Emulsion is a thermodynamically unstable system consisting
of at least two immiscible phase, one of which is dispersed in the other liquid
phase, the system being stabilized by an emulsifying agent. One phase is the
disperse phase which is distributed throughout the other continuous
phase or dispersion medium. Emulsions can be liquids or semi-solids. The
latter are referred to as creams. The particle or globule size is
0.1-10μ. When the globule size is < 5μ they are called fine emulsions
but can have emulsions <10nm which are called microemulsions.
Showing posts with label Dispersed System. Show all posts
Showing posts with label Dispersed System. Show all posts
STABILITY AND FORMULATION OF SUSPENSIONS
In the preparation of
suspensions, particle size is reduced. There is an increase in the specific
area, which cause an increase in surface free energy. These parameters are
expressed in the following relationship:
ΔF
= γΔA Where ΔF = increase in free energy
γ
= interfacial tension
ΔA
= increase in surface area.
With large F, the particles are
highly energetic and tend to regroup so as to reduce the total area. Thus
suspensions like other dispersed systems are thermodynamically unstable. The
particles tend to flocculate, i.e. form light, fluffy conglomerates, held
together by weak Van der Waal’s forces of attraction. But they may adhere
firmly to form aggregates, which grow and fuse to form a solid. The suspension
is then said to have undergone caking or forming a cake.
The smaller the ΔF the more the
thermodynamic stability. ΔF can be reduced by reducing γ (e.g. using wetting
agents or surfactants) or by reducing ΔA. γ cannot be reduced to zero, thus
particles although deflocculated, settle slowly, forming a hard cake
eventually, which is difficult to re-disperse. ΔA is reduced by deliberately
formulating loose aggregates or flocs which although settle rapidly, they do
not pack tightly at the bottom due to porous nature. They form a loose mass
that can be redistributed with minimum agitation.
Question:
A hypothetical
suspension contain 103 spherical particles of diameter d = 10-3
cm. (a)Assuming that the interfacial
tension between the solid and the liquid is γSL = 100 dyne/cm,
compute the total surface free energy, ΔF. (b) The solid particles are
divided to obtain 100 particles from
each initial particle. Compute the increase in total surface area and the total
surface free energy ΔF’ for the divided particles. (HINT: Compute the volume of
a particle to get its new radius and surface area. Assume that the density of
the particle is unity.
FORMULATION OF SUSPENSIONS:
Formulation of suspensions calls
for a compromise between:
1. Keeping
the particles in a suspension as long as possible and having a cake on
standing.
2. Deliberately
forming agglomerates which although settle rapidly are easy to re-disperse.
RECALL
i.
Forces acting between two articles in a disperse
system (resultant of attractive and repulsive forces, DLVO theory).
ii.
Particles are charged (How do particles in a
dispersed system acquire a charge? How can we ascertain that particles in a
disperse system are charged?)
iii.
Factors affecting zeta potential and their
effect on stability of dispersed systems.
iv.
What are the secondary minimum and its
importance in the formulation of suspensions?
Deflocculation:
Zeta potential is reflective of the potential at the
surface of a particle (Nernst Potential). When ξ potential is high, repulsive
forces are higher than attractive forces. Particles are deflocculated. Slowly
sedimentation occurs, forming a closely packed arrangement, smaller particles
filling the voids of larger ones. Lowermost articles are pressed together, the
energy barrier is overcome and particles touch. The particles remain attracted
to each other and form a hard cake.
Flocculation.
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Addition of a preferentially adsorbed ion, having a charge
opposite to that of the particle, neutralizes the surface potential and
progressively lowers the ξ potential, thus lowering repulsive forces. When
attractive forces still dominate, the particles approach each other more
closely forming aggregation called flocs. The system is flocculated. The
added substance is called flocculating agent. Addition of more
flocculating agent can increase the zeta potential to opposite direction
leading to deflocculation again.
Settling:
This one aspect of instability.
In order to control it let us see the factors involved:
SEDIMENTATION RATE:
1. Stoke’s law:
ν = 2r2 (δ – δ0 )g Where g = acceleration due to gravity
9 η0
ν =The velocity of
sedimentation,
r = radius of a spherical
particles
δ = density of particles
δ0 = density of medium
η0 = viscosity
To reduce the sedimentation
rate, we can reduce the particle size, r. (particles shall be deflocculated) or
increase viscosity (but should not impede flow).
