1 - 9 |
Designing the Process Design Process Westerberg AW, Subrahmanian E, Reich Y, Konda S, Cunningham DP, Dutoit AH, Granger HL, Konda S, Marshall KC, Milliken RC, Monarch IA, Neergaard JP, Patrick RH, Thomas ME |
11 - 16 |
A G2 Based Mdoom Testbed for Concurrent Process Engineering Lu ML, Batres R, Li HS, Naka Y |
17 - 21 |
Cafe in-Process Design - Potential and Limitations Bessling B, Lohe B, Schoenmakers H, Scholl S, Staatz H |
17 - 18 |
Joint 6th International-Symposium on Process-Systems-Engineering and 30th European Symposium on Computer-Aided Process-Engineering - PSE-97 Escape-7 - 25-29-May-1997, Trondheim, Norway - Supplement to Computers-and-Chemical-Engineering - Preface Skogestad S, Lien KM |
23 - 28 |
Combined Exergy and Pinch Approach to Process Analysis Sorin M, Paris J |
29 - 34 |
Equipartition of Forces - Extension to Chemical Reactors Sauar E, Kjelstrup S, Lien KM |
35 - 40 |
Process Synthesis for Reaction Systems with Cooling via Finding the Attainable-Region Nicol W, Hildenbrandt D, Glasser D |
41 - 46 |
Towards Automatic-Generation of Novel Reactor-Separator Networks with Multiple Multicomponent Feeds Bikic D, Glavic P |
47 - 52 |
Synthesis of Optimal Reactor Networks Using Mathematical-Programming and Simulated Annealing Cordero JC, Davin A, Floquet P, Pibouleau L, Domenech S |
53 - 58 |
A Case-Study on Synthesis in Preliminary Design Liang DM, Fraga ES |
59 - 64 |
Improved Sequential Strategy for the Synthesis of Near-Optimal Heat-Exchanger Networks Gundersen T, Traedal P, Hashemiahmady A |
65 - 70 |
A Comprehensive Global Optimization Approach for the Synthesis of Heat-Exchanger Networks with No Stream Splits Zamora JM, Grossmann IE |
71 - 76 |
An Agent-Based Environment for Operational Design Batres R, Lu ML, Naka Y |
77 - 82 |
Sharable Engineering Knowledge Databases for Intelligent System Applications Miller DC, Josephson JR, Elsass MJ, Davis JF, Chandrasekaran B |
83 - 88 |
Use of Intelligent Software Agents in an Industrial Pressure Relief and Blowdown Design Tool Struthers A |
89 - 94 |
Iges - An Intelligent Graphical Engineering System Wada T, Nakada Y, Morrow P, Lu ML |
95 - 100 |
Teo Program System for Optimizing the Daily Operation of Power-Plants Assenmacher P, Berning G, Toelle FJ |
101 - 106 |
Integrated Design of Responsive Chemical Manufacturing Facilities Rowe DA, Perkins JD, Walsh SP |
107 - 112 |
Design of Autonomous Decentralized Multieffect Evaporating Systems Koshijima I, Toki A, Kanda I, Niida K, Umeda T |
113 - 118 |
Operator Support Systems for New Kinds of Process Operation Work Lindheim C, Lien KM |
119 - 124 |
An Intelligent Parallel Control-System Structure for Plants with Multiple Operating Regimes Kordon A, Fuentes YO, Ogunnaike BA, Dhurjati PS |
125 - 130 |
Globally Optimal Robust-Control for Systems with Time-Varying Nonlinear Perturbations Vanantwerp JG, Braatz RD, Sahinidis NV |
131 - 136 |
Robust-Control of an Absorption Heat-Pump System Ohgata A, Yamashita Y, Nishitani H |
137 - 142 |
Nonlinear Structure Identification of Chemical Processes Menold PH, Allgower F, Pearson RK |
143 - 148 |
Operability Considerations in Chemical Processes - A Switchability Analysis Vu TT, Bahri PA, Romagnoli JA |
149 - 154 |
A Dynamical Supervisor Strategy for Multiproduct Processes Kosanovich KA, Piovoso MJ |
155 - 160 |
Dual-Mode Adaptive-Control of Nonlinear Processes Allgower F, Ogunnaike BA |
161 - 166 |
Robust H-2 Performance Analysis for a High-Purity Distillation Column Wu F, Goh KC, Walsh S |
167 - 172 |
