The second edition of this excellent book brings many new features, which were outlined in the preface to the 2nd Edition.

The pursuit of the golden balance between oversimplification and overload with theory has always been the primary goal of every author of book on rheology. Rheology is a tool for chemists and chemical engineers to solve many practical problems. They have to learn what to measure, how to measure, and what to do with the data. But, the learning process should not take users away from their major goals, such as manufacturing quality products, developing new materials, analysis of material durability.

The first four chapters of this book discuss various aspects of theoretical rheology and, by examples of many studies, show how particular theory, model, or equation can be used in solving different problems. The main emphasis is on liquids but solid materials are discussed in one full chapter.

The goal of rheological studies is not to measure some rheological variables but to generate relevant data and this requires experience and understanding of theory. The authors share their experiences of many years of experimental studies and teaching to show use of rheology in studies of materials. This is one very strong aspect of this book which will help to avert costly confusions - common when data are generated under wrong conditions or data are wrongly used.

Methods of measurement and raw data treatment are included in one large chapter which constitutes over one quarter of the book. Eight groups of methods are discussed here giving many choices for experimentation and guidance on where and how to use them properly.

The final chapter shows how to use rheological methods in different groups of products and methods of their manufacture. Usefulness of chemorheological (rheokinetical) measurements is also emphasized. This chapter continues with examples of purposeful applications in practical matters.

The authors were very meticulous in showing historical sequence of developments which led to the present advancements in rheology. This aspect is of interest of specialists in rheology, professors and their students because it shows in chronological order important events and teaches about their implications on further discoveries. References to various chapters and short summaries of achievements of many scientists give essential historical background of contributors to rheology as a science and as the method of solving many practical problems.

Many people need this book, ranging from students to accomplished rheologists because it contains expert advice of two very famous and accomplished scientists and teachers who know discoveries first-hand because they may have taken part in some of them and they intent to pass their knowledge to the next generations.

This book is very useful in industry but it is invaluable as a teaching tool in universities and colleges because it is consistent with programs of rheology courses. Practicality of this book will prepare students for typical tasks in industry.

**Preface to the 2nd Edition**

In preparing the Second Edition of this book, the general structure of the book is maintained and some necessary corrections and additions are made. The most important recent results published in periodicals till the middle of 2011 are added. In particular, Section 2.8.1 of Chapter 2, Section 3.5.2 of Chapter 3 and Subsection 5.8.1.2 of Chapter 5 are modified. A new Subsection 5.6.2.6 on Capillary breakup in elongational rheometry is added. Furthermore, Section 3.2.3 on Viscosity of anisotropic liquids and Section 3.6.3 on Instabilities in flow of elastic fluids of Chapter 3 are completely rewritten. Many other modifications in the text are made and some new figures are added. Also, all the detected misprints and errors found by ourselves or pointed out by colleagues are corrected.

After publication of the First Edition of the book, a lot of comments and advice from our friends and colleagues were received. We are very grateful to all of them for constructive criticism and valuable comments.

We are also grateful to our Editor, Dr. G. Wypych, for his hard work in improving the manuscript and making it ready for publication.