Question: A coarse powder with a true density of 2.44
g/cm3 and a mean diameter d
of 100 µm was dispersed in a 2% carboxymethylcelulose dispersion having a
density ρ0 of 1.010 g/cm3. The viscosity of the medium at
low shear rate was 27 poises. Using Stoke’s law, calculate the average velocity
of sedimentation of the powder in cm/sec.
2. Brownian motion:
Particles lower than 2μ show
Brownian movement and the rate of sedimentation is lower than would be expected
from Stoke’s law and may even remain suspended for prolonged periods of time
due to this phenomenon. But this effect is eliminated when high viscosity
liquids are used e.g. glycerin.
3. Effect of flocculation
In deflocculated systems, large
particles settle faster than smaller particles. Very small particles remain
suspended longer such that no distinct boundary between the supernatant and the
sediment. In flocculated systems, flocs tend to fall together, producing a
distinct boundary between sediment and the supernatant liquid. The supernatant
is clear, showing that very fine particles have been incorporated in flocs.
Here we use the term subsidence rather than sedimentation.
SEDIMENTATION PARAMETERS
Sedimentation volume, F
F = ratio of equilibrium or
final volume of the sediment, Vu to the original volume of the
suspension, Vo.
F
= Vu F ranges from 0-1
Vo
F is only a qualitative
representation, but no meaningful reference. A more useful parameter is the
degree of flocculation. The ideal suspension has F=1. This means there is no
sedimentation or caking and the suspension is esthetically appealing.
Degree of Flocculation, β
This is more meaningful. For a
completely deflocculated suspension,
F∞
= V∞
Vo
V∞ is very small.
Degree of flocculation d relates
the sedimentation volume of the flocculated suspension, F to the sedimentation
volume of the deflocculated suspension, F∞.
β = F
F∞
That is β = Vu/
Vo = Vu
V∞/ Vo V∞
That is if β = 5, the volume of
sediment in flocculated system is 5X that in a deflocculated system. If β
= 7, it is more preferable.
FORMULATION OF SUSPENSIONS
In the formulation of a stable
suspension,
1. We
need a structured vehicle to maintain deflocculated particles in suspension.
2. Principles
of flocculation are applied to produce flocs which although settle rapidly are
easily resuspended.
Structured vehicles are plastic or pseudoplastic,
frequently associated with thixotropy. They act by entrapping the deflocculated
particles so that settling is discouraged. Though sedimentation occurs to some
degree due to shear thinning property of the vehicles, a uniform dispersion is
reformed easily on application of shear. (remember flocculated systems cake on
standing). The principle then is to
formulate flocculated particles in a structured vehicle of hydrophilic colloid
and hence principles of controlled flocculation are applied.
How is controlled flocculation achieved?
1.
The first step is to reduce the particle size. Use
mortar and pestle, agitators, homogenizer, colloid mills etc
2.
Particles must be wetted. Some particles are not
easily wettable and will not remain in vehicle long enough to ensure uniformity
of dosage. Here wetting agents are needed as well as thickening agents to
increase viscosity and delay sedimentation. Such materials are called indiffusible
solids, e.g. sulfur, charcoal magnesium stearate. Their angle of contact is approximately 90º.
They are hydrophobic. Surfactants reduce surface tension and therefore
lower angle of contact. Also glycerin and other hydroscopic materials can be
used to improve wetting properties. Some powders however are easily wetted (eg
light kaolin, Ca carbonate, Zinc Oxide, Talc). They show small or no angle of
contact and sink. They easily mix with water and on shaking diffuse evenly
through liquid. These are diffusible or dispersible substances.
3.
Controlled flocculation
Electrolytes, surfactants and polymers are used to
control flocculation to avoid caking. They are known as flocculating agents.
Electrolytes:
They lower the electrical barrier between particles
(decrease the zeta potential), and form a bridge between particles to link them
in a loosely arranged structure. For example, bismuth subnitrate (positively
charged particles) is deflocculated (due to repulsive forces between
particles). Addition of potassium acid phosphate (KH2PO4), which is negatively
charged, decreases zeta potential due to adsorption of KH2PO4 on bismuth
subnitrate. Progressively zeta potential is reduced to zero and then reverts to
negative. At a certain zeta potential maximum flocculation occurs. At this
point, there is maximum degree of flocculation. Flocculation exists until zeta
potential is sufficiently negative to cause deflocculation again and subsequent
caking.Similarly, Aluminium chloride (positively charged)
added to sulfamerazine (negatively charged) would bring about the same effect.