On the Efficient Simulation and Analysis of Regenerative Processes in Cyclic Operation Unger J, Kolios G, Eigenberger G |
173 - 179 |
Interactive, Dynamic Simulation Using Extrapolation Methods Tyreus BD |
181 - 185 |
Estimation of Uncertainty in Dynamic Simulation Results Torvi H, Hertzberg T |
187 - 192 |
Development of an Object-Oriented Simulation System for Complex Solids Processes Gruhn G, Rosenkranz J, Werther J, Toebermann JC |
193 - 198 |
A Rigorous and Efficient Distillation Column Model for Engineering and Training Simulators Olsen I, Endrestol GO, Sira T |
199 - 204 |
Use of Simulation in Rating and Design of Distillation Units Eiden U, Scholl S |
205 - 210 |
Tools for Computer-Aided Analysis and Interpretation of Process Simulation Results Gaubert MA, Joulia X |
211 - 216 |
Separation of Nonideal Mixtures Based on Mass/Heat Exchange Principles - The Entrainer Selection and Sequencing Problem Ismail SR, Pistikopoulos EN, Papalexandri KP |
217 - 222 |
Minlp-Optimization of Complex Column Configurations for Azeotropic Mixtures Frey T, Bauer MH, Stichlmair J |
223 - 230 |
A Physical Limitation Based Framework for Separations Synthesis Oyoung L, Natori Y, Pressly TG, Ng KM |
231 - 236 |
Heuristic-Numeric Design of Separation Processes for Azeotropic Mixtures Schembecker G, Simmrock KH |
237 - 242 |
Complex Distillation Arrangements - Extending the Petlyuk-Ideas Christiansen AC, Skogestad S, Lien K |
243 - 247 |
Simulation Oriented Development of a New Heat-Integrated Distillation Column and Its Characteristics for Energy-Saving Takamatsu T, Nakaiwa M, Huang K, Akiya T, Noda H, Nakanishi T, Aso K |
249 - 254 |
Optimizing Control of Petlyuk Distillation - Understanding the Steady-State Behavior Halvorsen IJ, Skogestad S |
255 - 259 |
A Graduate Course in Computer-Integrated Process Operations Doyle FJ, Pekny JF, Reklaitis GV, Venkatasubramanian V |
261 - 266 |
An Undergraduate Course in-Process Dynamics Bequette BW |
267 - 272 |
Control of Systems with Recycle by Means of Compensators Scali C, Ferrari F |
273 - 278 |
Control Configuration Selection in Recycle Systems by Steady-State Analysis Semino D, Giuliani G |
279 - 284 |
Effect of Recycle on the Plant Zero Dynamics Jacobsen EW |
285 - 290 |
An Analysis of the Recycle Dynamics of a High-Pressure Production Process Bogle ID, Gobby D, Zwahlen AG |
291 - 296 |
Effect of Recycle Interactions on Dynamics and Control of Complex Plants Dimian AC, Groenendijk AJ, Kersten SR, Iedema PD |
297 - 304 |
Control and the Future of Technology Rosenbrock H |
305 - 310 |
Pollution Prevention with Chemical Process Simulators - The Generalized Waste Reduction (War) Algorithm Cabezas H, Bare JC, Mallick SK |
311 - 317 |
Computer-Aided Identification of Chemical-Reaction Hazards Bruneton C, Hoff C, Barton PI |
319 - 324 |
Process Concept Studio - An Experiment in Academic/Industrial Collaboration Rotstein GE, Sorensen S, Voudouris VT, Sorensen E, Sanchez A, Shah N, Macchietto S, Weiss RA |
325 - 330 |
Development of Novel Multiphase Reactors Using a Systematic Design Framework Mehta VL, Kokossis A |
331 - 335 |
Design of Industrial Packing/Production Processes with Operational Uncertainties Tahmassebi T |
337 - 342 |
Layout of Process Plants - A Novel-Approach Georgiadis MC, Macchietto S |
343 - 348 |
Optimization of a Production Process from the in-Vivo Response of a Diagnostical Drug Kvale S, Dyrstad K, Jacobsen T, Asbjornsen OA, Omtveit T |
349 - 354 |
The Optimal-Design of Refrigerant Mixtures for a 2-Evaporator Refrigeration System Churi N, Achenie LE |
355 - 360 |
Multicomponent Multiphase Film-Like Systems - A Modeling Approach Kenig EY |
