Bingham plastic

A Bingham plastic is a viscoplastic material that behaves as a rigid body at low stresses but flows as a viscous fluid at high stress. It is named after Eugene C. Bingham who proposed its mathematical form.[1].
Rheology   composition   Bingham plastic model
Rheology   composition   Bingham plastic model
testing   to be entered  with FludFlow3 Slurry calculating the relationship between Apparant Viscosity and Rate of Shear  as shown in the screen images below  As an alternative approach  test values of Shear Rate versus Shear Stress may be entered  with F
with FluidFlow3 Slurry fitting an appropriate curve to generate the relationship between Apparant Viscosity and Rate of Shear  as shown on the screen images below  Having defined the liquid type in the fluids database  FluidFlow3 Slurry automatically sele
Fig  3    a  and  b  Bingham plastic model   c  Operating range   d  Hysteretic behaviour in MR fluid devices
required for the cementitious composites of the future  A non reactive binder such as TecEco Tec Cements can supply the right rheology  and like a printer  very little will be wasted  1   Robotic Construction Methods will Require Self Hardening Composites
5 of that report  that the behavior of this model in the limit of zero shear rate  g   gives a curve that is asymptotic to t = t o + h cpg   the Bingham plastic  see Figure 10  This is not the strictly correct interpretation  When n is near unity  the dev
References
Source: http://en.wikipedia.org/wiki/Bingham_plastic

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A Bingham plastic is a viscoplastic material that behaves as a rigid body at low stresses but flows as a viscous fluid at high stress. It is named after Eugene C. Bingham who proposed its mathematical form.[1].

It is used as a common mathematical model of mud flow in offshore engineering, and in the handling of slurries. A common example is toothpaste[2], which will not be extruded until a certain hydrostatic pressure is used on the tube. It then is pushed out as a solid plug.

Explanation

Figure 1. Bingham Plastic flow as described by Bingham

Figure 1 shows a graph of the behaviour of an ordinary viscous (or Newtonian) fluid in red, for example in a pipe. If the pressure at one end of a pipe is increased this produces a stress on the fluid tending to make it move (called the shear stress) and the volumetric flow rate increases proportionally. However for a Bingham Plastic fluid (in blue), stress can be applied but it will not flow until a certain value, the yield stress, is reached. Beyond this point the flow rate increases steadily with increasing shear stress. This is roughly the way in which Bingham presented his observation, in an experimental study of paints.[3]

Figure 2. Bingham Plastic flow as described currently

Figure 2 shows the way in which it is normally presented currently.[2] The graph shows shear stress on the vertical axis and shear rate on the horizontal one. (Volumetric flow rate depends on the size of the pipe, shear rate is a measure of how the velocity changes with distance. It is proportional to flow rate, but does not depend on pipe size.) As before, the Newtonian fluid flows and gives a shear rate for any finite value of shear stress. However, the Bingham Plastic again does not exhibit any shear rate (no flow and thus no velocity) until a certain stress is achieved. For the Newtonian fluid the slope of this line is the viscosity, which is the only parameter needed to describe its flow. By contrast the Bingham Plastic requires two parameters, the yield stress and the slope of the line, known as the plastic viscosity.

The physical reason for this behaviour is that the liquid contains particles (e.g. clay) or large molecules (e.g. polymers) which have some kind of interaction, creating a weak solid structure, formerly known as a false body, and a certain amount of stress is required to break this structure. Once the structure has been broken, the particles move with the liquid under viscous forces. If the stress is removed, the particles associate again.

Definition

The material is rigid for shear stress ?, less than a critical value ?0. Once the critical shear stress (or "yield stress") is exceeded, the material flows in such a way that the shear rate, ?u/?y (as defined in the article on viscosity), is directly proportional to the amount by which the applied shear stress exceeds the yield stress:

\frac {\partial u} {\partial y} = \left\{\begin{matrix} 0 &, \tau < \tau_0 \\ (\tau - \tau_0)/ {\mu} &, \tau \ge \tau_0 \end{matrix}\right.

References

  1. ^ E.C. Bingham,(1916) U.S. Bureau of Standards Bulletin, 13, 309-353 "An Investigation of the Laws of Plastic Flow"
  2. ^ a b J. F. Steffe (1996) Rheological Methods in Food Process Engineering 2nd ed ISBN 0-9632036-1-4
  3. ^ E. C. Bingham (1922) Fluidity and Plasticity McGraw-Hill (New York) page 219
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