Surfactants:
Both ionic and non-ionic surfactants can bring about
flocculation. Since they also act as wetting agents their concentration is
crucial.
Polymers
The long chain high molecular weight compounds have
active groups along their chain. Part of the chain is adsorbed on particle
surface and the other part projects in the dispersion medium. By bridging
between the latter portions flocs are formed. Hydrophilic polymers act as
protective colloids and hence reduce the caking tendency. They also exhibit
pseudoplastic flow (eg gelatin). Sodium sulfathiazole is negatively charged in
aqueous solution. If it is precipitated from acid solution in presence of
gelatin it is positive, free flowing and does not cake. This is because gelatin
is positive and is coated on sulfathiazole. The coated particles are
flocculated and do not cake. The strong negative charge has been replaced by
small positive charge.
Flocculation in structured vehicle.
Suspending agents.
Controlled flocculation alone results in unsightly
preparations. Thus suspending agents are used to retard sedimentation of flocs
which would make the preparation unsightly. They try to make the sedimentation
volume F close to 1. For example, carboxymethyl cellulose (CMC) carbapol 934,
veegum, tragacanth, bentonite or combination. But addition of suspending agents
may lead to problems of incompatibilities. For example, if a positively charged
particles are dispersed and flocculated
by a correct negatively charged electrolyte, there is no problem when
the hydrocolloid is used to improve physical stability. This is because most
hydrocolloids are negatively charged. But if the particles were negatively
charged and cationic electrolyte is used for stabilization, addition of
hydrocolloid will cause incompatibility. Therefore to overcome such a problem,
we use protective colloid to change the sign from negative (ve-) to positive
(ve+). For example non-toxic fatty acid amine is used so that on addition of
hydrocolloid (anionic) there is no problem.
Types of thickening agents.
Polysaccharides
·
Natural: Acacia, tragacanth, starch, sodium
alginate
·
Semisynthetic: methylcellulose, hydroxymethyl
cellulose, sodium carboxy methyl Cellulose
Inorganic agents:
Clay, bentonite, Aluminium magnesium silicate,
Aluminium
hydroxide.
Synthetics: Carbomer (carboxy nvinyl polymer), colloidal
silicon dioxide
Rheological
considerations
Viscosity studies are very important in suspensions.
Viscosity affects
§ Settling
of particles
§ Flow
properties on shaking, pouring and spreading qualities of lotions and Flow
properties during manufacturing.
§ Passage
of suspensions in syringe needle.
An ideal suspending agent should have high viscosity
at negligible shear (during storage when the only shear is due to settling of
particles) and low viscosity at high shear rate 9that it free flowing during
agitation, pouring and spreading. Hence it should be pseudoplastic and preferably
thixotropic. Sometimes suspending agents are combined to give better properties
eg bentonite and CMC are combined and give average properties: bentonite has
marked hysteresis loop and CMC is thixopropic.
Preparation of suspensions
Small scale.
The insoluble matter is ground or levigated t a
smooth paste with a vehicle containing the dispersion stabilizer. The remaining
liquid phase in which any soluble drugs may be dissolved is gradually added.
Volatile ingredients are also dissolved in the vehicle. The slurry is
transferred to a tared container; the mortar is rinsed with successive portions
of the vehicle. Finally the dispersion is brought to final volume.
Large scale:
Mills are used ( ball mill, colloid mill, pebble
mill). Dough mixer or pony mixer may be needed as well. The colloid mill has a
cone shaped high velocity rotor centered in a stator at a small adjustable
clearance. The materials are fed through a hopper to the rotor by gravity, and
here they are sheared between the rotor and the stator., and forced out below
the stator, where it may be recycled or drawn off. The efficiency of the mill
depends on the clearance of discs, velocity of rotor and viscosity of
suspension.
SUSPENSIONS: Introduction, Desirable Qualities, Importance and Applications.
Pharmaceutical suspension = a coarse dispersion in which
finely divided solid particles are dispersed is a liquid medium.
IMPORTANCE:
Ø Suspensions
supply insoluble and often distasteful substances in a form which is pleasant
to the taste.
