959 - 976 |
MO optimization of phthalic anhydride industrial catalytic reactors using guided GA with the adapted jumping gene operator Bhat GR, Gupta SK |
977 - 988 |
Evaluation of control configurations for a depropaniser Chawla I, Rangaiah GR |
989 - 996 |
Characterization of slurry flow regime transitions by ERT Giguere R, Fradette L, Mignon D, Tanguy PA |
997 - 1001 |
A simple mechanism of bubble and slug formation in Taylor flow in microchannels Pohorecki R, Kula K |
1002 - 1010 |
Sustainable chemical technology through catalytic multistep reactions Murzin DY, Leino R |
1011 - 1016 |
Dissolution kinetics of ulexite in acetic acid solutions Ekmekyapar A, Demirkiran N, Kunkul A |
1017 - 1026 |
The use of ilmenite as an oxygen carrier in chemical-looping combustion Leion H, Lyngfelt A, Johansson M, Jerndal E, Mattisson T |
1027 - 1037 |
Influence of stirrer type on mixture homogeneity in continuous powder mixing: A model case and a pharmaceutical case Marikh K, Berthiaux H, Gatumel C, Mizonov V, Barantseva E |
1038 - 1048 |
Comparative study of droplet drying models for CFD modelling Woo MW, Daud WRW, Mujumdar AS, Talib MZM, Hua WZ, Tasirin SM |
1049 - 1052 |
Simulation of quench system of ethylene plant using real components Gao GY, Quan XL, Jiang B, Li XG |
1053 - 1058 |
Mechanism for the release of the industrial biocide CMI from clathrate crystal Kitamura M, Abe T, Kishida M |
1059 - 1072 |
Complementary modelling of fluid separation processes Kenig EY |