
Structure and Rheology of Molten Polymers
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Persons
Daniel Read is a Reader in the School of Mathematics at the University of Leeds, UK. His research includes development of models to predict rheology of entangled molten polymers, and of models to predict molecular structure from reactor kinetics. He is coauthor of the "BoB" code for entangled polymer rheology prediction.
Ronald Larson is Professor of Chemical Engineering at the University of Michigan. His research interests include rheology and flow of complex fluids, molecular simulations of such materials, and polyelectrolyte interactions.
Content
- Intro
- Preface to the Second Edition
- Preface to the First?Edition
- Contents
- 1 Introduction
- 1.1 Melt Structure and Its Effect on?Rheology
- 1.2 Overview of This Book
- 1.3 Applications of the Information Presented
- 1.4 Supplementary Sources of Information
- References
- 2 Structure of?Polymers
- 2.1 Molecular Size
- 2.1.1 The Freely-Jointed Chain
- 2.1.2 The Gaussian Size Distribution
- 2.1.2.1 Linear Molecules
- 2.1.2.2 Branched Molecules
- 2.1.3 The Dilute Solution and the Theta State
- 2.1.4 Polymer Molecules in the Melt
- 2.2 Molecular Weight Distribution
- 2.2.1 Monodisperse Polymers
- 2.2.2 Average Molecular Weights and Moments of the Distribution
- 2.2.3 Continuous Molecular Weight Distribution
- 2.2.4 Distribution Functions
- 2.2.5 Narrow Distribution Samples
- 2.2.6 Bimodality
- 2.3 Tacticity
- 2.4 Branching
- 2.5 Intrinsic Viscosity
- 2.5.1 Introduction
- 2.5.2 Rigid Sphere Models
- 2.5.3 The Free-Draining Molecule
- 2.5.4 Non-Theta Conditions and the Mark-Houwink-Sakurada Equation
- 2.5.5 Effect of Polydispersity
- 2.5.6 Effect of Long-Chain Branching
- 2.5.7 Effects of Short-Chain Branching
- 2.5.8 Determination of Intrinsic Viscosity-Extrapolation Methods
- 2.5.9 Effect of Shear Rate
- 2.6 Other Structure Characterization Methods
- 2.6.1 Membrane Osmometry
- 2.6.2 Light Scattering
- 2.6.3 Gel Permeation Chromatography
- 2.6.3.1 MWD of Linear Polymers
- 2.6.3.2 GPC with Branched Polymers
- 2.6.3.3 GPC with LDPE
- 2.6.3.4 Interactive Chromatography
- 2.6.3.5 Field Flow Fractionation
- 2.6.4 Mass Spectrometry (MALDI-TOF)
- 2.6.5 Nuclear Magnetic Resonance
- 2.6.6 Separations Based on Crystallizability: TREF, CRYSTAF, and CEF
- 2.6.7 Bivariate (Two-Dimensional) Characterizations
- 2.6.8 Molecular Structure from Rheology
- 2.7 Summary
- References
- 3 Polymerization Reactions and?Processes
- 3.1 Introduction
- 3.2 Classifications of Polymers and?Polymerization Reactions
- 3.3 Structural Characteristics of Polymers
- 3.3.1 Introduction
- 3.3.2 Chemical Composition-Role of Backbone Bonds in Chain Flexibility
- 3.3.3 Chemical Composition-Copolymers
- 3.3.4 Tacticity
- 3.3.5 Branching
- 3.4 Living Polymers Having Prescribed Structures
- 3.4.1 Anionic Polymerization
- 3.4.2 Living Free-Radical Polymerization (Reversible?Deactivation?Radical Polymerization-RDRP)
- 3.4.3 Model Polyethylenes for Research
- 3.5 Industrial Polymerization Processes
- 3.6 Free-Radical Polymerization of?Low-Density Polyethylene (LDPE)
- 3.6.1 Shear Modification
- 3.7 Linear Polyethylene via?Complex?Coordination?Catalysts
- 3.7.1 Catalyst Systems
- 3.7.2 Branching in High-Density Polyethylene
