Presented by Micro-Mesoscopic Modeling of Heterogeneous Chemically Reacting Flows (MMMHCRF) Over Catalytic/Solid Surfaces Sreekanth Pannala Computing and.

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Presentation transcript:

Presented by Micro-Mesoscopic Modeling of Heterogeneous Chemically Reacting Flows (MMMHCRF) Over Catalytic/Solid Surfaces Sreekanth Pannala Computing and Computational Science Directorate Computer Science and Mathematics

2 Pannala_MM_0611 Goal Develop a multiphysics and multiscale mathematics framework for accurate modeling of heterogeneous reacting flows over catalytic surfaces

3 Pannala_MM_0611 Flow over a catalyst surface Lattice Boltzmann (LBM) Kinetic Monte Carlo (KMC)Density Functional Theory (DFT) Closely coupled Reaction barriers Figure adapted from Succi et al., 2001  Chemically reactive flow over a surface is a basic building block which is central to many energy-related applications  Illustrative benchmark to demonstrate the capability to integrate scales of several orders of magnitude QM: ~1 nm KMC: ~1  m LBM: ~1 mm

4 Pannala_MM_0611 Approach: KMC–LBM coupling through Compound Wavelet Matrix  Construct a CWM from LBM and KMC  Use CWM for coupling of mesoscopic and microscopic simulations in time and space  Use a Multiple Time Stepping (MTS) algorithm for higher order accuracy in time  Use fractal projection to map the surface topographical information to construct the KMC in one less dimension KMC contribution LBM contribution Compound Wavelet Matrix (CWM) x-yy y x x x Fractal projection Actual surface KMC LBM tviqiviqi viqiviqi T x

5 Pannala_MM_0611 Increasing spatial or temporal scales Homogenization at the level corresponding to LBM, feeding from KMC to LBM CWM methodology in work: Transferring information from KMC to LBM Micro-information KMC Homogenized properties at next scale Wavelet transformation Objective: Develop algorithms to construct projection operators and time integration methods to connect the microscale (e.g., KMC) and the mesoscale (e.g., LBM) The interactions between various physical processes at different scales are encapsulated by CWM and can be employed in control and design of reacting surfaces Time separation between methods and scales simplifies the problem The method recovers the mean field behavior in the macroscopic limit

6 Pannala_MM_0611 Recent results*  1D reaction/diffusion simulation performed at two different length and time scales  Fine (KMC and diffusion equation using finite difference at fine scale)  Coarse (analytical species solution and diffusion equation using finite difference at coarse scale)  Reconstructed the fine simulation results to reasonable accuracy using CWM at fraction of cost  Method allows for bi-directional transfer of information, i.e., upscaling and downscaling *Frantziskonis et al. (under review)

7 Pannala_MM_ *Frantziskonis et al. (under review) Recent results*  Successfully applied CWM strategy for coupling reaction/diffusion system  A very unique, rigorous, and powerful way to bridge temporal and spatial scales for multiphysics/multiscale simulations Transferring mean field Transferring fine-scale statistics Species concentration A(0k,t) Time, t Coarse Fine Time, t A(0k,t) Transferring mean field A(0k,t) Time, t CWM reconstruction

8 Pannala_MM_0611 Applications Chemical looping combustion (CLC)  Efficient, low-emissions and amenable to CO 2 sequestration SCOT (staged combustion with oxygen transfer)  CLC adapted for transportation Polyethylene production  Important process which uses ~10% of crude petroleum Reactive flows through fibrous media  Light-weight, low-cost and high- strength composites  Fuel cell components  Scaffolds for biomedical applications Coal gasification and combustion  New technologies for cleaner and efficient coal combustion  Fibrous substrate for discontinuous fiber substrate  The voids found by probing the substrate with a fixed-size sphere are denoted by spheres Schematic of burning of coal particle using laser heating in microgravity environment showing the various regimes of combustion [Adapted from Wendt et al., 2002] Coal particle radiation z  pp zz aa aa r a bb Gas phase Gas flow in the char Pyrolysis front Not yet reacted coal

9 Pannala_MM_0611 Spouted bed coater (device scale) Coated fuel particle (small scale) 0.5- to 1-mm particles Coating encapsulates fission products Failure rate < 1 in 10 5 Quality depends on surface processes at nm length scale and ns time scales Links multiscale mathematics with petascale computing and GNEP  Design challenge: Maintain optimal temperatures, species, residence times in each zone to attain right microstructure of coating layers at nm scale  Truly multiscale problem: ~O(13) time scales, ~O(8) length scales Coating at high temperature (1300–1500°C) in batch spouted bed reactor for ~10 4 s Particles cycle thru deposition and annealing zones where complex chemistry occurs ~10 -3 m ~10 -1 m UO 2 ~10 -3 m Pickup zone (~ s) Si-C Inner Pyrolitic C Amorphous C Kernel Additional applications: Nuclear fuel coating process Ballistic zone Pickup zone (~ s) Transport reaction zone (~ s) Hopper flow zone (~s) Inlet gas

Going forward  Extend the methodology to multiple spatial dimensions  Couple the KMC with LBM simulator  Develop error measures and error control strategies  Implement the multiscale framework into highly scalable parallel environment  Apply the developed framework to the targeted applications 10 Pannala_MM_0611

11 Pannala_MM_0611 The Team Sreekanth Pannala Srdjan Simunovic Stuart Daw Phani Nukala Oak Ridge National Laboratory Rodney Fox George Frantziskonis Sudib Mishra Pierre Deymier Thomas O’Brien Dominic Alfonso Madhava Syamlal Ames Laboratory Iowa State University University of Arizona National Energy Technology Laboratory

12 Pannala_MM_0611 ORNL contact Sreekanth Pannala Oak Ridge National Laboratory (865) Pannala_MM_0611