[1] Ahmmed S. Ibrehem, Mohamed Azlan Hussain, Nayef Mohamed Ghasem, Mathematical Model and Advanced Control for Gas Phase Olefin Polymerization in Fluidized-Bed Catalytic Reactors, Chinese Journal of Chemical Engineering, 16(1), p. 84 (2007).
[2] Helal A.M., Elnashaie S.S., Numerical Construction of Bifurcation Diagrams for Non-Linear Complex Reaction Networks in Catalytic Reactors, Computers & Chemical Engineering, 14(6), p. 691(1990).
[3] Antonio Flores-Tlacuahuac, Lorenz T. Biegler, A Robust and Efficient Mixed-integer Non-Linear Dynamic Optimization Approach for Simultaneous Design and Control, Computer Aided Chemical Engineering, 20(1), p. 67 (2005).
[4] Kiashemshaki A., Mostoufi N., Pourmahdian S, Sotudeh-GharebaghR., Two phase Modeling of a Gas Phase Polyethylene Fluidized Bed Reactor, Chemical Engineering Science, 61, p. 3997 (2006).
[5] Aswin N. Venkat, P. Vijaysai and Ravindra D. Gudi
, Identification of Complex Nonlinear Processes Based on Fuzzy Decomposition of the Steady State Space,
Electronic Journal of Biotechnology,
10(4), (2007).
[6] Baker B.D., Richards C.E.,, Exploratory Application of Systems Dynamics Modeling to School Finance Policy, Journal of Education Finance, 27(3), p. 857 (2002).
[7] Biegler L., Improved Infeasible Path Optimizer for Sequential Modular Simulators-I: The Interface, Computers and Chemical Engineering, 9(3), p. 245 (1985).
[8] Bassam Alhamad, Jose A. Romagnoli, Vincent G. Gomes, On-Line Multi-Variable Predictive Control of Molar Mass and Particle Size Distributions in Free-Radical Emulsion Copolymerization, Chemical Engineering Science, 60(23), p. 6596 (2005).
[9] Babatunde A. Ogunnaike, Kapil Mukati, An Alternative Structure for Next Generation Regulatory Controllers : Part I: Basic Theory for Design, Development and Implementation, Journal of Process Control, 16(5), p. 499 (2006).
[10] Chatzidoukas C., Perkins J.D., Pistikopoulos E.N., Kiparissides C., Optimal-Grade Ransition and Selection of Closed-Loop Controllers in a Gas-Phase Olefin Polymerization Fluidized Bed Reactor, Chemical Engineering Science, 58, p. 3643 (2003).
[11] Chiaki Kuroda, Jinyoung Kim, Neural Network Modeling of Temperature Behavior in an Exothermic Polymerization Process, Neurocomputing, 43(1-4), p. 77 (2002).
[12] Charles D., Francis J. Doyle, Modeling of Particle Size Distribution in Emulsion co-Polymerization: Comparison with Experimental Data and Parametric Sensitivity Studies, Computers & Chemical Engineering, 26(7-8), p. 1133 (2002).
[13] Ang D.D., Pham Ngoc Dinh A., Thanh D.N.
, Regularization of an Inverse Two-Phase Stefan Problem,
34(5), p. 719 (1998).
[14] Dennis Van Hessem, Okko Bosgra, Stochastic Closed-Loop Model Predictive Control of Continuous Nonlinear Chemical Processes, Journal of Process Control, 16(3), p. 225 (2006).
[15] Del Vecchio D., Petit N., Boundary Control for An Industrial Under-Actuated Tubular Chemical Reactor, Ournal of Process Control, 15(7), p. 771 (2005).
[16] Dulce C.M. Silva, Nuno M.C. Oliveira, Optimization and Nonlinear Model Predictive Control of Batch Polymerization Systems, Computers & Chemical Engineering, 26(4-5), p. 649 (2002).
[17] Baker E.L., “Modeling and Optimization of Shaped Charge Liner Collapse and Jet Formation”, Ph.D. Dissertation, Washington State University, Pullman, Washington, (1992).
[18] Fine T.L., “Feed Forward Neural Network Methodology”, Springer, New York (1999).
[19] Francis J. Doyle, III , Christopher A. Harrison, Timothy J. Crowley, Hybrid Model-Based Approach to Batch-to-Batch Control of Particle Size Distribution in Emulsion Polymerization, Computers & Chemical Engineering, 27(8-9), p. 1153 (2003).