- 3.7.3 Ultrahigh Molecular Weight Polyethylene
- 3.8 Linear Low-Density Polyethylene via?Ziegler-Natta?Catalysts
- 3.9 Single-Site Catalysts
- 3.9.1 Metallocene Catalysts
- 3.9.2 Long-Chain Branching in Metallocene Polyethylenes
- 3.9.3 Post-Metallocene Catalysts
- 3.10 Polypropylene
- 3.11 Reactors for Polyolefins
- 3.12 Polystyrene
- 3.13 Summary
- References
- 4 Linear Viscoelasticity-Fundamentals
- 4.1 Stress Relaxation and?the?Relaxation?Modulus
- 4.1.1 The Boltzmann Superposition Principle
- 4.1.2 The Maxwell Model for the Relaxation Modulus
- 4.1.3 The Generalized Maxwell Model and?the?Discrete?Relaxation?Spectrum
- 4.1.4 The Continuous Relaxation Spectrum
- 4.2 The Creep Compliance and?the?Retardation Spectrum
- 4.3 Experimental Characterization of?Linear?Viscoelastic Behavior
- 4.3.1 Oscillatory Shear
- 4.3.2 Experimental Determination of the Storage and Loss Moduli
- 4.3.3 Creep Measurements
- 4.3.4 Other Methods for Monitoring Relaxation Processes
- 4.4 Calculation of Relaxation Spectra from?Experimental Data
- 4.4.1 Discrete Spectra
- 4.4.2 Continuous Spectra
- 4.5 Time-Temperature Superposition
- 4.5.1 Time/Frequency (Horizontal) Shifting
- 4.5.2 The Modulus (Vertical) Shift Factor
- 4.5.3 Validity of Time-Temperature Superposition
- 4.6 Time-Pressure Superposition
- 4.7 Alternative Plots of?Linear?Viscoelastic?Data
- 4.7.1 Van Gurp-Palmen Plot of Loss Angle Versus Complex Modulus
- 4.7.2 Cole-Cole Plots
- 4.8 Summary
- References
- 5 Linear Viscoelasticity-Behavior of Molten Polymers
- 5.1 Introduction
- 5.2 Zero-Shear Viscosity of Linear Polymers
- 5.2.1 Effect of Molecular Weight
- 5.2.2 Effect of Polydispersity
- 5.3 The Relaxation Modulus
- 5.3.1 General Features
- 5.3.2 How Can a Melt Act like a Rubber?
- 5.4 The Storage and Loss Moduli
- 5.5 The Creep and Recoverable Compliances
- 5.6 The Steady-State Compliance
- 5.7 The Plateau Modulus
- 5.7.1 Determination of GN0
- 5.7.2 Effects of Short Branches and Tacticity
- 5.8 The Molecular Weight between?Entanglements, Me
- 5.8.1 Definitions of Me
- 5.8.2 Molecular Weight between Entanglements (Me) Based?on?Molecular?Theory
- 5.9 Rheological Behavior of Copolymers
- 5.10 Effect of Long-Chain Branching on?Linear Viscoelastic Behavior
- 5.10.1 Introduction
- 5.10.2 Ideal Branched Polymers
- 5.10.2.1 Zero-Shear Viscosity of Ideal Stars and Combs
- 5.10.2.2 Steady-State Compliance of Model Star Polymers
- 5.10.3 Storage and Loss Moduli of Model Branched Systems
- 5.10.4 Randomly Branched Polymers
- 5.10.5 Low-Density Polyethylene
- 5.11 Use of Linear Viscoelastic Data to?Determine Branching Level
- 5.11.1 Introduction
- 5.11.2 Correlations Based on the Zero-Shear Viscosity
- 5.12 Summary
- References
- 6 Tube Models for Linear Polymers-Fundamentals
- 6.1 Introduction
- 6.2 The Rouse-Bueche Model for?Unentangled Polymers
- 6.2.1 Introduction
- 6.2.2 The Rouse Model for the Viscoelasticity of a Dilute Polymer Solution
- 6.2.3 Bueche's Modification for an Unentangled Melt
- 6.3 Entanglements and the Tube Model
- 6.3.1 The Critical Molecular Weight for Entanglement MC
- 6.3.2 The Plateau Modulus GN0
- 6.3.3 The Molecular Weight Between Entanglements Me
- 6.3.4 The Tube Diameter a
- 6.3.5 The Equilibration Time te
- 6.3.6 Identification of Entanglements and Tubes in Computer Simulation
- 6.4 Modes of Relaxation
