By Charles E. Leiserson
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2003, Report TSD-151, ME Department, Stanford University. 42 4. 5. 6. 7. K. C. M. , 2004, Proc. Int. Conf. Multiphase Flow, Yokohama. , Stenum, B. , 2002, Int. J. Multiphase Flow 28, 225–246. , Kim, J. , 1999, Phys. Fluids 11, 943–945. Paris, T. , 2001, Turbulence attenuation in a particle-laden channel ﬂow, Report TSD-137, Department of Mechanical Engineering, Stanford University. 8. D. Thesis, ME Department, Stanford University. 9. D. , 1990, Phys. Fluids A2, 1191–1203. 10. Sundaram, S. , 1999, J.
Under fully-developed conditions, atomization is balanced by the deposition of drops entrained in the turbulent gas . The idealized model of an annular ﬂow which we have explored considers a horizontal channel for which the bottom and top walls are arrays of sources (see Figure 1). Drops are represented by solid spherical particles. The atomization process is modeled by injecting the particles from x2 = dp /2 with a velocity of (15, 1, 0) v ∗ and a rate per unit area of RAb and from x2 = 2H − dp /2 with a velocity of (15, −1, 0) v ∗ and a rate per unit area of RAt , where v ∗ is the friction velocity and H is the half-height of the channel.
Davila, J. , 2001, Settling of particles near vortices and in turbulence, J. Fluid Mech. 440, 117–145. 11. , 1977, On the dispersion of small particles in an isotropic turbulent ﬂow, J. Fluid Mech. 83, 529–546. 12. D. , 1992, Preferential concentration of particles by turbulence, Phys. Fluids A 3, 1169–1178. Use of a Stochastic Method to Describe Dispersion and Deposition in an Idealized Annular Flow Thomas J. edu Abstract. A stochastic representation of ﬂuid turbulence has been developed to study the behavior of very dilute suspensions of solid spheres in a turbulent ﬂow.
Area-Efficient VLSI Computation by Charles E. Leiserson