Parameter estimation in heterogeneous catalysis

The detailed modelling of heterogeneous catalytic systems is challenging due to the unknown nature of new catalytic materials as well as the often required transient nature of the resulting models. Thus, this thesis deals with the methodologies involved in the kinetic modelling of heterogeneous catalysis and in particular NOx reduction systems. The methods presented increase the understanding of the interplay between model parameters and also decrease the number of necessary laboratory experiments. The effect of more efficient parameter estimation methods should result in faster model development which is required in any process development but especially for catalytic emission control. In the first paper, injection parameters for an engine rig with a NOx Storage and Reduction (NSR) system were optimised using different experimental designs at different load points. The optimised settings were used as a map for a control strategy complying with a European Transient Cycle (ETC). In the second paper, we developed a method that copes with the large number of unknown model parameters by applying a Latent Variable (LV) model to the Jacobian matrix in the fitting procedure. The LV model results in a low-dimensional approximation of the Jacobian with reduced parameter correlation and enables improved efficiency in parameter estimation. In the third paper, Experimental design for precise parameter estimation was performed in a batch-sequential way using D-optimality as the objective function. A screening methodology similar to that used for drug discovery in the pharmaceutical industry was applied for a large number of simulated candidate experiments. By applying an LV model to the Jacobian of all these experiments, a reduced parameter correlation was obtained and the number of necessary experiments was reduced. The results from the second and third paper pinpoint a number of benefits of using LV models including: 1) the determination of the effective rank, i.e. the number of independent phenomena present in the data at hand, 2) the analysis of the correlation structure which is useful in the parameter assessment and 3) the linear approximation in few dimensions enables more efficient computations. In the fourth paper, a detailed model for the Selective Catalytic Reduction of NOx using Hydrocarbon as a reducing agent (HC-SCR) over silver alumina (Ag-Al2O3) was developed. By applying an experimental design to the steady state levels and also selecting the run order, improved fitting properties were obtained due to the increased parameter sensitivity enabled by the transient experiments. This thesis also contains a description of the modelling techniques and challenges encountered during this thesis project. An assessment of the importance as well as the parameter correlation is given. This demonstrates the intimate interplay between model assumptions and the stipulated model parameters and exemplifies a thorough assessment of the whole modelling chain from initial experiments to model validation.

[1]  Pio Forzatti,et al.  Adequacy of lumped parameter models for SCR reactors with monolith structure , 1992 .

[2]  Thomas F. Coleman,et al.  A Preconditioned Conjugate Gradient Approach to Linear Equality Constrained Minimization , 2001, Comput. Optim. Appl..

[3]  J. Sjöblom,et al.  Modeling mass transport with microkinetics in monolithic NOx storage and reduction catalyst , 2007 .

[4]  M. J. H. van't Hoff,et al.  Etudes de dynamique chimique , 2010 .

[5]  Sandro Macchietto,et al.  Model-based design of experiments for parameter precision: State of the art , 2008 .

[6]  Young K. Park,et al.  A GENERALIZED APPROACH FOR PREDICTING COVERAGE-DEPENDENT REACTION PARAMETERS OF COMPLEX SURFACE REACTIONS : APPLICATION TO H2 OXIDATION OVER PLATINUM , 1999 .

[7]  John R. Kitchin,et al.  The Role of Adsorbate–Adsorbate Interactions in the Rate Controlling Step and the Most Abundant Reaction Intermediate of NH3 Decomposition on Ru , 2004 .

[8]  George E. P. Box,et al.  SEQUENTIAL DESIGN OF EXPERIMENTS FOR NONLINEAR MODELS. , 1963 .

[9]  T. Lundstedt,et al.  Experimental design and optimization , 1998 .

[10]  Flavio Manenti,et al.  Kinetic models analysis , 2009 .

[11]  Hong He,et al.  Review of Ag/Al2O3-Reductant System in the Selective Catalytic Reduction of NOx , 2008 .

[12]  T. Miyadera Alumina-supported silver catalysts for the selective reduction of nitric oxide with propene and oxygen-containing organic compounds , 1993 .

