Levich Institute Seminar Announcement, 03/20/2012
Tuesday, 03/20/2012
2:00 PM
Steinman Hall, Room #312
(Chemical Engineering Conference Room)

Dr. John Singh
Corning, Inc.

"Flow of Power Law Fluid in a Fixed Bed of Spheres or Cylinders"


An ensemble average of the equations of motion for a Newtonian fluid over particle configurations in a dilute fixed bed of spheres or cylinders yields Brinkman's equations of motion where the disturbance velocity produced by a test particle is influenced by the Newtonian fluid stress and a body force representing the linear drag on the surrounding particles. We consider a similar analysis for a power law fluid where the stress is related to the rate of strain by , where and are constants. In this case, the ensemble averaged momentum equation includes a body force resulting from the nonlinear drag exerted on the surrounding particles, a power-law stress associated with the disturbance velocity of the test particle, and a stress term that is linear with respect to the test particle's disturbance velocity. The latter term results from the interaction of the test particle's velocity disturbance with the random straining motions produced by the neighboring particles and is important only in shear thickening fluids where the velocity disturbances of the particles are long ranged. The solutions to these equations using scaling analyses for dilute beds and numerical simulations using the finite element method is presented. We show that the drag force acting on a particle in a fixed bed can be written as a function of a length scale at which the fluid velocity disturbance produced by a particle is modified by hydrodynamic interactions with its neighbors. This length scale is in turn a function of the concentration of the bed. This is also valid for the drag on a particle in a periodic array where the length scale is the lattice spacing. The effects of particle interactions on the drag in dilute arrays (periodic or random) of cylinders and spheres in shear thickening fluids is dramatic, where it arrests the algebraic growth of the disturbance velocity with radial position when for cylinders and for spheres. For concentrated random arrays of particles, we adopt an effective medium theory in which the drag force per unit volume in the medium surrounding a test particle is assumed to be proportional to the local volume fraction of the neighboring particles which is derived from the hard-particle packing. The predictions of the averaged equations of motion are validated by comparison with simulations of randomly distributed hydrodynamically interacting cylinders.

  • 11/2010- Present Senior Process Engineer, Corning Incorporated, Corning, NY
  • 12/2008- 11/2010 Research Associate, Chemical Engineering Department, Cornell University, Ithaca, NY
  • 10/2007- 11/2008 Postdoctoral Associate, Chemical Engineering Department, University of Delaware, Newark, DE
  • 10/2007 Doctor of Philosophy in Chemical Engineering, The Benjamin Levich Institute, City University of New York (CUNY)
  • 08/2003 Master of Philosophy in Chemical Engineering, The Graduate School and University Center CUNY
  • 06/2001 Bachelor of Technology in Chemical Engineering, Indian Institute of Technology (IIT) - New Delhi, India