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Sankaran Sundaresan

Sankaran Sundaresan

Norman John Sollenberger Professor in Engineering
Professor of Chemical and Biological Engineering

B.Tech., Indian Institute of Technology, Madras, 1976
M.S., University of Houston, 1978
Ph.D., University of Houston, 1980

Room: A315 Engineering Quad
Phone: 609-258-4583

Webpage: Multiphase Flow Research Group

Honors and Awards

  • Humboldt Research Award, 2014
  • Engineering Council's Excellence in Teaching Award, Princeton University, 2005, 2008, 2012
  • JM Burgers Visiting Professor of Fluid Mechanics, TU Delft, 2009-2012
  • Associate Editor, AIChE Journal, 2002-2011
  • Neal R. Amundson Lecture, University of Houston, January 2010
  • JM Burgers Lecture, Eindhoven, The Netherlands, 2009
  • Fellow, American Institute of Chemical Engineers, 2008
  • Moore Distinguished Scholar, California Institute of Technology, 2007
  • The President's Award for Distinguished Teaching, Princeton University, 2006
  • Thomas Baron Award in Fluid-Particle Systems, American Institute of Chemical Engineers, 2005
  • School of Engineering & Applied Science Distinguished Teacher Award, Princeton University, 2005
  • Distinguished Alumnus Award, Indian Institute of Technology, Madras, 2000
  • Richard H. Wilhelm Award, American Institute of Chemical Engineers, 1999


Research Areas

Research Interests

Origin and hierarchy of meso-scale structures in two-phase flows. Dispersed multiphase flows, frequently encountered in chemical reactors and separation devices, are almost always unstable, and complex spatio-temporal patterns are observed ubiquitously. One can usually observe structures at different length scales and time scales - micro, meso and macro scales - and they influence the mixing, mass transfer and heat transfer processes. Over the past decade, we have uncovered the origin and hierarchy of instabilities leading to formation of various meso-scale structures in:

  • gas-liquid flows in trickle beds,
  • fluid-solid flows in gas- and liquid-fluidized beds,
  • granular flows, and
  • dilute gas-solid flows in vertical pipes.

In each of these flow problems, we have identified the minimum physics which must be built into the averaged equations of motion to capture the meso-scale structures in a qualitatively correct manner. We are currently engaged in a similar analysis of gas-liquid flows in bubble columns. Using Lattice Boltzmann simulations to examine the details of flow behavior at the level of individual bubbles, we have uncovered two different regimes of bubble rise, viz. hindered rise and cooperative rise, which are obtained with nearly spherical and distorted bubbles, respectively. We have discovered a new columnar instability mechanism through which the lift force destabilizes the uniformly bubbling state in the cooperative bubble rise regime. We are currently studying the hierarchy of instabilities in this system.

Coarsened equations of motion for two-phase flows. The closure relations for the averaged equations of motion for dispersed two-phase flows, which are available in the literature, are usually valid for nearly homogeneous suspensions. Analysis of the averaged equations with these closures reveals that, in gas-particle flows and buoyant rise of bubbly suspensions, the dominant instability through which an uniform state breaks into meso-scale structures occurs at a length scale of the order or 10 - 50 particle (or bubble) diameter. This severely limits the value of the averaged equations as a tool for studying flows in large process vessels, as the required spatial resolution renders the calculations far beyond what is feasible today. With this in mind, we are developing coarsened equations of motion, where one has not only averaged over the flow patterns at the level of the individual particles, but also the meso-scale structures. This is necessary as our recent work has demonstrated that the fluctuations associated with the meso-scale structures can dwarf those at the particle level. Through detailed computational experiments, we are gathering information on the statistical and scaling properties of the meso-scale structures. These will be used to devise meso-scale structural models for coarse simulations of two-phase flows.

Contact stresses in granular assemblies. Flow of dense assemblies of granular materials is encountered in many devices used to handle and mix particles, and in fluidized beds. Frictional stresses transmitted through sustained contact of particles with multiple neighbors play an important role in the flow behavior obtained in such devices. For example, a stable operation of a circulating fluidized bed is possible only when the frictional contact between the particle assembly and the walls of the standpipe can provide a stabilizing effect. Through fluidization and defluidization experiments performed in tubes of different diameters and with glass beads of various diameters (63 - 150 μm), we have isolated the effect of wall friction and exposed the role of contact stresses in imparting stability to fluidized suspensions. This study has raised new questions about mechanism controlling the onset of bubbling in fluidized beds which we are currently pursuing. We are also extending this study to finer particles to investigate how cohesive interactions between particles modify the contact stresses.

Role of static electrification on gas-particle flows. Lateral segregation of particles occurs readily in vertical gas-particle flows and its origin has been a subject of much research. We identified a few years ago a hydrodynamic segregation mechanism arising from the density and velocity fluctuations, which are inherent in gas-particle flows. We have recently recognized that a modest level of electrostatic charges on the particles is enough to cause appreciable lateral segregation. We are now engaged in a study of electrostatic charges on particles and their effects on fluidization and pneumatic transport of particles.

Instantaneous snapshots of particle volume fraction distribution in fluidized suspensions revealing meso-scale structures. The five panels correspond to mean solids volume fractions of 0.025, 0.05, 0.15, 0.25, and 0.45, respectively. In these simulations of a kinetic theory model for gas-solid flows, an initially uniform suspension of 75 micrometers particles fluidized by air gave way to cluster and streamers in dilute systems and bubble-like voids in dense suspensions, which coalesce and break up frequently. The simulations were done in a 1cm x 1cm x 4cm triply periodic domain (16 x 16 x 64 nodes), with not imposed shear. The region where the particle volume fraction is below 0.06 is shown as colorless. Blue represents lower volume fractions while red indicates higher volume fractions.