NAT'L INST. OF STAND & TECH r

NiST

PUBLICATIONS

The Use of

Nomenclature in

Dispersion Science

and Technology

NIST Recommended Practice Guide

Special Publication 960-3

The Use of

Nomenclature in

Dispersion Science

and Technology

Vincent A. Hackley

Materials Science and

Engineering Laboratory

Chiara F. Ferraris

Building & Fire Research Laboratory

Previously issued as NIST

Special Publications 945 and 946

August 2001

U.S. Department of Commerce

Donald L.Evans, Secretary

Technology Administration

Karen H. Brown, Acting Under Secretary of Commerce for Technology

National Institute of Standards and Technology

Karen H. Brown, Acting Director
Certain commercial entities, equipment, or materials may be identified in this document in order to describe an experimental procedure or concept adequately.

Such identification is not intended to imply recommendation or endorsement

by the National Institute of Standards and Technology, nor is it intended to imply that the entities, materials, or equipment are necessarily the best avail- able for the purpose.

National Institute of Standards and Technology

Special Publication 960-3

Natl. Inst. Stand. Technol.

Spec. Publ. 960-3

72 pages (August 2001)

CODEN: NSPUE2

U.S. GOVERNMENT PRINTING OFFICE

WASHINGTON: 2001

For sale by the Superintendent of Documents

U.S. Government Printing Office

Internet: bookstore.gpo.gov Phone: (202) 512-1800 Fax: (202) 512-2250

Mail: Stop SSOP, Washington, DC 20402-0001
Foreword

Foreword

Measurements and standards are universally recognized as playing an integral role in the manufacturing process. They enhance reliability by providing a basis for quantifying and comparing material properties during each phase of

manufacturing, from raw materials to the finished product. Equally important

is the establishment of a uniform and widely accepted nomenclature for describing experimental methods and instrumentation, for sharing technical

ideas and concepts and to provide a sound basis on which to standardize measurement methods and data reporting practices. This is especially true in the

ceramics community, due to its cross-disciplinary nature and due to the utiliza- tion of ceramic powders throughout numerous industries. Ceramic suspensions, gels and pastes (i.e., dispersions) are the starting materials for a wide variety of applications, playing critical roles in the processing of

products ranging from whitewares, pigments, paper, and cement for the construction industry to multilayer ceramic packages and chemical mechanical

planarization slurries for the microelectronics industry. Unfortunately,

researchers and engineers working in these diverse fields often speak different

languages. Even within the same field, variations in terminology are common.

The need for broadly accepted, uniform and precise nomenclature was

acknowledged recently by the Ceramic Processing Characterization

Consortium (CPCC), a voluntary cooperative organization with participants

representing industry, instrument companies, academia and government. A

principal goal of the consortium was to develop guidelines and recommended

practices for the implementation of process measurements. CPCC members

identified nomenclature as a high priority issue in the areas of dispersion and

dispersion rheology. As a result, work was initiated on two nomenclature

guides, which were ultimately distributed as NIST Special Publications 945

and 946.

The present document is essentially a compilation, with updates, of these two

previous publications, and provides guidelines for the use of technical and sci- entific nomenclature relevant to ceramic dispersions.

hi

Table of Contents

Foreword //'/'

1. Introduction 7 2. Nomenclature for Dispersion Technology 2

2. 7 Physical Description of Dispersed Systems 2

2.7.7 Primary Terms 2

2.7.2 Related Terms 3

2.1.3 Recommendations 4

2.2 States of Subdivison (Dispersed Phase) 4

2.2.1 Definitions Based on Size 4

2.2.2 Definitions Based on Structure 5

2.2.3 Related Terms . . 6

2. 2. 4 Recommendations 7

2.3 Association and Dissociation Processes 8

2.3.1 Associaton Processes 8

2.3.2 Dissociation Processes 9

2.3.3 Related Terms 9

2.3.4 Recommendations 10

2.4 Dispersion Stability 10

2.4. 1 States of Stability 10

2.4.2 Stability Mechanisms 77

2.4.3 Interaction Terms 77

2.4.4 Related Terms 13

2.4.5 Recommendations 15

2.5 Interfacial and Electrokinetic Properties 15

2.5.1 The Interface 15

2.5.2 Adsorption Processes 16

2. 5. 3 Electrical Properties 18

2.5.4 Electrokinetic Effects 19

2.5.5 Related Terms 27

V
Table of Contents

2.6 Bibliography 23

2.6.1 Primary Sources 23

2.6.2 Other Sources 23

Acknowledgements 24

List of Reviewers 24

3. Nomenclature for Rheological Measurements 26

3. 1 Fundamental Rheological Properties 26

3.2 Functional Forms of Viscosity 27

3.3 Glossary of Basic Terminology 29

3.4 Classification of Equilibrium Flow Curves 34

3.5 Expressions for Describing Steady Shear

Non-Newtonian Flow 35

3.6 Time-Dependent Effects 38

3. 7 Oscillatory Measurements 39

3. 7. 1 Material Functions Derived from Oscillatory Tests 40

3. 8 Measurement Apparatus 43

3.8.1 Capillary Methods 43

3.8.2 Rotational Methods 44

3.9 Concrete and Other Coarse-Grained Materials 47

3.9. 1 Glossary of Rheological Terms 49

3. 9. 2 Glossary of Test Methods 50

3.10 Units and Symbols 53

3.10.1 Rheometric Units 53

3.10.2 List of Symbols 54

3.11 Bibliography 56

3.11.1 Primary Sources 56

3.11.2 Other Sources 56

Acknowledgements 57

Ad Hoc Review Committee 58

Index 59

vi
Introduction

1. INTRODUCTION

The use of nomenclature for describing dispersed particulate systems, along

with their associated properties and components, is often inconsistent and subject to misinterpretation in the technical and scientific literature. For example,

terms for describing the state of association of particles in suspension (e.g.,

aggregate or agglomerate) often carry specific connotations that vary among

different authors. This guide has been prepared as a resource for researchers,

engineers and students working in dispersion-based applications. In compiling

this guide, we drew on a number of resources, including books, review articles and published terminologies. To the extent possible, every effort was made to maintain a degree of uniformity with existing standards and conventions,

including published terminologies from the American Concrete Institute (ACI), the British Standards Institute (BSI), the International Union of Pure

and Applied Chemistry (IUPAC) and the Society of Rheology, as well as current and draft ASTM and ISO standards.

We intend this guide to serve as a resource for practitioners working in various

fields in which ceramic dispersions are used, where ceramic is broadly defined

as a non-metallic inorganic material. Equations have been used sparingly, and

only where necessary for clarity or where they are integral to the subject at hand. This is not, nor is it intended to be, an exhaustive compilation. Rather,

this document focuses on commonly encountered terms, and endeavors to provide a consistent framework for improved technical communication.

The technical nomenclature portion of this guide is divided into two sections.

The first section is derived from Special Publication 945, and deals with

general topics related to dispersion science and technology, such as particle

agglomeration and colloidal stability. The second section is based on Special

Publication 946, and provides definitions of terms and expressions relating to the measurement of rheological properties in liquid-based ceramic dispersions

(i.e., suspensions, pastes and gels). In addition to the glossaries of basic terms, the guide is organized so that the

reader can more readily locate related terms associated with specific subject

areas. Defined terms are indicated in boldface type. Where alternative or equivalent terms exist, they are shown in brackets adjacent to the preferred

term. Terms used in definitions, and which are defined separately in the guide,

are indicated in italic at their first appearance in that paragraph or section. The

only exception to this rule is the term viscosity in Part II, which is not

italicized when it appears by itself, due to its ubiquity throughout the text. Descriptions of instrumentation provided in this guide are generic in nature,

and are presented solely for the purpose of identifying key measurement

techniques and their associated nomenclature.

1
Nomenclature for Dispersion Technology

2. NOMENCLATURE FOR DISPERSION TECHNOLOGY

2.1 Physical Description of Dispersed Systems

2.1.1 Primary Terms

aerosol

Droplets or particles dispersed in a gaseous phase,

continuous phase

Constituting the medium, a phase that exhibits continuity throughout the

dispersion; e.g., the liquid in a suspension.

dispersed phase [discontinuous phase]

In a dispersion, the phase that is distributed in the form of discrete discontinuities (particles, droplets or bubbles), in a second immiscible phase that is continuous.

dispersion

In general, a two-phase system in which discontinuities of any kind (solid,

liquid, gas) are dispersed in a continuous phase of a different composition or

state; more specifically in the field of ceramics, the term dispersion is used to describe a suspension of solid particles in a liquid medium.

emulsion

A dispersion consisting of two or more liquid phases,

hydrosol

A sol in which water forms the dispersion medium,

liquid phase

Consisting of a condensed fluid; e.g., the dispersion medium in a suspension.

organosol

A sol in which an organic liquid forms the dispersion medium.

particulate phase [solid phase]

The particles in a suspension, gel or aerosol.

slip

A term that refers to a suspension prepared for the expressed purpose of consolidating the solid phase (e.g., by slip-casting, tape-casting or spray drying).

2
Primary Terms

slurry

A concentrated ceramic particulate suspension.

sol A liquid dispersion containing particles of colloidal dimensions,

suspension

A liquid in which solid particles are dispersed.

2.1.2 Related Terms

heterodisperse

Describes a polydisperse particulate system in which more than one discrete

size distribution mode occurs; e.g., bimodal, trimodal, etc. monodisperse

Realistically, all dispersions exhibit a finite spread in their particle size distri- bution. In practice, the term monodisperse can be used to identify a dispersed

system in which all particles are of nearly the same size, forming a narrow

(unimodal) distribution about an average value. Numerically, a dispersion may

be considered monodisperse if 90 % of the distribution (1.645 a, where a is the standard deviation of the size distribution) lies within ±5 % of the average

size, (d):

<d>

polydisperse

Describes a dispersed system in which many particle sizes occur. In practice, a system may be considered polydisperse if less than 90 % of the size distribution (1.645 a, where a is the standard deviation of the size distribution) lies within ±5 % of the average size, (d): !^>0.05

(d)

well-dispersed

A term used to describe a stable suspension in which the minimum particle

size has been achieved.

3
Nomenclature for Dispersion Technology

2.1.3 Recommendations

relative concentration terms

It is recommended that relative descriptive terms relating to particle concentration in suspension (e.g., dilute or concentrated) be defined in such a manner

that the reader has a clear understanding of their relevance to the measurement

or application at hand. For instance, in a light scattering measurement, "dilute"

may infer the absence of multiple scattering, whereas in an ultrasonic meas- urement this term may imply a linear response with concentration. These

conditions may vary by several orders of magnitude with respect to particle

concentration. Concentration can also by defined on a more fundamental basis,

taking into consideration the relative dominance of thermal, hydrodynamic. or surface forces in controlling suspension properties.

2.2 States of Subdivision (Dispersed Phase)

2.2.1 Definitions Based on Size

nanosize [nanophase]

A special state of subdivision implying that the particles (or atomic clusters)

have average dimensions smaller than roughly 1 00 nm, and exhibit properties not normally associated with the bulk phase (e.g., quantum optical effects).

colloid

State of subdivision implying that the particles have at least in one direction a dimension roughly between 1 nm and 1 um. Colloids are significantly affected

by Brownian motion when suspended in a liquid.

ultrafine

State of subdivision implying that the particles have in any given direction a maximum dimension lying roughly between 1 um and 10 um.

fine [subsieve range]

State of subdivision implying that the particles have in any given direction a maximum dimension less than roughly 37 um.

coarse [sieve range]

State of subdivision implying that the particles have in at least one direction a dimension greater than roughly 37 jam.

4
Definitions Based on Size

granule

State of subdivision generally referring to dry particulates with dimensions

lying roughly in the 50 urn to 200 urn range; typically, granules are aggregates of finer particles produced by spray-drying. Granulation is performed for ease of handling during subsequent consolidation operations.

2.2.2 Definitions Based on Structure

particle

Any condensed-phase tridimensional discontinuity in a dispersed system may

generally be considered a particle; e.g., droplets in an emulsion or solids dis- persed in a liquid. The term is normally used in reference to solid materials.

An aggregate may also be regarded as a particle.

droplet

Liquid-phase particle in an emulsion or aerosol.

particulate

Composed of distinct particles.

primary particle

Smallest identifiable subdivision in a particulate system. Primary particles

may also be subunits of aggregates.

microsphere

Refers to a spherical particle in the micrometer size range,

aggregate

A cohesive mass consisting ofparticulate subunits.

hard-aggregate

An aggregate that cannot be easily redispersed by the application of moderate

mechanical agitation (shaking, stirring, or ultrasonication) and/or mild chemical treatment. Hard-aggregates consist of subunits that have been chemically

bonded orfused.

agglomerate

In a suspension, an aggregate held together by physical or electrostatic forces,

coagulate [coagulum]

In a suspension, an aggregate formed by the addition of electrolyte.