Ø Suspensions
provide suitable forms of application of dermatological materials to the skin
and mucous membranes
Ø Suspensions
provide parenteral administration of insoluble drugs.
DESIRABLE QUALITIES OF A SUSPENSION
·
Is composed of small uniformly sized particles.
·
Suspended materials must not settle rapidly.
·
Should the particles settle, they must be easily
redistributed. They should not form a hard cake.
·
Should not be too viscous to pour freely from
the orifice of the container or to flow through a syringe needle.
·
For external lotions, suspensions must spread
easily on application, but not too mobile as to run off the surface. The lotion
must dry quickly to give a protective film.
·
Suspensions should have acceptable odour and
taste.
o Should
be resistant to microbial attack (may need a preservative)
o Must
have optimum physical, chemical and pharmacological activities.
PHARMACEUTICAL APPLICATION OF SUSPENSIONS
·
Suspensions provide liquid preparations of
insoluble drugs to patients who find it difficult to swallow tablets and
capsules.
·
To avoid hydrolysis, some drugs are synthesized
as insoluble salts and suspended in a suitable medium. Compare oxytetracycline
hydrochloride (insoluble) and oxytetracycline calcium (soluble).
·
To avoid prolonged contact with liquid, powders
are prepared and suspensions are made just prior to use. E.g. ampicillin syrup
(expires 7-14 days after reconstitution.
·
Provide alternative for aqueous sensitive drugs,
which are suspended in non-aqueous vehicles.
·
Formulation in finely divided particles offer a
high surface area suitable for some drug action e.g. kaolin suspension, Mg
trisilicate and MgCO3 suspensions.
·
Fine powders may provide protective action
against loss of volatile materials for inhalation e.g. Menthol and Eucalyptus
are adsorbed on light Mg carbonate for prolonged release (compared to
solutions).
·
Suspensions may mask an otherwise obnoxious
taste eg. Compare Paracetamol elixir (bitter) and suspension (no taste, can be
sweetened)., or chloramphenicol palmitate is more acceptable in children. Taste
is less noticeable in insoluble form.
·
Topical application may be suitable e.g.
calamine lotion leaves a protective action after the vehicle has evaporated.
·
Parenteral suspensions have controlled release
characteristics (variation in particle size increase duration of action, or
suspension may be formulated in oily phase).
·
Vaccines are often formulated as suspensions and
provide prolonged antigenic stimulus leading to increased antibody titre.
·
Some X-ray contrast media are formulated as
suspension (insoluble materials in aqueous vehicle).
APPLICATION OF COLLOIDS
The therapeutic
properties of some medicinal products are increased when they are formulated in
colloidal state. For example
1. Colloidol
calome (Hg nitrate , gelatin, NaCl) has higher antiseptic activity than in the
coarse powder.
2. Colloidal
Silver chloride (AgCl), Silver Iodide (AgI), and Silver (Ag) proteins are
germicidal which do not cause irritation as their ionic Ag salts.
3. Adsorption
of toxins from GIT by kaolin and the rate of neutralization of excess acidity
in the stomach by Aluminium hydroxide is higher if the compounds are in
colloidal form.
4. Blood
plasma substitutes are colloidal dispersions in which the particle size is big
to allow retention in blood vessels for adequate time (eg dextran inj BP,
polyvinyl pyrolidone (PVP).
5. Natural
and synthetic polymers are in colloidal range. Starch, cellulose are
pharmaceutical adjuncts; synthetic polymers are used as coatings to tablets for
protection against moisture and acid degradation in stomach.
6. Colloidal
dispersions containing radioactive isotopes are used for diagnostic and
therapeutic purposes in nuclear medicine. Technetium 99m sulphur
colloid is used in liver, spleen and bone scanning. Radioactive colloids that
accumulate in tumors, lesions or emboli indicating their location and size may
be used as diagnostics. The radiation emitted is made visible by scanning
devices. Radiocolloids are useful in treatment of cancer because they
accumulate in target organs.
PREPARATION OF COLLOIDS
Lyophobic dispersions
The most common medium for lyophobic dispersion is water.
