Kinetic Parameters Estimation using Vehicle Data for Exhaust Aftertreatment Devices

Similar documents
Three Way Catalyst and Lean NO x Trap Modeling for a Lean Burn SIDI Gasoline engine

Kinetic Parameter Identification for a DOC Catalyst Using SGB test and Advanced Optimization Algorithms

Emissions Catalyst Design using GT-SUITE. Dr. Chaitanya Sampara Mr. Dominik Artukovic

AUTOMOTIVE EXHAUST AFTERTREATMENT

Emissions Catalyst Design using GT-SUITE. Dr. Chaitanya Sampara Viridis Chemicals Private Limited

2011 DOE Crosscut Workshop on Lean Emissions Reduction Simulation April 2011 Dearborn, MI

ONE-DIMENSIONAL HIGH-FIDELITY AND REDUCED-ORDER MODELS FOR THREE- WAY CATALYTIC CONVERTER

Zeolite HC Traps: Experiments and Simulations

Correlation between LNT NH 3 and N 2 O selectivities under fast cycling conditions

A new transient CLEERS SCR protocol

Three-Way Catalytic Converter Modeling as a Modern Engineering Design Tool

The impacts of Pdin BEA zeolite on decreasing cold start HC emission of an E85 vehicle

Overview of LNT Modeling Approaches

Author Index. See for options on how to legitimately share published articles. Affiliation Index.

A mini review on the chemistry and catalysis of the water gas shift reaction

1D Simulation Modeling of SCR Catalyst at Steady State Condition

Understanding NH 3 emissions over a three-way catalyst in lean/rich conditions.

Combinatorial Heterogeneous Catalysis

Oxidative Coupling of Methane

Predicting the Effect of Catalyst Axial Active Site Distributions on a Diesel Oxidation Catalyst Performance

Simulation of Selective Catalytic Reduction using DARS 1D Tool

Identification of catalytic converter kinetic model using a genetic algorithm approach

Nonlinear dynamics of three-way catalyst with microkinetics and internal diffusion

Kinetics of the Fischer-Tropsch Reaction over a Ru- Promoted Co/Al 2 o 3 Catalyst

Model-based analysis of TWCcoated filters performance aspects

INTRODUCTION TO CATALYTIC COMBUSTION

Department of Chemical and Petroleum Engineering Sharif University of Technology, Iran

Preventing Thermal Runaways of LENR Reactors. Jacques Ruer sfsnmc

Microkinetic Modeling and Analysis of Ethanol Partial Oxidation and Reforming Reaction Pathways on Platinum at Short Contact Times

Fuel Cell Activities in MME Waterloo

Development and Validation of a multi-site kinetic model for NH 3 -SCR over Cu-SSZ-13. Rohil Daya Isuzu Technical Center of America

DARS overview, IISc Bangalore 18/03/2014

DETAILED DYNAMIC MODELING OF AUTO-THERMAL GASOLINE FUEL-PROCESSORS

A SCR Model based on Reactor and Engine Experimental Studies for a Cu-zeolite Catalyst

Objective: To Evaluate Predictions of Alternative Models

Experimental and kinetic studies of H 2 effect on lean exhaust aftertreatment processes: HC-SCR and DOC

LIST OF ABBREVIATIONS:

The Development and Application of an Evolutionary Algorithm for the Determination of Kinetic Parameters in Automotive Aftertreatment Models

Methane Oxidation Reactions

Examination paper for TKP 4155 / KP 8903 REACTION KINETICS AND CATALYSIS

By Rogéria Amaral and Sébastien Thomas

GPC 2001 GLOBAL POWERTRAIN CONGRESS:

Experimental and modeling study of the pyrolysis and combustion of dimethoxymethane

Water-Gas Shift Kinetics over Iron Oxide Catalysts at Membrane Reactor Conditions