5
Nomenclature for Dispersion Technology

floe In a suspension, an aggregate formed by the addition of a polymer. Floes are generally characterized by a loose structure (low density).

powder

A relatively dry, undispersed accumulation ofparticulate matter with a macroscopic consistency.

gel

Bicontinuous structure with a solid and a liquid component. The solid network

may consist ofparticles or polymers, held together by covalent, ionic or dis- persion (physical) forces. The network may be elastic, viscoelastic or plastic.

The scale of the mesh of the network (distance between cross links) is of

colloidal dimensions.

aerogel

A porous solid produced from a gel in such a way that very little shrinkage

occurs. Typically, the term refers to materials made by supercritical extraction

of the solvent, although structurally equivalent materials can be made under

ambient conditions by increasing network stiffness and/or elastic recovery, and

by reducing interfacial tension.

alcogel

A gel containing an alcoholic liquid phase,

hydrogel

A gel containing an aqueous liquid phase,

xerogel

Porous solid made by drying a gel under subcritical conditions.

2.2.3 Related Terms

average agglomeration number (AAN)

An estimate of the degree of agglomeration in a suspension. AAN is the aver- age number ofprimary particles contained within an agglomerate. AAN is calculated from the ratio of the median particle size, as determined by, for example, light scattering, sedimentation or electrical zone sensing techniques.

6
Related Terms

to the average equivalent spherical volume (VBET) given by the BET gas

adsorption method, such that: AAN = — = \—^

VBET I 6 ) where V50 is the equivalent spherical volume calculated from the median

diameter, D50 in um, SSA is the specific surface area in m2/g and p is the

particle density in g/cm3

.

equivalent spherical diameter

The diameter of a sedimenting particle determined from Stokes' law and

assuming a spherical shape. The term is sometimes used in conjunction with

other measurement techniques and theoretical constructs, where spherical

geometry is assumed.

fractal

A structure that has an irregular geometry under all scales of observation (i.e.,

it is non-Euclidian). The fractal dimension of a species, Df

, is the exponent to which a characteristic length scale must be raised to obtain proportionality

with the overall size of the species. Destabilized suspensions tend to form

aggregates with fractal structures. In this case, Df has a value lying between 1 and 3, where Df=3 is a fully dense object,

minimum particle size (MPS)

An experimental quantity operationally defined as the minimum particle size that can be achieved by a particular dispersion process as determined by an

appropriate measurement technique. The characteristic dimension used in determining the MPS should be clearly noted (e.g., mean size, median size,

modal size, etc.).

ultimate working unit

An individual particle or group of particles that retains its structure throughout

a dispersion process and subsequent application. See also minimum particle

size.

2.2.4 Recommendations

floccule

It is recommended that this term not be used in the ceramic literature, (see

floe)

7
Nomenclature for Dispersion Technology

hard, soft With the exception of the defined term hard-aggregate, it is recommended that such adjectives be avoided in the context of dispersed phase structure. If their use is deemed necessary to convey material-specific information, then the

author should make a clear statement that defines the meaning and extent of

usage.

2.3 Association and Dissociation Processes

2.3.1 Association Processes

aggregation

A general term defined as any process by which particles collect to form a cohesive mass or cluster; the resulting structure is called an aggregate.

agglomeration

Formation of aggregates in a suspension through physical (van der Waals,

hydrophobic) or electrostatic forces. The resulting structure is called an

agglomerate.

coagulation

A specific type of agglomeration in which formation of aggregates is induced

by the addition of electrolyte to a suspension. The resulting structure is termed the coagulate or coagulum, while the electrolyte additive is termed the

coagulant.

flocculation

Formation of aggregates in a suspension mediated by polymeric species, that are either attached to the particles or exist freely in the suspending medium.

The resulting structure is called a floe, while the polymer additive is termed a flocculant. Polymer bridging is a flocculation process.

gelation

Formation of a continuous (space-filling) solid network characterized by a

finite static shear modulus (stress/strain ratio); results from percolation of

bonds between particles or polymers. The resulting structure is termed a gel.

fusion

Process by which particles form irreversibly bonded structures; often characterized by the appearance of interparticle necks, (see also hard-aggregates)

8
heteroagglomeration, heterocoagulation, heteroflocculation

Generally refers to the aggregation of dissimilar particles; in ceramic applications, the formation of aggregates by the cohesion between particles of

different materials (e.g., alumina and silica).

orthokinetic aggregation

The process of aggregation induced by hydrodynamic motions, such as

stirring, sedimentation or convection.

perikinetic aggregation

The process of aggregation induced by Brownian motion.

sol-gel Process for making a gel from colloidal or molecular precursors.

2.3.2 Dissociation Processes

deagglomeration

Reversal of agglomeration, i.e., the dispersion of agglomerates to form a suspension.

deflocculation

Reversal offlocculation, i.e., the dispersion offloes to form a suspension.

comminution

Breaking down large pieces to the required size; term commonly used in association with milling of ceramic slurries.

peptization

Refers to the reversal of agglomeration by the addition of a strong acid or strong base, such as HC1 or NaOH.

2.3.3 Related Terms

diffusion-limited rate Refers to a rate of aggregation corresponding to the frequency of encounter

(collision rate) of the particles. Each collision results in particle adherence

(i.e., a sticking probability equal to 1). The rate of encounter is controlled by

the diffusion rate, which depends on the viscosity of the medium, the dimensions of the particles, and the concentration of the particles.

9
Nomenclature for Dispersion Technology

reaction-limited rate Refers to a rate of aggregation that is controlled by the reactivity of the

particles (i.e., the frequency of collisions resulting in particle sticking).

Usually characterized by a sticking probability much less than 1 . A low

sticking probability results from the presence of an energy barrier.

syneresis

Spontaneous shrinking of a gel with exudation of liquid,

ultrasonication

Application of high-energy, high-frequency sound to a suspension in order to disperse aggregates. Dispersion is thought to arise from the energy released

during fluid cavitation.

2.3.4 Recommendations

sonication, sonification

It is recommended that these terms not be used in the ceramic literature,

(see ultrasonication)

2.4 Dispersion Stability

2.4.1 States of Stability

colloidal stability

A physical state that characterizes the relative ability of colloids to remain

dispersed in a liquid; suspensions that do not aggregate at a significant rate are said to be colloidally stable. The precise connotation depends on the time

frame under consideration. Colloidal stability is a form of kinetic stability, and

is therefore considered a metastable thermodynamic state. From this perspective, aggregation may be described as a transition from a metastable to a stable state, occurring at rates that depend on the magnitude of the activation

energy barrier that separates them.

kinetic stability

Most dispersed systems are thermodynamically unstable, relative to their separate bulk phases; however, a dispersion may exist for an appreciable

length of time and therefore exhibit kinetic stability. The term may be used in reference to various destabilizing processes, e.g., aggregation, coalescence or sedimentation.

10
States of Stability

stable suspension

A suspension that has sufficient kinetic stability to prevent the occurrence of

significant aggregation as measured over a relevant time frame. Stability may

be ascertained by suitable experimental means, such as particle size, turbidity or sedimentation measurements.

unstable suspension

A suspension that lacks kinetic stability as measured over a relevant time

frame; a highly unstable suspension is one that is subject to rapid {diffusionlimited) aggregation.

2.4.2 Stability Mechanisms

electrostatic stabilization

Mechanism in which aggregation is inhibited by the presence of a mutually

repulsive electrostatic potential that surrounds each particle.

steric stabilization

Mechanism in which aggregation is inhibited by the presence of an adsorbed

polymer layer that is firmly anchored to the particle surface so as not to desorb during collisions. In general, a steric stabilizing agent has one portion

of its structure that exhibits low solubility in the dispersion medium and/or

high affinity for the particle surface, and the other portion is soluble in the

medium.

electrosteric stabilization

Mechanism in which aggregation is inhibited by the combined effects of electrostatic and steric stabilization. Usually associated with the adsorption of

polyelectrolytes onto the particle surface.

depletion stabilization

Mechanism in which aggregation is inhibited by the presence of free (non-adsorbed) polymer due to the creation of high-energy depletion zones

(i.e., depleted of polymer compared to the bulk solution) between closely

interacting particle surfaces.

2.4.3 Interaction Terms

DLVO

An abbreviation for a theory of the stability of colloidal dispersions describing

the pair-wise interaction between charged particles in a dielectric medium. The

11
Nomenclature for Dispersion Technology

theory, derived independently by Derjaguin and Landau, and by Verwey and

Overbeek, calculates the opposing effects of attractive van der Waals forces

and repulsive electrostatic forces on the interaction potential.

interaction potential

The potential free energy between two surfaces, typically presented as a function of separation distance. By convention, a positive potential is mutually

repulsive and a negative potential is mutually attractive. primary maximum

The first appearance of a maximum in the interaction potential energy curve with increasing separation distance. The primary maximum results from the

fact that repulsive and attractive forces decay at different rates as a function of

separation distance. In DLVO theory, a large primary maximum acts as an energy barrier, preventing aggregation ofparticles into the primary minimum.

primary minimum

The first appearance of a minimum in the interaction potential curve with

increasing separation distance. The primary minimum results from the fact that repulsive and attractive forces decay at different rates as a function of

separation distance. In DLVO theory, a deep (negative) primary minimum

acts as an energy well, allowing particles to adhere and resulting in a loss of

colloidal stability.

secondary minimum

A shallow energy minimum (usually of the order of a few kT) in the interaction potential curve occurring at relatively large separation distances beyond

that of the primary maximum. In the presence of such an energy well, secondary minimum aggregation may occur. Because of the shallow nature of the

secondary minimum, the aggregates formed are held together weakly and as such tend to be unstable toward rather small energy inputs such as stirring.

Born repulsion [hard core repulsion]

As two surfaces are brought into close contact, the attractive van der Waals

force between them increases continuously. At some point in their approach,

the electron clouds of the two surfaces begin to overlap, giving rise to a repulsive force termed the Born or hard core repulsion. This results in a steep

increase in the interaction potential curve at very small interatomic separation

distances, becoming effectively infinite when interpenetration occurs.

solvation [structural] forces

Non-DLKO forces that occur at extremely small separation distances (typically

12
a few molecular diameters) when particles interact through an intervening

fluid medium. These forces arise whenever liquid molecules are induced to order into quasi-discrete layers between surfaces, and can result in a monotonically increasing (repulsive), monotonically decreasing (attractive) or oscillatory

interaction potential In aqueous solvents these forces may be referred to as hydration forces. Hamaker constant

In the case ofparticle interactions, a material constant that measures the rela- tive strength of the attractive van der Waals forces between two surfaces.

Particles interacting through an intervening fluid medium will experience a reduced attractive potential due to the presence of the third component.

hard sphere interaction

A largely theoretical construct in which the interaction potential between

approaching particles is assumed to equal zero, except upon contact where it goes abruptly to infinity (i.e., no interpenetration occurs).

noninteracting

If no barrier to particle approach, contact and adherence exists, the particles

are said to be noninteracting. If the primary minimum is sufficiently deep,

every collision will result in particles sticking together. The rate of aggregation will then be kinetically controlled {diffusion-limited rate).

2.4.4 Related Terms

critical coagulation concentration (CCC)

The molar concentration of electrolyte, C , necessary to induce rapid

(diffusion-limited) aggregation. Experimentally determined by extrapolation

of In W versus In C to In W=0, where W is the stability ratio. coagulant

An electrolyte additive that induces coagulation in a suspension.

Schulze-Hardy rule

An empirical rule summarizing the general tendency of the critical coagulation concentration to vary inversely with the sixth power of the

counter ion charge number of added electrolyte.

lyotropic series

An ordered series of ions indicating, in decreasing order, their effectiveness in

13
Nomenclature for Dispersion Technology

influencing the behavior of colloidal dispersions. Typically associated with an

ion's relative propensity to coagulate a dispersion.

stability ratio

Ratio of the diffusion-limited to reaction-limited rate constants for aggregation. A large ratio indicates a high degree of colloidal stability, whereas a ratio of unity indicates that diffusion-limited conditions prevail and the

system is colloidally unstable. The rate constants are determined experimentally

from the initial rates of aggregation. Usually denoted by the symbol, W.

defoaming agent [antifoaming agent]

A surfactant that, when present in small amounts, prevents the formation of a foam or aides in the coalescence of bubbles.

dispersing agent [stabilizing agent, dispersant]

A substance that, when present in small amounts, facilitates the dispersion of

aggregates and improves the kinetic stability ofparticles. For example,

polyelectrolytes are often used as dispersing agents in ceramic processing.

surface active agent [surfactant]

A substance that lowers the interfacial tension between the solution in which it is dissolved, and other phases which are present (e.g., solid particles in a suspension), and, accordingly, is positively adsorbed at the interface.

polyelectrolyte

A macromolecular substance that, on dissolving in water or other ionizing

solvent, dissociates to give polyions (polycations or polyanions) - multiple

charged ions - together with an equivalent amount of counter ions. A

polyelectrolyte can be a polyacid, a polybase, a polysalt or a polyampholyte.

