| 123 - 134 |
Extended channel model for prediction of the pressure drop in single-phase flow in packed columns
Mackowiak J |
| 135 - 144 |
Structure and activity relationships for amine-based CO2 absorbents-II
Singh P, Niederer JPM, Versteeg GF |
| 145 - 152 |
Reducing energy consumption and CO2 emissions in extractive distillation
Gutierrez-Guerra R, Segovia-Hernandez JG, Hernandez S |
| 153 - 165 |
Improving vacuum gas oil hydrotreating operation via a lumped parameter dynamic simulation modeling approach
Remesat D, Young B, Surcek WY |
| 166 - 180 |
Osmotic dehydration of apricot: Kinetics and the effect of process parameters
Ispir A, Togrul IT |
| 181 - 192 |
Enhancing impinging jet heat or mass transfer by fluidically generated flow pulsation
Tesar V |
| 193 - 199 |
Heat transfer: Solving scaling problems at the design stage
Hawthorn D |
| 200 - 209 |
Optimum design of cooling water systems for energy and water conservation
Panjeshahi MH, Ataei A, Gharaie M, Parand R |
| 210 - 215 |
Electrolysis and heat pretreatment methods to promote CO2 sequestration by mineral carbonation
Li WZ, Li W, Lia BQ, Bai ZQ |
| 216 - 225 |
Evaluation of ratio control schemes in a two-temperature control structure for a methyl acetate reactive distillation column
Kumar MVP, Kaistha N |
| 226 - 232 |
Modelling the hold up of lifters in rotary dryers
Van Puyvelde DR |
| 233 - 243 |
Environmentally conscious design of chemical processes and products: Multi-optimization method
Li CS, Zhang XP, Zhang SJ, Suzuki KZ |