361 - 366 |
Modeling and Control of a Food Extrusion Process Elsey J, Riepenhausen J, Mckay B, Barton GW, Willis M |
367 - 371 |
Time-Delay Neural Networks for the Classification of Flow Regimes Yamashita Y |
373 - 378 |
Centralized and Decentralized Control of Retrofit Heat-Exchanger Networks Uzturk D, Akman U |
379 - 384 |
Online Optimization and Choice of Optimization Variables for Control of Heat-Exchanger Networks Glemmestad B, Skogestad S, Gundersen T |
385 - 390 |
Model-Based Optimization and Control of a Reactor System with Heterogeneous Catalyst Carlberg PJ, Feord DM |
391 - 396 |
A Case-Study in Control-Structure Selection for a Chemical Reactor Walsh SP, Chenery S, Owen P, Malik TI |
397 - 402 |
Study on Nonminimum-Phase Behavior and Optimal Operation Kuhlmann A, Bogle D |
403 - 408 |
Input Selection for Disturbance Rejection Under Manipulated Variable Constraints Cao Y, Rossiter D, Owens D |
409 - 414 |
The Robust Performance Number - A New Tool for Control-Structure Design Trierweiler JO, Engell S |
415 - 420 |
Inclusion of Model Uncertainty in a Computational Framework for Dynamic Operability Assessment Ross R, Swartz CL |
421 - 426 |
Multilevel-Hierarchical Minlp Synthesis of Process Flowsheets Kravanja Z, Grossmann IE |
427 - 432 |
Logmip - A Disjunctive 0-1-Nonlinear-Optimizer for Process Systems Models Vecchietti A, Grossmann IE |
433 - 438 |
Testing a New Parallel Preconditioner on Linear-Systems Arising from Flowsheeting Simulation Paloschi JR |
439 - 444 |
A Parallel Block Frontal Solver for Large-Scale Process Simulation - Reordering Effects Mallya JU, Zitney SE, Choudhary S, Stadtherr MA |
445 - 450 |
Global Optimization of Minlp Problems in-Process Synthesis and Design Adjiman CS, Androulakis IP, Floudas CA |
451 - 456 |
Mixed-Integer Dynamic Optimization Allgor RJ, Barton PI |
457 - 462 |
Towards an Efficient Numerical Procedure for Mixed-Integer Optimal-Control Mohideen MJ, Perkins JD, Pistikopoulos EN |
463 - 468 |
A Neural-Network Strategy for Batch Process Optimization Krothapally M, Palanki S |
469 - 474 |
Retrofit and Optimization of Industrial Heat-Exchanger Networks - A Complete Benchmark Problem Nielsen JS, Hansen MW, Kristensen KP |
475 - 480 |
Process Optimization by Simulated Annealing and Nlp Procedures - Application to Heat-Exchanger Network Synthesis Athier G, Floquet P, Pibouleau L, Domenech S |
481 - 486 |
A General Formulation for the Synthesis of Combined Heat and Power-Systems with Minimum Annual Cost Wilkendorf F, Corominas J, Espuna A, Puigjaner L |
487 - 492 |
Different Strategies for Solving Bilinear Integer Nonlinear-Programming Problems with Convex Transformations Harjunkoski I, Porn R, Westerlund T, Skrifvars H |
493 - 498 |
Implementation of Novel Processes in Existing Process Networks - Evaluation of the Industrial-Production of C-4 Chemicals by Optimization Dijkema GP, Steenkamp EM, Verheijen PJ |
499 - 504 |
Handling Implicit Model Formulations in Minlp Optimization Noronha S, Gruhn G, Kravanja Z |
505 - 510 |
Generation of Reduced Statistical-Models for Nlp and Minlp Optimization Noronha S, Gruhn G |
511 - 516 |
Energy Savings in Methanol Synthesis - Use of Heat Integration Techniques and Simulation Tools Marechal F, Heyen G, Kalitventzeff B |
517 - 522 |
Retrofit of Complex and Energy Intensive Processes Kralj AK, Glavic P |
523 - 528 |
Driving-Force Distribution and Exergy Loss in the Thermodynamic Analysis of Distillation-Columns Zemp RJ, Defaria SH, Maia MD |
529 - 534 |
Comparative Energy-Consumption in Batch and Continuous Distillation Oppenheimer O, Sorensen E |