[20] Mourue G., Dochain D., Wertz V., Descamps P.,Identification and Control of An Industrial Polymerisation Reactor, Control Engineering Practice, 12(7), p. 909 (2004).
[21] Gangadhar Gattu Evanghelos Zafiriou, A Methodology for on-Line Setpoint Modification for Batch Reactor Control in the Presence of Modeling Error, Chemical Engineering Journal, 75(1), p. 21 (1999).
[22] Ravi Sriniwas G., Arkun Y., Joseph Schork F., Estimation and Control of an α-Olefin Polymerization Reactor, Ournal of Process Control, 5(5), p. 303 (1995).
[23] Hatzantonis H., Yiannoulakis H., Yiagopoulos A., Kiparissides C., Recent Developments in Modeling Gas-Phase Catalyst Olefin Polymerization Fluidized Bed Reactor: The Effect of Bubble Size Variation on the Reactor’s Performance, Chemical Engineering Science, 5, p. 3237 (2000).
[24] Huang B., Mujumdar A.S., Use of Neural Network to Predict Industrial Dryer Performance, Drying Technology, 3, p. 525 (1993).
[25] Hiroya Seki, Morimasa Ogawa, Satoshi Ooyama, Kouji Akamatsu, Masahiro Ohshima, Wang Yang, Industrial Application of a Nonlinear Model Predictive Control to Polymerization Reactors, Control Engineering Practice, 9(8), p. 819 (2001).
[26] Joachim Horn, Trajectory Tracking of a Batch Polymerization Reactor Based on Input-Output-Linearization of a Neural Process Model, Computers & Chemical Engineering, 25(11-12), p. 1561 (2001).
[27] Joaquim A., Dente R., Vilela mendes, Characteristic Functions and Process Identification by Neural Networks, Neural Networks, 10, p. 1465 (1997).
[28] Jesus Flores-Cerrillo, John F. MacGregor, Latent Variable MPC for Trajectory Tracking in Batch Processes, Journal of Process Control, 15(6), p. 651 (2005).
[29] Choi K.Y., Ray W.H., The Dynamic Behaviour of Fluidized Bed Reactors for Solid Catalyzed Gas Phase Olefin Polymerization, Chem. Eng. Sci., 40, p. 2261 (1985).
[30] Kenneth R. Harris, Ahmet Palazolu, Control of Nonlinear Processes Using Functional Expansion Models, Computers & Chemical Engineering, 27(8-9), p. 1061 (2003).
[32] Powell M.J.D., in “Numerical Analysis, Proceedings of the Biennial Conference Held at Dundee”, G.A. Watson eds., Lecture Notes in Mathematics, Vol. 630, Springer-Verlag, Berlin, New York, 1978, p. 144 (1977).
[33] Bazaraa M.S., Sherali H.D., Shetty C.M., “Nonlinear Programming:Theory and Algorithms”, 2nd edition, John Wiley & Sons, Inc., New York, (1993).
[34] Hussain M.A., Shafiur Rahman M., Ng C.W., Prediction of Pores Formation (Porosity) in Foods During Drying: Generic Models by the Use of Hybrid Neural Network, Journal of Food Engineering, 51(3), p. 239 (2002).
[35] Mourad M., Hémati M., LaguérieMing C., Drying of Maize in a Fluidized Bed: II: A Kinetic, Model,of, Drying, Chemical Engineering Journal and the Biochemical Engineering Journal, 60, p. 39 (1995).
[36] Morimasa Ogawa, Masahiro Ohshima, Koji Morinaga, Fuminao Watanabe, Quality Inferential Control of an Industrial High Density Polyethylene Process, Journal of Process Control, 9(1), p. 51 (1999).
[37] Mourad M., He´ mati M., Lague´ rieMing C., Drying of Maize in a Fluidized Bed: II: a Kinetic Model of Drying, The Chemical Engineering Journal and the Biochemical Engineering Journal, 60 (1–3, 12), p. 39 (1995).
[38] Mariano Asteasuain, Alberto Bandoni, Claudia Sarmoria, Adriana Brandolin,Simultaneous Process and Control System Design for Grade Transition in Styrene Polymerization, Chemical Engineering Science, 61(10), p. 3362 (2006).
