The yield stress—a review or ‘παντα ρει’—everything flows?
Introduction
The subject of yield stresses has, in the last decade or so, generated a fair amount of debate in the rheological literature (see below for details). Following a previous paper by this author in 1985 [1], some writers using the expression tried to clarify what they meant by yield stress, rather than simply introducing it without cautious definition. However, there is still enough unenlightened and uncritical use of the expression by some authors-who seem unaware of the controversy that has gone on-to justify a review of the subject, and possibly to round off discussion in the area.
As an example of the continued importance of yield stresses and allied ideas, we note that in the last dozen years or so the phrases yield stress or yield point have been cited nearly 2500 times in the general scientific and engineering literature (All citation statistics quoted here are derived from the Institute for Scientific Information Citation Databases, 1985 to date). As to the particular continued use of the concept in Rheology, we note that in a recent, extra-large volume of Rheology Abstracts [40 (3), 1997], over 500 papers were reviewed, and more than 1 in 15 of them made reference to either yield stress or plasticity.
A typical dictionary definition of the verb ‘to yield’ would be ‘to give way under pressure’ and this implies an abrupt and profound change in behaviour to a less resistant state. As a qualitative description of a general change in the mechanical response of a material, it is completely satisfactory and unobjectionable, since many materials show a radical transformation in flow (or deformation) behaviour over a relatively narrow range of stress, and have obviously ‘yielded’, for example as seen in Fig. 1 where the flow properties of a 6% suspension of iron oxide in mineral oil (redrawn from [2]), change from a very viscous liquid (∼105 Pa s) at low stresses (∼0.7 Pa) to a quite mobile liquid (0.5 Pa s) at a slightly higher stress (∼3 Pa).
Historically this kind of behaviour was graphically portrayed in linear plots of applied stress against shear rate, which is not surprising, given the limited shear-rate ranges available—typically 1–100 s−1. However, plotted as, say, the logarithm of viscosity against the logarithm of applied stress, the phenomenon is much better illustrated. Within the limited range of measurable shear rates, it looked as though the viscosity of such a ‘yield-stress’ liquid was increasing asymptotically as the applied shear stress was decreased. Indeed, for all practical purposes it looked as though there was a definite stress where the viscosity did become infinite, see for example Fig. 2 which is derived from Fig. 3.8 of Han’s book [3]. Looking at it the other way around, below this critical stress the material in question appeared to be an infinite-viscosity solid, and above the critical stress, a (very shear-thinning) liquid!.
The controversy begins here, since many people would then go on to strictly define a solid as a material that does not flow, i.e. continue to deform under stress. Hence, for them, below the yield stress there is no flow! This came about because those involved truly could not measure any sensible flow below the yield stress, that is to say, within the experimental means at their disposal at the time. The position taken here is that such experimental limitations have now been removed, and the picture has changed profoundly. However, without any further hesitation, we can say that the concept of a yield stress has proved and, used correctly, is still proving very useful in a whole range of applications, once it is properly defined, delimited and circumscribed.
Obviously, the idea of a yield stress was well imbedded in the domain of metals long before it was brought over into the liquids area by Schwedoff and Bingham early in this century. Indeed, the Bingham model was introduced in one of his books in 1922 in a chapter headed ‘The Plasticity of Solids’. (The original publication of the Bingham equation was in 1916 [4].)
However, the definition of the yield stress of a solid (for instance a metal) is itself far from being simple and easily described, and before we embark on a study of the subject for liquids, it is well worthwhile devoting some space to this topic. For instance, looking at some popular definitions offered nowadays, we have:Penguin Dictionary of Physics [5]:
“yield point—a point on a graph of stress versus strain… at which the strain becomes dependent on time and the material begins to flow.
yield stress—the minimum stress for creep to take place. Below this value any deformation produced by an external force will be purely elastic.
yield value—the minimum value of stress that must be applied to a material in order that it shall flow”.
“yield point—the lowest stress at which strain increases without increase in stress.
yield strength—the stress at which a material exhibits a specified deviation from [linear] proportionality between stress and strain”.
“yield stress—the level of stress at which substantial deformation suddenly takes place.”
“yield stress—the stress at which a substantial amount of plastic deformation takes place under constant load. This sudden yielding is characteristic of iron and annealed steels. In other metals, deformation begins gradually…”
“yield stress—the minimum stress at which a… material will deform without significant increase in load… some materials do not have a well-defined yield point and in others it is not a well-defined value.”
