| 2351 - 2358 |
An interpretation of the behavior of EoS/G(E) models for asymmetric systems
Kontogeorgis GM, Vlamos PM |
| 2359 - 2377 |
Gradient diffusion coefficients - theory and experiment
Bowen WR, Liang YC, Williams PM |
| 2379 - 2392 |
Multiphase multicomponent equilibria for mixtures containing polymers by the perturbation theory
Favari F, Bertucco A, Elvassore N, Fermeglia M |
| 2393 - 2400 |
On the computation of a nonlinearity measure using functional expansions
Harris KR, Colantonio MC, Palazoglu A |
| 2401 - 2415 |
Process intensification: operating characteristics of rotating packed beds - determination of liquid hold-up for a high-voidage structured packing
Burns JR, Jamil JN, Ramshaw C |
| 2417 - 2428 |
Consistent structure and thermodynamic characteristics of transport potential model proposed for liquid-liquid solvent extraction
Nabeshima M |
| 2429 - 2439 |
PI/PID controller tuning via LQR approach
He JB, Wang QG, Lee TH |
| 2441 - 2453 |
Boundary effect on slow motion of a composite sphere perpendicular to two parallel impermeable plates
Chen SB, Ye XN |
| 2455 - 2479 |
Optimal reactor design from a geometric viewpoint. Part II. Critical sidestream reactors
Feinberg M |
| 2481 - 2489 |
Active species injection in flue gas denitrification
Li RN, Liu X |
| 2491 - 2506 |
Main fundamental gas reactions in denitrification and desulfurization from flue gas by non-thermal plasmas
Li RN, Liu X |
| 2507 - 2513 |
Mathematical analysis of polymer degradation with chain-end scission
Kostoglou M |
| 2515 - 2528 |
An overall rate-based stage model for cross flow distillation columns
Muller NP, Segura H |
| 2529 - 2546 |
On the development of novel chemicals using a systematic synthesis approach. Part I. Optimisation framework
Marcoulaki EC, Kokossis AC |
| 2547 - 2561 |
On the development of novel chemicals using a systematic optimisation approach. Part II. Solvent design
Marcoulaki EC, Kokossis AC |