Alexander Ya. Malkin,

Moscow, Russia

**Avraam I. Isayev**

Akron, Ohio, USA

Preface

Introduction. Rheology: Subject and Goals

1 Continuum Mechanics as a Foundation of Rheology

1.1 Stresses

1.1.1 General theory

1.1.2 Law of equality of conjugated stresses

1.1.3 Principal stresses

1.1.4 Invariants of a stress tensor

1.1.5 Hydrostatic pressure - spherical tensor and deviator

1.1.6 Equilibrium (balance) equations

1.2 Deformations

1.2.1 Deformations and displacements

1.2.1.1 Deformations

1.2.1.2 Displacements

1.2.2 Infinitesimal deformations: principal values and invariants

1.2.3 Large (finite) deformations

1.2.4 Special cases of deformations - uniaxial elongation and simple shear

1.2.4.1 Uniaxial elongation and Poisson's ratio

1.2.4.2 Simple shear and pure shear

1.3 Kinematics of deformations

1.3.1 Rates of deformation and vorticity

1.3.2 Deformation rates when deformations are large

1.4 Summary - continuum mechanics in rheology

1.4.1 General principles

1.4.2 Objects of continuum as tensors

References

Questions for Chapter 1

2 Viscoelasticity

2.1 Basic experiments

2.1.1 Creep (retarded deformation)

2.1.2 Relaxation

2.1.3 Fading memory

2.2 Relaxation and creep - spectral representation. Dynamic functions

2.2.1 Retardation and relaxation spectra - definitions

2.2.2 Dynamic functions

2.3 Model interpretations

2.3.1 Basic mechanical models

2.3.2 Complicated mechanical models - differential rheological equations

2.3.3 Non-mechanical models

2.4 Superposition - The Boltzmann-Volterra principle

2.4.1 Integral formulation of the superposition principle

2.4.2 Superposition principle expressed via spectra

2.4.3 Simple transient modes of deformation

2.4.3.1 Relaxation after sudden deformation

2.4.3.2 Developing stresses at constant shear rate

2.4.3.3 Relaxation after steady shear flow

2.4.3 Relationship between relaxation and creep functions

2.4.4 Relaxation function and large deformations

2.4.3.4 Relationship between relaxation and creep functions

2.4.3.5 Relaxation function and large deformations

2.5 Relationships among viscoelastic functions

2.5.1 Dynamic functions - relaxation, creep, and spectra

2.5.2 Constants and viscoelastic functions

2.5.3 Calculation of a relaxation spectrum

2.5.3.1 Introduction - general concept

2.5.3.2 Kernel approximation - finding a continuous spectrum

2.5.3.3 Computer-aided methods for a discrete spectrum

2.6 Viscoelasticity and molecular models

2.6.1 Molecular movements of an individual chain

2.6.1.1 A spring-and-bead model ("free draining chain")

2.6.1.2 Model of a non-draining coil

2.6.1.3 Model of a rotating coil

2.6.2 Relaxation properties of concentrated polymer solutions and melts

2.6.2.1 Concept of entanglements

2.6.2.2 Two-part distribution of friction coefficient

2.6.2.3 Non-equivalent friction along a chain

2.6.2.4 Viscoelastic entanglements

2.6.2.5 Rubber-like network

2.6.2.6 "Tube" (reptation) model

2.6.2.7 Some conclusions

2.6.3 Viscoelasticity of polydisperse polymers

2.7 Time-temperature superposition. Reduced ("master") viscoelastic curves

2.7.1 Superposition of experimental curves

2.7.2 Master curves and relaxation states

2.7.3 "Universal" relaxation spectra

2.8 Non-linear effects in viscoelasticity

2.8.1 Experimental evidences

2.8.1.1 Non-Newtonian viscosity

2.8.1.2 Non-Hookean behavior of solids

2.8.1.3 Non-linear creep

2.8.1.4 Non-linear relaxation

2.8.1.5 Non-linear periodic measurements

2.8.2 Linear - non-linear correlations

2.8.3 Rheological equations of state for non-linear viscoelastic behavior

2.8.3.1 The K-BKZ model

2.8.3.2 The Wagner models

2.8.3.2 The Leonov model

2.8.3.4 The Marrucci models

2.8.4 Comments - constructing non-linear constitutive equations and experiment

References

Questions for Chapter 2

3 Liquids

3.1 Newtonian and non-Newtonian liquids. Definitions

3.2 Non-Newtonian shear flow

3.2.1 Non-Newtonian behavior of viscoelastic polymeric materials