Frequently used as dispersing agents in ceramic slurries.

sedimentation

The settling of suspended particles or droplets due to the influence of gravity or an applied centrifugal field.

sedimentation volume

The volume ofparticulate sediment formed in a suspension. If the sediment is formed in a centrifugal field, the strength of this field should be explicitly

indicated, otherwise normal gravity is understood.

Brownian motion [thermal motion]

Random fluctuations in the density of molecules in a liquid, due to thermal

14
Related Terms

energy, cause other molecules and small dispersed particles to move along

random pathways. This random motion is termed Brownian motion, and is most noticeable for colloidal particles.

coacervation

When a colloidal suspension loses stability, a separation into two liquid phases

may occur. This process is termed coacervation. The phase that is more

concentrated in the colloid is the coacervate, and the other phase is the

equilibrium solution.

2.4.5 Recommendations

deflocculant, dispersing aid

It is recommended that these terms not be used in the ceramic literature,

(see dispersing agent)

2.5 Interfacial and Electrokinetic Properties

2.5.1 The Interface

interface

A boundary between two immiscible phases, at least one of which is condensed. Experimentally, the portion of the sample through which the first derivative of any concentration versus location plot has a measurable departure

from zero. In a suspension, the region of contact between the particle surface

and the suspending medium.

interfacial region [interphase]

The region that exists between two phases where the properties vary from

those in the bulk.

surface region

The tridimensional region, extending from the free surface of a condensed

phase towards the interior, where the properties differ from the bulk.

electrical double layer (EDL)

The term describes the non-random array of ions at an interface in which two

oppositely charged layers coexist. For particles dispersed in a fluid, the EDL

consists of the surface charge and the solution charge. The solution charge

may be further subdivided into Stern and diffuse layers, which is often referred

to as the triple layer model.

15
Nomenclature for Dispersion Technology

double layer thickness

Length characterizing the decrease of potential with distance from a charged

interface. Typically defined as 1/k, where k is the Debye-Huckel parameter.

For low potentials it represents the distance over which the potential falls to

lie or about one third, of the value of the surface potential.

diffuse layer

The region surrounding a suspended particle in which non-specifically

adsorbed ions are accumulated and distributed by the opposing action of the

electric field and thermal motion.

Stern layer [compact layer]

Counter and co-ions in immediate contact with a surface are said to reside in the Stern layer, and form with the fixed surface charge a molecular capacitor.

Often equated with the immobile portion of the electrical double-layer that exists inside the shear plane.

inner Helmholtz plane (IHP)

At a charged interface, an imaginary plane representing the distance of closest approach of desolvated ions to the surface, and containing the ions or molecules that are specifically adsorbed.

outer Helmholtz plane (OHP)

At a charged interface, an imaginary plane representing the distance of closest approach of solvated (hyrdrated) ions to the surface. Often equated with the

position of the shear plane.

shear plane [plane of shear, surface of shear]

In calculating the electrokinetic potential from electrokinetic phenomena it is often assumed that a sharp plane separates the liquid adhering to the solid

surface from the mobile liquid. This imaginary plane is considered to lie close

to the solid surface.

2.5.2 Adsorption Processes

adsorption

The process by which a substance is accumulated at an interface or in an

interfacial region. Should not be confused with absorption, which denotes

accumulation inside a material or phase.

adsorbate

A substance that is adsorbed at the interface or into the interfacial region of a substrate material or adsorbent.

16
Adsorption Processes

adsorbent

The substrate material onto which a substance is adsorbed,

adsorption isotherm

The relationship between the equilibrium quantity of a substance adsorbed and

the composition of the bulk phase, at constant temperature.

specific adsorption

Ions are specifically adsorbed when they are present in the Stern layer in amounts that exceed those expected from simple electrostatic considerations.

Empirically, ions that are specifically adsorbed have a noticeable effect on the

isoelectric point.

non-specific adsorption

Ions are non-specifically adsorbed when they are kept in the interphase only

by long-range coulombic interactions. They are believed to retain their

solvation shell and in the position of closest approach to the interface they are separated from it by one or more solvent molecular layers. Empirically, ions

that are non-specific (indifferent) have no measurable effect on the value of the

isoelectric point.

chemical adsorption [chemisorption]

Molecules are chemically adsorbed when they exist within the Stern layer and

form bonds with the surface groups, which have a significant valence contribution. Empirically, ions that are chemically adsorbed have a noticeable effect on the isoelectric point of a suspension and exhibit a significant enthalpy

(heat of adsorption).

physical adsorption [physisorption]

Adsorption in which the forces involved are intermolecular (i.e., van der

Waals, hydrogen bonding) of the same kind as those responsible for the

non-ideality of real gases and the condensation of vapors, and which do not

involve a significant change in the electronic orbital patterns of the species

involved.

monolayer adsorption

Adsorption in which only a single layer of molecules becomes adsorbed at an

interface. In monolayer adsorption, all adsorbed molecules are in the position

of closest approach to the substrate surface. multilayer adsorption

Adsorption in which more than a single layer of molecules is adsorbed at the

interface. Molecules adsorbed in excess of monolayer adsorption are not in

the position of closest approach to the substrate surface.

17
Nomenclature for Dispersion Technology

coadsorption

The simultaneous adsorption of two or more species,

desorption

The process by which the amount of an adsorbed substance is reduced.

2.5.3 Electrical Properties

isoelectric point (IEP)

For many ceramic systems, the pH at which dispersed particles show no elec- trophoretic mobility and the zeta potential has a value of zero. More generally,

the pi value at which zeta is zero, where / is the potential determining ion.

point of zero charge (PZC)

A particle carrying no fixed charge. The precise identification of pzc depends on the definition adopted for surface charge. Typically for ceramic systems,

the pH at which hydroxyl and proton adsorption is just balanced to cancel net charge; here, the hydroxyl and proton are defined as the charge determining

species.

surface charge density

The quantity of electrical charge accumulated at a particle-solution interface,

expressed per unit area; usually represented by the symbol a .

streaming potential

When a liquid under a pressure gradient is forced through a capillary or porous

plug, excess charges (ions) near the wall are swept along by the liquid creating an accumulation of charge downstream. An electric field is also created, which

opposes this accumulation. After a steady state has been established, the

measured potential difference across the capillary or plug is called the

streaming potential and is related to the pressure gradient and to the shear

plane potential.

zeta potential [electrokinetic potential, shear plane potential]

The potential drop, across the mobile part of the electrical double layer, that

is responsible for the electrokinetic phenomena. C, is positive if the potential

increases from the bulk of the liquid phase towards the shear plane. Certain

assumptions or estimations regarding the double layer properties must be

made in order to calculate £ from experimental data. It is therefore essential to indicate in all cases which equations have been used in the calculation of

It can be shown, however, that for the same assumptions about the double

18
Electrical Properties

layer properties, all electrokinetic phenomena must give the same value for the

electrokinetic potential.

potential determining ions

Those species of ions that by virtue of their equilibrium distribution between

two phases determine the difference in Galvani potential between these

phases. They are often, but not always, identical with the ions that stabilize a

colloidal suspension formed from these phases.

co-ions

In systems containing large ionic species (e.g., colloids), co-ions are those

that, compared to the large ions, have low molecular mass and the same

polarity. For instance, in a suspension of negatively charged particles

containing sodium chloride, the chloride ions are co-ions and the sodium

ions are counterions.

counterions

In systems containing large ionic species (e.g., colloids), counterions are those

that, compared to the large ions, have low molecular mass and the opposite

polarity. For instance, in a suspension of negatively charged particles

containing sodium chloride, the sodium ions are counterions and the chloride

ions are co-ions.

charge reversal

The process wherein a charged particle is caused to assume a new charge of

the opposite polarity. Such a change can be brought about by oxidation,

reduction, dissociation, adsorption or ion exchange.

2.5.4 Electrokinetic Effects

electrokinetics

Referring to the relative motions of charged species in an electric field. The

field may be applied, or it may be created by the motion of a liquid or adjacent

solid phase.

electro-osmosis

When a liquid moves in response to an applied electric field, while an adjacent

solid phase remains stationary (e.g., in a capillary or porous plug), this is called electro-osmotic flow. Fluid motion is due to the reaction of charged

species within the fluid, usually dissolved ions, to the applied field.

19
Nomenclature for Dispersion Technology

electrophoresis

The motion of charged particles in an applied electric field,

electrophoretic mobility (static, dynamic)

The electrophoretic velocity per unit field strength, symbol ue=v/£; ue

is positive if the particle moves toward lower potential and negative in the

opposite direction. When measured in a d.c. electric field, ue

is referred to as the static mobility. When measured in a high-frequency field it is referred to as the dynamic mobility, and given the symbol ud or u(co). Dynamic mobility

may be a complex quantity at high frequencies.

electroacoustics

Referring to the electric-acoustic coupling in a fluid containing charged

colloids or ions; an effect that is responsible for the electrokinetic sonic

amplitude, colloid vibration potential and ion vibration potential.

acoustophoresis

The induced motion ofparticles subjected to an acoustic field. Charged

particles will generate an electric field as a result of this motion

(see ultrasonic vibration potential).

ultrasonic vibration potential (UVP)

When a sound wave propagates through a fluid containing charged particles

(ions or colloids), coherent acoustophoretic motion of the particles creates alternating dipoles that generate a macroscopic potential difference termed the

ultrasonic vibration potential.

ion vibration potential (IVP)

The ultrasonic vibration potential of an ionic solution; also known as the

Debye effect.

colloid vibration current (CVI)

The alternating electrical current generated by the vibration potential of a

colloidal suspension. The CVI is related to dynamic mobility of the particles;

related to colloid vibration potential.

colloid vibration potential (CVP)

The ultrasonic vibration potential of a colloidal suspension. The resulting

potential difference is related to the dynamic mobility of the particles; reciprocal effect to electrokinetic sonic amplitude.

20
Electrokinetic Effects

electrokinetic sonic amplitude (ESA)

When a high-frequency alternating electric field is applied to a dispersion of

charged colloids, the oscillatory electrophoretic motion of the particles relative

to the surrounding medium results in a measurable acoustic field whose amplitude is related to the dynamic mobility, reciprocal effect of colloid vibration

potential. The phase difference between the applied field and the resulting

acoustic response can also be used to estimate the particle size distribution.

2.5.5 Related Terms

amphoteric

Refers to a type of surface in which the same surface group (reactive site) is able to function as both an acid and a base. That is, the site may dissociate to release a proton or accept a proton.

zwitterionic

Refers to a type of surface in which two distinct surface groups (reactive sites) are present. One is capable of dissociating to release a proton (acid group), and

the other is capable of accepting a proton (base group).

hydrophilic

May be used to describe the character of interaction of a particular atomic

group (or substance) with an aqueous medium. In this usage the term has the

relative qualitative meaning of "water loving." The more general term,

lyophilic ("solvent loving"), is used to distinguish a class of colloidal systems.

hydrophobic

The tendency of hydrocarbons (or of lipophilic hydrocarbon-like groups in solutes) to form intermolecular aggregates in an aqueous medium, and

analogous intramolecular interactions. In this usage the term has the relative

qualitative meaning of "water fearing." The more general term, lyophobic

("solvent fearing"), is used to distinguish a class of colloidal systems.

indifferent electrolyte [supporting electrolyte]

An ionic solution, whose constituents are not electroactive (i.e., they have no

significant effect on the surface potential of the material under study; no

oxidative or reductive capacity) in the range of applied potentials being studied,

and whose ionic strength (and, therefore, contribution to the conductivity) is usually much larger than the concentration of an electroactive substance to be

dissolved in it. The ions constituting an indifferent electrolyte are said to exhibit no specificity for the particle surface.

21
Nomenclature for Dispersion Technology

A measure of electrolyte concentration given by 7= 7/4Xcz z^, where cf are the

concentrations, in moles per liter, of the individual ions, i, and zz are their ion

charge numbers.

Debye-Hiickel parameter

A parameter in the Debye-Hiickel theory of electrolyte solutions, denoted as k. For aqueous solutions at 25 °C, k=3.288V/ in reciprocal nanometers, where /

is the ionic strength. See double layer thickness.

double layer compression [screening]

Increasing ionic strength causes the electrical potential near a charged surface

to fall off more rapidly with distance. This is referred to as double layer compression or screening, because the double layer thickness shrinks as the Debye-Hiickel parameter increases with increasing ionic strength.

electroviscous effects For dispersions of charged particles, these are those components of the

viscosity connected with the charge on the particles.

suspension effect The Donnan e.m.f. between a suspension and its equilibrium liquid. The

effect is most commonly encountered with pH measurements in colloidal

suspensions.

potentiometric analysis

Analysis based on the measurement of electrical potential using, for example,

a pH or ion-selective electrode. Potentiometry is often combined with

titrimetric analysis in the determination ofparticle surface charge.

titrant

The solution containing the active agent with which a titration is made,

titration

The process of determining the amount of a substance A by adding increments

of substance B with provision for some means of recognizing the point at which all of A has reacted. This allows the amount of A to be found from the

known amount of B added up to this point.

titrimetric analysis

Analysis of test sample properties based on titration.