535 - 540 |
Experimental Investigation of Multiple Steady-States and Parametric Sensitivity in Azeotropic Distillation Wang CJ, Wong DS, Chien IL, Shih RF, Wang SJ, Tsai CS |
541 - 546 |
Multiple Steady-States of Distillation and Its Realization Kiva VN, Alukhanova BM |
547 - 552 |
Mixed-Integer Optimization of Combined Solvent-Extraction and Distillation Processes Glanz S, Stichlmair J |
553 - 557 |
Short-Cut Evaluation of Distillation Sequences Jobson M |
559 - 564 |
Modeling and Control of an Industrial Azeotropic Train Tonelli SM, Brignole NB, Brignole EA |
565 - 570 |
Monitoring of a Distillation Column Using Modified Extended Kalman Filter and a Reduced-Order Model Yang DR, Lee KS |
571 - 576 |
Process Design for Operability - A Styrene Polymerization Application Russo LP, Bequette BW |
577 - 582 |
Handling Infeasibilities in Predictive Control Alvarez T, Deprada C |
583 - 588 |
Hierarchical Modeling of Recipe Controllers - A Practical Approach Brettschneider H, Christmann U, Fleck S, Hamann S, Hanisch HM |
589 - 594 |
Development of a Suitable Optimal Operating Control Strategy for Large-Scale Dryers Maciel R, Wolf MR, Vasconcelos LG |
595 - 600 |
Control Design for Nonlinear Process Models Using Linear Robust-Control Methods - An FCCU Example Goh KC, Wu F, Walsh S |
601 - 606 |
Control of a Pilot-Scale Karr Liquid-Liquid-Extraction Column Wachs A, Benyamin J, Semiat R, Lewin DR |
607 - 612 |
Application of Optimal Adaptive-Control Based on Generalized Minimum-Variance to a Packed Distillation Column Caglayan N, Karacan S, Hapoglu H, Alpbaz M |
613 - 618 |
Fuzzy Predictive Control of Highly Nonlinear pH Process Kavsekbiasizzo K, Skrjanc I, Matko D |
619 - 624 |
Integrated Information Modeling Strategies for Safe Design in the Process Industries Mcalinden LP, Sitoh PJ, Norman PW |
625 - 630 |
Application of the Intelligent Alarm System for the Plant-Operation Yamanaka F, Nishiya T |
631 - 636 |
Interactive Self-Modeling of Chemical-Reaction Systems Using Multivariate Data-Analysis Sans D, Nomen R, Sempere J |
637 - 642 |
Applying Artificial Neural-Network Models to Control a Time-Variant Chemical-Plant Milanic S, Sel D, Hvala N, Strmcnik S, Karba R |
643 - 648 |
Adaptation Phase in Case-Based Reasoning System for Process Equipment Selection Virkkihatakka T, Kraslawski A, Koiranen T, Nystrom L |
649 - 654 |
Fault-Diagnosis, Direct Graphs, and Fuzzy-Logic Tarifa EE, Scenna NJ |
655 - 660 |
Signed Digraph Based Multiple-Fault Diagnosis Vedam H, Venkatasubramanian V |
661 - 666 |
Fuzzy Rule Generation from Data for Process Operational Decision-Support Wang XZ, Chen BH, Yang SH, Mcgreavy C, Lu ML |
667 - 672 |
Process Industry Information-Systems - Modeling Support Tools Mannarino GS, Henning GP, Leone HP |
673 - 678 |
Scheduling of Batch Processes - An Industrial Application in Paint Industry Orcun S, Discioglu A, Altinel K, Hortacsu O |
679 - 684 |
The Maximum Order Tree Method - A New Approach for the Optimal Scheduling of Product Distribution Lines Mokashi SD, Kokossis A |
685 - 690 |
A Hybrid Global Optimization Method for Design of Batch Chemical Processes Yuan XG, Chen ZZ |
691 - 696 |
Modeling of the Supervising Control-System of a Multipurpose Batch Plant Gonnet S, Chiotti O |
697 - 702 |
Design and Synthesis of Batch Plants Minlp Solution Based on a Stochastic Method Xia QS, Macchietto S |
703 - 708 |
Design of Multipurpose Plants Using the Resource-Task Network Unified Framework Barbosapovoa AP, Pantelides CC |
709 - 714 |
Local Thermodynamic Models Used in Sensitivity Estimation of Dynamic-Systems Storen S, Hertzberg T |