Insoluble organic and inorganic compounds usually with a low degree of
hydration are dispersed in aqueous medium and are intrinsically unstable. The
particles tend to coalesce or aggregate to reduce the surface area and hence
surface energy. Thus special means must be utilized to stabilize these systems
–preventing the otherwise spontaneous coalescence or coagulation of the
disperse phase after it has been finely dispersed. There are two methods of
preparing lyophobic sols, namely Condensation methods (aggregation of
small molecules or ions until particles of colloidal dimensions are obtained)
and dispersion methods (reducing coarse particles to colloidal
dimensions through comminution or peptization).
Condensation Method:
This method involves aggregation of small molecules or
ions until particles of colloidal dimensions result.
To illustrate this method, the preparation of sulphur
hydrosol is exemplified. Whereas sulphur is insoluble in water, it soluble in
alcohol. Alcohol and water are miscible. Sulphur
is dissolved in alcohol, and the solution is mixed with water to produce a
bluish-white colloidal dispersion. The dispersion must be stabilized to avoid precipitation
or agglomeration. The same method can be used to prepare hydrosol of stearic
acid, mastic acid and other polymers.
Suphur vapor may also be stremed in water to produce a
colloidal dispersion. This is a less common method.
Condensation may also be produced chemically. For example
bubbling hydrogen sulphide (H2S) gas into a solution of sulphur
dioxide (SO2) :
2H2S + SO2 ===> 3S + H2O
or mixing solutions of sodium thiosulphate and sulfuric acid:
===>H2SO4 + 3NaS2O3 4S
+NaSO4 + H2O
Aluminium hydrxide sol is produced by hydrolysis of
Aluminium chloride.
AlCl3 + 3 H2O ===> Al(OH)3
+ 3HCl
** See preparation of White
lotion (precipitated ZnS and S)
Dispersion method:
The methods involve reducing coarse particles to colloidal
dimensions through comminution or peptization.
Mechanical disintegration:
Using equipment such as
micronizers, colloid mills, homogenizers, or even simple mortar and pestle,
solids and liquids are sheared or attrited into fine size for dispersion.
Ultrasonic generators produce waves that break soft materials e.g. sulphur,
talcum and graphite into very small particles or droplets. Thus method is used
to produce very fine emulsions for I.V. use.
The dispersion must be stabilized
to avoid re-crystallization, coagulation or calescence.
Peptization:
This involves breaking up
aggregates into smaller particles. It is synonymous to defflocculation. It can
be brought by removing flocculating agent (eg electrolyte) or addition of a
deffloculating agents or peptizing agents (eg surfactants, ions or water
soluble polymers). Eg activated charcoal produces a grey dispersion, Addition
of 0.1% Na laurylsulphate or octoxynol disintegrates the particles into fine
ones, results in fine deep black dispersion.
Purification
of colloidal dispersions
Hydrosols may contain low molecular weight water-soluble
impurities including salts formed by reaction producing the dispersion. The
salts tend to coagulate the dispersion and hence must be removed. Blood ( a colloidal dispersion of plasma proteins)
of patients with renal insufficiency has high concentration of urea and other
metabolites. These as well must be removed to acceptable levels. Substances in
true solutions may be separated from those in colloidal dispersion by means of
dialysis or ultrafiltration.
Dialysis:
This is based upon the fact that colloidal particles do
not diffuse (or diffuse very slowly) through membrane of parchment, cellophane,
collodion or certain animal tissues, while particles of molecular or ionic
dimensions diffuse relatively rapidly. Thus if
the low molecular weight
impurities are to be removed from a colloidal dispersion the latter is placed
inside a sac made of one of the above mentioned membranes and dipped in water.
The small solutes will diffuse out while pure colloidal materials are retained.
The rate of
dialysis is increased increasing the area of membrane (e.g. using numerous
hollow fibres, stirring and maintaining a high concentration gradient (dialysis
fluid must be replenished continuously). If the impurities are electrolytes,
the dialysis process can be speeded up by applying an electric potential to the
sol. The process is then known as electrodialysis, and the equipment
used is electrodialyser. Application of pressure in a dialytic process
also speeds up the process. This is known as ultrafiltration.
Application
of dialysis.
OPTICAL PROPERTIES OF COLLOIDS, Faraday-Tindall effect
If a narrow beam of light is
passed through a colloid, its path is visible. This is not possible with true
solutions. The visible cone seen is due to light-scattering action by the
colloidal particles and is known as the Faraday-Tindall effect.
