User:Richiewayne/Shear Thickening Fluids (Dilatants)

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Comparison of the behavior of four types of fluids with shear rate as a function of applied shear stress

A shear thickening fluid, also called a dilatant, is a Non-Newtonian fluid where the shear viscosity increases with applied shear stress. This behavior is only one type of deviation from Newton’s Law, and it is controlled by such factors as particle size, shape, and distribution. The properties of these suspensions depend on Hamaker theory and Van der Waals forces and can be stabilized electrostatically or sterically. Shear thickening behavior occurs when a colloidal suspension transitions from a stable state to a state of flocculation.Such behavior is currently being researched for use in body armor applications by companies like Dow Corning with their Active Protection System. A large portion of the properties of these systems are due to the surface chemistry of particles in dispersion, known as colloids.

Definition[edit]

There are two types of deviation from Newton's Law that are observed in real systems. The most common deviation is shear thinning behavior, where the viscosity of the system decreases as the shear rate is increased. The second deviation is shear thickening behavior where, as the shear rate is increased, the viscosity of the system also increases. This behavior is observed because the system crystallizes under stress and behaves more like a solid than a solution[1] . Thus, the viscosity of a shear-thickening fluid is dependent on the shear rate. The presence of suspended particles often affects the viscosity of a solution. In fact, with the right particles, even a Newtonian fluid can exhibit non-Newtonian behavior. An example of this is cornstarch in water and is included in the Examples section below.

The parameters that control shear thickening behavior are: particle size and particle size distribution, particle volume fraction, particle shape, particle-particle interaction, continuous phase viscosity, and the type, rate, and time of deformation. In addition to these parameters, all shear thickening fluids are stabilized suspensions and have a volume fraction of solid that is relatively high.[2]

Viscosity of a solution as a function of shear rate is given via the Power Law equation,[3] where η is the viscocity, K is a material-based constant, and γͦ is the applied shear rate.

Dilatant behavior occurs when n is 2 or greater.[4]

Below is a table of viscosity values for some common materials. [5] [6] [7]

Material Viscosity (cP)
Benzene 601
Carbon Tetrachloride 880
Ethanol 1,060
Mercury 1,550
Pentane 2,240
Sulfuric Acid 27,000
Water at 298K 891
Water at 460K 1 to 5
Blood 10
Anti-Freeze 14
Maple Syrup 150-200
Honey 2,000-3,000
Chocolate Syrup 10,000-25,000
Peanut Butter 150,000-250,000
Ketchup 50,000-70,000

Stabilized Suspensions[edit]

A suspension (chemistry) is composed of a fine, particulate phase dispersed throughout a differing, heterogeneous phase. Shear-thickening behavior is observed in systems with a solid, particulate phase dispersed within a liquid phase. These solutions are different from a Colloid in that they are unstable; the solid particles in dispersion are sufficiently large for Sedimentation, causing them to eventually settle. Whereas the solids dispersed within a colloid are smaller and will not settle. There are multiple methods for stabilizing suspensions, including electrostatics and sterics.

Energy of repulsion as a function of particle separation

In an unstable suspension, the dispersed, particulate phase will come out of solution in response to forces acting upon the particles, such as gravity or Hamaker attraction. The magnitude of the effect these forces have on pulling the particulate phase out of solution is proportional to the size of the particulates; for a large particulate, the gravitational forces are greater than the particle-particle interactions, whereas the opposite is true for small particulates. Shear thickening behavior is typically observed in suspensions of small, solid particulates, indicating that the particle-particle Hamaker attraction is the dominant force. Therefore, stabilizing a suspension is dependent upon introducing a counteractive repulsive force.

Hamaker theory describes the attraction between bodies, such as particulates. It was realized that the explanation of Van der Waals forces could be upscaled from explaining the interaction between two molecules with induced dipoles to macro-scale bodies by summing all the intermolecular forces between the bodies. Similar to Van der Waals forces, Hamaker theory describes the magnitude of the particle-particle interaction as inversely proportional to the square of the distance. Therefore, many stabilized suspensions incorporate a long-range repulsive force that is dominant over Hamaker attraction when the interacting bodies are at a sufficient distance, effectively preventing the bodies from approaching one another. However, at short distances, the Hamaker attraction dominates, causing the particulates to coagulate and fall out of solution. Two common long-range forces used in stabilizing suspensions are electrostatics and sterics.

