THE ADSORPTION OF MIXED SYSTEMS ON COLLOIDAL CARBON BLACK Scott Michael .

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THE ADSORPTION OF MIXED SURFACTANT SYSTEMS ONCOLLOIDAL CARBON BLACKScott Michael RichardsonA Thesis Submitted to the Department of Chemistry inConformity with the Requirements for the Degree of Masterof Science.Queen's UniversityKingston, Ontario, CanadaJuly 1997Copyright O Scott Michael Richardson, 1997

Library(*IofNationalCanadaBibliothèque nationaledu CanadaAcquisitions andBibliographie ServicesAcquisitions etservices bibliographiques395 Wellington StreetOttawaON KtAON4395. rue WellingtonOttawaON KtAON4canadaCanadaYour fi&Ourvcrrs relwmcuN m reMIIMQ)The author has granted a nonexclusive licence allowing theNational Library of Canada toreproduce, loan, distribute or seilcopies of this thesis in microfonn,paper or electronic formats.L'auteur a accordé une licence nonexclusive permettant à laBibliothèque nationale du Canada dereproduire, prêter, distribuer ouvendre des copies de cette thèse sousla forme de microfiche/fïlm, dereproduction sur papier ou sur foxmatélectronique.The author retains ownership of thecopyright in this thesis. Neither thethesis nor substantial extracts fkom itmay be printed or othenvisereproduced without the author'spermission.L'auteur conserve la propriété dudroit d'auteur qui protège cette thèse.Ni la thèse ni des extraits substantielsde celle-ci ne doivent être imprimésou autrement reproduits sans sonautorisation.

This thesis investigates the behaviour of carbon black as a mode1 hydrophobiecolloid in mixed surfactant systems. Adsorption isotherms were prepared for a series ofnonylphenol polyethylene oxide surfactants of v-gchah length. Additionalisotherms were prepared for sodium dodecyl sulfate and tetradecylaimethylammoniumbromide. Subsequent work was done in order to determine the individual surfactantconcentrations in mixed surfactant systems.Electrokinetic and acoustophoretic measurements were used to measure thecharge on the carbon black particle surface in the presence and absence of surfactants.Measurernents were carried out in both single and mixed surfactant systems.Experimental design was directed at understanding the behaviour of the surfactantadsorption under changing conditions of pH and temperature.A preliminary study of the particle size distribution in aggregated carbon blacksystems was aIso conducted.

TABLE OF CONTENTSPageABSTRACT .TABLE OF CONTENTS .i.riLIST OF FIGURES . v.ABBREVIATIONS . vri.SYMEIOLS . vu1LIST OF TABLES . xCHAPTER 1. NTRODUCTION . 1C HAPTER 2. BACKGROUND AND THEORY .-52.1 .1 Electrostatic Repulsion. 52.1.1 Gouy-Chapman Mode1 of the Electncal interface.122.1 -3 van der Waals Forces Between Colloida1 Particles .132.1.4 Harnaker Equation .152.1.5 Steric Stabilization . 172.1.6 interaction Potential Curves .212.1.7 Effect of Added Stabilizers .252.2Surfactants. 262.2.1 Micelle Definition and Energy Description .272.2.2 Nonionic Surfactants .-292.2.3 Cloud Point Temperature .30312.2.3 HLB Classification .

2.2.5 Applications .3 22.3Adsorption lsotherms for Nonionic Surfactants. . 341.3.1 Methods for Evaluating Surfactant Concentrations .352.3.2 Shape o f Isotherms .362.3.3 Steric Layer Thickness .392.4Acoustophoresis .-422.1.1 Principles o f Operation . 422.4.2 Electroacoustics. .442.4.3 Advantages of Electroacoustics . -462.4.4 Electrical Nature of the Solid Liquid [nterface .48CHAPTER 3 . EXPERlMENTAL .493.1Materials.493.1 -1 Nonionic Surfactants .493.1 2 Ionic Surfactants. 503.1 -3 Carbon Black .5032Adsorption Isotherm Preparation . -523 .3.1 Nonionic Surfactant Analysis.533 2 . 2 Anionic Surfactant Analysis.533 -3-3 Cationic Surfactant Anaiysis .-563.4Pen Kem 7000 Acoustophoretic Titrator . -573.5Pen Kem 50 1 Zeta Meter .58