715 - 720 |
Dynamic Simulation of an Absorption Heat Transformer Incorporated with an Evaporation Plant Granfors A, Nilsson B, Jernqvist A, Aly G |
721 - 726 |
Simplifying Hypotheses in Computer-Aided Modeling - A Singular Perturbation Approach Weiss M, Preisig HA |
727 - 732 |
Dynamic Optimization of Differential-Algebraic Systems Through the Dynamic Simulator Dynsim Gani R, Grancharova A |
733 - 738 |
Phase-Equilibrium Dominant Parameter Matrix of Multicomponent Distillation Trains Gros HP, Urlic LE, Brignole EA |
739 - 744 |
Dynamic Modeling, Sensitivity Analysis and Parameter-Estimation of Industrial Yeast Fermenters Pertev C, Turker M, Berber R |
745 - 750 |
Design of Virtual-Labo-System for Metabolic Engineering - Development of Biochemical-Engineering System Analyzing Tool-Kit (Best Kit) Okamoto M, Morita Y, Tominaga D, Tanaka K, Kinoshita N, Ueno JI, Miura Y, Maki Y, Eguchi Y |
751 - 756 |
Hybrid Modeling of Biochemical Processes - A Comparison with the Conventional Approach Deazevedo SF, Dahm B, Oliveira FR |
757 - 762 |
Modeling of Interconnected Reactor Systems Described by Nonlinear PDEs Kubicek M, Pinkas P, Jirat J, Snita D, Marek M |
763 - 768 |
Dynamic Mathematical-Model of Deep Bed Filtration Process Osmak S, Gosak D, Glasnovic A |
769 - 773 |
An Open Software Architecture for Batch Process Simulation Fritz M, Engell S |
775 - 783 |
Reactor and Process Synthesis Glasser D, Hildebrandt D |
785 - 790 |
A Case-Study for Reactor Network Synthesis - The Vinyl-Chloride Process Lakshmanan A, Biegler LT |
791 - 796 |
Global Optimization of Nonconvex Minlps Smith EM, Pantelides C |
797 - 803 |
Multiscale Modeling, Estimation and Control of Processing Systems Stephanopoulos G, Dyer M, Karsligil O |
805 - 809 |
The Modusim Concept for Modular Modeling and Simulation in Chemical-Engineering Dieterich EE, Eigenberger G |
811 - 816 |
Fully Adaptive Model Size-Reduction for Multicomponent Separation Problems Vonwatzdorf R, Marquardt W |
817 - 822 |
Dynamic Multiple-Phase Flash Simulation - Global Stability Analysis Versus Quick Phase Determination Muller D, Marquardt W |
823 - 828 |
The Formal Representation of Process System Modeling Assumptions and Their Implications Hangos KM, Cameron IT |
829 - 834 |
Structural and Symbolic Techniques for Automatic Characterization of Differential-Algebraic Equations Murata VV, Biscaia EC |
835 - 840 |
A Formal Graphical Based Process Modeling Methodology Drengstig T, Wasbo SO, Foss BA |
841 - 846 |
Application of the Modeling and Simulation Environment Promot/Diva to the Modeling of Distillation Processes Trankle F, Gerstlauer A, Zeitz M, Gilles ED |
847 - 852 |
Specialized Programming Methods in the Model-Predictive Control of Large-Scale Systems Doyle FJ, Pekny JF, Dave P, Bose S |
853 - 859 |
Interior-Point Sqp Strategies for Structured Process Optimization Problems Albuquerque JS, Gopal V, Staus GH, Biegler LT, Ydstie BE |
861 - 866 |
Linear Parameter Varying Model-Predictive Control for Steam-Generator Level Control Kothare MV, Mettler B, Morari M, Bendotti P, Falinower CM |
867 - 872 |
Performance Analysis of Online Batch Optimization Systems Loeblein C, Perkins JD, Srinivasan B, Bonvin D |
873 - 879 |
Model-Predictive Control for Nonlinear Batch Processes with Asymptotically Perfect Tracking Lee KS, Lee JH |
881 - 886 |
An Interpolating Model-Predictive Control Strategy with Application to a Waste Treatment-Plant Qin SJ, Martinez VM, Foss BA |
887 - 892 |
Real-Time Optimization of a Cat Cracker Unit Lid T, Strand S |
893 - 897 |