3.2.2 Non-Newtonian behavior of structured systems - plasticity of liquids

3.2.3 Viscosity of anisotropic liquids

3.3 Equations for viscosity and flow curves

3.3.1 Introduction - the meaning of viscosity measurement

3.3.2 Power-law equations

3.3.3 Equations with yield stress

3.3.4 Basic dependencies of viscosity

3.3.4.1 Viscosity of polymer melts

3.3.4.2 Viscosity of polymer solutions

3.3.4.3 Viscosity of suspensions

3.3.5 Effect of molecular weight distribution on non-Newtonian flow

3.4 Elasticity in shear flows

3.4.1 Rubbery shear deformations - elastic recoil

3.4.2 Normal stresses in shear flow

3.4.2.1 The Weissenberg effect

3.4.2.2 First normal stress difference - quantitative approach

3.4.2.3 Second normal stress difference and secondary flow

3.4.3 Normal stresses and elasticity

3.4.4 Die swell

3.5 Structure rearrangements induced by shear flow

3.5.1 Transient deformation regimes

3.5.2 Thixotropy and rheopexy

3.5.3 Shear induced phase transitions

3.6 Limits of shear flow - instabilities

3.6.1 Inertial turbulency

3.6.2 The Toms effect

3.6.3 Instabilities in flow of elastic liquids

3.6.3.1 Dynamic structure formation and secondary flows in elastic fluids

3.6.3.2 Secondary flows in the flow of elastic fluids

3.6.3.3 Shear banding

3.7 Extensional flow

3.7.1 Model experiments - uniaxial flow

3.7.2 Model experiments - rupture

3.7.3 Extension of industrial polymers

3.7.3.1 Multiaxial elongation

3.7.4 The tubeless siphon effect

3.7.5 Instabilities in extension

3.7.5.1 Phase transitions in extension

3.7.5.2 Rayleigh instability

3.7.5.3 Instabilities in extension of a viscoelastic thread

3.8 Conclusions - real liquid is a complex liquid

References

Questions for Chapter 3

4 Solids

4.1 Introduction and definitions

4.2 Linear elastic (Hookean) materials

4.3 Linear anisotropic solids

4.4 Large deformations in solids and non-linearity

4.4.1 A single-constant model

4.4.2 Multi-constant models

4.4.2.1 Two-constant potential function

4.4.2.2 Multi-member series

4.4.2.3 General presentation

4.4.2.4 Elastic potential of the power-law type

4.4.3 The Poynting effect

4.5 Limits of elasticity

4.5.1 Standard experiment - main definitions

4.5.2 Plasticity

4.5.3 Criteria of plasticity and failure

4.5.3.1 Maximum shear stress

4.5.3.2 The intensity of shear stresses ("energetic" criterion)

4.5.3.3 Maximum normal stress

4.5.3.4 Maximum deformation

4.5.3.5 Complex criteria

4.5.4 Structure effects

4.5.4.1 Strengthening

4.5.4.2 Thixotropy

References

Questions for Chapter 4

5 Rheometry. Experimental Methods

5.1 Introduction - Classification of experimental methods

5.2 Capillary viscometry

5.2.1 Basic theory

5.2.2 Corrections

5.2.2.1 Kinetic correction

5.2.2.2 Entrance correction

5.2.2.3 Pressure losses in a reservoir of viscometer

5.2.2.4 Temperature correction

5.2.2.5 Pressure correction

5.2.2.6 Correction for slip near a wall

5.2.2.7 Adsorption on a channel surface

5.2.3 Flow in incompletely filled capillary

5.2.3.1 Motion under action of gravitation forces

5.2.3.2 Motion caused by surface tension forces

5.2.4 Limits of capillary viscometry

5.2.5 Non-viscometric measurements using capillary viscometers

5.2.6 Capillary viscometers

5.2.6.1 Classification of the basic types of instruments

5.2.6.2 Viscometers with the assigned load

5.2.6.3 Cup viscometers

5.2.6.4 Glass viscometers

5.2.7 Viscometers with controlled flow rate

5.2.7.1 Instruments with a power drive

5.2.7.2 Instruments with hydraulic drive

5.2.7.3 Extrusion rheometers

5.2.7.4 Technological capillary tube viscometers

5.3 Rotational rheometry

5.3.1 Tasks and capabilities of the method

5.3.1.1 Viscometric and non-viscometric measurements

5.3.1.2 The method of a constant frequency of rotation

5.3.1.3 The method of a constant torque

5.3.2 Basic theory of rotational instruments

5.3.2.1 Instruments with coaxial cylinders