.Conductivity Experiments. 59Aggregation Studies . -593.7.1 Zeta Potential Measurements of Ionic Surfactants . 603.7.2 Image AnaIysis Work . 13.7.3 Analysis of SDS as a Function of Tirne .61CHAPTER 4 . RESULTS AND DISCUSSION .-.*.*.-.*.623.1Adsorption Isotherms . 623.2Electrokinetic Zeta Potential Measurements . 714.3Acoustophoresis Experirneots . 801.4Spike Addition of TTAB to SDS Stabilized Systems . 824.5Conductivlty Experiments .-85.CHAPTER 5 . CONCLUSIONS AND FURTHER WORK .86REFERENCES .91VITAE .94

LIST OF FIGURESFigure 2.1 Schematic Drawing ofthe Electrical Double Layer.(after israelachvili 1992).11Figure 2.2 (a) Stenc Stabilization of Colloidal Particles with Nonionic Surfactants.(b) Electrosteric Stabilization with Ionic Surfactants. .,.20Figure 2.3 (a) Electrostatic Repulsion Energy as a Function of Surface PotentialT 25 O C : (1) 40 mV,(2) 60 mV, (3) 80 mV.for a PS Latex System r 0.1 pun'(b) van der Waals Attraction Energy as a Function of Particle Radius,A i j i 1.95 x 1 0 - l J, T 25 O C : (1) 50 nm, (2) 100 nm, (3) 150 MI . 23Figure 2.4 (a) Total interaction Potential of a PS Latex System, r 0.05 p,Ai ji 1.95 x 1 0 - l J. T 15 O C : (1) 80 mV, (2) 60 mV, (3) 40 mV.(b) Effect of Steric Layer Thïckness, r 0.05 p,A ljl 1.95 x 10'19 J, T 25 O C :( 1 ) 2.25 m ( ,2 ) 2.90 nm,( 3 ) 3.45 m. .24Figure 2.5 Idealized L4 Type Isothenn for Adsorption of Nonionic Surfactantsat the Solid/Solution interface (after G.D. Parfitt and C.H. Rochester 1983).37Figure 2.6 Schematic of Acoustophoretic Mechanism(afier B.J. Marlow and D. Fairhurst 1988).43Figure 3.1 ü V Spectrum of SDS:Methylene Blue Cornplex. .55Figure 4.1 Adsorption Isotherm for CO-850 on ST1120 Carbon Blackpnol m-'.65( )- pmol g-'. ().-Figure 4.2 Adsorption Isotherm for SDS on ST1120 Carbon Black( ) - p o l g'i, ().- pmol rn" . 66Figure 4.3 Mixed Adsorption Isotherm of SDS and CO-720 on ST1110Carbon Black (*)Total Adsorption, (a) CO-720 ( 0 )SDS .69Figure 4.4 Adsorption Isotherm for SDS, TTAB and CO-720 on ST1120Carbon Black. (m) SDS, ( ) CO-720 . 70Figure 4.5 Equilibrium Process in Mixed AnionicKationic Surfactant System(after Scamehom et al. 1988).75

Figure 1.6 Zeta Potential as a Function of Temperature for CO-710/SDS Systems( )16 OC. ( i ) 2 4 O C . (m) 32 O C . 80Figure 4.7 PIot of Zeta Potential as a Function of Added T'T'ABto STI 120Stablized with SDS/CO.720 . 84Figure 1.8 Determination of CMC of T'LU fiom Conductivity,. 87Measurements in DDW .Figure 4.9 Titration of T'AB with SDS in DDW . 88