- 6.4.1 Reptation
- 6.4.2 Primitive Path Fluctuations
- 6.4.3 Reptation Combined with Primitive Path Fluctuations
- 6.4.4 Constraint Release-Double Reptation
- 6.4.4.1 Monodisperse Melts
- 6.4.4.2 Bidisperse Melts
- 6.4.4.3 Polydisperse Melts
- 6.4.5 Rouse Relaxation within the Tube
- 6.5 An Alternative Picture for Entangled Polymers: Slip-Links
- 6.6 Summary
- References
- 7 Tube Models for Linear Polymers-Advanced Topics
- 7.1 Introduction
- 7.2 Limitations of Double Reptation Theory
- 7.3 Constraint-Release Rouse Relaxation in?Bidisperse Melts
- 7.3.1 Non-Self-Entangled Long Chains in a Short-Chain Matrix
- 7.3.2 Self-Entangled Long Chains in a Short-Chain Matrix
- 7.3.3 Thin Tubes, Fat Tubes, and the Viovy Diagram
- 7.4 Polydisperse Melts and "Dynamic?Dilution"
- 7.4.1 Polydisperse Chains
- 7.4.2 Tube Dilation or "Dynamic Dilution"
- 7.5 Input Parameters for Tube Models
- 7.6 Summary
- References
- 8 Determination of?Molecular Weight Distribution Using?Rheology
- 8.1 Introduction
- 8.2 Viscosity Methods
- 8.3 Empirical Correlations Based?on?the?Elastic Modulus
- 8.4 Methods Based on Double Reptation
- 8.5 Generalization of Double Reptation
- 8.6 Dealing with the Rouse Modes
- 8.7 Models that Account for Additional Relaxation Processes
- 8.8 Determination of Polydispersity Indexes
- 8.9 Summary
- References
- 9 Tube Models for Branched Polymers
- 9.1 Introduction
- 9.2 General Effect of LCB on Rheology
- 9.2.1 Qualitative Description of Relaxation Mechanisms in?Long-Chain-Branched Polymers
- 9.3 Star Polymers
- 9.3.1 Deep Primitive Path Fluctuations
- 9.3.2 Dynamic Dilution
- 9.3.3 Comparison of Milner-McLeish Theory to Linear Viscoelastic Data
- 9.3.3.1 Monodisperse Stars
- 9.3.3.2 Bidisperse Stars
- 9.3.3.3 Star/Linear Blends
- 9.4 Multiply Branched Polymers
- 9.4.1 Dynamic Dilution for Polymers with Backbones
- 9.4.2 Branch Point Motion
- 9.4.3 Backbone Relaxation
- 9.5 Tube Model Algorithms for Polydisperse Branched Polymers
- 9.5.1 "Hierarchical" and "BoB" Dynamic Dilution Models
- 9.5.2 The "Time-Marching" Algorithm
- 9.5.3 Data and Predictions for Model Polymers and Randomly Branched?Polymers
- 9.6 Slip-Link Models for Branched Polymers
- 9.6.1 Symmetric Star Polymers and Blends with Linear Polymers
- 9.6.2 Branch Point Hopping in Slip-Link Simulations
- 9.7 Summary
- References
- 10 Nonlinear Viscoelasticity
- 10.1 Introduction
- 10.2 Nonlinear Phenomena-A Tube Model Interpretation
- 10.2.1 Large Scale Orientation-The Need for a Finite Strain Tensor
- 10.2.2 Chain Retraction and the Damping Function
- 10.2.3 Convective Constraint Release and Shear Thinning
- 10.3 Constitutive Equations
- 10.3.1 Boltzmann Revisited
- 10.3.2 Integral Constitutive Equations
- 10.3.3 Differential Constitutive Equations
- 10.4 Nonlinear Stress Relaxation
- 10.4.1 Doi and Edwards Predictions of the Damping Function
- 10.4.2 Estimating the Rouse Time of an Entangled Chain
- 10.4.3 Damping Functions of Typical Polymers
- 10.4.4 Normal Stress Relaxation
- 10.4.5 Double-Step Strain
- 10.5 Dimensionless Groups Used?to?Plot?Rheological?Data
- 10.5.1 The Deborah Number
- 10.5.2 The Weissenberg Number
- 10.6 Transient Shear Tests at Finite Rates
- 10.6.1 Stress Growth and Relaxation in Steady Shear
- 10.6.2 Large- and Medium-Amplitude Oscillatory Shear