Electrostatically-Stabilized Suspensions[edit]

Particle in solution stabilized via the electrostatic double-layer force

Suspensions of similarly charged particles dispersed in a liquid electrolyte are stabilized through an effect described by the Helmholtz double layer model. The model is comprised of two layers. The first layer is the charged surface of the particle, which creates an electrostatic field that affects the ions in the electrolyte. In response, the ions create a diffuse layer of equal and opposite charge, effectively rendering the surface charge neutral. However, the diffuse layer creates a potential surrounding the particle that differs from the bulk electrolyte.

The diffuse layer serves as the long-range force for stabilization of the particles. When particles near one another, the diffuse layer of one particle overlaps with that of the other particle, generating a repulsive force. The following equation provides the energy between two colloids as a result of the Hamaker interactions and electrostatic repulsion.

Where:

V = Energy between a pair of colloids

R = Radius of colloids

-H = Hamaker constant between colloid and solvent

h = Distance between colloids

C = Surface ion concentration

k = Boltzmann constant

T = Temperature in Kelvin

= Surface excess

= Inverse Debye length

Particle in suspension stabilized via steric hindrance.

Sterically-Stabilized Suspensions[edit]

Different from elecrostatics, sterically-stabilized suspensions rely on the physical interaction of polymer chains attached to the surface of the particles to keep the suspension stabilized; the adsorbed polymer chains act as a spacer to keep the suspended particles separated at a sufficient distance to prevent the Hamaker attraction from dominating and pulling the particles out of suspension. The polymers are typically either grafted or adsorbed onto the surface of the particle. With grafted polymers, the backbone of the polymer chain is covalently bonded to the particle surface. Whereas an adsorbed polymer is a copolymer composed of lyophobic and lyophilic region, where the lyophobic region non-covalently adheres to the particle surface and the lyophilic region forms the steric boundary or spacer.

Theories Behind Shear Thickening Behavior[edit]

Dilatancy in a colloid, or its ability to order in the presence of shear forces is dependent on the ratio of interparticle forces. As long as interparticle forces such as Van der Waals forces dominate, the suspended particles remain in ordered layers. However, once shear forces dominate, particles enter a state of flocculation and are no longer held in suspension; they begin to behave like a solid. When the shear forces are removed, the particles spread apart and once again form a stable suspension. This is opposite of the shear thinning effect where the suspension is initially in the state of flocculation and becomes stable when a stress is applied.[8]


Shear thickening behavior is highly dependent upon the volume fraction of solid particulate suspended within the liquid. The higher the volume fraction, the less shear required to initiate the shear thickening behavior. The shear rate at which the fluid transitions from a Newtonian flow to a shear thickening behavior is known as the critical shear rate.


Order to Disorder Transition[edit]

When shearing a concentrated stabilized solution at a relatively low shear rate, the repulsive particle-particle interactions keep the particles in an ordered, layered, equilibrium structure. However, at shear rates elevated above the critical shear rate, the shear forces pushing the particles together overcome the repulsive particle-particle interactions, forcing the particles out of their equilibrium positions. This leads to a disordered structure, causing an increase in viscosity.[9]

The critical shear rate here is defined as the shear rate at which the shear forces pushing the particles together are equivalent to the repulsive particle interactions.

Transient hydroclustering of a particles in solution.

Hydroclustering[edit]

When the particles of a stabilized suspension transition from an immobile state to mobile state, small groupings of particles form hydroclusters, increasing the viscosity. These hydroclusters are composed of particles momentarily compressed together, forming a irregular, rod-like chain of particles akin to a logjam or traffic jam. In theory the particles have extremely small interparticle gaps, rendering this momentary, transient hydrocluster as incompressible. It is possible that additional hydroclusters will form through aggregation. [10]

Examples[edit]

Silly Putty[edit]

An integral part of many childhoods, Silly Putty was first made from silicone oil and boric acid during World War II in an attempt to make synthetic rubber[11]. This material can stretch without tearing yet parts can be broken off, it has a rebound of 80% when bounced like a ball, and even keeps its shape when hit with hammer yet it flattened by a child's palm[12].