RAMRelative acoustophoretic mobilitySDSSodium dodecyl sulfateTTABTetradecyItrimethylammonium bromideCMCCritical micelle concentrationDDWDeionized distilled waterRPMRevolutions per minutewUltravioletPEOPoiyethylene oxideEOEthylene oxide unitMBASMethylene blue active substanceCVPCotloid vibrational potentialST1120Sterling carbon blackDLVOColloidal Stability theones of B. Dejaguin. L.D. Landau, J.W. Venveyand J. Th. OverbeekPBPoisson-BoltzmannC.C.C.Critical coagulation concentrationPSPo 1ystyrene

Electrical force. NElectrical charges, CPermittivity of fiee space, kg-'m-'s4 A'Dielectric constant of the mediumSeparation distance between the centers of the charges. mWork to b twog charges together &om an infîîite distance, JConcentration of positive ions in the bulk medium. moles L-'Charge on the ion, CElernentary electric charge, CSurface potential, VBoltzmann constant, J K"Temperature, KCharge density, C m-'Valency nurnberConcentration of n type ions in the bulk medium. moles L"The reciprocal of the thickness of the double layer, m"Electrostatic potential on the particle, VCounter ion charge numberParticle radius, mHamaker constant, ISurface to surface distance, mHa, a2Particle radius, mVolume of a molecule of the dispersion medium, rn3Polymer solvent interaction parameterConcentration of the polymer in the steric layer. mol m".Vlll

Stenc layer thickness, mNurnber of moles of surfactant adsorbed on a unit mass of soiid,moles kg-'Total nurnber of moles of solution before adsorption, molesChange in mole fraction of surfactant resulting from adsorptionMass of insoluble adsorbent, kgAmount adsorbed, mol rnS2Number of moles of surfactant adsorbed. molesSurface area of substrate, m'Zeta potential, VFluid density, kg m"Particle density, kg m-'Fluid viscosity. N s rn"Volume fiaction of the particleDielectric constantParticle weight BactionWavelength of light. nm

LIST OF TABLESTable 1.1 Exarnples of ColIoidal Dispersions.9Table 2.1 Selected HLB Values of Nonionic Surfactants. 32.39Table 3.1 Nonionic Surfactants and Physical Data .,.Table 3.2 Absorptivity Data for Nonionic Surfactants . 50. 5 1Table 3.3 Physical Properties of Sterling3 1 120 .Table 3.4 Surface Area Measurements on ST1 120 Carbon Black. 51Table 4.1 Absorption Isothenn Data for Surfactants on STI 130 .64Table 4.2 Zeta Potential of Carbon Black Solutions as a function of added SDS . 72Table 4.3 Zeta Potential Measurements of Mixed TTAB/SDS Solution . 73Table 4.3 Zeta Potential of STl 120 Stabilized with Nonionic Surfactants .77Table 4.5 Effect of Temperature on the Zeta Potential of SDSKO-720 Systems . 79Table 4.6 Detemination of the Critical Micelle Concentration of SDS.85Table 3.7 Determination of the Critical Micelle Concentration of TTAB.85

CHAPTER 1. INTRODUCTIONColloids are an intricate part of our world. One accepted definition of a colloid isany system that has one or more of its components with at least one dimension in thenanometer-micrometer size range. Exarnples include: aerosols, foams, inks, andpharmaceuticals. These are al1 systems that contain srna11 particles or large molecules.The ability to control and predict the stability of a colloidal system is of vitalinterest in a broad range of industries including: pharmaceuticals, detergency, xerography,and cosmetics. EEorts to understand this stability stem fiom increased product life,efficient dmg delivery. and consistent product performance. The ability to manipulate acolloid is based upon an understanding of the factors that impart stability to the system.Equally important is a thorough understanding of the factors which can destabilize asystem.One of the more frequently encountered types of colloidal systems is dispersions.Dispersions consist of one phase of matenal homogeneously rnixed in a second. n i ephases can be liquid, gas or solid. Examples of some of these systems are listed below inTable 1.1.' As will be discussed in Chapter 2. there has been an intensive effort duringthe past several decades to develop a unimg theory to understand and predict colloidalstability. One of the primary means of generating stable dispersions is through theintelligent application of stabilizers or surfactants.

