Dynamic Plasticity

Chapter 6: Flow of a Bigham Fluid

This chapter is devoted to the motion of a Bingham body through various devices; through a tube with or without friction at the wall, flow in a viscosimeter, flow in the field of natural slopes, etc. Plastic flow through conical converging dies will not be described (Cristescu [1975] [1976], Fu and Loo [1995]). For general concept on strain rate intensity factor see Aleksandrov et al. [2003].

6.1 Flow of a Bingham Fluid Through a Tube

We consider a tube of length l and of radius R (Buckingham [1921]). We work in cylindrical coordinates.

At z=0 we have (Fig. 6.1.1)


that is a pressure is applied.


Fig. 6.1.1: The flow in a tube.

We assume telescopic flow i.e.,


The rate of deformation tensor in cylindrical coordinates are


From here for our problem we have


The constitutive equation for a Bingham (viscoplastic/rigid) fluid is:


with the plastic part


If only


From (6.1.3) and (6.1.5) we obtain


Thus for the only non zero component:


We observe now that f ?<0 or ( ?? z / ?r)<0 since ? z decreases with increasing r. Therefore sign D rz= ?1. Since all D ij=0 all =0, besides D rz and ? rz. We have thus


The equations of motion in cylindrical coordinates are:


Introducing (6.1.8) in (6.1.9) 1 and (6.1.9) 2, and by disregarding the body forces and the accelerations, we have:


thus ? depends on z

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