Simulation of Engine Exhaust Aftertreatment with CFD using Detailed Chemistry

3. DIFFERENT MODEL TYPES

THE ROLE OF SENSITIVITY ANALYSIS IN MODEL IMPROVEMENT

Identification of Catalytic Converter Kinetic Model Using a Genetic Algorithm Approach

Kinetic Modeling of C3H6 Inhibition on NO Oxidation over Pt Catalyst

STRATEGIES FOR THE ENHANCEMENT OF LOW- TEMPERATURE CATALYTIC OXIDATION OF METHANE EMISSIONS

RISE TIME EVALUATION OF THE HEAT FLUX MICROSENSOR (HFM) ON A HOT- AIR-GUN TEST RIG

Apportioning of Fuel and Thermal NO x

Available online at ScienceDirect. IFAC-PapersOnLine (2015)

International Journal of Scientific Research and Innovative Technology ISSN: Vol. 4 No. 4; April CO Oxidation.

Review for Final Exam. 1ChE Reactive Process Engineering

The Low Temperature Conversion of Methane to Methanol on CeO x /Cu 2 O catalysts: Water Controlled Activation of the C H Bond

TRITIUM RECOVERY FROM WASTE USING A PALLADIUM MEMBRANE REACTOR

UQ in Reacting Flows

Student Laboratory Module: The Kinetics of NH 3 Cracking. Jason C. Ganley 23 September

HYDROGEN PRODUCTION THROUGH SORPTION ENHANCED REFORMING

CHE 611 Advanced Chemical Reaction Engineering

Reduced Order Model Design for Three Way Catalytic Converters

Be prepared to discuss the quantitative comparison method in the oral exam.

Global kinetic modelling of the reaction of soot with NO x and O 2 on Fe 2 O 3 catalyst

SCR. Current progress in Simulation of AdBlue Spray Preparation. Carsten Schmalhorst. AVL ITS Europe

CHEMICAL KINETICS. Collision theory and concepts, activation energy and its importance VERY SHORT ANSWER QUESTIONS

Structure-Function Studies. in Heterogeneous Catalysis

Chapter 14 Chemical Kinetics

Worldwide Pollution Control Association

Part One: Reaction Rates. 1. Even though a reaction is thermodynamically favorable it may not occur at all if it is kinetically very slow.

Rocket Propulsion. Combustion chamber Throat Nozzle

MICRO SOLID OXIDE FUEL CELL ON THE CHIP

Towards a fully LED-based solar simulator - spectral mismatch considerations

PART I Fundamentals COPYRIGHTED MATERIAL

20.1 Xenon Production Xe-135 is produced directly in only 0.3% of all U-235 fissions. The following example is typical:

Chemical Kinetics and Equilibrium

In-Situ Differential Scanning Calorimetry in the Studies of Oxide Catalysts and Mechanisms in Oxidative Heterogeneous Catalysis

EVALUATION OF ATMOSPHERIC PROCESSES FOR OZONE FORMATION FROM VEHICLE EMISSIONS

Application of Environmental Technology Management. (ETM) to Automobile Exhaust Emission Reduction. Meshari AL-Harbi

The Seeding of Methane Oxidation

Introduction. Mathematical model and experimental

Hydrocarbon Storage Simulation in Rhodium Software and Validation via Reactor Testing

Oxygen Reduction Reaction

An Introduction to Chemical Kinetics

To increase the concentration of product formed in a PFR, what should we do?

The Combination of Detailed Kinetics and CFD in Automotive Applications

6.111 Lecture # 12. Binary arithmetic: most operations are familiar Each place in a binary number has value 2 n

5. Collection and Analysis of. Rate Data

Combustion Theory and Applications in CFD

10/2/2008. hc λ. νλ =c. proportional to frequency. Energy is inversely proportional to wavelength And is directly proportional to wavenumber

DARS Digital Analysis of Reactive Systems

Synthesis gas production via the biogas reforming reaction over Ni/MgO-Al 2 O 3 and Ni/CaO-Al 2 O 3 catalysts

DESIGN AND CONTROL OF BUTYL ACRYLATE REACTIVE DISTILLATION COLUMN SYSTEM. I-Lung Chien and Kai-Luen Zeng

1. Why are chemical reactions important to energy, environmental and process engineering? Name as many reasons as you can think of.