[13]  J. Pérez‐Ramírez,et al.  Evolution, achievements, and perspectives of the TAP technique , 2007 .

[14]  O. Levenspiel Chemical Reaction Engineering , 1972 .

[15]  G. Yablonskii,et al.  Moment-Based Analysis of Transient Response Catalytic Studies (TAP Experiment) , 1998 .

[16]  Alison J. Burnham,et al.  Frameworks for latent variable multivariate regression , 1996 .

[17]  E. Barrett,et al.  The Determination of Pore Volume and Area Distributions in Porous Substances. II. Comparison between Nitrogen Isotherm and Mercury Porosimeter Methods , 1951 .

[18]  Alison J. Burnham,et al.  LATENT VARIABLE MULTIVARIATE REGRESSION MODELING , 1999 .

[19]  Peter P. Valko,et al.  Principal component analysis of kinetic models , 1985 .

[20]  K. Papadakis,et al.  Development of a dosing strategy for a heavy-duty diesel exhaust cleaning system based on NOX storage and reduction technology by Design of Experiments , 2007 .

[21]  Paul J. Lewi From data to knowledge to more data. Where is the portal to progress , 2004 .

[22]  Yves Schuurman,et al.  Dynamic methods for catalytic kinetics , 2008 .

[23]  André Bardow,et al.  Optimal experimental design of ill-posed problems: The METER approach , 2008, Comput. Chem. Eng..

[24]  Raquel Prado,et al.  Introduction to Design of Experiments , 2008 .

[25]  Azael Fabregat,et al.  Nonlinear kinetic parameter estimation using simulated annealing , 2002 .

[26]  C. Hardacre,et al.  A fast transient kinetic study of the effect of H2 on the selective catalytic reduction of NOx with octane using isotopically labelled 15NO , 2007 .

[27]  H. L. Lucas,et al.  DESIGN OF EXPERIMENTS IN NON-LINEAR SITUATIONS , 1959 .

[28]  Dionisios G. Vlachos,et al.  Is the water–gas shift reaction on Pt simple?: Computer-aided microkinetic model reduction, lumped rate expression, and rate-determining step , 2005 .

[29]  John F. MacGregor,et al.  ASQC Chemical Division Technical Conference 1971 Prize Winning Paper Some Problems Associated with the Analysis of Multiresponse Data , 1973 .

[30]  M. Tagliabue,et al.  Multivariate approach to zeolite synthesis , 2003 .

[31]  Erik Fridell,et al.  NOx storage on BaO(100) surface from first principles: a two channel scenario , 2002 .

[32]  Karl Pearson F.R.S. LIII. On lines and planes of closest fit to systems of points in space , 1901 .

[33]  Petr Kočí,et al.  Modelling of micro/nano-scale concentration and temperature gradients in porous supported catalysts , 2007 .

[34]  H. S. Fogler,et al.  Elements of Chemical Reaction Engineering , 1986 .

[35]  W. Maier,et al.  Strategies for the discovery of new catalysts with combinatorial chemistry , 2004 .

[36]  Markus Kögel,et al.  Phenomenological Studies on the Storage and Regeneration Process of NOx Storage Catalysts for Gasoline Lean Burn Applications , 2002 .

[37]  Hai Wang,et al.  Thermodynamic consistency in microkinetic development of surface reaction mechanisms , 2003 .

[38]  Michel Cabassud,et al.  Sequential Experimental Design Strategy for Rapid Kinetic Modeling of Chemical Synthesis , 2005 .

[39]  D. Vlachos,et al.  Parameter Optimization of Molecular Models: Application to Surface Kinetics , 2003 .

[40]  Hai Wang,et al.  A new approach to response surface development for detailed gas‐phase and surface reaction kinetic model optimization , 2003 .

[41]  Charles N. Satterfield,et al.  Heterogeneous catalysis in practice , 1980 .

[42]  Petr Zamostny,et al.  Identification of kinetic models of heterogeneously catalyzed reactions , 2002 .