22
2.6 Bibliography

2.6.1 Primary Sources

Compendium of Chemical Terminology - IUPAC Recommendations, Compiled

by V. Gold, K.L. Loening, A.D. McNaught, and P. Sehmi, Blackwell Scientific

Publications, Oxford, UK, 1987.

L.L. Schramm, The Language of Colloid and Interface Science - A Dictionary

of Terms, American Chemical Society, Washington, DC, 1993.

RJ. Hunter, Foundations of Colloid Science, Volume 1, Oxford University

Press, Oxford, UK, 1989.

P.C. Hiemenz and R. Rajagopalan, Principles of Colloid and Surface

Chemistry, 3rd Edition, Marcel Dekker, NY, 1997.

G.Y. Onoda and L.L. Hench, "Physical Characterization Terminology,"

Chapter 5, pp. 35-37 in Ceramic Processing Before Firing, Edited by G.Y.

Onoda and L.L. Hench, John Wiley & Sons, NY, 1978.

2.6.2 Other Sources

Adsorption ofInorganics at Solid-Liquid Interfaces, Edited by M.A. Anderson

and A.J. Rubin, Ann Arbor Science Publishers, Ann Arbor, MI, 1981.

Chemical Processing of Ceramics, Edited by B.I. Lee and E.J.A. Pope, Marcel

Dekker, NY, 1994.

Sample Preparation for the Determination ofParticle Size Distribution of

Ceramic Powders, ISO/DIS 14703, 1998.

Particle Size Analysis: Dispersing Agents for Powders in Liquids, ISO

Working Document 14887, 1997.

Surface and Colloid Chemistry in Advanced Ceramics Processing, Edited by

R.J. Pugh and L. Bergstr~m, Marcel Dekker, NY, 1994.

Ultrasonic and Dielectric Characterization Techniques for Suspended

Particulates, Edited by V.A. Hackley and J. Texter, American Ceramic

Society, Westerville, OH, 1998.

23
Bibliography

CJ. Brinker and G.W. Scherer, Sol-Gel Science, Academic Press, NY, 1990.

D.F. Evans and H. Wennerstrom, The Colloidal Domain, VCH Publishers, NY,

1994.

E.K. Fischer, Colloidal Dispersions, John Wiley & Sons, NY, 1950.

R.J. Hunter, Zeta Potential in Colloid Science - Principles and Applications,

Academic Press, NY, 1981.

D. Myers, Surfaces, Interfaces, and Colloids - Principles and Applications,

Chapter 10, "Colloids and Colloidal Stability," VCH Publishers, NY, 1991.

D.H. Napper, Polymeric Stabilization of Colloidal Dispersions, Academic

Press, NY, 1983.

R.H. Ottewill, "Stability and Instability in Dispersed Systems," Journal of

Colloid and Interface Science, 58, 357-373 (1977).

Th.F. Tadros, "Control of the Properties of Suspensions," Colloids and

Surfaces, 18, 137-173 (1986).

Acknowledgements

A number of terms were included courtesy of the American Chemical Society

from the book by L.L. Schramm. Some definitions contained in the

Compendium of Chemical Terminology were used, in part or in whole, courtesy of the International Union on Pure and Applied Chemistry.

List of Reviewers

James H. Adair, Merrilea J. Mayo

The Pennsylvania State University, Particulate Materials Center

Jon A. Casey

IBM, Materials Technology

Robert A. Condrate

Alfred University, New York State College of Ceramics

Matthew Frey, William Hunt, Thomas Wood

3M Company, Ceramic Technology Center

24
Acknowledgements

George Y. Onoda (retired), Ajit Jillavenkatesa

National Institute of Standards and Technology, Ceramics Division

Robert J. Hunter

University of Sydney, School of Chemistry, Australia

George W. Scherer

Princeton University, Department of Chemical Engineering

Ponisseril Somasundaran

Columbia University, Langmuir Center for Colloids and Interfaces
Nomenclature for Rheological Measurements

3. NOMENCLATURE FOR RHEOLOGICAL MEASUREMENTS

3.1 Fundamental Rheological Properties

elastic A conservative property in which part of the mechanical energy used

to produce deformation is stored in the material and recovered on release of

stress.

electroviscous The collective effects by which the presence of an electrical double-layer influences the flow behavior of a liquid. The double-layer is usually associated with charged particles suspended in the liquid or

polyelectrolytes dissolved in solution. There are three electroviscous effects: primary The increase of fluid viscosity due to distortion of the double

layer during shear. Distortion exerts a drag, increasing energy dissipation.

secondary The increase of fluid viscosity due to the interaction or overlap of adjacent double-layers. Responsible for the formation of

gelatin.

tertiary The variation in fluid viscosity that arises from geometrical

changes within the fluid due to double-layer interactions. The viscosity

of a polyelectrolyte solution depends on the conformation of the

molecules, which in turn is affected by intramolecular electrostatic interactions between charged segments located along the polymer

backbone or on side chains.

plastic The property of a solid body that is in the elastic state when the stress

is below a critical value, termed the yield stress, and in the plastic state when

this value is exceeded. During ideal plastic flow, energy dissipation and stress are independent of the rate of deformation.

viscoelastic A time-dependent property in which a material under stress produces both a viscous and an elastic response. A viscoelastic material will

exhibit viscous flow under constant stress, but a portion of mechanical energy

is conserved and recovered after stress is released. Often associated with

polymer solutions, melts and structured suspensions, viscoelastic properties

are usually measured as responses to an instantaneously applied or removed

constant stress or strain or a dynamic stress or strain.

viscoelectric An effect by which the electric field near a charged interface

influences the structure of the surrounding fluid and thereby modifies the

viscosity of the fluid. 26
Fundamental Rheological Properties

viscoplastic A hybrid property in which a material behaves like a solid

below some critical stress value, the yield stress, but flows like a viscous liquid when this stress is exceeded. Often associated with highly aggregated sus- pensions and polymeric gels.

viscous The tendency of a liquid to resist flow as a result of internal friction. During viscous flow, mechanical energy is dissipated as heat and the stress that develops depends on the rate of deformation.

3.2 Functional Forms of Viscosity

Viscosity nomenclature related to oscillatory measurements is defined here in general terms, but is described more explicitly in section 3.7. apparent viscosity, r|app The value of viscosity evaluated at some nominal

average value of the shear rate. The apparent viscosity applies, for instance, in the capillary method, where a range of shear rates are employed.

coefficient of fluidity [fluidity], (|) Reciprocal of the coefficient ofviscosity.

(p = 1 /ri

coefficient of viscosity [viscosity], r| The ratio of shear stress to shear rate under simple steady shear. The abbreviated form "viscosity" is used most

often in practice, and is frequently employed without discriminating between

Newtonian and non-Newtonian behavior. When the quotient is independent

of shear rate (i.e., follows the Newtonian model), it is considered a material

constant. When the quotient is dependent on shear rate (i.e., non-Newtonian),

it should be referred to as the non-Newtonian viscosity.

r\ = <j If

complex viscosity, r\* The frequency-dependent viscosity function deter- mined during forced harmonic oscillation ofshear stress; contains both real and imaginary parts.

differential viscosity, r) diff The derivative of shear stress with respect to shear rate.

rj

diff =da/dy

27
Nomenclature for (theological Measurements

dynamic viscosity, r\' The ratio of the loss modulus to the angular frequency,

determined during forced harmonic oscillation (dynamic) measurements. The

real part of the complex viscosity.

ri'=G"/a)

infinite shear viscosity, The high shear rate limiting value of viscosity.

Often associated with the second Newtonian region in pseudoplastic fluids.

inherent viscosity [logarithmic viscosity], r] inh A natural logarithmic

function of the relative viscosity reduced by the solute concentration.

n'link C

intrinsic viscosity [limiting viscosity number], [nj The zero concentration

limiting value of the reduced specific viscosity. A characteristic function for the single molecule in solution. [r|] is equivalent to the effective hydrodynamic

specific volume for the solute.

[77] = \imr]red c->0 kinematic viscosity, v The ratio of the viscosity of a fluid to its density.

v = Vs /p

out-of-phase viscosity, r) " The ratio of the storage modulus to the angular

frequency, determined during forced harmonic oscillation (dynamic) measurements. The imaginary part of the complex viscosity.

r/"= G'/co

plastic viscosity, r| pl For a Bingham model, the excess of the shear stress over the yield stress divided by the shear rate, and equal to the differential

viscosity. For non-ideal Bingham materials, the differential viscosity determined

in the high-shear limiting, linear portion of the flow curve; associated with

viscoplastic fluids.

77 , = \\mda I dj

28
Functional Forms of Viscosity

reduced viscosity7 [viscosity number], r| red The ratio of any viscosity function to the concentration, c, of the solute or particulate phase. By normalizing

viscosity in this way, concentration effects become more apparent. For

instance, the reduced specific viscosity is: nred =Tlsp /c

relative viscosity [viscosity ratio], r) r Ratio of the viscosity in a suspension

or solution to the viscosity of the suspending medium or solvent.

n, = r

i lris

specific viscosity7

. r| sp The relative viscosity minus unity.

zero shear viscosity7 , rj The low shear rate limiting value of viscosity.

Associated with the first Newtonian region in many pseudoplastic fluids.

r/ =limr/

3.3 Glossary of Basic Terminology

apparent yield stress For non-ideal viscoplastic materials, where the yield

stress is indefinite, an apparent yield stress can be defined, for example, by

extrapolation from the linear, high-shear-rate portion of the flow curve to the

stress axis, (see Bingham relation)

compliance The quotient of strain and stress (e.g., shear compliance). The

reciprocal of modulus.

deformation Movement of parts or particles of a material body relative to one another such that the continuity of the body is not destroyed, resulting in a change of shape or volume or both.

dilatant A property often associated with suspensions of irregularly shaped

particles, in which the liquid exhibits an increase in volume while being

sheared. The term is also used in common practice to mean shear-thickening,

the increasing resistance to shear with increasing shear rate. It is possible for

either of these two effects to exist in the absence of the other.

29
Nomenclature for Rheological Measurements

dynamic equilibrium A state in which dynamic opposing forces just bal- ance to obtain a quasi-equilibrium condition. Dynamic equilibrium is achieved

during steady shear flow when break down and rebuilding of structure occur

at similar rates, and the viscosity is constant at a given shear rate. dynamic [oscillatory] shear flow Condition under which stress and strain

vary harmonically with time during a rheometric experiment.

Einstein's Law of Viscosity Describes the relationship between the viscosity

of a dilute dispersion and the volume fraction of the dispersed particles. The

relationship is derived with two major assumptions, that the particles are solid

spheres and that their concentration is very low.

-3- = l + 2.5 (() + ....

where r| s

is the viscosity of the suspending medium and <|> is the volume

fraction. The factor 2.5 is known as the Einstein coefficient. To describe more

concentrated dispersions, higher terms in the power series have been retained

and analyzed with varying success.

equilibrium [steady state] flow Condition under which a constant stress or shear rate is maintained for a sufficient time to allow dynamic equilibrium to be achieved in a fluid containing time-dependent structure. An equilibrium

flow curve can be used to characterize the time-independent flow properties of

a material.

elastic modulus [modulus of elasticity] A modulus of a body that obeys

Hooke's law.

flow Continuously increasing deformation of a material body under the

action of finite forces. When the force is removed, if the strain does not eventually return to zero, then flow has occurred.

flow curve A graphical representation of the behavior of flowing materials in which shear stress is related to shear rate. Hooke's law Provides that the quotient of stress and strain (i.e., the modulus)

is a constant. A body obeying Hooke's law cannot be viscoelastic nor does

flow occur. laminar flow Flow without turbulence.

30
Glossary of Basic Terminology

modulus The quotient of stress and strain where the type of stress and strain

is defined by the type of deformation employed (e.g., shear modulus in shear

deformation).

Navier-Stokes equations The equations of motion for a Newtonian fluid

model describing the balance between external forces (like gravity), the

pressure force and the viscous force. Newtonian Flow model of fluids in which a linear relationship exists

between shear stress and shear rate, where the coefficient ofviscosity is the constant of proportionality.

no-slip Condition in which fluid adjacent to a surface moves with the

velocity of that surface. The assumption of no-slip is key to most rheometric

measurements. Slippage is a significant concern in concentrated suspensions.

non-equilibrium flow Condition under which shear is varied at a rate that does not permit dynamic equilibrium to be achieved. A thixotropic loop is the

result of non-equilibrium flow conditions during shear cycling.

non-Newtonian Any laminarflow that is not characterized by a linear

relationship between shear stress and shear rate. normal stress, an The component of stress that acts in a direction normal

to the plane of shear.