Thermoacoustic Instabilities Research

High Pressure DSC Differential Scanning Calorimeter

How sulphur really forms on the catalyst surface

SCR-Catalyst Materials for Exhaust Gas Detection D. Schönauer-Kamin, R. Moos

Method and process for combustion synthesized supported cobalt catalysts for fixed bed Fischer Tropsch reaction

Affiliation Index. Subject Index

Transcription:

Kinetic Parameters Estimation using Vehicle Data for Exhaust Aftertreatment Devices Karthik Ramanathan India Science Lab General Motors, Global Research and Development Center Bangalore, India Acknowledgments: Chander Sharma, Wei Li, Dave Belton, Dave Radke, Michael Keat, Jeremey Tassone

Kinetic modeling for exhaust AT system Obtaining the right reaction mechanisms, rate expressions and rate constants. Necessary for improved predictability of the model. Kinetic Models Microkinetic models (fundamental) Developed based on elementary surface reaction steps (e.g., adsorption, desorption, dissociation, surface reaction, etc) Change in rate-controlling step captured automatically. interaction among competing reactions/species accounted for naturally Computationally intensive, takes a lot of time to develop, too many parameters Global kinetics (semi-emprical) Semi-empirical form of rate expressions (e.g., Langmuir-Hinshelwood) postulated based on mechanistic hypotheses Takes into account inhibition by other species Inhibition terms can be PGM-dependent i.e., Rh and Pt can have different inhibition terms. Reasonable predictive capabilities Helps in rapid design evaluations and control algorithms Kinetic parameters estimated by fitting to experimental data 2

Kinetic model development and usage Lab Reactor Experiments MODEL CALIBRATION Lab Reactor Model Reaction Mechanisms, Rate Expressions, Kinetic Parameters LAB REACTOR EXPERIMENTS Synthetic gas mixtures Better reproducibility Controlled experiments Easy to separate effects of many reactions. VEHICLE TESTS Highly transient More species in the exhaust More uncertainties Engine Tests MODEL VALIDATION Prediction of Behavior on Vehicle AT Converter Model 3

Lack of portability of Kinetic models: Lab to Vehicle Kinetic parameters are very sensitive to washcoat and catalyst formulations Kinetic parameters are very sensitive to catalyst aging Aging protocols (lab-scale, road-aged) Difficult to get same levels of aging Activity as a function of length Reaction path could depend on species that are present in real exhaust but not present in synthetic exhaust Hydrocarbons (different C-numbers) CO 2, H 2 O (can play promoting and inhibiting roles) Kinetic parameters are very sensitive to feed compositions/temperature Transient, engine type, load, speed, outdoor temperatures, drive-cycle, fuel type and additives. Need to validate/tune the kinetic mechanism/parameters using vehicle data. 4

Kinetic model development and usage Lab Reactor Experiments MODEL CALIBRATION Lab Reactor Model Reaction Mechanisms, Rate Expressions, Kinetic Parameters MODEL VALIDATION Prediction of Behavior on Vehicle Engine Tests AT Converter Model MODEL FINE- TUNING AT Converter Model Fine tuned Kinetic Parameters 5

