| 2839 - 2848 |
System identification of steam pressure in a fire-tube boiler
Vasquez JRR, Perez RR, Moriano JS, Gonzalez JRP |
| 2849 - 2856 |
Application of model predictive control to the BSM1 benchmark of wastewater treatment process
Shen WH, Chen XQ, Corriou JP |
| 2857 - 2876 |
A novel MINLP-based representation of the original complex model for predicting gasoline emissions
Furman KC, Androulakis IP |
| 2877 - 2890 |
Three-dimensional numerical study of heat and mass transfer in fluidized beds with spray nozzle
Nagaiah C, Warnecke G, Heinrich S, Peglow M |
| 2891 - 2896 |
The finite differences method for solving systems on irregular shapes
Lakner M, Plazl I |
| 2897 - 2902 |
On the dynamical instability of packed-bed reactors in the presence of catalyst deactivation
Jaree A, Boonsomlanjit B, Limtrakul J |
| 2903 - 2913 |
MPEC problem formulations and solution strategies with chemical engineering applications
Baumrucker BT, Renfro JG, Biegler LT |
| 2914 - 2919 |
Steady state optimization with guaranteed stability of a tryptophan biosynthesis model
Gerhard J, Monnigmann M, Marquardt W |
| 2920 - 2932 |
Control structure design for the ammonia synthesis process
Araujo A, Skogestad S |
| 2933 - 2945 |
Implementation and analysis of numerical solution of the population balance equation in CFD packages
Silva LFLR, Damian RB, Lage PLC |
| 2946 - 2957 |
Finite pointset method for simulation of the liquid-liquid flow field in an extractor
Drumm C, Tiwari S, Kuhnert J, Bart HJ |
| 2958 - 2965 |
Comparing predictions of PEM fuel cell behavior using Maxwell-Stefan and CFD approximation equations
Martinez MJ, Shimpalee S, Van Zee JW |
| 2966 - 2985 |
An embedded fault detection, isolation and accommodation system in a model predictive controller for an industrial benchmark process
Kettunen M, Zhang P, Jamsa-Jounela SL |
| 2986 - 2993 |
Control of a nonlinear continuous bioreactor with bifurcation by a type-2 fuzzy logic controller
Galluzzo M, Cosenza B, Matharu A |
| 2994 - 3001 |
Adaptive extremum-seeking control of convection-reaction distributed reactor with limited actuation
Hudon N, Guay M, Perrier M, Dochain D |
| 3002 - 3010 |
A systematic visual approach to molecular design via property clusters and group contribution methods
Eljack FT, Eden MR |
| 3011 - 3022 |
Selecting optimal weighting factors in iPDA for parameter estimation in continuous-time dynamic models
Varziri MS, Poyton AA, McAuley KB, McLellan PJ, Ramsay JO |
| 3023 - 3029 |
Prediction of isothermal crystallization parameters in monomer cast nylon 6
Lin JX, Wang CY, Zheng YY |
| 3030 - 3037 |
Design and control of transesterification reactive distillation with thermal coupling
Wang SJ, Wong DSH, Yu SW |
| 3038 - 3056 |
Identification of integrating and unstable processes from relay feedback
Liu T, Gao FR |
| 3057 - 3066 |
Controllability analysis of alternate schemes to complex column arrangements with thermal coupling for the separation of ternary mixtures
Tamayo-Galvan VE, Segovia-Hernandez JG, Hernandez S, Cabrera-Ruiz J, Alcantara-Avila JR |
| 3067 - 3083 |
A rule-based genetic algorithm for the scheduling of single-stage multi-product batch plants with parallel units
He YH, Hui CW |
| 3084 - 3089 |
Modeling the effect of pigment morphology on the dynamic compression of coating layers using DEM
Azadi P, Farnood R, Yan N |
| 3090 - 3111 |
Design of responsive supply chains under demand uncertainty
You FQ, Grossmann IE |
| 3112 - 3120 |
Modelling systems defined by RTD curves
Hocine S, Pibouleau L, Azzaro-Pantel C, Domenech S |
| 3121 - 3129 |
Latent variable projections of sensitivity data for experimental screening and kinetic modeling
Sjoblom J, Creaser D |
| 3130 - 3142 |
Synthesis of non-isothermal heat integrated water networks in chemical processes
Bogataj M, Bagajewicz MJ |
| 3143 - 3152 |
Heat exchanger network area targeting considering stream allocation to shell or tubes
Akbari A, Omidkhah MR, Hojjati MR |
| 3153 - 3169 |
Supply chain redesign through optimal asset management and capital budgeting
Naraharisetti PK, Karimi IA, Srinivasan R |
| 3170 - 3175 |
An implementation variant of the polynomial finite difference method with orthogonal collocation and adjustable element length
Vaca M, Monroy-Loperena R, Jimenez-Gutierrez A |
| 3176 - 3186 |
Object-oriented modelling of virtual-labs for education in chemical process control
Martin-Villalba C, Urquia A, Dormido S |
| 3187 - 3197 |
Numerical study of particle dispersion behind a sudden expansion geometry and its effect on step heights
Mohanarangam K, Tu JY, Chen L |
| 3198 - 3212 |
Genetic algorithm for the optimization of rubber insulated high voltage power cables production lines
Milani G, Milani F |
| 3213 - 3223 |
Simulation of flat falling film evaporator system for concentration of black liquor
Bhargava R, Khanam S, Mohanty B, Ray AK |
| 3224 - 3237 |
Three-dimensional mathematical modeling of dispersed two-phase flow using class method of population balance in bubble columns
Bannari R, Kerdouss F, Selma B, Bannari A, Proulx P |
| 3238 - 3245 |
Discrete element modeling of the transient heat transfer and toner fusing process in the Xerographic printing of coated papers
Azadi P, Yan N, Farnood R |
| 3246 - 3253 |
Robust discrete control of nonlinear processes: Application to chemical reactors
Garcia-Sandoval JP, Gonzalez-Alvarez V, Castillo-Toledo B, Pelayo-Ortiz C |
| 3254 - 3263 |
Hybrid fuzzy predictive control based on genetic algorithms for the temperature control of a batch reactor
Causa J, Karer G, Nunez A, Saez D, Skrjanc I, Zupancic B |
| 3264 - 3273 |
Biomass estimation in batch biotechnological processes by Bayesian Gaussian process regression
di Sciascio F, Amicarelli AN |
