1059 - 1075 |
Effect of different thermodynamic models on the design of homogeneous azeotropic distillation columns Gutierrez-Antonio C, Iglesias-Silva GA, Jimenez-Gutierrez A |
1076 - 1084 |
Obtaining solubility data from a liquid-liquid equilibrium cell Oliveira MLN, Malagoni RA, Fehr M, Franco MR |
1085 - 1106 |
Two-phase pressure drop in a trickle bed reactor involving Newtonian/non-Newtonian liquid phase Bansal A, Wanchoo RK, Sharma SK |
1107 - 1121 |
Kinetics of enzymatic hydrolysis of steam-exploded cotton gin waste Shen JC, Agblevor FA |
1122 - 1143 |
Optimal fed-batch operation for recombinant cells with segregational plasmid instability Shin HS, Lim HC |
1144 - 1158 |
Application of drift-flux model in liquid-solid circulating fluidized bed Natarajan P, Velraj R, Seeniraj RV |
1159 - 1175 |
High-temperature solar chemical reactors for hydrogen production from natural gas cracking Abanades S, Flamant G |
1176 - 1183 |
Integrated process for isolation and complete utilization of rice straw components through sequential treatment Zhao JS, Fu CG, Yang ZY |