Kinetic Parameter Estimation from Vehicle Data Illustration through Three-Way Catalyst as an example using 1D model Three-Way Catalyst Chemistry and Kinetics Reaction rates expressions Turn-over numbers (mol/mol-site/sec) Oxidation, reduction, SR and WGS reactions S. No. Reactions Oxidation Reactions 1 CO + 0.5O 2 CO 2 2 C 3 H 6 + 4.5O 2 3CO 2 + 3H 2 O 3 C 3 H 8 + 5O 2 3CO 2 + 4H 2 O 4 H 2 + 0.5O 2 H 2 O NO Reduction Reactions 5 CO + NO CO 2 + 0.5 N 2 6 C 3 H 6 + 9NO 3CO 2 + 3H 2 O + 4.5N 2 7 H 2 + NO H 2 O + 0.5N 2 Water-Gas and Steam Reforming Reaction 8 CO + H 2 O CO 2 + H 2 Ceria Reactions: 9 C 3 H 6 + 3H 2 O 3CO + 6H 2 Ceria Reactions (Oxygen Storage) 10 2Ce 2 O 3 + O 2 4CeO 2 11 Ce 2 O 3 + NO 2CeO 2 + 0.5N 2 Estimate pre-exponentials and activation energies 12 CO + 2CeO 2 Ce 2 O 3 + CO 2 13 C 3 H 6 + 12CeO 2 6Ce 2 O 3 + 3CO + 3H 2 O 14 C 3 H 8 + 14CeO 2 7Ce 2 O 3 + 3CO + 4H 2 O 15 H 2 + 2CeO 2 Ce 2 O 3 + H 2 O 6

Vehicle data Six engine/vehicle experiments from GM powertrain Dataset detail, and Drive cycle Abbreviation Used for Data set 1, FTP cycle Set 1 Calibration Data set 2, FTP cycle Set 2 Calibration Data set 3, FTP cycle Set 3 Calibration Data set 4, FTP cycle Set 4 Calibration Data set 5, FTP cycle Set 5 Validation Data set 6, NUDC cycle Set 6 Validation All datasets trying to meet Bin5 emission standard or similar. 4 used for calibration and 2 for validation 5 of them on FTP cycle, 1 on NUDC All TWC were CC, 100k or more aged, very similar catalyst formulations (amount of PGM different) Active site density (mole-site/m 3 ) calculated from PGM loading and dispersion Different length, frontal area, CPSI, substrate thickness, PGM loading 7

Vehicle Data Quality Lack of synchronization between EO and TP data. Time alignment and absolute value measured Out of phase 8

Kinetic Parameter Estimation methodology Objective: Predict the first drive cycle (125s or so) using 1D model Estimate parameters through optimization to minimize error between measured and simulated data Combination of evolutionary/exploratory and local optimization methods. (isight) - Pointer Automatic Optimizer (PAO) 9

Choosing the data points for optimization Key to any successful parameter estimation Only include data points that are sensitive to the parameters that are being estimated Trying to estimate kinetic parameters when the data is obtained at very slow or very fast kinetics would be ineffective. Define conversion efficiency to automatically identify the data points for inclusion/exclusion Based on cumulative emissions Engine Out TP out Identify time instant after which conversion efficiency does not go below zero (or 10%). 10

Choosing the objective function Need to predict the entire time-dependent emission profile and NOT just the final value. Norm of the relative errors between cumulative predicted and measured TP out emissions Cumulative values show better sensitivity (than instantaneous values) to the kinetic parameters Automatically has more weight to light-off, and avoids problems with 100% conversion Individual objective functions for species Increased efficiency, helps in getting sensitivity information Objective functions are scaled for number of data points for each species and normalized for each species [each and every value contributed to the objective function is of O(1)] 11

Evolution of estimated kinetic parameters Predicting light-off: WGS and SR not included in optimization Base kinetics from controlled laboratory experiments and literature Estimating only the pre-exponentials Slowly increasing the complexity of the optimization Only CO and HC in objective functions Assuming values for certain parameters (relaxed later) Including inhibition terms Expanding the lower and upper bounds as necessary Reaction kinetics A1 A2 A3 A4 Optimization Pointer Automatic Optimizer Same as A1 Same as A1 Manual tuning Algorithm Total: 17 Optimization Parameters Same as A1 -- Initial values Base kinetics A1 A2 A3 Objective function include CO and HC (Single objective function) CO, HC, and NO (Single objective function) CO,HC and NO (Three different objective functions, one each for CO, HC and NO) -- Datasets used Set 1, 2, 3, 4 Same as A1 Same as A1 Set 1 Comments Good match for CO and HC. NO predictions are off Improvements in NO predictions but low sensitivity for CO and HC oxidation reactions. Improved predictions for HC and NO but more sensitivity towards Ceria reactions Right sensitivities with good match for CO, HC and NO 12