Clearly the definition is quite varied even within this small sample of everyday science publications: for instance, at one point it is ‘departure from linearity’; then ‘increase in deformation without increase in stress’ and then ‘the onset of creep or flow’, etc. Secondly, it is hedged about by all kinds of non-quantitative qualifiers, such as ‘specified deviation’, ‘substantial deformation’, ‘substantial amount’, ‘without significant increase in load’, ‘not… well-defined’, etc. All of this is in contrast, for instance, to the Young’s modulus of the same material, which is a well-specified quantity, which can be assigned precisely.
However we could say that a simplistic definition of the yield stress of a solid is essentially the point at which, when increasing the applied stress, the solid first shows liquid-like behaviour, i.e. continual deformation. If this is the case, then we can say that conversely, a simple definition of the yield stress of a liquid is the point at which, when decreasing the applied stress, solid-like behaviour is first seen, i.e. no continual deformation.
The liquids that appear to have a yield stress are legion. Among them are Bingham’s many original examples such as clay, oil paint, toothpaste, drilling mud, molten chocolate, etc., then later, materials as diverse as creams of all sorts, ketchups and other culinary sauces, molten filled rubbers and printing inks, etc., were found to show similar behaviour. Now such disparate systems as ceramic pastes, electro-viscous fluids, thixotropic paints, heavy-duty washing liquids, surface-scouring liquids, mayonnaise, yoghurts, purees, liquid pesticides, bio-mass broths, blood, water-coal mixtures, molten liquid-crystalline polymers, plastic explosives, foams, rocket propellant pastes, etc., can be added to the extensive list.
In the following sections, we will trace the history of the subject and then look at the present position with regard to these kinds of materials in order to see where there is use and abuse of the yield-stress concept.
Section snippets
Bingham’s yield stress and plasticity
Professor Eugene C. Bingham has left his name indelibly in the area of Rheology. His most conspicuous contributions were in the defining of the word Rheology (see chapter 1 of [10]) and commencing the first society of Rheology (and also being its journal’s first editor), but he also endowed us with one of Rheology’s most memorable and enduring non-Newtonian laws-the Bingham model or equation, with its ‘Bingham’ yield-value and plastic viscosity, which over the last dozen years or so has been
Simple theories that seem to predict a yield stress
Simple descriptions of the viscosity of dispersions usually produce situations where the viscosity is predicted to become infinite. One of the simplest is that due to Quemada [73], which is a simplified form of the Krieger-Dougherty equation:where η and ηc are the viscosities of the suspension and the continuous phase, and φ and φm the phase volume and the maximum phase volume respectively.
These theories assume that, as the concentration of the dispersed phase is increased, the
Colloid science
The use of the simple Bingham model is much favoured by colloid chemists, even if there is plenty of evidence of departure from linearity at low shear rates. The appearance of an apparent yield stress (often measured as the extrapolated Bingham value) is used as a measure of maximum flocculation in a suspension, that is to say the overall attractive forces between the suspended particles are a maximum. This is often brought about by altering the pH of the system in order to minimise the
General
If a yield-stress material behaves as a solid below the yield stress, we may quite properly ask the question, ‘How do solids behave below their yield stress, especially when examined over very long time periods of stress?’. A number of comprehensive texts have appeared over recent years giving us an overview of this behaviour, probably the most extensive being that of Frost and Ashby [109]. Their deformation maps cover most solid materials, e.g. metals, ceramics, ice, etc. They show that, if
General comments
If we accept a pragmatic approach and feel that we need to measure yield stress, then what is the best method? The answer will be controlled by the end use (see Astarita’s comments in [35]). Once obvious artefacts such as wall slip have been removed or accounted for, and we are able to measure down to shear rates as low as 10−3 s −1, we are usually left with a curve that, on a logarithmic basis of shear rate against shear stress, shows a shallow slope, (sometimes as low as 10% in stress per
Conclusions
The arguments raised here as to the non-existence of a true yield stress are certainly not new, for instance we can quote again Reiner’ statement in 1928 at the first ever Rheology Meeting referring to Bingham materials, ‘there was no yield point’ [14]. We can also note the comment from the 70-year-old, seldom-quoted but excellent work of Hatschek on colloidal solutions [159], who, very pointedly, said of Bingham’s straight-line-with-intercept idea, ‘…[this] has hardly been realised
Acknowledgements
I am indebted to Geraint Roberts for help in preparing the graphs; to Cris Gallegos for supplying some viscometric data and to Derek Bell for checking the controlled-stress rheometer specifications data.
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