CONCENTRATION DISTRIBUTIONS OF SAND SLURRIES IN HORIZONTAL PIPE FLOW

ABSTRACT Concentration distributions for sand slurries flowing in pipes of diameter ranging between 50 and 500 mm have been measured. Particle diameters ranged between 0.18 and 2.4 mm. The concentration distributions have been used in a critical examination of the suspension mechanisms for flows without stationary deposits. Although the classical Schmidt-Rouse diffusion mechanism applies for slurries of fine particles, a pipe diameter dependence of the diffusion coefficient has been detected. This deviation could be due to a form of turbulence suppression by the density gradient in the slurry. For large particles, settling velocities and flow velocities were found to be of minor importance. Particle interaction effects appeared to be confined to the near-wall regions and were most important for the largest particles in the smallest pipe. A method for predicting concentration distributions in the absence of particle interaction effects is proposed.

[1]  Wilhelm Schmidt,et al.  Der Massenaustausch in freier Luft und verwandte Erscheinungen , 1926 .

[2]  Raffi M. Turian,et al.  Flow of noncolloidal slurries in pipelines , 1989 .

[3]  P. Saffman The lift on a small sphere in a slow shear flow , 1965, Journal of Fluid Mechanics.

[4]  R. Bagnold Experiments on a gravity-free dispersion of large solid spheres in a Newtonian fluid under shear , 1954, Proceedings of the Royal Society of London. Series A. Mathematical and Physical Sciences.

[5]  D. Inman,et al.  Observations of rapidly flowing granular-fluid materials , 1985, Journal of Fluid Mechanics.

[6]  C. A. Shook,et al.  PREDICTION OF VERTICAL LIQUID SOLID PIPE FLOW USING MEASURED CONCENTRATION DISTRIBUTION , 1995 .

[7]  Clifton A. Shook,et al.  A conductivity probe for measuring local concentrations in slurry systems , 1987 .

[8]  Mihail C. Roco,et al.  Slurry flow : principles and practice , 1991 .

[9]  K. Wilson,et al.  Dispersive-force modelling of turbulent suspension in heterogeneous slurry flow , 1988 .

[10]  H. Schlichting Boundary Layer Theory , 1955 .

[11]  G. Wallis One Dimensional Two-Phase Flow , 1969 .

[12]  Randall Gordon Gillies,et al.  Pipeline flow of coarse particle slurries , 1993 .

[13]  K. C. Wilson,et al.  An improved two layer model for horizontal slurry pipeline flow , 1991 .

[14]  C. A. Shook Experiments with concentrated slurries of particles with densities near that of the carrier fluid , 1985 .

[15]  Hunter Rouse,et al.  Modern Conceptions of the Mechanics or Fluid Turbulence , 1937 .

[16]  S. Tolansky,et al.  The etching of diamond, II. Cleavage, dodecahedron and cube faces , 1954, Proceedings of the Royal Society of London. Series A. Mathematical and Physical Sciences.

[17]  M. C. Roco,et al.  Modeling of slurry flow: The effect of particle size , 1983 .

[18]  Clifton A. Shook,et al.  The lateral variation of solids concentration in horizontal slurry pipeline flow , 1987 .