Model Calibration Results (Dataset-2) 13

Model Calibration Results (Dataset-1) 14

% Error % Error Model Calibration (%) Error at 125s 160 Dataset-1 120 Dataset-1 140 100 120 100 80 60 40 20 0 350 300 250 200 150 CO HC NO Dataset-3 % Error % Error 80 Base Kinetics Kinetics A1 60 Kinetics A2 Kinetics A3 Kinetics 40 A4 20 0 350 300 250 Base Kinetics 200 Kinetics A1 Kinetics A2 Kinetics 150 A3 Kinetics A4 CO HC NO Base Kinetics Kinetics A1 Kinetics A2 Kinetics A3 Kinetics A4 Dataset-4 B K K K K 100 100 50 50 0 CO HC NO 0 CO HC NO HC NO 15

Model Prediction (Dataset-5) 16

Summary Kinetics obtained from laboratory experiments do not translate directly for predicting vehicle data. Kinetic modeling at the vehicle level needed to predict vehicle data Prediction of time-dependent cumulative emissions (rather than emissions at a given time instant) is critical Choice of data points, objective functions, parameters, methods of optimization crucial for successful optimization (/ parameter estimation) Calibrated model able to predict light-off for TWC applications reasonably well. Model was further fine-tuned for lean-gasoline applications Model calibration for SULEV emission standards more challenging Quality of experimental data becomes very critical. Model is only as good as the experimental data. 17

Key Points 1 Choice of parameters Choose all the unknown parameters. Estimated parameters are only as good as uncertain (known) parameters. Chosen parameters should have good sensitivity to the measured outputs. Choice of Experiments and Model Right experiments: Transient/Steady-State Parameters to be estimated should have a good sensitivity on the measured outputs Model should describe the experimental condition well. Choice of 1D, 2D, 3D Inclusion/Exclusion of heat loss, flow effects 18

Key Points 2 Choice of Objective function Log-based (log of simulated/measured), sum of squares of the difference (simulated-measured) Important to pick a objective function that shows sufficient sensitivity to the parameters that are being estimated. Separate objective functions can help in sensitivity analysis Weighting the objective function More weight to reliable data points Scaling the objective function Important to get all the outputs scaled to same order of magnitude (concentrations, temperature) With number of data-points Exclusion of inappropriate data that are insensitive to the parameters and exclusion of inaccurate experimental data. 19

Key Points 3 Choice of Optimization methods/algorithm Exploratory and/or local optimization methods Pointer Automatic Optimizer (isight) Parameter Estimation Process Initial guess crucial for local methods Physical bound and constraints for the parameters Smaller the space (narrow bounds), less the time for optimization Flexible to relax the bounds Scale the parameters O(1) Estimating the right parameters from the right data Increase the complexity systematically Start with fewer parameter (most dominant ones) Local sensitivity analysis can help determine the dominant parameters. 20

Key Points 4 Runtime, Analysis and other factors When using isight, start with all unknown (and uncertain) parameters Helps in creating a database, which can be later used for analysis. Computational time for each simulation (and objective function calculation) and the time available for optimization process can help in deciding the optimization method (local or exploratory or mix of the two) Failures in the numerical code Penalty for failure runs Split the available data into two buckets one for calibration and one for validation Analyze the optimization results Sensitivity to certain parameters Relaxing the bounds (some parameters hitting the bounds) Use values from previous optimization runs as initial guesses. 21