Model-Predictive Control of a Crude-Oil Distillation Column Hovd M, Michaelsen R, Montin T |
899 - 903 |
A 2-Tier Methodology for Synthesis of Operating Procedures Li HS, Lu ML, Naka Y |
905 - 910 |
Integrating Knowledge-Based and Mathematical-Programming Approaches for Process Safety Verification Srinivasan R, Dimitriadis VD, Shah N, Venkatasubramanian V |
911 - 916 |
Dynamic Modeling Helps Relief Valve Study During Live ICI-Project Collins SN, Falgowski M, Malik TI |
917 - 922 |
An Expert-System for Automated Hazard Analysis Based on Multimodel Approach Suh JC, Lee BW, Kang IK, Yoon ES |
923 - 928 |
A Prototype for Integrating Automatic Fault-Tree Event Tree HAZOP Analysis Kuo DH, Hsu DS, Chang CT |
929 - 933 |
A Hybrid Ann-Es System for Dynamic Fault-Diagnosis of Hydrocracking Process Zhao JS, Chen BZ, Shen JZ |
935 - 940 |
A Hybrid Framework for Large-Scale Process Fault-Diagnosis Mylaraswamy D, Venkatasubramanian V |
941 - 946 |
Intelligent Fault-Diagnosis Based on Weighted Symptom Tree Model and Fault-Propagation Trends Oh YS, Yoon JH, Nam D, Han C, Yoon ES |
947 - 952 |
Modeling and Control of a Chemical Waste-Water Treatment-Plant Miller RM, Itoyama K, Uda A, Takada H, Bhat N |
953 - 958 |
Life-Cycle Oriented Process Synthesis at Conceptual Planning Phase Ishii N, Fuchino T, Muraki M |
959 - 964 |
Reaction-Path Synthesis for Environmental-Impact Minimization Buxton A, Livingston AG, Pistikopoulos EN |
965 - 970 |
Chemical Process Route Selection Based on Assessment of Inherent Environmental-Hazard Cave SR, Edwards DW |
971 - 976 |
Rationalizing the Water-Use in the Batch Process Industry Almato M, Sanmarti E, Espuna A, Puigjaner L |
977 - 982 |
Optimization of Pollution-Control Operations in Industrial Sites Considering Decay Capabilities of the Receptors Kiperstok A, Sharratt PN |
983 - 988 |
Reactive Distillation Column Design with Vapor/Liquid/Liquid Equilibria Gumus ZH, Ciric AR |
989 - 994 |
Nonlinear Dynamics of Reactive Distillation Processes for the Production of Fuel Ethers Mohl KD, Kienle A, Gilles ED, Rapmund P, Sundmacher K, Hoffmann U |
995 - 1000 |
Predicting Multiple Steady-States in Distillation - Singularity Analysis and Reactive Systems Guttinger TE, Morari M |
1001 - 1006 |
A Singular Ty Theory Approach to the Study of Reactive Distillation Gehrke V, Marquardt W |
1007 - 1012 |
Modeling and Simulation of the Chemical-Reaction Heat-Pump System Adopting the Reactive Distillation Process Chung Y, Jeong HK, Song HK, Park WH |
1013 - 1018 |
Design Targets of Separator and Reactor-Separator Systems Using Conceptual Programming Shah PB, Kokossis A |
1019 - 1024 |
Optimization Accounting for Property Prediction Uncertainty in Polymer Design Maranas CD |
1025 - 1030 |
Inferential Estimation of Polymer Quality Using Stacked Neural Networks Zhang J, Martin EB, Morris AJ, Kiparissides C |
1031 - 1036 |
Simultaneous-Optimization of Mixing Patterns and Feed Distribution in LDPE Autoclave Reactors Sund EB, Lien K |
1037 - 1042 |
Hierarchical Time-Optimal Control of a Continuous Co-Polymerization Reactor During Start-Up or Grade Change Operation Using Genetic Algorithms Lee MH, Han C, Chang KS |
1043 - 1048 |
Experimental-Study of the Nonlinear Geometric Control of a Batch Emulsion Polymerization Reactor Gentric C, Pla F, Corriou JP |
1049 - 1054 |
Modeling and Control of Tubular Solution Polymerization Reactors Vega MP, Lima EL, Pinto JC |
1055 - 1060 |
Robust Scheduling with Processing Time Uncertainty Honkomp SJ, Mockus L, Reklaitis GV |
1061 - 1066 |
