Audit industrial thickeners with new on-line instrumentation

Abstract A theory of sedimentation-consolidation evolved in the last decades of the 20th century and is accepted today by researchers worldwide. This theory provides a reliable method of thickener design, simulation and control. However, a process model, simple or sophisticated, empirical or phenomenological, is useful only if it is possible to determine, in an objective way, its experimental parameters. Although it is important for a mineral processing plant to perform periodical laboratory test to determine thickening parameters, and adjust the operation in this way, laboratory tests not always represent the behavior of the material in a thickener. Research workers at the University of Concepcion developed new instrumentation, algorithms and software to determine the material properties of the thickener feed, such as settling velocity of the suspension and the compressibility of the sediment produced. Work was made in a major Chilean copper mineral processing plant to test the new instrumentation. In this paper, the auditing of one molybdenum thickener and a tailings thickener are presented using the two new online instrument.

[1]  Fernand Meyer,et al.  Topographic distance and watershed lines , 1994, Signal Process..

[2]  R. Bürger,et al.  Sedimentation and Thickening : Phenomenological Foundation and Mathematical Theory , 1999 .

[3]  Raimund Bürger,et al.  Settling velocities of particulate systems: 9. Phenomenological theory of sedimentation processes: numerical simulation of the transient behaviour of flocculated suspensions in an ideal batch or continuous thickener , 1999 .

[4]  R. Bürger,et al.  A Century of Research in Sedimentation and Thickening , 2002 .

[5]  Raimund Bürger,et al.  Second-order schemes for conservation laws with discontinuous flux modelling clarifier–thickener units , 2010, Numerische Mathematik.

[6]  S. Diehl A regulator for continuous sedimentation in ideal clarifier–thickener units , 2008 .

[7]  Lee R. White,et al.  The consolidation of concentrated suspensions. Part 1.—The theory of sedimentation , 1987 .

[8]  W. Russel,et al.  An asymptotic description of transient settling and ultrafiltration of colloidal dispersions , 1989 .

[9]  Peter J. Scales,et al.  Thickener modelling – from laboratory experiments to full-scale prediction of what comes out the bottom and how fast , 2015 .

[10]  R. Jackson,et al.  The resolution of shocks and the effects of compressible sediments in transient settling , 1988, Journal of Fluid Mechanics.

[11]  Raimund Bürger,et al.  Sedimentation and suspension flows: Historical perspective and some recent developments , 2001 .

[12]  R. Bürger,et al.  Mathematical model and numerical simulation of the settling of flocculated suspensions , 1998 .

[13]  Raimund Bürger,et al.  Numerical simulation of clarifier-thickener units treating ideal suspensions with a flux density function having two inflection points , 2006, Math. Comput. Model..

[14]  Kerry A. Landman,et al.  The continuous‐flow gravity thickener: Steady state behavior , 1988 .

[15]  F. Betancourt,et al.  Modeling and controlling clarifier–thickeners fed by suspensions with time-dependent properties , 2014 .