Corn Starch and Water (Oobleck)[edit]

Cornstarch is a common thickening agent used in cooking. It is also a very good example of a shear thickening system. When a force is applied to a 1:2.5 mixture of water and cornstarch, the cornstarch acts as a solid and resists the force. For a great demo of this behavior, check out this video.

Silica and Poly(Ethylene Glycol)[edit]

Silica nano-particles are dispersed in a solution of poly(ethylene glycol). The Silica particles provide a high strength material when flocculation occurs. This allows it to be used in applications such as liquid body armor and brake pads.

Applications[edit]

Body Armor[edit]

The incorporation of shear thickening fluids into Kevlar® fabrics is being investigated to improve stab resistance and augment balistic protection. This could potentially develop a new wave of body armor that enable a reduction in stiffness and weight, increasing their comfort and allowing the protection to extend beyond the torso.[13] Here is a video on how shear thickening fluids are used to make liquid body armor.

See Also[edit]

Newtonian Fluid

Non-Newtonian fluid

Bingham plastic

Colloid

Double layer (interfacial)

Rheology

DLVO theory

Hamaker theory

Suspension (chemistry)

References[edit]

  1. ^ Coleman, Paul C. Painter, Michael M. (1997). Fundamentals of polymer science : an introductory text (2nd ed.). Lancaster, Pa.: Technomic. pp. 412–413. ISBN 1-56676-559-5.{{cite book}}: CS1 maint: multiple names: authors list (link)
  2. ^ Galindo-Rosales, Francisco J.; Rubio-Hernández, Francisco J.; Velázquez-Navarro, José F. (22 May 2009). "Shear-thickening behavior of Aerosil® R816 nanoparticles suspensions in polar organic liquids". Rheologica Acta. 48 (6): 699–708. doi:10.1007/s00397-009-0367-7.
  3. ^ Cunningham, Neil. "Rheology School". Brookfield Engineering. Retrieved 4 June 2011.
  4. ^ Griskey, Richard (May 1971). "Flow of Dilatant (Shear-Thickening) Fluids". AlChE Journal. 17 (3): 725–728. doi:10.1002/aic.690170341. {{cite journal}}: Unknown parameter |coauthors= ignored (|author= suggested) (help)CS1 maint: date and year (link)
  5. ^ Barnes, H.A. (1989). An introduction to rheology (5. impr. ed.). Amsterdam: Elsevier. ISBN 0444871403. {{cite book}}: Unknown parameter |coauthors= ignored (|author= suggested) (help)
  6. ^ Atkins, Peter (2010). Physical chemistry (9th ed.). New York: W. H. Freeman and Co. ISBN 978-1429218122.
  7. ^ "Viscosity Chart". Research Equipment Limited. Retrieved 4 June 2011.
  8. ^ Morrison, Ian (2002). Colloidal Dispersions: suspensions, emulsions, and foams. Wiley-Interscience. p. 512. ISBN 0471176257. {{cite book}}: Unknown parameter |coauthors= ignored (|author= suggested) (help)
  9. ^ Boersma, Willem H (1990). "Shear Thickening (Dilatancy) in Concentrated Dispersions". AIChE. 36 (3): 321–332. doi:10.1002/aic.690360302. {{cite journal}}: Unknown parameter |coauthors= ignored (|author= suggested) (help)
  10. ^ Farr, R. S. (June 1997). "Kinetic theory of jamming in hard-sphere startup flows". Physical Review E. 55 (6): 7206–7211. doi:10.1103/PhysRevE.55.7203. {{cite journal}}: Unknown parameter |coauthors= ignored (|author= suggested) (help)CS1 maint: date and year (link)
  11. ^ Thayer, Ann (27 November 2000). "What's That Stuff?". Chemical & Engineering News. Retrieved 26 May 2011.
  12. ^ Thayer, Ann (27 November 2000). "What's That Stuff?". Chemical & Engineering News. Retrieved 26 May 2011.
  13. ^ Galindo-Rosales, Francisco J.; Rubio-Hernández, Francisco J.; Velázquez-Navarro, José F. (22 May 2009). "Shear-thickening behavior of Aerosil® R816 nanoparticles suspensions in polar organic liquids". Rheologica Acta. 48 (6): 699–708. doi:10.1007/s00397-009-0367-7.