Hostname: page-component-cd9895bd7-dzt6s Total loading time: 0 Render date: 2024-12-19T18:22:41.369Z Has data issue: false hasContentIssue false

Revisiting the 1954 suspension experiments of R. A. Bagnold

Published online by Cambridge University Press:  15 February 2002

M. L. HUNT
Affiliation:
Division of Engineering and Applied Sciences, California Institute of Technology, Pasadena, CA 91125, USA
R. ZENIT
Affiliation:
Instituto de Investigaciones en Materiales, Universidad Nacional Autónoma de México, México D.F. 04510, México
C. S. CAMPBELL
Affiliation:
Department of Mechanical Engineering, University of Southern California, Los Angeles, CA 90089-1453, USA
C. E. BRENNEN
Affiliation:
Division of Engineering and Applied Sciences, California Institute of Technology, Pasadena, CA 91125, USA

Abstract

In 1954 R. A. Bagnold published his seminal findings on the rheological properties of a liquid–solid suspension. Although this work has been cited extensively over the last fifty years, there has not been a critical review of the experiments. The purpose of this study is to examine the work and to suggest an alternative reason for the experimental findings. The concentric cylinder rheometer was designed to measure simultaneously the shear and normal forces for a wide range of solid concentrations, fluid viscosities and shear rates. As presented by Bagnold, the analysis and experiments demonstrated that the shear and normal forces depended linearly on the shear rate in the ‘macro-viscous’ regime; as the grain-to-grain interactions increased in the ‘grain-inertia’ regime, the stresses depended on the square of the shear rate and were independent of the fluid viscosity. These results, however, appear to be dictated by the design of the experimental facility. In Bagnold’s experiments, the height (h) of the rheometer was relatively short compared to the spacing (t) between the rotating outer and stationary inner cylinder (h/t = 4.6). Since the top and bottom end plates rotated with the outer cylinder, the flow contained two axisymmetric counter-rotating cells in which flow moved outward along the end plates and inward through the central region of the annulus. At higher Reynolds numbers, these cells contributed significantly to the measured torque, as demonstrated by comparing Bagnold's pure-fluid measurements with studies on laminar-to-turbulent transitions that pre-date the 1954 study. By accounting for the torque along the end walls, Bagnold’s shear stress measurements can be estimated by modelling the liquid–solid mixture as a Newtonian fluid with a corrected viscosity that depends on the solids concentration. An analysis of the normal stress measurements was problematic because the gross measurements were not reported and could not be obtained.

Type
Research Article
Copyright
© 2002 Cambridge University Press

Access options

Get access to the full version of this content by using one of the access options below. (Log in options will check for institutional or personal access. Content may require purchase if you do not have access.)