Nanoparticle motion trajectories and deposition in an inlet channel of wall-flow diesel particulate filter

A two-dimensional gas–particle two-phase flow model in an inlet channel of diesel particulate filter (DPF) has been developed. The interaction between the gas and the particle is treated as one-way coupling due to the extremely dilute particle concentration. The drag force, the Brownian excitation, and the partial slip are included in the particle motion equation. The particle motion trajectories for various particle source locations and various particle sizes are presented. The dependences of the velocity field of the channel on wall permeability and upstream velocity are evaluated. The effects of particle size, upstream velocity, wall permeability, Brownian motion, and partial slip on the particle deposition are investigated. The three dominant mechanisms, which are drag force, Brownian motion, and particle inertia, are analyzed deeply. These results demonstrate that the drag force always plays the most primary role in determining the particle motion and deposition. On the other hand, the effects of Brownian motion and particle inertia vary with Pe number and Rep* number, respectively. As Pe number and Rep* number increase, the effect of particle inertia enhances, while the effect of Brownian motion lowers. The predicted velocity field is compared with the results obtained from the classical one-dimensional model, and the computational pressure loss of DPF is compared with the experimental values. The reasonable agreements of the two cases are both observed.

[1]  John H. Johnson,et al.  A One-Dimensional Computational Model for Studying the Filtration and Regeneration Characteristics of a Catalyzed Wall-Flow Diesel Particulate Filter , 2003 .

[2]  Edward J. Bissett,et al.  Mathematical model of the thermal regeneration of a wall-flow monolith diesel particulate filter , 1984 .

[3]  M. Kostoglou,et al.  Fundamental Studies of Diesel Particulate Filters: Transient Loading, Regeneration and Aging , 2000 .

[4]  Mansour Masoudi Hydrodynamics of Diesel Particulate Filters , 2002 .

[5]  M. Kostoglou,et al.  Periodically Reversed Flow Regeneration of Diesel Particulate Traps , 1999 .

[6]  John H. Johnson,et al.  Modeling and Numerical Simulation of Diesel Particulate Trap Performance During Loading and Regeneration , 2002 .

[7]  John H. Johnson,et al.  A 2-D Computational Model Describing the Heat Transfer, Reaction Kinetics and Regeneration Characteristics of a Ceramic Diesel Particulate Trap , 1998 .

[8]  Andrea Prosperetti,et al.  Averaged equations for inviscid disperse two-phase flow , 1994, Journal of Fluid Mechanics.

[9]  Martin Votsmeier,et al.  Transport and reaction in catalytic wall-flow filters , 2005 .

[10]  Farhang Shadman,et al.  Thermal regeneration of diesel-particulate monolithic filters , 1985 .

[11]  G. Ahmadi,et al.  Dispersion and deposition of particles in a turbulent pipe flow with sudden expansion , 1998 .

[12]  S. Patankar Numerical Heat Transfer and Fluid Flow , 2018, Lecture Notes in Mechanical Engineering.

[13]  Raymond M. Brach,et al.  Experiments on the Low-Velocity Impact of Microspheres with Planar Surfaces , 1995 .

[14]  Zhaoyan Zhang,et al.  A One-Dimensional Numerical Model for Diesel Particulate Trap Performance Study during Loading and Regeneration , 2005 .

[15]  Athanasios G. Konstandopoulos,et al.  Inertial Contributions to the Pressure Drop of Diesel Particulate Filters , 2001 .

[16]  Barton E. Dahneke,et al.  Particle Bounce or Capture—Search for an Adequate Theory: I. Conservation-of-Energy Model for a Simple Collision Process , 1995 .

[17]  Christopher J. Rutland,et al.  Development of a CFD Model to Study the Hydrodynamic Characteristics and the Soot Deposition Mechanism on the Porous Wall of a Diesel Particulate Filter , 2005 .

[18]  Athanasios G. Konstandopoulos,et al.  Multi-channel simulation of regeneration in honeycomb monolithic diesel particulate filters , 2003 .

[19]  Goodarz Ahmadi,et al.  Deposition of particles in a turbulent pipe flow , 1997 .

[20]  D. Drew Mathematical Modeling of Two-Phase Flow , 1983 .

[21]  A. Zydney,et al.  Effect of electrostatic, hydrodynamic, and Brownian forces on particle trajectories and sieving in normal flow filtration. , 2004, Journal of colloid and interface science.

[22]  Zhenhua Guo Modeling and simulation of wall -flow diesel particulate filter during loading and regeneration , 2006 .

[23]  G. Saracco,et al.  Catalytic traps for diesel particulate control , 1999 .

[24]  Martin R. Maxey,et al.  The motion of small spherical particles in a cellular flow field , 1987 .

[25]  Goodarz Ahmadi,et al.  Brownian diffusion of submicrometer particles in the viscous sublayer , 1991 .

[26]  Goodarz Ahmadi,et al.  A sublayer model for deposition of nano- and micro-particles in turbulent flows , 2000 .

[27]  Goodarz Ahmadi,et al.  WALL DEPOSITION OF SMALL ELLIPSOIDS FROM TURBULENT AIR FLOWS—A BROWNIAN DYNAMICS SIMULATION , 2000 .

[28]  M. Kostoglou,et al.  Reciprocating flow regeneration of soot filters , 2000 .

[29]  M. Elimelech,et al.  Particle Deposition onto a Permeable Surface in Laminar Flow , 1995 .

[30]  John H. Johnson,et al.  Wall-Flow Diesel Particulate Filters—Their Pressure Drop and Collection Efficiency , 1989 .

[31]  J. Gong,et al.  Numerical Simulation of Gas-Particle Two-Phase Flow Characteristic During Deep Bed Filtration Process , 2007 .

[32]  John H. Johnson,et al.  A 2-D Computational Model Describing the Flow and Filtration Characteristics of a Ceramic Diesel Particulate Trap , 1998 .