Peclet number, Pe A dimensionless group used to compare the effect of

applied shear with the effect of thermal (Brownian) motion; Pe=r2 y/D,

where r is the particle radius and D is the translational diffusion coefficient. For Pe « 7, particle behavior is dominated by diffusional relaxation, whereas

fox Pe »1, hydrodynamic effects dominate.

Poiseuille flow Laminarflow in a pipe of circular cross section under a constant pressure gradient, (see also Capillary Methods)

Reynolds number, Re A dimensionless group that expresses the ratio of the

inertial forces to the viscous forces; Re=Dvp/ri, where D is a characteristic

length (e.g., particle size or pipe diameter), v is a typical fluid speed, and r\lp

is the kinematic viscosity of the fluid. The transition from laminar to turbulent

flow is characterized by high Re values.

31
Nomenclature for Rheological Measurements

rheology The science of the deformation and flow of matter. rheometric Refers to the measurement of rheological properties.

shear The relative movement of parallel adjacent layers.

shear compliance, J The ratio of shear strain to its corresponding shear

stress. The reciprocal of shear modulus.

shear modulus [modulus of rigidity], G The ratio of shear stress to its corresponding shear strain. The reciprocal of shear compliance.

shear rate (rate of shear strain), y The rate of change of shear strain with

time (dy / dt). For liquids, the shear rate, rather than strain, is generally used

in describing flow.

shear stress, cr The component of stress that causes successive parallel

layers of a material body to move, in their own planes (i.e., the plane of

shear), relative to each other.

shear strain, y The relative in-plane displacement, Ax, of two parallel layers

in a material body divided by their separation distance, y. Alternatively, the

shear strain can be defined as tan 0, where is the angle of deformation as shown in Figure 1

.

Ax

4

Fig. 1. Shear strain schematic.

shear-thickening An increase in viscosity with increasing shear rate during

steady shearflow. The term dilatant is commonly used in practice to indicate

shear-thickening, although this usage is strictly incorrect.

shear-thinning [pseudoplastic] A decrease in viscosity with increasing

shear rate during steady shearflow.

32
Glossary of Basic Terminology

simple shear In simple shear there is no change in the dimension normal to the plane of shear, and the relative displacement of successive parallel layers

of a material body are proportional to their distance from a reference layer.

The type offlow used in most rheometric measurements on fluids can be

approximated by simple shear.

steady shear flow Condition under which a fluid is sheared continuously in one direction during the duration of a rheometric experiment.

stress Force per unit area.

structure In rheology, structure is a term that refers to the formation of stable physical bonds between particles (or chemical bonds between macromolecules) in a fluid. These bonds result in aggregate, floe, or network structure, which impacts the rheological behavior of the fluid and provides elastic and

plastic properties. The term may be extended to include structural effects caused by electroviscous interactions, physical bonds between polymers

(e.g., associative thickeners), shear-induced alignment of anisotropic particles,

and close-packing (radial distribution) correlations in concentrated suspensions.

The term "structure" is commonly invoked even when little is known about the cause of observed changes in rheological properties.

Weissenberg effect The tendency of some viscoelastic fluids to flow in a

direction normal to the direction of shear. The effect is manifested by behavior such as the climbing of a fluid up a rotating rod. Weissenberg number, Wi A measure of the degree of nonlinearity or the

degree to which normal stress differences are exhibited in a flow. For steady,

simple shear, the Weissenberg number is the product of the shear rate and a

characteristic time of the fluid. In oscillatory shear it is the product of the

shear rate amplitude and the characteristic time of the fluid. In converging

flows it is proportional to the Deborah number.

yield response For non-ideal viscoplastic materials, the yield stress can be

indefinite and yielding may occur continuously over a narrow range of stress values. In this case, the behavior may be more properly termed a yield response.

yield stress, a

y A critical shear stress value below which an ideal plastic or

viscoplastic material behaves like a solid (i.e., will not flow). Once the yield

stress is exceeded, a plastic material yields (deforms plastically) while a

viscoplastic material flows like a liquid.

33
Nomenclature for Rheological Measurements

3.4 Classification of Equilibrium Flow Curves

Steady-shear flow curves for suspensions and solutions measured under equilibrium conditions may exhibit a variety of behaviors over a limited range of

shear rates. Additionally, some materials may exhibit more than one distinct behavior over different shear rate regions of the same flow curve. Several

types of behavior can be classified according to their characteristic shape. The

following classification system covers the six most frequently encountered

flow types as illustrated in the accompanying graph.

1 . Newtonian Differential viscosity and coefficient ofviscosity are constant with shear rate.

2. shear-thickening Differential viscosity and coefficient ofviscosity increase

continuously with shear rate.

3. shear-thinning [pseudoplastic] Differential viscosity and coefficient of

viscosity decrease continuously with shear rate. No yield value.

4. shear thinning [pseudoplastic]

with yield response Differential

viscosity and coefficient ofviscosity

decrease continuously with shear

rate once the apparent yield stress, aann, has been exceeded, app'

5. Bingham plastic (ideal)

Obeys the Bingham relation

ideally. Above the Bingham

yield stress (aBin Figure 2) the

differential viscosity is constant and is called the plastic viscosity,

while the coefficient ofviscosity

decreases continuously to some

limiting value at infinite shear

rate.

shear rate Fig. 2. Identification of flow curves based on their characteristic shape.

6. Bingham plastic (non-ideal) Above the apparent yield stress the

coefficient ofviscosity decreases continuously, while the differential viscosity

approaches a constant value with increasing shear rate. Extrapolation of the

flow curve from the linear, high shear rate region (plastic region) to the

34
Classification of Equilibrium Flow Curves

stress axis gives the apparent Bingham yield stress (gb

* in Figure 2). The

differential viscosity in the linear region is termed the plastic viscosity.

3.5 Expressions for Describing Steady Shear Non-Newtonian

Flow

The expressions shown in this section are used to characterize the non- Newtonian behavior of fluids under equilibrium, steady shearflow conditions.

Many phenomenological and empirical models have been reported in the liter- ature. Only those having a direct and significant implication for suspensions,

gels and pastes have been included here. A brief description of each relationship is given with examples of the types of materials to which it is typically

applied. In defining the number of parameters associated with a particular

model, the term "parameter" in this case refers to adjustable (arbitrary)

constants, and therefore excludes measured quantities. Some of these

equations have alternative representations other than the one shown. More

detailed descriptions and alternative expressions can be found in the sources

listed in the bibliography.

° = °b +rlpiY

y = for a < a B The Bingham relation is a two parameter model used for describing viscoplastic

fluids exhibiting a yield response. The ideal Bingham material is an elastic solid at low shear stress values and a Newtonian fluid above a critical value

called the Bingham yield stress, aB

. The plastic viscosity region exhibits a

linear relationship between shear stress and shear rate, with a constant

differential viscosity equal to the plastic viscosity, r\^.

Carreau-Yasuda

A model that describes pseudoplastic flow with asymptotic viscosities at zero

(r| ) and infinite (r^) shear rates, and with no yield stress. The parameter X

is a constant with units of time, where MX is the critical shear rate at which

viscosity begins to decrease. The power-law slope is (n-1) and the parameter a

Bingham

35
Nomenclature for Rheological Measurements

represents the width of the transition region between rj and the power-law

region. If r| and rj^ are not known independently from experiment, these

quantities may be treated as additional adjustable parameters.

Casson

~l/2 1/2 , 1/2 -1/2 a =ay +ri P

i y

y = for a < a y A two parameter model for describing flow behavior in viscoplastic fluids exhibiting a yield response. The parameter a

y

is the yield stress and r| pl is the

differential high shear (plastic) viscosity. This equation is of the same form as the Bingham relation, such that the exponent is 1/2 for a Casson plastic and 1 for a Bingham plastic.

Cross

rio-rioo

A model, similar in form to the Carreau-Yasuda relation, that describes

pseudoplastic flow with asymptotic viscosities at zero (t\q) and infinite (n,^)

shear rates, and no yield stress. The parameter X is a constant with units of

time, and m is a dimensionless constant with a typical range from 2/3 to 1 . If

r)o and are not known independently from experiment, these quantities

may be treated as additional adjustable parameters.

Ellis

1+ *

a-1 °2/

A two parameter model, written in terms of shear stress, used to represent a pseudoplastic material exhibiting a power-law relationship between shear

stress and shear rate, with a low shear rate asymptotic viscosity. The parameter

g2 can be roughly identified as the shear stress value at which r\ has fallen to half its final asymptotic value.

Herschel-Bulkley

g = oy +kyn

36
Steady Shear Non-Newtonian Flow

A three parameter model used to describe viscoplastic materials exhibiting a yield response with a power-law relationship between shear stress and shear

rate above the yield stress, a

y

. A plot of log (a - a

y

) versus log y

gives a slope n that differs from unity. The Herschel-Bulkley relation reduces to the

equation for a Bingham plastic when w=l.

Krieger-Dougherty

A model for describing the effect of particle self-crowding on suspension viscosity, where O is the particle volume fraction, Om is a parameter representing

the maximum packing fraction and [nj is the intrinsic viscosity. For ideal

spherical particles [r|]=2.5 (i.e., the Einstein coefficient). Non-spherical or highly charged particles will exhibit values for [r\] exceeding 2.5. The value of

[r|] is also affected by the particle size distribution. The parameter Om is a function of particle shape, particle size distribution and shear rate. Both [rj] and Om may be treated as adjustable model parameters.

The aggregate volume fraction (representing the effective volume occupied by

particle aggregates, including entrapped fluid) can be determined using this equation if Om is fixed at a reasonable value (e.g., 0.64 for random close packing or 0.74 for hexagonal close packing) and [r\] is set to 2.5. In this case, O is the adjustable parameter and is equivalent to the aggregate volume fraction.

A model, expressed in terms of shear stress, used to represent a pseudoplastic

material exhibiting a power-law relationship between shear stress and shear

rate, with both high (r| x) and low (r| ) shear rate asymptotic viscosity limits. The parameter a2 can be roughly identified as the shear stress value at which

r| has fallen to half its final asymptotic value. The Meter and Carreau-Yasuda

models give equivalent representations in terms of shear stress and shear rate, respectively. If r) and r| x are not known independently from experiment,

these quantities may be treated as additional adjustable parameters.

Meter

Tlo-Tloo

37
Nomenclature for Rheological Measurements

Powell-Eyring

/ xsinh

_1 (xy)

11 = Tloo + VHo "iW

—. " xy Derived from the theory of rate processes, this relation is relevant primarily

to molecular fluids, but can be used in some cases to describe the viscous

behavior of polymer solutions and viscoelastic suspensions over a wide range

of shear rates. Here, is the infinite shear viscosity, r| is the zero shear

viscosity and the fitting parameter x represents a characteristic time of the

measured system. If r| and are not known independently from experiment, these quantities may be treated as additional adjustable parameters.

power-law [Ostwald-de Waele]

a = Ky n A two parameter model for describing pseudoplastic or shear-thickening

behavior in materials that show a negligible yield response and a varying

differential viscosity. A log-log plot of a versus y

gives a slope n (the powerlaw exponent), where n<l indicates pseudoplastic behavior and n>l indicates

shear-thickening behavior.

3.6 Time-Dependent Effects

Time-dependence includes those effects associated with transient flow conditions as well as those effects associated with irreversible changes that result from shear history.

creep The response of a material to the instantaneous application of a constant stress.

creep function In an applied stress test, where an instantaneous and constant

stress is applied to a material while the shear rate (or shear strain) is measured

over time, the shear rate (or strain) vs. time function is termed the creep

function. The function J(t)=y(t)/F is referred to as the creep compliance.

Deborah number, De The ratio of a characteristic relaxation time of a

material to the duration of the observation. In equilibrium flow, the effective

duration of the experiment is infinity, and De=0. In oscillatory shear, it is the

product of the frequency and the relaxation time of the fluid. In converging

flows, the Deborah number is proportional to the Weissenberg number.

38
Time-Dependent Effects

flow hysteresis A condition resulting from differences in the rate of energy

dissipation due to shear history. In a typical rheometric test, shear stress or shear rate is ramped at a fixed speed up to a maximum value, then ramped

back down at the same speed to the beginning. In hysteresis, one flow curve

lies above the other, forming a continuous loop whose internal area depends on the shear and thermal history of the material, and on how rapidly the stress or shear rate was ramped. If the down-curve lies below the up-curve, then it is referred to as a thixotropic loop, whereas if the down-curve lies above the upcurve, then it is called a negative thixotropic loop.

negative thixotropy [anti-thixotropy] A reversible time-dependent increase

in viscosity at a particular shear rate. Shearing causes a gradual growth in structure over time.

relaxation time, x A time characterizing the response of a viscoelastic

material to the instantaneous application of a constant strain.

retardation time, x A time characterizing the response of a viscoelastic

material to the instantaneous application of a constant stress. rheomalaxis An irreversible decrease of viscosity during shearing.