[39] Mahmood Alizadeh, Navid Mostoufi, Saeed Pourmahdian, Rahmat Sotudeh-Gharebagh, Modeling of Fluidized Bed Reactor of Ethylene Polymerization, Chemical Engineering Journal, 97, p. 27 (2004).
[40] Nayef Mohamed Ghasem, Mohd Zaki Sulaiman and Mohd Azlan Hussain, Simulation, Optimization and Parametric Studies of a Solid Catalyzed Gas Phase Ethylene Polymerization Fluidized Bed Reactor, Journal of Chemical Eng. of Japan, 38 p. 171 (2005).
[41] Abel O., Helbig A., Marquardt W., Zwick H., Daszkowski T., Productivity Optimization of An Industrial Semi-Batch Polymerization Reactor Under Safety Constraints, Journal of Process Control, 10(4), p. 351 (2000).
[42] Patwardhan R., Lakshminaraynan S., Shah S., Constrained nonlinear MPC Using Hammerstein and Wiener Models: PLS framework, AICHE Journal, 44(7), p. 1611 (1998).
[43] Gill P.E., Murry W., Wright M.H., “Practical Optimization”, Academic Press, New York, 1981.
[44] Evanghelos Zafiriou and Hung-Wen Chiou, On the Effect of Constrint Softening on the Stability and Performance of Model Predictive Controllers, AIChE, 1, p. 6 (1992).
[45] Roos. Sala, F. Valz-Gris and L. Zanderighi, A Fluid-Dynamic Study of a Continuous Polymerisation Reactor, Chemical Engineering Science, 29, p. 2205 (1974).
[46] Reddy B.V., Nag P.K., Axial and Radial Heat Transfer Studies in a Circulating Fluidized Bed, International Journal of Energy Research, 21, p. 1109 (1997).
[47] Rao C.V., Wright S.J., Rawlings J.B., Application of Interior-Point Methods to Model Predictive Control, Journal of Optimization Theory and Applications, 99(3), p. 723 (1998).
[48] Sala R., Valz-Gris F., Zanderighi L., A Fluid-Dynamic Study of a Continuous Polymerisation Reactor, Chemical Engineering Science, 29, p. 2205 (1974).
[49] Zeman R.J., Amundson N.R., Continuous Polymerization Models-Part II : Batch Reactor Polymerization, Chemical Engineering Science, 20, p. 637 (1965).
[50] Roberto Lemoine-Nava, Antonio Flores-Tlacuahuac, Enrique Sald´ıvar-Guerra,Non-linear Bifurcation Analysis of the Living Nitroxide-Mediated Radical Polymerization of Styrene in a CSTR, Chemical Engineering Science, 61(2), p. 370 (2006).
[51] Shaw A.M., Doyle F.J., Schwaber J.S., A Dynamic Neural Network Approach to Nonlinear Process Modeling, Computers and Chemical Engineering, 21, p. 371 (1997).
[52] Smith M., "Neural Networks for Statistical Modeling", International Thomson Computer Press, Boston (1996).
[53] Sablani S.S., A Neural Network Approach for Non-Iterative Calculation of Heat Transfer Coefficient in Fluid-Particle Systems, Chem. Eng. Process., 40,
p. 363 (2001).
[54] Shahaf G., Marom S., Learning in Networks of Cortical Neurons, Journal of Neuroscience, 21, p. 8782 (2001).
[55] Shaw A.M., Doyle F.J., Schwaber J.S l., A Dynamic Neural Network Approach to Nonlinear Process Modeling, Computers and Chemical Engineering, 21, p. 371 (1997).
[56] Sit S.P., Grace J.R., Effect of Bubble Interaction on Interphase Mass Transfer in Gas Fluidized Beds, Chemical Engineering Science, 36, p. 327 (1981).
[57] Smith, "Neural Networks for Statistical Modeling", International Thomson Computer Press, Boston,
(1996).
[58] Sreekanth S.S., Ramaswamy H.S., Sablani S.S., Prasher S.O., A Neural Network Approach for Evaluation of Surface Heat Transfer Coefficient, Journal of Food Processing and Preservation, 23(4), p. 329 (1999).
[59] Sang, Hyun, Neural Network Modeling of Temperature Behavior in An Exothermic Polymerization Process, Neurocomputing, 43(1-4), p. 77 (2002).
