2439 - 2439 |
Untitled Reklaitis GV |
2441 - 2457 |
Chemical product design: challenges and opportunities Gani R |
2459 - 2468 |
A virtual finite element model for centered and eccentric mixer configurations Rivera C, Heniche M, Ascanio G, Tanguy P |
2469 - 2480 |
Modelling of a dynamic multiphase flash: the positive flash Application to the calculation of ternary diagrams Thery R, Llovell F, Meyer X, Gerbaud V, Joulia X |
2481 - 2491 |
Explicit model predictive control of gas-liquid separation plant via orthogonal search tree partitioning Grancharova A, Johansen TA, Kocijan J |
2493 - 2508 |
Intermediate storage in batch/continuous processing systems under stochastic operation conditions Orban-Mihalyko E, Lakatos BG |
2509 - 2521 |
Global optimization of reactive distillation networks using IDEAS Burri JE, Manousiouthakis VI |
2523 - 2540 |
A strong tracking predictor for nonlinear processes with input time delay Wang D, Zhou DH, Jin YH, Qin SJ |
2541 - 2545 |
Solving distillation problems by terrain methods Lucia A, Yang F |
2547 - 2551 |
Synthesis of robust water reuse networks for single-component retrofit problems using symmetric fuzzy linear programming Tan RR, Cruz DE |
2553 - 2567 |
An enhanced pseudo-binary-mixture (PBM) algorithm for multistage separation processes Ishii Y, Otto FD |
2569 - 2581 |
A hybrid genetic algorithm for efficient parameter estimation of large kinetic models Katare S, Bhan A, Caruthers JM, Delgass WN, Venkatasubramanian V |
2583 - 2594 |
Multiobjective dynamic optimization of a semi-batch epoxy polymerization process Mitra K, Majumdar S, Raha S |
2595 - 2604 |
Simulation of the consolidation of paper coating structures: probabilistic versus deterministic models Bertrand F, Gange T, Desaulniers E, Vidal D, Hayes RE |
2605 - 2610 |
Infinite horizon model predictive control with no terminal constraint Marjanovic O, Lennox B |
2611 - 2619 |
An online application of dynamic PLS to a dearomatization process Komulainen T, Sourander M, Jamsa-Jounela SL |
2621 - 2633 |
Adaptive Linear Dynamic Matrix Control applied to an integrating process Guiamba IRF, Mulholland M |
2635 - 2646 |
Fast and robust fault diagnosis for a class of nonlinear systems: detectability analysis Li LL, Zhou DH |
2647 - 2657 |
Solving mixed integer nonlinear programming problems with line-up competition algorithm Yan LX, Shen K, Hu SH |
2659 - 2666 |
Computing the distance between a nonlinear model and its linear approximation: an L-2 approach Kihas D, Marquez HJ |
2667 - 2675 |
Multimodel analysis and controller design for nonlinear processes Wen T, Marquez HJ, Chen TW, Liu JZ |
2677 - 2693 |
A bifurcation approach to understanding instabilities in gas-fluidized beds using a single phase compressible flow model Johri J, Glasser BJ |
2695 - 2707 |
An ESDIRK method with sensitivity analysis capabilities Kristensen MR, Jorgensen JB, Thomsen PG, Jorgensen SB |
2709 - 2715 |
Emission control in palm oil mills using artificial neural network and genetic algorithm Ahmad AL, Azid IA, Yusof AR, Seetharamu KN |
2717 - 2726 |
A systematic generation of reactor designs - I. Isothermal conditions Hillestad M |
2727 - 2733 |
Study of the numerical instabilities in Lagrangian tracking of bubbles and particles in two-phase flow Goz MF, Lain S, Sommerfeld M |
2735 - 2747 |
Dynamic models for start-up operations of batch distillation columns with experimental validation Elgue S, Prat L, Cabassud M, Le Lann JM, Cezerac J |
2749 - 2763 |
Analysis of linear programming in model predictive control Saffer DR, Doyle FJ |
2765 - 2777 |
Modeling and scale up of airlift bioreactor Znad H, Bales V, Kawase Y |
2779 - 2790 |
Adaptive genetic programming for steady-state process modeling Grosman B, Lewin DR |
2791 - 2821 |
New measures and procedures to manage financial risk with applications to the planning of gas commercialization in Asia Aseeri A, Bagajewicz MJ |
2823 - 2835 |
Production scheduling in a steelmaking-continuous casting plant Pacciarelli D, Pranzo M |
2837 - 2843 |
Techniques for solving industrial nonlinear data reconciliation problems Kelly JD |
2845 - 2849 |
Stochastic maximum principle for optimal control under uncertainty Rico-Ramirez V, Diwekar UM |
2851 - 2851 |
Modeling and simulation of saline extractive distillation columns for the production of absolute ethanol (vol 27, pg 527, 2003) Llano-Restrepo M, Aguilar-Arias J |