1 - 10 |
The dual-quadrature method of generalized moments using automatic integration packages Favero JL, Lage PLC |
11 - 23 |
Comparison of diffusion models in the modeling of a catalytic membrane fixed bed reactor coupling dehydrogenation of ethylbenzene with hydrogenation of nitrobenzene Abo-Ghander NS, Logist F, Grace JR, Van Impe JFM, Elnashaie SSEH, Lim CJ |
24 - 34 |
Coupled simulation of an industrial naphtha cracking furnace equipped with long-flame and radiation burners Hu GH, Wang HG, Qian F, Van Geem KM, Schietekat CM, Marin GB |
35 - 43 |
crystSim: A software environment for modelling industrial batch cooling crystallization Falola A, Borissova A |
44 - 51 |
Mathematical modeling and parametric study of coke-burning process in a hydrocracker reactor Behroozi A, Hatamipour MS, Rahimi A |
52 - 63 |
Energy efficiency optimisation of wastewater treatment: Study of ATAD Rojas J, Zhelev T |
64 - 73 |
Model-based analysis of micro-separators for portable direct methanol fuel-cell systems Zenith F, Kraus M, Krewer U |
74 - 81 |
Innovative dimethyl ether synthesis in a reactive dividing-wall column Kiss AA, Suszwalak DJPC |
82 - 93 |
Distributed parameter model for pH process including distributed continuous and discrete reactant feed Stebel K, Metzger M |
94 - 105 |
Parallel tools for the bifurcation analysis of large-scale chemically reactive dynamical systems Continillo G, Grabski A, Mancusi E, Russo L |
106 - 114 |
Improved stiction compensation in pneumatic control valves Cuadros MADL, Munaro CJ, Munareto S |
115 - 125 |
Inferential MIMO predictive control of the particle size distribution in emulsion polymerization da Silva B, Dufour P, Sheibat-Othman N, Othman S |
126 - 138 |
Optimal selection of control structure using a steady-state inversely controlled process model Sharifzadeh M, Thornhill NF |
139 - 150 |
Optimal control and CFD modeling for heat flux estimation of a baking process Ousegui A, Moresoli C, Dostie M, Marcos B |
151 - 170 |
An automata based method for online synthesis of emergency response procedures in batch processes Yeh ML, Chang CT |
171 - 184 |
Optimal production planning under time-sensitive electricity prices for continuous power-intensive processes Mitra S, Grossmann IE, Pinto JM, Arora N |
185 - 203 |
Rigorous scheduling of mesh-structure refined petroleum pipeline networks Cafaro DC, Cerda J |
204 - 212 |
On the combinatorial structure of discrete-time MIP formulations for chemical production scheduling Maravelias CT |
213 - 223 |
Integrated business and engineering framework for synthesis and design of enterprise-wide processing networks Quaglia A, Sarup B, Sin G, Gani R |
III - IV |
Editorial note: Best paper of 2010 award Venkatasubramanian V, Gani R |