Table 1.1 Examples of Colloidal DispersionsDispersed PhaseDispersion MediumNameExarnplesLiquidGasLiquid aerosolFog, liquid spraysSolidGasSolid aerosolSmoke, dustGasLiquidFoarnSoap solutionsLiquidLiquidEmulsionMilk. mayonnaiseSolidLiquidColloidal SuspensionAu sol, Agi solGasSolidSoIid FoamExpanded PolystyreneLiquidSolidSolid EmulsionOpal, pearlSolidSolidSolid suspensionPigmented plasticsSurfactants are a class of molecules that have a unique chernical structure. Thereare three general classes of surfactants: anionic, cationic and nonionic. Ln general theirmolecular makeup consists of both a hydrophobie and a hydrophilic portion. in this thesisthe following terrns will be used to descnbe surfactant structure. The hydrophobicportion (usually a hydrocarbon chah) will be referred to as the tail. The hydrophilic(charge bearing or containhg polar groups) will be referred to as the head. The dualnature of these types of molecules allows thern to preferentially position themselves at theinterface between non miscible components. Surfactants find widespread use in colloidalsystems. They are often the only means of generating stable dispersions in some systems.More recently, mixtures of surfactants have been employed in the area of colloidalstability. Mixtures oflen exhibit spergistic behaviour which is unavailable in single

surfactant systems. However, the properties of these mixtures are complex and are atpresent not well understood.One of the driving forces for understanding surfactant behaviour in these rnixedsystems is the potential to optirnize their use and performance. Emulsion polyrnerizationis an example of a colloidal system that relies heavily on the properties of surfactants.The synthesis of the polymer and the final particie size distribution in the product areintncately linked to surfactant behavior in the colloidal system. Of fundamentalimportance is a thorough understanding of surfactant behaviour during the seeding orgrowing process of the primary particles. During this process seed particles are firstgenerated, these primary particles c m be aggregated to form the secondary particles.Surfactants play a prime role in both the growth of the pnmary particles and thesubsequent stabilization of the secondary particles. Control over the extent anduniformity of the secondary particle size is a result of a number of processes. Currentlythere exist some opposing ideas regarding the role of the surfactants during the particlegrowth and stabilization phases.Emulsion polyrnerization typically involves a number of different chemicals andfactors that exert influence on the final particle size distribution. Some of the moreimportant factors include shear rate. temperature, pH1 and type of surfactants.Recent research into narrowly dispersed aggregates at the Xerox Research Centreof Canada has provided a starting point to begin this investigation into mixed surfactantsystems. From the procedure developed at Xerox, narrowly dispersed aggregates areproduced fiom a pnmary particle size of 0.15 p with a final aggregafe size anywherebetween 5 and 10 Fm. The primas. particles are stablized with a mixture of anionic and

nonionic surfactants. Cationic surfactant is added to the systems to destabilize it and tobegin the aggregation process. There are several hypotheses directed at explaining thebehavior/roie of the individual surfactant components in the mixture.The surfactants in this system initially serve to keep the latex particles stable insoiution. Aggregation is induced by the addition of cationic surfactant, which causes theformation of a thick viscous gel. This gel is subsequently broken up at higher temperatureto form aggregates with a remarkably narrow size distribution. The restabilization isthought to be primarily a function of the aggregate size and of the surfactant concentrationand conformation on the particle surface. in order to M e r understand and explain theprocess, a method of determining the concentration and effect of individual surfactants int h i s complex mixture was required.This thesis describes a first attempt at obtaining analytical techniques fordetermining individual surfactant concentrations is such complex systems. A secondaryobjective of this research project was to investigate if narrow aggregate distributionscould be obtained by aggregating dispersions of colloidal carbon black.