The Faraday-Tindall effect is
employed in the ultramicroscope and electron microscope. In the
ultramicroscope an intense beam of light is passed through a sol against a dark
background at right angle to the plane of observation. The particles are observes
as bright spots and can be counted. For Better resolution, an electron
microscope is used and very minute particles (molecular level) can be observed
in terms of size, shape, and structure. The electron microscope uses a beam of
high-energy electrons instead of the normal light.
The light scattering property is
also used to determine the concentration of sol through measurement of
turbidity, a phenomenon known as turbidimetry. Turbidity, τ, is a fractional
decrease in intensity due to scattering as the incident light passes through a
solution.
τ = 1 ln Is
l I
Where l = length of dispersion through which the light
passes
Is = Light scattered in all directions
I
= Intensity of incident light
If the turbidity of suspension of
known concentration is determined, the concentration of a certain value can be
determined.
We can also use turbidity to
measure molecular weight.
Hc / τ = 1/M +2Bc Where H and B are constants of a particular system,
c
is concentration and M is the molecular weight.
STABILITY OF COLLOIDS
Effect of added electrolytes on ζ
The addition of electrolytes to a
colloidal system reduces zeta potential or even reverses it. The electrolytes
supply additional anions and cations so that the density of ions of opposite
charge to the charge on the wall is increased. Thus the ionic atmosphere is
compressed near the surface and the potential gradient in the fixed layer is
greatly increased and the potential in the diffuse layer (as well as the zeta
potential) is decreased. As the concentration of the counterions in the liquid
increases, the ζ is continuously reduced tending to zero, and may even
be reduced. The higher the valence of the electrolyte, the higher the reduction
of potential. Thus trivalent ions are more effective than divalent ions, which
are in turn more effective than monovalent ions.
The presence and magnitude or
absence of charge on colloidal particles is an important factor in stability of
colloidal systems. However, lyophilic and lyophobic colloids differ in their
stability requirements and hence each is approached separately.
Stability of lyophobic
colloids
A lyophobic sol is
thermodynamically unstable. It is produced from insoluble substances which have
been subdivided as polymolecular aggregates throughout the liquid phase. The
enormous increase in surface area results in an increase in surface energy.
Particles therefore have a tendency to aggregate and precipitate in order to
reduce this energy. The tendency to aggregate is offset by the repulsive forces
between particles due to the charge at the surface of the particles. Not
however that there exist Van der Waal forces of attraction between particles.
Thus there are two opposing forces between any two colloidal particles,
attraction and repulsion.
Forces acting between two
particles in colloidal sol
Consider two particles in close
proximity. They attract each other by Van der Waals forces of attraction
which vary inversely as x7 ( where x = distance between them). The
particles also repel each other due to electrostatic forces which vary
inversely as x2. The resultant force between the particles as a function of
their distance apart was explained independently by Derjaguin and Landau in the
USSR and by Verwey and
Overbeek in the Netherlands
in the early 1940’s. This is now called DLVO theory, and is summarized in the
following figure:
Consider two particles
approaching each other. Curve A represents the Van der Waals attractive energy (which decrease with
second power of the inter-particle distance). Curve R represents the
electrostatic repulsive forces (which decrease exponentially with the seventh
power of the inter-particle distance). The combination of these two opposing forces,
attraction dominates at large distance and shallow trough is exhibited at x3.
This so-called secondary minimum is significant in controlled flocculation
in preparation of suspensions.. As the particles still approach each other,
repulsion begin to dominate at intermediate distance, to reach maximum at x2,
so called primary maximum. Repulsion occurs because when particles
approach each other the two atmospheres of counterions surrounding them begin
to interpenetrate or overlap at point o. Repulsion occurs because of
the work involved in distorting the diffuse double layer and in pushing water
and counterions aside, which increase as the particles approach further to
reach maximum at point x2. At this point the potential energy
barrier exceeds the kinetic energy of the approaching particles, and the
particles will not come close to each other, and the dispersion shall be
stable. But if the kinetic energy exceeds the potential energy, at x2
or beyond, the particles continue to approach each other past this point, where
van der Waals forces of attraction become more important than the repulsive
forces. The net potential energy decrease to zero and then becomes
negative as the particles continue to approach each other, until when they
touch at point a (x1) otherwise known as primary minimum.