Attributed to permanent changes in the material structure. rheopexy An effect by which a material recovers some of its pre-sheared vis- cosity at a faster rate when it is gently sheared compared to when it is allowed

to stand. Not to be confused with negative thixotropy.

stress growth When an instantaneous and constant strain (or shear rate) is applied to a material while stress is measured over time, an increasing stress

vs. time or modulus vs. time function is termed stress growth.

stress relaxation When an instantaneous and constant strain (or shear rate)

is applied to a material while stress is measured over time, a decreasing stress

vs. time or modulus vs. time function is termed stress relaxation.

thixotropy A reversible time-dependent decrease in viscosity at a particular

shear rate. Shearing causes a gradual breakdown in structure over time.

3.7 Oscillatory Measurements

forced harmonic oscillation is a dynamic rheometric test in which both stress and strain vary harmonically with time, and both viscous and elastic parame39
Nomenclature for Rheological Measurements

ters are derived from the material response. Such tests are almost always car- ried out in the linear viscoelastic regime, which is characterized by a linear

response of dynamic viscosity and elasticity with increasing strain amplitude.

3.7.1 Material Functions Derived from Oscillatory Tests

In a typical sinusoidal oscillation experiment, the applied stress and resulting

strain wave forms can be described as follows:

c = o cos cot y = y cos (cot - 8)

where a is the stress amplitude

Yo is the strain amplitude

co=27tf is the angular frequency

/ is time

5 is the phase lag (loss angle)

Fig. 3. Sinusoidal wave forms for stress and strain functions.

The phase lag and amplitude ratio (a /y ) will generally vary with frequency,

but are considered material properties under linear viscoelastic conditions. For

an ideal solid, 5=0°, and the response is purely elastic, whereas for a Newtonian fluid yielding a purely viscous response, 5=90°.

The material functions can be described in terms of complex variables having

both real and imaginary parts. Thus, using the relationship:

40
Material Functions De • ^ J from ' - - %

cos x + j sinx = e

JX where j = V-T

Then the stress and strain can be expressed as follows:

G=ft(p e

ja>t )

where (Yo^'J 5

) is termed the complex strain amplitude. The shear storage

modulus [or storage modulus, for short], which represents the in-phase

(elastic) component of oscillatory flow, is defined as: G' = storage modulus ^cos5

Yo The out-of-phase (viscous) component is termed the shear loss modulus

[or loss modulus, for short]:

G" = loss modulus = —sin 5

Yo The complex shear modulus, G*, is then defined as follows:

complex stress amplitude a an . . _ G* = = —- cos 5 + —- j sin o complex strain amplitude y y

so that: G* = G' + jG"

Tan 5 = G"/G'

The function G7G' measures the

relative importance of viscous to

elastic contributions for a material

at a given frequency.

Additionally, a complex viscosity, rj*, can be defined using the complex strain

rate, y = jcoy, such that:

Fig. 4. Vectorial representation of moduli.

complex stress amplitude

complex strain rate amplitude jy co _o_ e

j 8 = G*/

41
Nomenclature for Rheological Measurements

or alternatively

where r)' is termed the dynamic viscosity, and is equivalent to the ratio of the

stress in phase with the rate of strain (a sin 5) to the amplitude of the rate of

strain (coyq). The term r)" is referred to as the out-of-phase viscosity, and is equivalent to the ratio of the stress 90° out of phase with the rate of strain (a

cos 8) to the amplitude of the rate of strain (coyo) in the forced oscillation.

Finally, an absolute shear modulus is defined as the ratio of the amplitude of

the stress to the amplitude of the strain in forced oscillation {simple shear), or:

Alternatively, forced oscillation experiments can be equivalently described in terms of compliance, as opposed to the derivation above based on the modulus. Similar arguments lead to the following analogous terms: complex shear compliance, J* The ratio of the complex strain (y*) to complex stress (g*) in forced oscillation (simple shear).

shear storage compliance, J' The ratio of the amplitude of the strain in phase with the stress (y cos 5) to the amplitude of the stress (a ) in forced

oscillation (simple shear).

shear loss compliance, J" The ratio of the amplitude of the strain 90° out of

phase with the stress (y sin 8) to the amplitude of the stress (a ) in forced

oscillation (simple shear).

absolute shear compliance, \J*\ The ratio of the amplitude of the strain (y ) to the amplitude of the stress (a ) in forced oscillation (simple shear).

G* = ^L = (G ' 2 +G"2 )

1/2 Yo

42
Measurement Apparatus

3.8 Measurement Apparatus

There are two common methods used for rheometric measurements on fluid

systems: capillary (or tube) and rotational. In this section, a brief summary is given for each general method along with descriptions of common measure- ment devices and geometries. Measurement devices can be grouped into one

of two general classifications. A viscometer is a device used principally for the measurement of viscosity, while a rheometer is a device used for the

measurement of rheological properties over a varied and extended range of

conditions. More detailed descriptions of these instruments and methods can

be found in the primary sources listed in the bibliography. Only a brief

coverage is provided here.

3.8.1 Capillary Methods

In capillary methods the test fluid is made to flow through a narrow tube as a result of hydrostatic or applied pressure. Capillary measurements are considered the most precise way of determining the viscosity of Newtonian

and some non-Newtonian viscous fluids, and are generally simpler in design

and less expensive relative to rotational instruments. Poiseuille's Law, which

relates the rate of flow through a capillary to the viscosity of the liquid, is the

basis for the capillary method.

Glass Capillary Viscometer

Widely used for measuring the viscosity of Newtonian fluids, including dilute

solutions and suspensions, the glass capillary viscometer is the simplest and

least expensive viscometric system available commercially. Typically, in this technique, the time required for a given volume of fluid to flow through a defined length, L, of glass capillary under its own i — —

hydrostatic head is measured. The flow time, t, is related to the viscosity using a simple relationship

derived from Poiseuille's Law, of the form: / \

Fig. 5. Ostwald type capillary viscometer. A

and B are timing marks, C is a filling mark.

L

43
Nomenclature for Rheological Measurements

where A and B are instrument constants. The second term on the right hand

side is related to the kinetic energy correction, and can be ignored for long

flow times. In this case, a simple linear equation results. The viscometer can be easily calibrated using a standard fluid with known viscosity at the

measurement temperature. Capillaries with different diameters can be used for

different viscosity ranges, while maintaining reasonable flow times.

Extrusion Capillary Viscometer

These instruments are widely used for measuring viscous fluids, such as asphalt cements, polymer melts, and stable concentrated suspensions.

Extrusion viscometers have the advantage of high precision and simple design,

and are less subject to temperature effects that can occur during shearing of

highly viscous fluids in rotational devices.

Fig. 6. Diagram of a simple extrusion viscometer.

Extrusion viscometers use a cylindrical piston to force the test fluid from a reservoir through the capillary tube at a constant velocity. By measuring the

pressure drop across the capillary as a function of flow rate for multiple

capillaries of the same diameter, d, but differing length, L, it is possible to determine the viscosity as a function of shear rate.

3.8.2 Rotational Methods

In rotational methods the test fluid is continuously sheared between two

surfaces, one or both of which are rotating. These devices have the advantage

of being able to shear the sample for an unlimited period of time, permitting

transient behavior to be monitored or an equilibrium state to be achieved,

under controlled rheometric conditions. Rotational methods can also incorporate oscillatory and normal stress tests for characterizing the viscoelastic

properties of samples. In general, rotational methods are better suited for the

measurement of concentrated suspensions, gels and pastes, but are generally

less precise as compared to capillary methods.

44
Rotational measurements fall into one of two categories: stress-controlled or

rate-controlled. In stress-controlled measurements, a constant torque is applied to the measuring tool in order to generate rotation, and the resulting

rotation speed is then determined. If a well-defined tool geometry is used, the

rotation speed can be converted into a corresponding shear rate. In rate- controlled measurements, a constant rotation speed is maintained and the

resulting torque generated by the sample is determined using a suitable stress- sensing device, such as a torsion spring or strain gauge. Some commercial

instruments have the capability of operating in either stress-controlled or

rate-controlled modes.

Simple Rotational Viscometer ("Brookfield type")

The least expensive commercial variant of the controlled-rate rotational

viscometer is commonly referred to as a "Brookfield type" viscometer. This

device measures fluid viscosity at fixed rotation speeds by driving a measurement tool ("spindle"), immersed in the test fluid, through a

calibrated torsion spring. Viscous drag of the fluid against the spindle causes

the spring to deflect, and this deflection is correlated with torque. The

calculated shear rate depends on the rotation speed, the tool geometry and

he size and shape of the sample container. Conversion factors are needed

to calculate viscosity from the measured

torque, and are typically pre-calibrated for

specific tool and container geometries. For

Newtonian fluids the torque is proportional

to the product of viscosity and rotational

speed, but this proportionality is lost in the case of a non-Newtonian fluid. Because

these instruments are robust and fairly

simple to use, they have found wide

application in industry, but they offer limited capabilities and precision for research-oriented applications.

Rotational Rheometer

High-precision, continuously-variableshear instruments in which the test fluid

is sheared between rotating cylinders, cones or plates, under controlled-stress or controlled-rate conditions, are termed

rotational rheometers. Instruments producing oscillatory strains are

available, and a few commercial

Fig. 7. Schematic diagram

of a Brookfield-type

viscometer.

45
nomenclature for Rheological Measurements

systems permit measurement of the normal stress. The basic rotational system

consists of four parts: (i) a measurement tool with a well-defined geometry,

(ii) a device to apply a constant torque or rotation speed to the tool over a wide range of shear stress or shear rate values, (iii) a device to determine the

stress or shear rate response, and (iv) some means of temperature control for the test fluid and tool. Depending on the design specifications, rheometers may

also include built-in corrections or compensations for inertia, drift, and temperature fluctuations during measurement.

Most rheometers are based on the relative rotation about a common axis of one of three tool geometries: concentric cylinder, cone and plate or parallel

plates (See Figure 8).

V?/.W///////////////M'/SA V//////////,s/M//////m W//,s//M//////,s/,s///X

(a) (b) (c)

Fig. 8. Schematic diagram of basic tool geometries for the

rotational rheometer: (a) concentric cylinder, (b) cone and plate,

(c) parallel plate.

In the concentric cylinder (also called Couette or Coaxial) geometry either

the inner, outer or both cylinders may rotate, depending on instrument design.

The test fluid is maintained in the annulus between the cylinder surfaces. This

tool geometry comes in several configurations, of which the three most com- monly encountered are illustrated in Figure 9. The double-gap configuration

is useful for low viscosity fluids, as it increases the total area, and therefore

the viscous drag, on the rotating inner cylinder, and generally increases the

accuracy of the measurement. The cone and hollow cavity configurations are

specifically designed to reduce or account for end effects. In addition, to prevent slippage, the inner cylinder surface is sometimes serrated or otherwise

46
Rotational Methods

roughened. The concentric cylinder geometry is typically used for the analysis

of fluid suspensions.

(a) (b) (c)

Fig. 9. Schematic diagram showing three alternative cylindrical

tool designs in cut-away view: (a) double gap, (b) cone and plate

at the bottom, (c) hollow cavity at the bottom to trap air.

The cone and plate geometry consists of an inverted cone in near contact with a lower plate. The cone is usually designed with an angle of less than 4°. Either the upper or lower surface may rotate depending on instrument design.

The parallel plate geometry can be considered a simplified version of the cone and plate, having an angle of 0°. The test fluid is constrained in the arrow gap between the two surfaces. Cone and plate and parallel plate

measurement tools are most often used for highly viscous pastes, gels, and

concentrated suspensions.

3.9 Concrete and Other Coarse-Grained Materials

Ceramic materials are typically fabricated from particles in the subsieve or

fine size range (i.e., less than roughly 37 |im), though coarse agglomerates

may play a role during some phase of processing. On the other hand, concrete

is classified as a ceramic material, but containing a considerably broader range

of particle sizes, from less than one micrometer up to about 20 mm (i.e., well

into the sieve range). This wide range results from the heterogeneous concrete composition, which includes cement (5 (im to 60 |Lim), mineral fillers (< 1 |Lim to 100 jam), fine aggregates (0.1 mm to 5 mm) and coarse aggregates (4 mm

to 30 mm or higher in some special concretes) or stones.

