Computers & chemical engineering

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  Año 2004, Número 1

  • A mathematical programming approach for cyclic production and cleaning scheduling of multistage continuous plants

    Lazaros G. Papageorgiou, Jose M. Pinto, Alessandro Alle

    págs. 3-15

    

  • Feasibility of equilibrium-controlled reactive distillation process: application of residue curve mapping

    Cristhian Almeida-Rivera, Johan Grievink

    págs. 17-25

    

  • Optimal sensor location and reduced order observer design for distributed process systems

    Julio Rodríguez Banga, Ioannis G. Kevrekidis, Christos E. Frouzakis, Antonio Alvárez Alonso

    págs. 27-35

    

  • Selection of internals for reactive distillation column¿case-based reasoning approach

    Lars Nyström, Andrzej Kraslawski, Yuri Avramenko

    págs. 37-44

    

  • Planning, scheduling and budgeting value-added chains

    R. Huertas, Luis Puigjaner Corbella, M. Badell, J. Romero

    págs. 45-61

    

  • Design of tubular reactors in recycle systems

    Costin S. Bildea, Susana C. Cruz, Piet D. Iedema, Alexandre C. Dimian

    págs. 63-72

    

  • CAPD¿computer-aided plant design

    A. Burdorf, H. Schmidt-Traub, M. Lederhose, B. Kampczyk

    págs. 73-81

    

  • Multiobjective process controllability analysis

    Yi Cao, Zhijia Yang

    págs. 83-90

    

  • Short-term site-wide maintenance scheduling

    Lionel O'Young, Kwok-Yuen Cheung, Haruo Sakamoto, Kentaro Hirata, Chi-Wai Hui

    págs. 91-102

    

  • Optimal design of membrane processes for wastewater treatment and metal recovery

    Ana M. Eliceche, Sergio M. Corvalán, Inmaculada Ortiz Uribe

    págs. 103-109

    

  • Coordinating feedback and switching for control of spatially distributed processes

    Nael H. El-Farra, Panagiotis D. Christofides

    págs. 111-128

    

  • The effect of model simplification assumptions on the differential index of lumped process models

    K.M. Hangos, G. Szederkényi, Zs. Tuza

    págs. 129-137

    

  • Multi-site utility integration¿an industrial case study

    Kwok-Yuen Cheung, Lionel O'Young, Kentaro Hirata, Chi-Wai Hui, Haruo Sakamoto

    págs. 139-148

    

  • Automating reactor network synthesis: finding a candidate attainable region for the water¿gas shift (WGS) reaction

    D. Glasser, D. Hildebrandt, L.T. Biegler, S. Kauchali, B. Hausberger

    págs. 149-160

    

  • On the use of reduced order models in bifurcation analysis of distributed parameter systems

    Elling W. Jacobsen, Yi Liu

    págs. 161-169

    

  • A mixed integer programming approach for scheduling commodities in a pipeline

    F. Neves Jr, L. Magatão, L.V.R. Arruda

    págs. 171-185

    

  • Computation of frequency locking regions for a discontinuous periodically forced reactor

    S. Crescitelli, L. Russo, G. Continillo, E. Mancusi

    págs. 187-194

    

  • Robust model-based tracking control using parametric programming

    Vassilis Sakizlis, Vivek Dua, Efstratios N. Pistikopoulos, John D. Perkins

    págs. 195-207

    

  • A new algorithm for developing dynamic radial basis function neural network models based on genetic algorithms

    Haralambos Sarimveis, Stefanos Mazarakis, George Bafas, Alex Alexandridis

    págs. 209-217

    

  • Control structure design for complete chemical plants

    Sigurd Skogestad

    págs. 219-234

    

  • MINLP retrofit of heat exchanger networks comprising different exchanger types

    Aleksander Sor¿ak, Zdravko Kravanja

    págs. 235-251

    

  • Optimisation and experimental verification of startup policies for distillation columns

    Pu Li, Günter Wozny

    págs. 253-265

    

  • The effect of model fidelity on real-time optimization performance

    T.E. Marlin, W.S. Yip

    págs. 267-280