Rtn-Based Rolling Horizon Algorithms for Medium-Term Scheduling of Multipurpose Plants Dimitriadis AD, Shah N, Pantelides CC |
1067 - 1072 |
Rescheduling Algorithms in Case of Unit Failure for Batch Process Management Ko D, Moon I |
1073 - 1077 |
Ethylene Plant Scheduling System Based on a Minlp Formulation Tjoa IB, Ota Y, Matsuo H, Natori Y |
1079 - 1085 |
Continuous-Time Representation for Multistage Plant Scheduling - Formulation and Case-Study Tahmassebi T |
1087 - 1092 |
Application of Repetitive SA Method to Scheduling Problems of Chemical Processes Murakami Y, Uchiyama H, Hasebe S, Hashimoto I |
1093 - 1098 |
A Practical Method of Removing Ill-Conditioning in Industrial Constrained Predictive Control Ishikawa A, Ohshima M, Tanigaki M |
1099 - 1103 |
Model-Based Analysis and Control of a Cementation Process Stolehansen K, Wregget DA, Gowanlock D, Thwaites PE |
1105 - 1110 |
A Modeling and Simulation Study on a Naphtha Reforming Unit with a Catalyst Circulation and Regeneration System Lee JW, Ko YC, Jung YK, Lee KS, Yoon ES |
1111 - 1115 |
Real-Time Simulation of a Vcm-Plant Lundstrom P, Sira T, Ausen T |
1117 - 1122 |
Application of Wavelet Analysis to Fault-Detection in Oil Refinery Daiguji M, Kudo O, Wada T |
1123 - 1129 |
Statistical-Data Analysis of a Chemical-Plant Santen A, Koot GL, Zullo LC |
1131 - 1136 |
Optimization of an Industrial 3-Phase Distillation Column Train with Experimental-Verification Schneider R, Wozny G, Fieg G |
1137 - 1142 |
Optimization of a Wood Chip Refining Process-Based on Fuzzy Relational Models Qian Y, Liu HB, Zhang XP, Tessier PJ |
1143 - 1148 |
Subspace Identification Based Inferential Control of a Continuous Pulp Digester Amirthalingam R, Lee JH |
1149 - 1154 |
The False Nearest Neighbors Algorithm - An Overview Rhodes C, Morari M |
1155 - 1160 |
Nonlinear Modeling of LPG Percent-C5 Content of Catalytic Reformer Debutaniser Column Aoyama A, Walsh SP |
1161 - 1166 |
Systems Modeling Using Genetic Programming Willis M, Hiden H, Hinchliffe M, Mckay B, Barton GW |
1167 - 1172 |
Multiscale Rectification of Random Errors Without Fundamental Process Models Bakshi BR, Bansal P, Nounou MN |
1173 - 1178 |
Confidence-Bounds for Neural-Network Representations Shao R, Martin EB, Zhang J, Morris AJ |
1179 - 1184 |
Performance Evaluation of Catalytic Processes Christiansen LJ, Brunicheolsen N, Carstensen JH, Schroder M |
1185 - 1190 |
Online Data Reconciliation and Optimization - Refinery Applications Chiari M, Bussani G, Grottoli MG, Pierucci S |
1191 - 1196 |
Optimal Periodic Scheduling of Multipurpose Plants in the Continuous-Time Domain Schilling G, Pantelides CC |
1197 - 1202 |
Rule-Based Reactive Rescheduling System for Multipurpose Batch Processes Kim MS, Lee IB |
1203 - 1208 |
Obtaining Realistic Production Plans for a Batch-Production Facility Bassett MH, Pekny JF, Reklaitis GV |
1209 - 1214 |
A Multiple-View Batch Plant Information Model Simensen J, Johnsson C, Arzen KE |
1215 - 1220 |
A Cyclic Operating Policy for Batch Distillation - Theory and Practice Sorensen E, Prenzler M |
1221 - 1226 |
Optimal Operation Policy for Multieffect Batch Distillation System Hasebe S, Noda M, Hashimoto I |
1227 - 1231 |
Adaptive and Predictive Control Strategies for Batch Distillation - Development and Experimental Testing Fileti AM, Pereira JA |
1233 - 1238 |
Neuro-Fuzzy Modeling and Control of a Batch Process Involving Simultaneous Reaction and Distillation Wilson JA, Martinez EC |
1239 - 1244 |
Modeling and Optimization of an Industrial Batch Process for the Production of Dioctyl Phthalate Ishikawa T, Natori Y, Liberis L, Pantelides CC |