[60] Simant R. Upreti, Baranitharan S. Sundaram, Ali Lohi, Optimal Control Determination of MMA Polymerization in Non-Isothermal Batch Reactor Using Bifunctional Initiator, European Polymer Journal, 41(12), p. 2893 (2005).
[61] Thomas, Francis, An Anti-Windup Scheme for Multivariable Nonlinear Systems, Journal of Process Control, 14(8), p. 899 (2004).
[62] Tarmy B.I., Coulaloglou, Industrial View of Gas/Liquid/Solid Reactor Development, Chemical Engineering Science, 47, p. 3231 (1992).
[63] Stephen Whitaker, "Handbook of Heat and Mass Transfer", vol.3, Catalyst, Kinetics, and Reactor Engineering, Ch. 26, p. 1061 (1989).
[64] Tabis B., Essekkat A., Three-Phase Multi-Compartment Model for Fluidized-Bed Catalytic Reactor. Autothermicity and Multiplicity of Steady States, Chem.Eng.Sci., 47(2), p. 407 (1992).
[65] Toomey R.D., Johnstone, Gaseous Fluidization of Solid Particles, Chemical Engineering Progress, 48,
p. 220 (1952).
[66] Wolf J.A., Moyer J.T., Lazarewicz M.T., Contreras D., Benoit-Marand M., O'Donnell P., Finkel L.H.,
Neuron or Other Electrically Excitable Cell,
Physical Science Journal,
1(3), p. 13 (2005).
[67] Wei, Danial, "Control Relevant Model Reduction of Voltra Series Models, Department of Chemical, Bio and Materials Engineering and Control Systems Engineering", Arizona State University, USA, (1997).
[68] Werther, Modeling and Scale-Up of Industrial Fluidized Bed Reactors, Chemical Engineering Science, 35(1-2), p. 3 (1983).
[69] Xie, Edwards Allen, Noah Fahlgren, Adam Calamar, Scott A. Givan, James C. Carrington, Expression of Arabidopsis MIRNA Genes,
American Society of Plant Biologists,
138, p. 2145 (2005).
[70] Xuejing Zheng, Makarand S. Pimplapure, Günter Weickert, Joachim Loos, Study the Porosity Effects of Ziegler Natta Catalyst on Polymerization System, European polymer journal, 68, p. 680 (2006).
[71] Xie T.T., McAuley K.B., Hsu J.C.C., Bacon D.W., Gas Phase Ethylene Modeling, Ind. Eng. Chem. Res., 33, p. 449 (1994).
[72] Zabrodsky S.S., “Hydrodynamics and Heat Transfer in Fluidized Beds”. MIT Press, Cambridge, MA, U.S.A (1966).
[73] Ye Y., “Interior Point Algorithms for Quadratic Programming”, Paper Series No. 89-29, Dept. of Management Sciences, University of Iowa, Iowa City, (1988).
[74] Victor M. Zavala, Antonio Flores-Tlacuahuac and Eduardo Vivaldo-Lima, Dynamic optimization of a Semi-Batch Reactor for Polyurethane Production, Chemical Engineering Science, 60, p. 3061 (2005).
[75] Zeybek Z., Yüce S., Hapolu H., Alpbaz M., Adaptive Heuristic Temperature Control of a Batch Polymerisation Reactor, Chemical Engineering and Processing, 43(7), p. 911 (2004).
[76] Vieira R.A.M., Embiruçu M., Sayer C., Pinto J.C., Lima E.L., Control Strategies for Complex Chemical Processes. Applications in Polymerization Processes, Computers & Chemical Engineering, 27(8-9), p. 1307 (2003).
[77] Zhihua Xiong, Jie Zhang, Modelling and Optimal Control of Fed-Batch Processes Using a Novel Control Affine Feed Forward Neural Network, Neurocomputing, 61, p. 317 (2004).
[78] Yuan Tian, Jie Zhang, Julian Morris, Optimal Control of a Batch Emulsion Copolymerisation Reactor Based on Recurrent Neural Network Models, Chemical Engineering and Processing, 41(6), p. 531 (2002).
[79] Yaohui [Reference to Lu], Yaman, Quasi-Min-Max MPC Algorithms for LPV Systems, Automatica, 36(4), p. 527 (2000).