Book contents
- Frontmatter
- Contents
- Preface
- 1 Polymer Processing
- 2 Fundamentals
- 3 Extrusion
- 4 Temperature and Pressure Effects in Flow
- 5 The Thin Gap Approximation
- 6 Quasi-Steady Analysis of Mold Filling
- 7 Fiber Spinning
- 8 Numerical Simulation
- 9 Polymer Melt Rheology
- 10 Viscoelasticity in Processing Flows
- 11 Stability and Sensitivity
- 12 Wall Slip and Extrusion Instabilities
- 13 Structured Fluids
- 14 Mixing and Dispersion
- Postface
- Author Index
- Subject Index
- Plate section
- References
13 - Structured Fluids
Published online by Cambridge University Press: 05 June 2012
- Frontmatter
- Contents
- Preface
- 1 Polymer Processing
- 2 Fundamentals
- 3 Extrusion
- 4 Temperature and Pressure Effects in Flow
- 5 The Thin Gap Approximation
- 6 Quasi-Steady Analysis of Mold Filling
- 7 Fiber Spinning
- 8 Numerical Simulation
- 9 Polymer Melt Rheology
- 10 Viscoelasticity in Processing Flows
- 11 Stability and Sensitivity
- 12 Wall Slip and Extrusion Instabilities
- 13 Structured Fluids
- 14 Mixing and Dispersion
- Postface
- Author Index
- Subject Index
- Plate section
- References
Summary
Introduction
Many polymeric liquids have a microstructure even at rest. This might be a consequence of the presence of dispersed particulates or, in the case of liquid crystalline polymers, because of the rigidity of the polymer molecules. Continuum equations describing the stress and microstructure evolution are available for some limiting cases, permitting calculations of flow in complex geometries. The levels of description of the stress states are not comparable to that for entangled flexible polymer melts, so the resulting calculations are less likely to be in quantitative agreement, but they are still very useful for gaining insight into the development of morphology. We address three cases of structured fluids in this chapter: fiber suspensions, such as those that might be used for thermoplastic composites; liquid crystalline polymers; and fluids that exhibit a yield stress, which might include nanoparticle-filled melts.
Fiber Suspensions
The continuum approach to the rheology of fiber suspensions is based on a 1922 solution by Jeffery for the creeping-flow mechanics of a single ellipsoid in a shear flow. The ellipsoid rotates in a nonsinusoidal fashion, spending most of the period near a fixed angle to the flow direction. The ellipsoid aligns with the flow direction at all times in the limit of an infinite aspect ratio. The key assumptions in deriving a constitutive equation for a fiber suspension from Jeffery's result for the ellipsoid are that the suspending fluid is Newtonian and the suspension is dilute.
- Type
- Chapter
- Information
- Polymer Melt ProcessingFoundations in Fluid Mechanics and Heat Transfer, pp. 217 - 230Publisher: Cambridge University PressPrint publication year: 2008