5.3.2.2 Instruments with conical surfaces

5.3.2.3 Bi-conical viscometers

5.3.2.4 Disk viscometers

5.3.2.5 Viscometers with spherical surfaces

5.3.2.6 End (bottom) corrections in instruments with coaxial cylinders

5.3.2.7 On a role of rigidity of dynamometer

5.3.2.8 Temperature effects

5.3.3 Limitations of rotational viscometry

5.3.4 Rotational instruments

5.3.4.1 Introduction - general considerations

5.3.4.2 Rheogoniometers and elastoviscometers

5.3.4.3 Viscometers with assigned rotational speed

5.3.4.4 Rotational viscometers for special purposes

5.3.4.5 Rotational instruments for technological purposes

5.3.5 Measuring normal stresses

5.3.5.1 Cone-and-plate technique

5.3.5.2 Plate-and-plate technique

5.3.5.3 Coaxial cylinders technique

5.3.5.4 Hole-pressure effect

5.4 Plastometers

5.4.1. Shear flow plastometers

5.4.2 Squeezing flow plastometers

5.4.3 Method of telescopic shear

5.4.3.1 Telescopic shear penetrometer

5.5 Method of falling sphere

5.5.1 Principles

5.5.1.1 Corrections

5.5.2 Method of rolling sphere

5.5.3 Viscometers with falling sphere

5.5.4 Viscometers with falling cylinder

5.6 Extension

5.6.1 General considerations

5.6.2. Experimental methods

5.6.2.1 The simplest measuring schemes

5.6.2.2 Tension in a controlled regime

5.6.2.3 Tubeless siphon instruments

5.6.2.4 Flow in convergent channels

5.6.2.5 High strain rate methods

5.6.3 Biaxial extension

5.7 Measurement of viscoelastic properties by dynamic (oscillation) methods

5.7.1 Principles of measurement - homogeneous deformation

5.7.2 Inhomogeneous deformations

5.7.3 Torsion oscillations

5.7.4 Measuring the impedance of a system

5.7.5 Resonance oscillations

5.7.6 Damping (free) oscillations

5.7.7 Wave propagation

5.7.7.1 Shear waves

5.7.7.2 Longitudinal waves

5.7.8 Vibration viscometry

5.7.8.1 Torsion oscillations

5.7.8.2 Oscillation of a disk in liquid

5.7.8.3 Oscillations of sphere

5.7.8.4 Damping oscillations

5.7.9 Measuring viscoelastic properties in non-symmetrical flows

5.7.9 About experimental techniques

5.7.9.1 Rotational instruments

5.7.9.2 Devices with electromagnetic excitation

5.7.9.3 Torsion pendulums

5.8 Physical methods

5.8.1 Rheo-optical methods

5.8.1.1 Basic remarks

5.8.1.2 Stress - optical rules for polymer melts

5.8.1.3 Stress-optical rule for polymer solutions

5.8.1.4 Viscometers for optical observations

5.8.1.5 Polarization methods for measuring stresses

5.8.1.6 Visualization of polymer flow in dies

5.8.2. Velocimetry

5.8.3 Viscometers-calorimeters

References

Questions for Chapter 5

6 Applications of Rheology

6.1 Introduction

6.2 Rheological properties of real materials and their characterization

6.2.1 Polymer materials

6.2.2 Mineral oils and oil-based products

6.2.3 Food products

6.2.4 Cosmetics and pharmaceuticals

6.2.5 Biological fluids

6.2.6 Concentrated suspensions

6.2.7 Electro- and magneto-rheological materials

6.2.8 Concluding remarks

6.3 Rheokinetics (chemorheology) and rheokinetic liquids

6.3.1. Formulation of problem

6.3.2. Linear polymerization

6.3.3 Oligomer curing

6.3.3.1 Viscosity change and a gel-point

6.3.3.2 Curing at high shear rates

6.3.3.3 Curing after gel-point

6.3.4 Intermolecular transformations

6.4 Solution of dynamic problems

6.4.1 General formulation

6.4.2 Flow through tubes

6.4.3 Flow in technological equipment

6.4.3.1 Pumping screw

6.4.3.2 Calendering and related processes

6.4.3.3 Extension-based technologies

6.4.3.4 Molding technologies

6.4.3.5 Compression molding

6.4.3.6 Injection molding

6.4.3.7 Injection-compression molding

References

Questions for Chapter 6

Notations

Answers

Index

Prof. Dr. Alexander Ya. Malkin, Principal Research Fellow, Institute of Petrochemical Synthesis, Russian Academy of Sciences, Moscow, Russia

Prof. Dr. Avraam I. Isayev, Distinguished Professor, Institute of Polymer Engineering, The University of Akron, Akron, USA