This corresponds to a very stable situation in which particles adhere, and are
attached permanently (irreversible caking in suspensions). In other words, the
particles agglomerate or the sol is said to coagulate. This situation is
irreversible because no kinetic energy can be applied to overcome the potential
energy. In practice the particles cannot approach further than this point, but
theoretically, if the particles were to approach further than the touching
distance, they will meet with very rapid rise in potential energy, because they
will be interpenetrating each other, causing the atomic orbitals to overlap and
face repulsive Bonn
repulsive forces.
Addition of Electrolytes decrease
the height of the primary maxima and the range over which the
electrostatic repulsion is effective, and hence lead to coagulation. The lowest
concentration at which an electrolyte coagulates the sol is called coagulation
value, Cv. It does not depend on valence of the anion, but
depends on the valence of the counterions, decreasing by one or two orders of
magnitude for each increase in heir valencies. This is the Schulze-Hardy
rule.
Effects of added solvents:
The addition of water
miscible solvents e.g. alcohol, glycerin, propylene glycol or polyethylene
glycol (to aqueous dispersions) lowers the dielectric constant ε of the
medium. This reduces the thickness of the double layer and therefore the range
over which electrostatic repulsion is effective, and lowers the size of
potential energy barrier. Thus addition solvents to aqueous dispersion lead to
coagulation. At concentration to low to cause coagulation, solvents make
dispersions more sensitive to coagulation by added electrolytes, i.e. they
lower the Cv
Stabilization by adsorbed
surfactants:
Recall that surfactant molecules
are amphiphiles having a polar and
non-polar parts. When placed in a medium of dispersed system, they accumulate
at interfaces and orient themselves in such a way that the hydrocarbon
(non-polar) part is in contact with non-polar particles or oil droplets while
the polar group is oriented towards the polar (usually water) phase. This is
known as oriented physical absorption. The adsorption of ionic
surfactants increases the charge density and the zeta potential ζ of disperse
particles. This in turn increases electrostatic repulsion among non-polar
organic particles and hence stabilization of the system. This is known as charge
stabilization.
Water-soluble non-ionic
surfactants are usually hydrated making the particle surface where they are
adsorbed to be surrounded by a thin layer of water. This hydrophilic shell
forms a steric barrier which prevents close contact between particles and hence
coagulation. This known as steric stabilization. Moreover, non-ionic surfactants
reduce the sensitivity of hydrophobic sols towards coagulation by salts, i.e.
they increase the coagulation value Cv.
Surfactants added to a
flocculated sol tend to pry apart the flocs by wedging themselves between the
particles and their area of contact. This allows in more surfactant molecules
and hence breaks-up the flocs. The system becomes deflocculated or undergoes peptization.
Peptization is defined as
formation of colloidal dispersion by action of solvent i.e. breaking up of
large particles into colloidal range. Peptization can be spontaneous e.g.
albumin and water form a “solution” due to extensive solvation. But some action
may be needed to bring about peptization. E.g. precipitated substances may be
brought into colloidal dispersions either by providing a peptizing agent usually
a surfactant, or by removing a flocculating agent similar to
deflocculation). When activated charcoal is added to water with stirring,
grains are broken up incompletely. The suspension is no good. Addition of 0.1%
sodium laurylsulphate or octoxynol disintegrates the particles to fine ones and
the dispersion changes color from gray to deep black. Alumium hydroxide Al(OH)3
in the presence of aluminium chloride (AlCl3) is a poor colloidal
dispersion. Washing with water removes AlCl3 and a good colloidal
dispersion forms.
Ophthalmic and parenteral
suspensions should be deflocculated to prevent irritation and capillary
blockage respectively. But because deflocculated systems tend to cake, a
process of controlled flocculation is used in preparing such suspensions.
Stabilization by adsorbed
polymers;
Water-soluble polymers act like
surfactants and are adsorbed at interface. The polar part attracts and encloses
water of hydration forming a sheath that surrounds the particles. This layer is
part of the particles and prevents the particles from touching each other to
coagulate. This kind of steric stabilization is said have protective
action. The sol thus protected has resistance to coagulation by salts. The
water-soluble polymers whose adsorption stabilizes hydrophilic sols
against coagulation are called protective colloids, e.g. gelatin, serum
albumin, povidone and dextran. The stabilizing efficiency of a protective
colloid is determined by its gold number. (define the gold number
of a polymer)
Some protective colloids at
concentrations below those at which they exert a protective action may cause sensitization,
i.e. a decrease in the stability of hydrophobic sols.