- 10.7 The Viscometric Functions
- 10.7.1 Dependence of Viscosity on Shear Rate
- 10.7.1.1 Empirical Viscosity Models
- 10.7.1.2 Viscosity Function in Terms of Tube Models
- 10.7.1.3 Effect of Molecular Weight Distribution on Viscosity
- 10.7.1.4 Effect of Long-Chain Branching on Viscosity
- 10.7.2 Normal Stress Differences in Steady Simple Shear
- 10.8 Experimental Methods for?Shear?Measurements
- 10.8.1 Rotational Rheometers
- 10.8.1.1 Generating Step Strain
- 10.8.1.2 Flow Irregularities in Cone-Plate Rheometers
- 10.8.1.3 Measurement of the Second Normal Stress Difference
- 10.8.2 Sliding Plate Rheometers
- 10.8.3 Optical Methods-Flow Birefringence
- 10.8.4 Capillary and Slit Rheometers
- 10.8.5 The Cox-Merz Rule
- 10.9 Extensional Flow Behavior of Melts and?Concentrated Solutions
- 10.9.1 Introduction
- 10.9.2 Solutions versus Melts
- 10.9.3 Linear, Monodisperse Polymers
- 10.9.4 Effect of Polydispersity
- 10.9.5 Linear Low-Density Polyethylene
- 10.9.6 Model Branched Systems
- 10.9.7 Long-Chain Branched Metallocene Polyethylenes
- 10.9.8 Randomly Branched Polymers and LDPE
- 10.9.9 Stress Overshoot in Extensional Flow
- 10.10 Experimental Methods for?Extensional?Flows
- 10.10.1 Introduction
- 10.10.2 Rheometers for Uniaxial Extension
- 10.10.3 Uniaxial Extension-Approximate Methods
- 10.10.4 Rheometers for Biaxial and Planar Extension
- 10.11 Summary
- References
- 11 Tube Models for Nonlinear Viscoelasticity of Linear and Branched Polymers
- 11.1 Introduction
- 11.2 Relaxation Processes Unique?to?the?Nonlinear Regime
- 11.2.1 Retraction
- 11.2.2 Convective Constraint Release
- 11.3 Monodisperse Linear Polymers
- 11.3.1 No Chain Stretch: The Doi-Edwards Equation
- 11.3.2 Chain Stretch: The Doi-Edwards-Marrucci-Grizzuti (DEMG) Theory
- 11.3.3 Convective Constraint Release (CCR) and the GLaMM Model
- 11.3.4 Toy Models Containing CCR and Chain Stretch
- 11.3.4.1 "Rolie-Poly" Model for CCR
- 11.3.4.2 Differential Model of Ianniruberto and Marrucci
- 11.3.5 Comparison of Theory with Data for Monodisperse Linear Polymers: Shearing Flows
- 11.3.6 Extensional Flows of Melts and Solutions of Linear Polymers
- 11.3.7 Constitutive Instabilities and Slip
- 11.3.8 Entanglement Stripping and Chain Tumbling
- 11.3.9 Processing Flows
- 11.4 Polydisperse Linear Polymers
- 11.5 Polymers with Long-Chain Branching
- 11.5.1 The Pom-Pom Model
- 11.5.2 Revisions to the Pom-Pom Model
- 11.5.2.1 Drag-Strain Coupling
- 11.5.2.2 Correction for Reversing Flows
- 11.5.2.3 Second Normal Stress Difference and Other Corrections: The?Extended Pom-Pom Model
- 11.5.2.4 Stress Overshoots, Accelerated Relaxation, and Entanglement Stripping
- 11.5.3 Empirical Multi-Mode Pom-Pom Equations for Commercial Melts
- 11.6 Towards Prediction of Nonlinear Viscoelasticity from Molecular Parameters
- 11.6.1 Seniority and Priority
- 11.6.2 Computational Prediction of Nonlinear Rheology for?Polydisperse?Branched?Polymers
- 11.7 Summary
- References
- 12 State of the Art and?Challenges for?the Future
- 12.1 State of the Art
- 12.2 Progress and Remaining Challenges
- Appendix?A: Structural?and Rheological Parameters for Several Polymers
- Appendix?B: Some?Tensors Useful?in Rheology
- Nomenclature
- Author Index
- Subject Index
- _GoBack
- Leere Seite
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