[43]  Thomas F. Coleman,et al.  A Subspace, Interior, and Conjugate Gradient Method for Large-Scale Bound-Constrained Minimization Problems , 1999, SIAM J. Sci. Comput..

[44]  Douglas M. Bates,et al.  Nonlinear Regression Analysis and Its Applications , 1988 .

[45]  R. Gorte Temperature-programmed desorption for the characterization of oxide catalysts , 1996 .

[46]  Gregory Stephanopoulos Chemical and Biological Engineering , 2003 .

[47]  J. Hansen,et al.  Defusing the global warming time bomb. , 2004, Scientific American.

[48]  Svante Wold,et al.  The utility of multivariate design in PLS modeling , 2004 .

[49]  Ing-Marie Olsson,et al.  Controlling coverage of D‐optimal onion designs and selections , 2004 .

[50]  Eric Walter,et al.  Qualitative and quantitative experiment design for phenomenological models - A survey , 1990, Autom..

[51]  Anna Granly Hansen,et al.  Microkinetic modeling as a tool in catalyst discovery , 2007 .

[52]  E. Abbott Flatland: A Romance of Many Dimensions , 1884 .

[53]  Tamás Turányi,et al.  Reaction rate analysis of complex kinetic systems , 1989 .

[54]  C. D. Gelatt,et al.  Optimization by Simulated Annealing , 1983, Science.

[55]  E. Fridell,et al.  A kinetic study of oxygen adsorption/desorption and NO oxidation over Pt/Al2O3 catalysts , 1999 .

[56]  Ken-ichi Shimizu,et al.  Selective catalytic reduction of NO over supported silver catalysts--practical and mechanistic aspects. , 2006, Physical chemistry chemical physics : PCCP.

[57]  Stoltze,et al.  Bridging the "pressure gap" between ultrahigh-vacuum surface physics and high-pressure catalysis. , 1985, Physical review letters.

[58]  V. Zhdanov,et al.  Role of steps in the NO–CO reaction on the (111) surface of noble metals , 2003 .

[59]  David W. Bacon,et al.  Prospects for reducing correlations among parameter estimates in kinetic models , 1978 .

[60]  George Stephanopoulos,et al.  Valid parameter range analyses for chemical reaction kinetic models , 2002 .

[61]  R. Schlögl,et al.  Bridging the pressure and material gap in heterogeneous catalysis. , 2007, Physical chemistry chemical physics : PCCP.

[62]  Jonas Jansson Studies of Catalytic Low-Temperature CO Oxidation over Cobalt Oxide and Related Transition Metal Oxides , 2002 .

[63]  Gerhard Emig,et al.  Sequential experimental design procedures for precise parameter estimation in ordinary differential equations , 1975 .

[64]  M. J. Box Some Experiences with a Nonlinear Experimental Design Criterion , 1970 .

[65]  R. Burch,et al.  A review of the effect of the addition of hydrogen in the selective catalytic reduction of NOx with hydrocarbons on silver catalysts , 2006 .

[66]  J. Goodwin,et al.  Characterization of Catalytic Surfaces by Isotopic-Transient Kinetics during Steady-State Reaction , 1995 .

[67]  D. Murzin,et al.  Kinetic considerations of H2 assisted hydrocarbon selective catalytic reduction of NO over Ag/Al2O3: I. Kinetic behaviour , 2006 .

[68]  John H. Kalivas Optimization using variations of simulated annealing , 1992 .

[69]  Experimental study of mass transfer limited reaction—Part I: Use of fibre optic spectrometry to infer asymmetric mass transfer coefficients , 2005 .

[70]  R. Fricke,et al.  Unusual Activity Enhancement of NO Conversion over Ag/Al2O3 by Using a Mixed NH3/H2 Reductant Under Lean Conditions , 2004 .

[71]  C. Campbell,et al.  Microkinetic modeling of ethylene oxidation over silver , 2004 .

[72]  Per Stoltze Microkinetic simulation of catalytic reactions , 2000 .

[73]  K. Shimizu,et al.  Silver-alumina catalysts for selective reduction of NO by higher hydrocarbons: structure of active sites and reaction mechanism , 2001 .