CHAPTER 2. BACKGROUND AND THEORY2.1DLVO TheoryThe ability to control and manipulate colloidal stability has been the focus of alarge and concentrated effort for the past several decades. Depending on the applicationof a colloidal system, fme-control over the stability of the system can have a ciramaticinfluence on the end-use properties. In the area of colfoid science the theones ofDejaguin, Landau, Verwey and Overbeek (DLVO theory) are often used to defme andpredict the stability of a given system.The DLVO theory unified the theones goveming attraction and repulsion incolloidal particle systems. The theory deals with the potential energy of interactionbetween colloidal particles as a function of distance. It combines the attractive (van derWaals) and repulsive (electrostatic) energies between particles to predict the totalinteraction energy. The major contributing factors to the repulsive and attractive forcesacting between colloidal particles will be outlined next.2.1.1Electrostatic RepulsionElectrostatic repulsion arises between colloidal particles when two similarlycharged surfaces approach each other at a small distance of separation. The repulsion is adirect consequence of the interaction between the sirnilady charged surfaces.'There has been a vast amount of theoretical and experimental work directed atexplaining the nature of the electrical interface. The interface exists between the solid and

its surrounding solution environment. Repulsive electncal forces acting between thesurfaces of similarly charged colloids are often the primary means of stabilization within asystem.'Colloidal particles may acquire surface charge through one or a combination of thefollowing mechanisms: (i) preferential dissolution of surface ions. (ii) direct ionization ofsurface groups, (iii) substitution of surface ions, (iv) specific ion adsorption." The forcesacting between "charged surfaces" have their ongin in Coulomb's Law. This lawdescribes the interaction between point charges separated by a distance r in a vacuum.Coulomb's law m u t be modified in order to extend its applicability to colloicial systems.'The interaction of two charges in a vacuum, separated by distance r, can bedescribed by Equations 2.1 and 7.2whereFe1 elecûicaI force, Nq 1 ,qz electncal charges,&O permittivity of fiee space, kg" m*' s4 A'E dielectric constant of the mediumC

r separation distancew thebetween the centers of the charges, mwork necessary to bring two charges together fiom an infinitedistance, J.For charges of the same sign the work will be positive and the interaction will berepulsive. The quantity of work is defined as the "elecû-ical potential" at r due to thecharge q,, and is given the symbol Y.in order to describe systems of more practical interest Coulomb's law must bemodified by the Boltzmann distribution to account for al1 ions present in the system.which is descnbed by Equatior?2.3. If the surface has a negative electrical potential(negative surface charge), the concentration of positive charges in the region surroundingthe surface c m be calcuiated by the following expression:wherepositive ions surrounding the surface, moles L*'c, concentration ofCo concentration of positive ionsZ, charge one elementary electnc charge,Y surface potential, Vk BoItmiann constant, JT temperature. K.the ion, CK-'Cin the bulk medium, moles L"

One of the approximations often invoked to describe the electrical interface is toexpress the charge density of the surface as a fûnction of potential upon rnoving awayfiom the charged surface. Charge density is related to the surroundhg ion concentrationprofile as s h o w by Equation 2.4jwheredensity. C rn'jP' charge21 vaiencye eiementaryY surface potential,k Boltzmann constant, Jn1o concentrationT temperature,nurnberelectric charge. CVK-'of n type ions in the b u k medium, moles L-'K.Reiating Equation 2.4 to the potential results in the Poisson-Boltzmann (PB) equationThe Poisson equation implies that the potentiais associated with the variouscharges combine in an additive manner, whereas the Boltzmann distribution irnplies an

exponential relationship between the charges and the potential. The PB equation has noexplicit solution and must be soived for limiting cases. The solution to the abovedifferential equation under conditions of low surface potential and the condition ofelectroneutrality results in the Debye-Huckel approximation which is expressed asEquation 2.6,Wherey 0 thepotential at the particle surface, VK thereciprocai of the thickness of the double layer, m-'.The thickness of the double layer for surface potentials less than 25 mV is calculatedaccording to Equation 2.7The thickness of the double layer varies inversely with the concentration ofsolution electrolytes, and the square of the valency of the counter ion. By changing eitherthe concentration or the identity of the surroundhg electrolyte, the thickness of the doublelayer cm be manipulated. in systems whose stability is entirely dependent on electricdouble layer interactions this has important implications. This strong dependence on ionvalency and concentration is the basis for the Schulze-Hardy rule!The Schulze-Hardymle predicts the amount of inert electrolyte necessary to destabilize a colloidal system.

