Preliminary Program subject to change
20027 Computational Fluid Dynamics in Chemical Reaction Engineering
OverviewThis session is devoted to the application and development of computational fluid dynamics for reacting systems.
Primary SponsorCatalysis and Reaction Engineering Division (20)
Co-Sponsor(s)North American Mixing Forum (06)

Chair

Anthony G. Dixon
Professor
Worcester Polytechnic Institute
100 Institute Road
Worcester, MA 01609
Phone Number: (508) 831-5350
Fax Number: (508) 831-5853
Email: agdixon@wpi.edu

CoChair

Nitin H. Kolhapure
DuPont Engineering Research and Technology
1007 Market St
Wilmington, DE 19898
Phone Number: 302-774-2282
Fax Number: 302-774-2457
Email: nitin.h.kolhapure@usa.dupont.com
Welcoming Remarks
Multi-Environment Probability Density Function Method for Modeling Turbulent Combustion Using Detailed Chemistry
Qing Tang1, Wei Zhao1, Mike Bockelie1 and Rodney O. Fox2, (1)Reaction Engineering International, 77 West 200 South, Suite 210, Salt Lake City, UT 84101, (2)Iowa State University, 2114 Sweeney Hall, Ames, IA 50011-2230
Modeling Coupled Reactive Flow and Evaporation within a Multistage Reactor
Hua Bai1, Debashis Chakraborty1, Daniel Trauth1, Genong Li2 and Aseem Jain2, (1)The Dow Chemical Company, 2301 Brazosport Blvd. B1225, Freeport, TX 77541, (2)Fluent Inc., 10 Cavendish Court, Lebanon, NH 03766
Comparison of a Fully Coupled and a Decoupled Solver for the Simulation of Fluid Catalytic Cracking
Edward Baudrez1, Juray De Wilde2, Geraldine J. Heynderickx1 and Guy B. Marin1, (1)Chemische Proceskunde en Technische Chemie, Universiteit Gent, Laboratorium voor Petrochemische Techniek, Krijgslaan 281, S5, Gent, 9000, Belgium, (2)Materials and Process Engineering Department, Université Catholique de Louvain, Bâtiment Réaumur, Place Sainte Barbe, 2, Louvain-la-Neuve, 1348, Belgium
Cfd Modeling of a Fixed Bed Reactor for Strongly Endothermic Reactions
M. Ertan Taskin1, Anthony G. Dixon1 and Hugh Stitt2, (1)Chemical Engineering, Worcester Polytechnic Institute, 100 Institute Road, Worcester, MA 01609, (2)Johnson Matthey Catalysts, PO Box 1, Billingham, Cleveland, TS23 1LB, United Kingdom
Pore-Scale Simulation of Transport Processes in Fixed-Beds: Combining a Lattice Boltzmann Cfd Method and a Particle Tracking Method
Hannsjörg Freund1, Jürgen Bauer2, Thomas Zeiser3 and Gerhard Emig2, (1)Physical and Chemical Process Engineering, Max Planck Institute for Dynamics of Complex Technical Systems, Sandtorstr. 1, Magdeburg, 39106, Germany, (2)Department of Chemical Reaction Engineering, University of Erlangen-Nuremberg, Egerlandstr. 3, Erlangen, 91058, Germany, (3)Regionales Rechenzentrum Erlangen, University of Erlangen-Nuremberg, Martensstr. 1, Erlangen, 91058, Germany
Cfd Modeling of Slurry Bubble Column Reactor for Fisher-Tropsch Synthesis
Andrey Troshko, Fluid Business Unit, ANSYS Inc., 10 Cavendish Court, Lebanon, NH 03766
Predicting Combustion in Packed Bed Reactor Using Udfs and Eulerian Model
Anhkien Le, Chemical and Process Engineering, The University of Sheffield, Mappin Street, Sheffield, S1 3JD, United Kingdom and Xuanhai Le, Faculty of Chemical Engineering, University of Technology, Vietnam National University Hochiminh City, 268 Ly Thuong Kiet St, District 10, Hochiminh, Vietnam
Concluding Remarks

Catalysis and Reaction Engineering Division