[74]  Dionisios G. Vlachos,et al.  Hierarchical, multiscale surface reaction mechanism development: CO and H2 oxidation, water–gas shift, and preferential oxidation of CO on Rh , 2005 .

[75]  Thomas F. Coleman,et al.  An Interior Trust Region Approach for Nonlinear Minimization Subject to Bounds , 1993, SIAM J. Optim..

[76]  W. Marquardt Special Issue: model-based experimental analysis , 2008 .

[77]  Ing-Marie Olsson,et al.  D-optimal onion designs in statistical molecular design , 2004 .

[78]  P. Glarborg,et al.  The thermal DeNOx process: Influence of partial pressures and temperature , 1995 .

[79]  K. Routray,et al.  Kinetic parameter estimation for a multiresponse nonlinear reaction model , 2005 .

[80]  Roberto C. Dante,et al.  Fractional factorial design of experiments for PEM fuel cell performances improvement , 2003 .

[81]  M. Skoglundh,et al.  Ag–Al2O3 catalysts for lean NOx reduction—Influence of preparation method and reductant , 2009 .

[82]  Sandro Macchietto,et al.  Novel anticorrelation criteria for model‐based experiment design: Theory and formulations , 2008 .

[83]  P. A. Barnes,et al.  A new approach to the statistical optimisation of catalyst preparation , 1992 .

[84]  F. Thyrion,et al.  Kinetic study of oxidative dehydrogenation of propane over Ni-Co molybdate catalyst , 2003 .

[85]  Jae-Soon Choi,et al.  Spatially resolved in situ measurements of transient species breakthrough during cyclic, low-temperature regeneration of a monolithic Pt/K/Al2O3 NOx storage-reduction catalyst , 2005 .

[86]  G. Bond The Use of Kinetics in Evaluating Mechanisms in Heterogeneous Catalysis , 2008 .

[87]  Constantinos Theodoropoulos,et al.  An Input/Output Model Reduction-Based Optimization Scheme for Large-Scale Systems , 2005, Multiscale Model. Simul..

[88]  J. Ross,et al.  Mechanistic differences in the selective reduction of NO by propene over cobalt- and silver-promoted alumina catalysts: kinetic and in situ DRIFTS study , 2000 .

[89]  W. G. Hunter,et al.  The Experimental Study of Physical Mechanisms , 1965 .

[90]  C. Ekberg,et al.  Assessment of uncertainty in parameter evaluation and prediction. , 2000, Talanta.

[91]  D. Duprez,et al.  A model of oxygen transport in Pt/ceria catalysts from isotope exchange , 1999 .

[92]  Michael P. Harold,et al.  NOX storage and reduction on a Pt/BaO/alumina monolithic storage catalyst , 2004 .

[93]  A. Hellman,et al.  Activation of Al2O3 by a long-ranged chemical bond mechanism. , 2008, Physical review letters.

[94]  H. Grönbeck,et al.  Identifying surface species by vibrational spectroscopy: Bridging vs monodentate nitrates , 2008 .

[95]  S. Arrhenius Über die Reaktionsgeschwindigkeit bei der Inversion von Rohrzucker durch Säuren , 1889 .

[96]  D. Hâncu,et al.  Microkinetic modeling for hydrocarbon (HC)-based selective catalytic reduction (SCR) of NOx on a silver-based catalyst , 2009 .

[97]  Dale F. Rudd,et al.  The Microkinetics of heterogeneous catalysis , 1993 .

[98]  D. Himmelblau,et al.  Optimization of Chemical Processes , 1987 .

[99]  E. Fridell,et al.  NOx storage on BaO: theory and experiment , 2004 .

[100]  Jennifer S. Holmgren,et al.  Strategies and applications of combinatorial methods and high throughput screening to the discovery of non-noble metal catalyst , 2004 .

[101]  D. Chatterjee,et al.  Development and application of a model for a NOx storage and reduction catalyst , 2007 .

[102]  Erik Fridell,et al.  Mean field modelling of NOx storage on Pt/BaO/Al2O3 , 2002 .