47
Nomenclature for Rheological Measurements

As a result of the broad range of particle sizes and the presence of sieve-size

particles, methods to measure the flow properties of concrete differ significantly from those methods specified for applications involving suspensions of fine

particles. Test methods applied to concrete tend to be largely empirical in nature or they are scaled up versions of the techniques described in section 3.8 for fine particle suspensions. In the former case are the most commonly used

tests in the industry; they generally represent an attempt to "imitate" a mode of

placement or flow of the concrete during production. In the latter case are less common methods that attempt to measure fundamental rheological properties

of concrete. In addition, rheological test methods for concrete tend to fall into one of four general categories:

confined flow The material flows under its own weight or under an applied

pressure through a narrow orifice. The orifice is defined as an opening roughly

three to five times larger than the maximum particle size. Because coarse aggregates are often of the order of 30 mm, the orifice must typically be

90 mm to 150 mm in diameter. Confined flow methods include flow cone,

filling ability devices, flow test through an opening and the Orimet apparatus.

free flow The material either flows under its own weight, without any

confinement or an object penetrates the material by gravitational settling. Free flow methods include slump, modified slump, penetrating rod and turning tube

viscometer.

vibration The material flows under the influence of applied vibration. The

vibration is applied by using a vibrating table (e.g., Ve-Be time or remolding

test), dropping the base supporting the material (DIN slump cone test), an

external vibrator (e.g., LCL apparatus) or an internal vibrator (e.g., settling

method).

rotational rheometers The material is sheared between two parallel

surfaces, one or both of which are rotating. These tests are analogous to rheometers described in section 3.8.2, except in this case the gap between sur- faces must be scaled up to reflect the much larger dimensions of the concrete

particles. Rotational rheometers include BTRHEOM, CEMAGREF, two-point

or Tattersall, IBB, and BML.

Separate glossaries of rheological terms and test methods are provided below.

For more detailed summaries of the numerous rheological tests used throughout the concrete industry, including empirical tests that are widely implemented, see Ferraris (1999) in the list of primary sources.

48
Glossary of Rheological Terms

3.9.1 Glossary of Rheological Terms

Much of the rheological work on concrete and other cementitious materials

has, historically, been directed toward the practical exploitation of the material

and, as a result, numerous terms are in common use that are unique to the

concrete, mortar and cement industries. The most frequently encountered

rheological terms are defined here.

consistency The relative mobility or ability of freshly mixed concrete or mortar to flow; the usual measurements are slump for concrete, flow for mortar or grout, and penetration resistance for neat cement paste, (see: normal

consistency, plastic consistency, wettest stable consistency)

consistency factor A measure of grout fluidity, roughly analogous to

viscosity, that describes the ease with which grout may be pumped into pores

or fissures; usually a laboratory measurement in which consistency is reported

in degrees of rotation of a torque viscometer in a specimen of grout.

consolidation The process of inducing a closer arrangement of the solid

particles in freshly mixed concrete or mortar, during and after placement until

setting, by the reduction of voids. Consolidation is accomplished by vibration,

centrifugation, rodding, tamping or some combination of these actions. This

term is also applicable to similar manipulation of other cementitious mixtures,

soils, aggregates or the like.

finishing Leveling, smoothing, consolidating and otherwise treating the

surfaces of fresh or recently placed concrete or mortar to produce the desired

appearance and service.

impending slough Consistency of a shotcrete mixture containing the

maximum amount of water such that the product will not flow or sag after placement.

mobility The ability of fresh mixed concrete or mortar to flow.

normal consistency (1) The degree of wetness exhibited by a freshly mixed

concrete, mortar, or neat cement grout when the workability of the mixture is considered acceptable for the purpose at hand. (2) The physical condition of

neat cement paste as determined with the Vicat apparatus in accordance with a standard test method (e.g., ASTM C 187).

49
Nomenclature for Rheological Measurements

plastic consistency Condition of freshly mixed cement paste, mortar or concrete such that deformation will be sustained continuously in any direction

without rupture.

slump A measure of consistency of freshly mixed concrete, mortar or stucco equal to the subsidence measured to the nearest 5 mm (1/4 in) of the molded

specimen after removal of the slump cone.

wettest stable consistency The condition of maximum water content at which cement grout and mortar will adhere to a vertical surface without

sloughing.

workability [placeability] That property of freshly mixed concrete or mortar

that determines the ease and homogeneity with which it can be mixed, placed,

consolidated and finished.

3.9.2 Glossary of Test Methods

BML Commercial rotational rheometer derived from the two-point test. The

principle of operation is identical to the two-point test, but the shape of the vane has been modified. The vane is as shown in Figure 10(c).

<

(a) (b)

Fig. 10. Various vane geometries used in concrete rheometers:

(a) two-point test or Tattersall, (b) IBB, (c) BML.

50
Glossary of Test Methods

BTRHEOM Commercial parallel plate concrete rheometer. Measurements

can be performed with and without applied vibration.

CEMAGREF Coaxial rotational rheometer originally developed for testing

fluid lava. It has been occasionally employed to test concrete. Only one prototype currently exists. DIN slump cone test A vibration method. A variation of the slump cone test in which the cone is placed on a metal sheet. After filling the cone with concrete, it is lifted and the metal support sheet is raised on one side and dropped

from a pre-established height (usually about 1 00 mm) a specified number of

times. The spread of the concrete is measured. This standard test is described

in DIN 1045.

filling ability Confinedflow method measuring the ability of concrete to flow into a predefined form. Several different molds are used: U-shaped and

L-shaped are the most common. In both cases the concrete is forced by gravity

to flow into and fill the mold. The volume occupied by the concrete at the

end of the test is a measure of the ability of the concrete to flow or its filling

ability.

flow cone [V-funnel cone] Confinedflow method consisting in filling a funnel with concrete or cement paste and determining the time for the material

to flow out through the orifice. This time is a measure of the material's ability to flow. There are several types of funnel, some with round and others with

parallel piped orifice and upper opening.

flow test Used in accordance with ASTM CI 362. This test measures the flow

of concrete or mortar into a perforated tube. This method is applicable for concrete with coarse aggregates less than 37.5 mm in diameter. The instrument

consists of a hollow perforated tube that is inserted in the concrete sample,

after which the material is allowed to flow into the hollow tube. The height of

the concrete in the hollow tube is considered a measure of the consistency of

the concrete. IBB Commercially available rotational rheometer. It is derived from the two- point test. The principle of operation is identical, but the vane shape has been

modified, and the vane moves in a planetary motion and on its axis. The vane

is shaped like the letter H and is shown in Figure 10(b).

LCL apparatus A vibration method. The concrete is poured behind a gate in a large parallel piped container. The gate is opened and the vibrator is turned

51
-Y* --^ ?-^->--

-'-r-i fA: -1- ^= ^'--^ Y^,-;-'- v -^A^YY --YYY. : Y r-YYfVtYr

on. The time for the concrete to y/ow and occupy the whole container is measured. A longer time suggests a lower ability of the concrete to flow. modified slump test Modification of the slump test described in ASTM

CI 43. It permits the measurement of the rate at which the concrete is slumping, which gives an estimate of the concrete plastic viscosity. This test was developed at NIST, but is not currently a standard method (see Ferraris

(1999) in primary sources).

Orimet apparatus Confinedflow method instrument consisting of a tube

600 mm in length that is closed at the bottom by a removable trap door. The

time for the concrete to flow through the tube once the trap is released is determined. This time is a measure of the ability of concrete to flow.

penetrating rod Free flow method measuring the distance a rod of fixed mass can penetrate a concrete sample. It is a crude determination of whether

the yield stress of the concrete is higher or lower than a predefined value. It is used to monitor concrete at the job site. A specific application of this test is the Vicat apparatus.

settling method [Fritsch test] A vibration method, this test measures the

capability of concrete to consolidate under vibration. Concrete is placed in a container with an internal vibrator. The time to obtain full consolidation is measured. The full consolidation is determined when the surface of the concrete no longer moves. slump cone test Free flow method in which a truncated metal cone, open at both ends and sitting on a horizontal surface, is filled with concrete and lifted gradually. The slump of the concrete is measured. This standard test is described in ASTM CI 43.

turning tube viscometer Freeflow method consisting of a tube 60 mm in diameter and 800 mm long that can be filled with cement paste or mortar. A

ball is dropped into the fluid and its velocity is measured between two points

370 mm apart. Using the Stokes equation, the viscosity can be calculated.

two-point test [Tattersall rheometer] First commercially available rotational rheometer for concrete. It is the first attempt to shear concrete at different

rates and to measure the induced stress. It consists of a bucket filled with

concrete and a vane, shown in Figure 10(a), that rotates at controlled speeds.

The torque generated during rotation is measured.

52
Glossary of Test Methods

Ve-Be time [remolding test] Measures the ability of concrete to change

shape under vibration. Concrete is placed in a slump cone. After the cone is lifted away, the time it takes for the concrete to remold itself into a cylinder

while under vibration is measured.

Vicat apparatus Afree flow method, the Vicat apparatus is a penetration

device used in the testing of hydraulic cements and similar materials. The

full description of this instrument and the correct procedure to determine the

normal consistency of cement is described in ASTM CI 87.

3.10 Units and Symbols

3.10.1 Rheometric Units

All units should conform to the International System of Units (SI) as defined

by the National Institute of Standards and Technology. 1 The use of CGS and

other non-SI units is discouraged. For convenience, SI units are shown in Table 1 in association with their common non-SI equivalents (including decimal submultiples and conversion factors where appropriate). Table 2 shows

the Si-derived units with their underlying base units. Table 1. SI and equivalent rheometric units.

Quantity SI Units Equivalent CGS Units

viscosity Pa • s 10 P (poise) or 1000 cP (centipoise)

kinematic viscosity m2 • s"

1 104 St (stoke) or 106 cSt (centistoke)

shear stress Pa 0.1 dyn • cm"2 strain unitless

shear rate s1 S"

1 modulus Pa 0.1 dyn • cm-2 compliance Pa" 1 10 cm2 • dyn-1 frequency Hz

angular frequency 27Tf phase angle rad

1 B.N. Taylor, Guide for the Use ofthe International System of Units (SI), NIST Special Publication 811, 2nd Edition, National Institute of Standards and Technology, U.S. Government

Printing Office, Washington, DC, 1995.

53
Nomenclature for Rheological Measurements

Table 2. SI derived units expressed in terms of SI base units.

Symbol Special Name Other SI Units SI Base Units

Pa Pascal N-m-2 kg • nr 1

• s" 2 Hz Hertz s-1 rad radian m • nr 1 =1

3.10.2 List of Symbols

a shear stress an

llUlllldl oil Coo a

y

ctrpcc yiClU JllCJS

1//

c train oil dill Y shear rate [rate of shear strain]

De Deborah number

Pe Peclet number

Re Reynolds number

*1 coefficient of viscosity [viscosity]

^laop "rr apparent viscosity

Tl A iff lain differential viscosity

lnnniie snear viscosity

^inh inherent viscosity

M intrinsic viscosity

Tired reduced viscosity nr relative viscosity ns viscosity of suspending medium or solvent n sp specific viscosity

"Ho zero shear viscosity

V kinematic viscosity

fluidity

G shear modulus

G* complex shear modulus

G' shear storage modulus

G" shear loss modulus

\G*\ absolute shear modulus

77* complex viscosity

n' dynamic viscosity (real component of the complex viscosity)

n" imaginary component of the complex viscosity

54
: .!,

-

. * S

J shear compliance

J* complex shear compliance

J' shear storage compliance

J" shear loss compliance

1 7"*| ausoiuie snear compliance

Ti iciaAallUll llllic, l Clal ualiuil nine a Ml Cos aliipilLUtiC YO strain amplitude

5 phase angle

CO angular frequency

/ frequency
3.11 Bibliography

This bibliography cites sources used in the compilation of this guide. It is not, nor is it intended to be, an exhaustive list of references available on the vast subject of rheology or rheological instrumentation. Nevertheless, it may serve

as a good starting point for those who are relatively new to this field or searching for relatively fundamental information.

3.11.1 Primary Sources

American Concrete Institute, Cement and Concrete Terminology, ACI 116R-90,

ACI Manual of Concrete Practice 2000, Part I, Farmington Hills, ML

British Standards Institution, Glossary ofRheological Terms, BS 5168:1975.

A.A. Collyer and D.W. Clegg, Editors, Rheological Measurement, Chapman

and Hall, London, 1998.

J.M. Dealy, "Official Nomenclature for Material Functions Describing the

Response of a Viscoelastic Fluid to Various Shearing and Extensional

Deformations," Journal ofRheology, 39[1], 253-265 (1995).

C.F. Ferraris, "Measurement of the Rheological Properties of High

Performance Concrete: State of the Art Report," Journal ofResearch ofthe

National Institute ofStandards and Technology, 104[5], 461-478 (1999).

A. Kaye, R.F.T. Stepto, W.J. Work, J.V. Alem-n and A.Ya. Malkin, "Definition

of Terms Relating to the Non-Ultimate Mechanical Properties of Polymers,"

IUPAC Recommendations 1997, Pure and Applied Chemistry, 70, 701-754

(1998).

3.11.2 Other Sources

H.A. Barnes, "Shear-Thickening ("Dilatancy") in Suspensions of

Nonaggregating Solid Particles Dispersed in Newtonian Liquids," Journal of

Rheology, 33[2], 329-366 (1989).

M. Bohdanecky and J. Kovr, Viscosity ofPolymer Solutions, Elsevier,

Amsterdam, 1982.

56
E. C. Bingham, "An Investigation of the Laws of Plastic Flow," U.S. Bureau of

Standards Bulletin, 13, 309-353 (1916).

