| 1335 - 1343 |
Optimal reactor systems for Van de Vusse reaction scheme with multicomponent feed
Bikic D, Butinar B, Glavic P |
| 1345 - 1362 |
Multiple data sets for model updating in real-time operations optimization
Yip WS, Marlin TE |
| 1363 - 1368 |
Study on flexibility of sensor network for linear processes
Li B, Chen BZ |
| 1369 - 1377 |
Two different approaches for RDC modelling when simulating a solvent deasphalting plant
Aparicio JJC, Jeronimo MAS, Martins FG, Coelho MA, Martins C, Braga AS, Costa CA |
| 1379 - 1397 |
An improved method for nonlinear model reduction using balancing of empirical gramians
Hahn J, Edgar TF |
| 1399 - 1413 |
Markovian inventory policy with application to the paper industry
Yin KK, Liu H, Johnson NE |
| 1415 - 1425 |
A hybrid global optimization approach for solvent design
Wang YP, Achenie LEK |
| 1427 - 1436 |
Nonlinear long range predictive control of an openloop unstable reactor
Hapoglu H |
| 1437 - 1447 |
A time-delay compensation strategy for processes with uncertainties
Zhao FT, Tian YC, Tade MO, Li H |
| 1449 - 1457 |
Numerical solution of non-linear algebraic equations with discontinuities
Shacham M, Brauner N |
| 1459 - 1471 |
Bifurcation analysis of reactive distillation systems with liquid-phase splitting
Qi ZW, Sundmacher K |
| 1473 - 1479 |
Automatic implementation of thermodynamic models for reliable parameter estimation using computer algebra
Dominguez A, Tojo J, Castier M |
| 1481 - 1492 |
Solution of constrained optimization problems by multi-objective genetic algorithm
Summanwar VS, Jayaraman VK, Kulkarni BD, Kusumakar HS, Gupta K, Rajesh J |
| 1493 - 1500 |
A tuned approach of the predictive-adaptive GPC controller applied to a fed-batch bioreactor using complete factorial design
Rodrigues JAD, Toledo E, Maciel R |