this arnount is most often referred to as the critical coagulation concentration (c.c.c). Atthe C.C.C. the surface charge of the particles will have been screened by the addedelectrolyte, this causes the attractive forces to dominate and the dispersion will becomeunstable.The solution taken as a whole will be electrically neutral. However in the vicinityof the charged surface, at the particle-solvent interface. there will exist an irnbalance ofelectrical charges. This charge irnbalance in the system depends heavily on the net chargeof the surface. The region of excess charge of opposite sign around a charged surface iscommonly referred to as the "ionic atmosphere" or "charge cloud" associated with thatpotential. This ionic atmosphere consists of a higher concentration of counter ions overCO-ionsas predicted fiom Equation 7.3. In colloidal systems the "charge cloud" inconjunction with the charged interface is commonly referred to as the "electncal doubielayer" associated with the particle.As a consequence of the dynarnic nature of a solution, the ions present in thedouble layer exist in a d i f i s e state. This results in a surrounding ionic environment thatis rapidly undergoing change. Taking account of this added complexity, Gouy andChapman developed a mode1 to describe the electrical double layer that relates thepotential of the surface to the diffise portion of the double layer.' It does not involve thessurnption of low potentials invoked in the Debye-Huckle approximation. A schematic ofthe interface is given in Figure 2.1.

FFUSE LAYER (MOBILE IONS)I\BOUND (IMMOBILE) COUNTER-IONSPARTICLE SURFACE IONSFigure 2.1 Schematic Drawing of the Electncal Double Layer(after Israelachvili 1992).

2.1.2Gouy-Chapman Mode1 of the Electrical InterfaceThe "Stem Layer" is the small space separating the ionic atmosphere around asurface rom the acnial diffuse double layer. and consists of tightly bound counter ionsthat are not ''fiee" to move with the thermal motion of the aqueous system. The StemLayer has a thickness on the order of a few angstroms, and its width accounts for the finitesize of charged groups and ions specifically associated with the surface.'It is assumed that the electrical potential in the solution surrounding the surfacedecreases exponentially with distance. This approximation is not valid at points close tothe surface, where the potential decreases much more rapidly due to the presence of boundcounter ions in the Stem Layer which are more effective at screening the surface charge.Several simplifjmg assumptions are employed to theoretically treat the nature of theinterface. These include: (i) ions fiom both the solution and the surface are treated aspoint charges, (ii) the surface is treated as a Mform charge, (iii) charges of opposite signc m approach infinitely closely. and (iv) the dielectric constant of the solvent is assurnedto remain constant throughout the double layer.The actual surface potential represented by y is replaced in the Gouy-Chapmanmodel with y,. This is the potential of the surface at the interface between the Stem planeand the solution. The Gouy-Chapman model accounts for the mobility of ions in aqueoussolution. The diffuse model of the double layer reflects the change in potential associatedwith the surface on moving away fiom the interface.No exact analytical expressions exist for solving the equations associated with thenature of the interface, recourse to nurnencal solutions or to various approximations areofien invoked. According to Overbeek. the rate of double layer overlap in typical

Brownian motion between particles is too fast for adsorption equilibrium to bemaintained.' Often models of the interface assume that the potential remains constantduring particle collision or that the surface charge remains constant; the true situation liesbetween these two assurnptions.Reerink and Overbeek developed an expression to calculate the interactionpotential caused by the overlap of the d i h e portion of two double layers. Thisinteraction is referred to as the electrostatic repdsion term (TlR). The main assumption intheir derivation is that the interparticle separation is large compared to the thickness of thedouble layers. For equal sph

Total nurnber of moles of solution before adsorption, moles Change in mole fraction of surfactant resulting from adsorption Mass of insoluble adsorbent, kg Amount adsorbed, mol rnS2 Number of moles of surfactant adsorbed. moles Surface area of substrate, m' Zeta potential, V Fluid density, kg m" Particle density, kg m-' Fluid viscosity. N s rn"

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