F.R. Eirich, Editor, Rheology - Theory and Applications, Vol. 1, Academic

Press, NY, 1956; Vol. 3, 1960; Vol. 4, 1967.

J.W. Goodwin, "Rheology of Ceramic Materials," Ceramic Bulletin, 69 [10],

1694-1698 (1990).

P.C. Hiemenz and R. Rajagopalan, Principles of Colloid and Surface

Chemistry, 3rd Edition, Chapter 4, pp. 145-192, Marcel-Dekker, 1997.

R.J. Hunter, "Rheology of Colloidal Dispersions," Chapter 18 in Foundations

of Colloid Science, Vol. 2, Oxford University Press, NY, 1989.

J. Mewis and A.J.B. Spaull, "Rheology of Concentrated Dispersions,"

Advances in Colloid and Interface Science, 6, 173-200 (1976).

D. Quemada, "Models for Rheological Behavior of Concentrated Disperse

Media under Shear", pp. 571-582 in Advances in Rheology, Vol. 2: Fluids,

Universidad Nacional Autonoma de Mexico, Mexico, 1984.

H.N. Stein, "Rheological Behavior of Suspensions," pp. 3-48 in Encyclopedia

ofFluid Mechanics, Vol. 5: Slurry Flow Technology, Gulf Publishing

Company, Houston, 1986.

J.R. Van Wazer, J.W. Lyons, K.Y. Kim, and R.E. Colwell, Viscosity and Flow

Measurement - A Laboratory Handbook ofRheology, Interscience Publishers,

New York, 1963.

R.W. Whorlow, Rheological Techniques, Ellis Horwood Ltd., Chichester, 1980.

A.A. Zaman, Techniques in Rheological Measurements: Fundamentals and

Applications, Instructional Module, NSF Engineering Research Center for

Particle Science and Technology, University of Florida, Gainesville, 1998.

Acknowledgments

American Concrete Institute, International Union of Pure and Applied

Chemistry (IUPAC), and The Society of Rheology (Journal of Rheology)

have kindly granted permission to use or adapt their published definitions in

57
Acknowledgements

developing the current document. Their publications are fully cited in the list of primary sources shown above. Extracts from BS 5168:1975 are reproduced

with the permission of British Standards Institution under license number

PDM999 0296. Complete copies of the standard can be obtained by post from

BSI Customer Services, 389 Chiswick High Road, London W4 4AL.

Ad Hoc Review Committee

Lennart Bergstrom

YKI (Institute for Surface Chemistry), Stockholm, Sweden

John M. Dealy

Faculty of Engineering, McGill University, Montreal, Canada

Edward J. Garboczi

Leader, Inorganic Materials Group, National Institute of Standards and

Technology, Gaithersburg, MD

Robert J. Hunter

School of Chemistry, University of Sydney, Sydney, Australia

Kamal Khayat

Department of Civil Engineering, University of Sherbrooke, Sherbrooke,

Canada

Francois de Larrard

Methodes et Materiels de Construction et d'Entretien des Routes, Laboratoire

Central des Ponts et Chaussees, Bouguenais, France

Makio Naito

Japan Fine Ceramics Center, Nagoya, Japan

Celik Ozyildirim

Virginia Transportation Research Council, Charlottesville, VA

Ponserril Somasundaran

Langmuir Center for Colloids & Interfaces, Department of Chemical

Engineering, Columbia University, New York, NY

Abbas A. Zaman

NSF Engineering Research Center for Particle Science & Technology,

University of Florida, Gainesville, FL

58
Index

Index

A

AAN. See average agglomeration

number

acoustophoresis, 20

adsorbate, 16

adsorbent, 17

adsorption, 16

chemical, 17

monolayer, 17

multilayer, 17

non-specific, 17

physical, 17

specific, 17

adsorption isotherm, 17

aerogel, 6

aerosol, 2

agent

antifoaming, 14

defoaming, 14

dispersing, 14

stabilizing, 14

surface active, 14

agglomerate, 5

agglomeration, 8

aggregate, 5

aggregation, 8

orthokinetic, 9

perikinetic, 9

alcogel, 6

amphoteric, 21

anti-thixotropy. See thixotropy,

negative

average agglomeration number, 6

B

Bingham equation, 35

BML, 50

Born repulsion, 12

Brownian motion, 14

BTRHEOM, 51

C

capillary methods, 43

Carreau-Yasuda equation, 35

Casson equation, 36

CCC. See critical coagulation

concentration

CEMAGREF, 51

charge reversal, 19

chemisorption, 17

coacervation, 15

coadsorption, 18

coagulant, 13

coagulate, 5

coagulation, 8

coagulum. See coagulate

coaxial. See concentric cylinder

coefficient of fluidity, 27

co-ions, 19

colloid, 4

comminution, 9

compact layer, See Stern layer

compliance, 29

absolute shear modulus, 42

complex shear, 42

shear, 32

shear loss, 42

shear storage, 42

concentration. See relative

concentration terms

concentric cylinder, 46

cone configuration, 46

double-gap configuration, 46

hollow cavity configuration, 46

confined flow methods, 48

consistency, 49

normal, 49

59
plastic, 50

wettest stable, 50

consistency factor, 49

consolidation, 49

Couette. See concentric cylinder,

counterions, 19

creep, 38

creep function, 38

critical coagulation

concentration, 13

Cross equation, 36

CVP. See potential, colloid vibration

D

deagglomeration, 9

deborah number, 38

Debye effect. See potential, ion

vibration

Debye-H,ckel parameter, 22

defloceulant. See agent, dispersing

deflocculation, 9

deformation, 29

desorption, 18

diffuse layer, 16

dilatant, 29

dispersant, 14

dispersing aid. See agent, dispersing

dispersion, 2

DLVO, 11 double layer. See electrical double

layer

double layer compression, 22

droplet, 5

dynamic equilibrium, 30

E

EDL. See electrical double layer

Einstein coefficient, 30

Einstein's law of viscosity, 30

elastic, 26

electrical double layer, 15

electroacoustics, 20

electroactive. See indifferent

electrolyte

electrokinetics, 19

electrokinetic sonic amplitude, 21

electro-osmosis, 19

electrophoresis, 20

electroviscous, 26

electroviscous effects primary, 26

secondary, 26

tertiary, 26

Ellis equation, 36

emulsion, 2

equivalent spherical diameter, 7

ESA. See electrokinetic sonic

amplitude

F

filling ability, 51

finishing, 49

floe, 6

flocculation, 8

floccule, 7

flow, 30

dynamic shear, 30

equilibrium, 30

laminar, 30

non-equilibrium, 3

1

oscillatory. See flow, dynamic

shear

steady shear, 33

steady state. See flow, equilibrium

flow cone, 51

flow curve, 30

Bingham plastic, ideal, 34

Bingham plastic, non-ideal, 34

Newtonian, 34

pseudoplastic with yield, 34

shear-thickening, 34

60
shear-thinning with yield, 34

shear-thinning, 34

flow hysteresis, 39

flow test, 51

fluidity. See coefficient of fluidity

forced harmonic oscillation, 39

fractal, 7

free flow methods, 48

Fritsch test. See settling method

fusion, 8

G

gel, 6

gelation, 8

granule, 5

H

Hamaker constant, 13

hard core repulsion. See Born

repulsion

hard sphere interaction, 13

hard-aggregate, 5

Herschel-Bulkley equation, 36

heteroagglomeration, 9

heterocoagulation, 9

heterodisperse, 3

heteroflocculation, 9

Hooke's law, 30

hydration forces. See solvation

forces

hydrogel, 6

hydrophilic, 21

hydrophobic, 21

hydrosol, 2

IIBB, 51

IEP. See isoelectric point

IHP. See plane, inner Helmholtz

impending slough, 49

indifferent electrolyte, 21

interface, 15

interfacial region, 15

interphase, 15

ionic strength, 22

isoelectric point, 18

IVP. See potential, ion vibration

K

Krieger-Dougherty equation, 37

L

LCL apparatus, 51

limiting viscosity number. See

viscosity, intrinsic

loss angle. See phase lag

lyophilic. See hydrophilic

lyophobic. See hydrophobic

lyotropic series, 13

M

Meter equation, 37

microsphere, 5

minimum particle size, 7

mobility (concrete), 49

mobility

dynamic, 20

electrophoretic, 20

static, 20

modified slump test, 52

modulus, 31

absolute shear, 42

complex shear, 41

elastic, 30

shear, 32

shear loss, 41

shear storage, 41

61
4 ^mmm.

modulus of elasticity. See modulus,

elastic

modulus of rigidity. See modulus,

shear

monodisperse, 3

MPS. See minimum particle size

N

nanosize, 4

Navier-Stokes equations, 31

Newtonian, 31

noninteracting, 13

non-Newtonian, 31

no-slip, 31

O

OHP. See plane, outer Helmoltz, 2

Orimet apparatus, 52

Ostwald-de Waele equation. See

power-law

outer Helmholtz plane, 16

P

particle, 5

coarse, 4

fine, 4

primary, 5

ultrafine, 4

particulate, 5

Peclet number, 31

penetrating rod, 52

peptization, 9

phase

continuous, 2

discontinuous, 2

dispersed, 2

liquid, 2

particulate, 2

solid, 2

phase lag, 40

physisorption, 17

placeability. See workability

plane

inner Helmholtz, 16

outer Helmholtz, 1

6

shear, 16

plane of shear. See plane, shear

plastic, 26

point of zero charge, 18

Poiseuille flow, 31

Poiseuille's Law, 43

polydisperse, 3

polyelectrolyte, 14

potential

colloid vibration, 20

electrokinetic, 19

interaction, 12

ion-vibration, 20

shear plane, 1

8

streaming, 18

ultrasonic vibration, 20

zeta, 18

potential determining ions, 19

potentiometric analysis, 22

powder, 6

Powell-Eyring equation, 38

power-law equation, 38

primary maximum, 12

primary minimum, 12

pseudoplastic. See shear-thinning

PZC. See point of zero charge

R

rate

diffusion-limited, 9

reaction-limited, 10

rate of shear strain. See shear rate rate-controlled (rheometric), 45

relative concentration terms, 4

relaxation time, 39

62
index

remolding test. See Ve-Be time

retardation time, 39

Reynolds number, 31

rheology, 32

rheomalaxis, 39

rheometer, 43

Tattersall, 52

rheometric, 32

rheopexy, 39

rotational methods, 44

rotational rheometers, 48

s

Schulze-Hardy rule, 13

screening, 22

secondary minimum, 12

sedimentation, 14

sedimentation volume, 14

settling method, 52

shear, 32

simple, 33

shear rate, 32

shear-thickening, 32

shear-thinning, 32

sieve range. See particle, coarse

slip, 2

slump, 50

slump cone test, 52

slurry, 3

sol, 3

sol-gel, 9

solvation forces, 12

sonication, 10

sonification, 10

stability

colloidal, 10

kinetic, 10

stability ratio, 14

stabilization

depletion, 11

electrostatic, 11

electrosteric, 11

steric, 11 Stern layer, 16

strain

shear, 32

strain amplitude, 40

stress, 33

normal, 33

shear, 32

yield, 33

stress amplitude, 40

stress growth, 39

stress relaxation, 39

stress-controlled (rheometric), 45

structural forces, 12

structure, 33

subsieve range. See particle, fine

supporting electrolyte, 21

surface charge density, 18

surface of shear, 16

surface potential, See potential,

surface

surface region, 15

surfactant, 14

suspension, 3

stable, 11 unstable, 11 suspension effect, 22

syneresis, 10

T

Tattersall. See rheometer,

Tattersall

thermal motion, 14

thixotropy, 39

negative, 39

titrant, 22

titration, 22

titrimetric analysis, 22

triple layer model. See electrical

double layer

two-point test, 52

63
U

ultimate working unit, 7

ultrasonication, 10

UVP. See potential, ultrasonic

vibration

V

Ve-Be time, 53

V-funnel cone. See flow cone

vibration methods, 48

Vicat apparatus, 53

viscoelastic, 26

viscoelectric, 26

viscometer, 43

Brookfield type. See simple

rotational

extrusion capillary, 44

glass capillary, 43

simple rotational, 45

turning tube, 52

viscoplastic, 27

viscosity

apparent, 27

coefficient of, 27

complex, 27

differential, 27

dynamic, 28

infinite shear, 28

intrinsic, 28

kinematic, 28

non-Newtonian, 27

out-of-phase, 28

plastic, 28

reduced, 29

relative, 29

specific, 29

zero shear, 29

viscosity number. See viscosity,

reduced

viscosity ratio. See viscosity,

relative

viscous, 27

W

Weissenberg effect, 33

Weissenberg number, 33

well-dispersed, 3

workability, 50

X

xerogel, 6

Y

yield response, 33

yield stress, 33

apparent, 29

Z

zero point of charge. See point of zero charge

zeta potential. See potential, zeta

zwitterionic, 21

64



August 2001