| 1465 - 1475 |
Valve positioning control for process through-put maximization
Jha SK, Kaistha N |
| 1476 - 1484 |
Indirect cooling crystallization process analysis
Eftouney RS, El-Rifaii MA |
| 1485 - 1490 |
Determining the pinch point and calculating the freshwater target for water-using systems with single contaminant
Liu ZY, Yang YZ, Zhang Y |
| 1491 - 1496 |
Evaluations of Euler-Euler simulations of bubble columns based on numerical tracer experiments
Bothe D, Shirzadi H, Warnecke HJ |
| 1497 - 1513 |
Hydrodynamics of gas-liquid slug flow along vertical pipes in turbulent regime - A simulation study
Mayor TS, Pinto AMFR, Campos JBLM |
| 1514 - 1523 |
Power and mixing time study involving a Maxblend (R) impeller with viscous Newtonian and non-Newtonian fluids
Fradette L, Thome G, Tanguy PA, Takenaka K |
| 1524 - 1528 |
Effect of operating conditions on the concentration of monoglycerides using molecular distillation
Fregolente LV, Fregolente PBL, Chicuta AM, Batistella CB, Filho RM, Wolf-Maciel MR |
| 1529 - 1538 |
Feeding of oxygen along the height of a circulating fast fluidized bed membrane reactor for efficient production of hydrogen
Abasharl MEE, Elnashaie SSEH |
| 1539 - 1552 |
Application of a CFD code (FLUENT) to formulate models of catalytic gas phase reactions in porous catalyst pellets
Kolaczkowski ST, Chao R, Awdry S, Smith A |
| 1553 - 1560 |
Comparison of mixing technologies for the production of concentrated emulsions
Fradette L, Brocart B, Tanguy PA |