ELECTROKINETIC PHENOMENA
Electrokinetic phenomena include Electrophoresis,
electrosmosis, sedimentation potential and Streaming potential, whereby a
potential is created when charged particles move with respect to a stationary
liquid or particles move upon application of a potential. The phenomena are
evidence that particles are charged.
Electrophoresis:
When a dc electric field is
applied to a dispersion, the particles move towards the electrode of a charge
opposite to that on their surface. The counterions located inside their hydration
shell are dragged along. The counterions in the diffuse layer outside the plane
of shear will move towards the other electrode. This phenomenon is called
electrophoresis. The rate of migration of particles is observed by means of an
ultramicroscopic and is a function of the charge on particle. As mentioned
earlier, the potential at the plane of shear is the Zeta potential. The sign
and magnitude of zeta potential can be measured from a knowledge of the
direction and rate of migration.
ζ = ν
x 4πη x (9 x 104)
E ε
Where ν is the velocity of
migration (cm/sec)
η = viscosity of the medium
(poise), ε is the dielectric constant
E is potential gradient
(volts/cm).
ζ is in volts.
The expression v/E is known as mobility.
Sedimentation potential:
The reverse of electrophoresis,
that is a potential is created when particles undergo sedimentation (against a
stationary liquid).
Electrosmosis:
If a charged surface is immobile
(e.g. a packed bed of particles), application of an electric field causes the counterions
in the free water to move towards the opposite electrode, dragging the solvent
with them. Thus the liquid moves relative to the stationary charged surface,
and the phenomenon is known as electrosmosis. The pressure produced is the
electroosmotic pressure. By determining the rate of flow of a liquid under
standard conditions, Zeta potential can be measured.
Streaming potential
If the liquid is made to flow
past a charged surface in a capillary tube by applying hydrostatic pressure,
the displacement of the counterions in the free water produces a potential
difference between the two ends of the tube or bed. This potential is known as
Streaming Potential. Measuring this potential, Es, and knowing the applied
pressure, P, we can obtain from zeta potential from the following equation:
ζ = 4πηκΕl
εP
ELECTROKINETIC PROPERTIES OF COLLOIDS
Particles in a liquid medium may become charged. Because
of this charge on the surface of the particles, electro kinetic properties
arise.
There are several ways in which a colloidal particle may
acquire a charge:
·
Selective adsorption of a particular ion
species present in a dispersion or a solution. The ion may have been added to
the solution or in the case of water, it may be the hydronium (H+)
or hydroxyl (OH- ).
Thus particles in water are negatively charged due to preferential adsorption
of (OH- )
ions. Ionic surfactants are also adsorbed and impart corresponding charge.
·
Particles also acquire charge through ionization
of groups or moieties at the surface. In proteins, one end of the polypeptide
has carboxylic acid group (COOH) which ionize to give a negative charge. The
other end group has amino group (NH2) and ionize to give a positive
charge. The predominating charge depends on the pH of the medium. Thus the
particles may be negatively or positively charged or neutral. Similarly
Aluminium hydroxide gel (Al(OH)3) form Al3+ in acid and
[Al(OH)]4+ in alkalis.
·
Non-ionizing particles may also acquire a charge
due to a difference in dielectric constant between the disperse phase
and the dispersion medium. The phase with a greater e acquires a negative
charge.
Electric Double Layer.
Due to a charge on the particles
in a colloidal sol, ions of opposite charge are attracted firmly to the surface
of the charged particle to form a layer.
The ions of opposite charge further distribute themselves diffusely in the vicinity of the particle to form a second
layer. The two layers constitute a phenomenon known as the electrical double
layer. Although the particle is charges, the system is electrically neutral,
because the two layers described above neutralize each other.
In order to understand the
electrical double layer better, let us follow an example of silver iodide sol.
Silver iodide may be obtained in the following reaction:
------>AgNO3 + NaI Ag I
+ NaNO3
If the reaction is carried out
with excess AgNO3 there will be excess Ag+ than I – ions
on the surface of the AgI precipitate, and the particle will be positively
charged. The NO3- ions will surround the particles and
will form the first layer. Na+ and other NO3-
ions will distribute diffusely to form the second layer of the electrical
double layer. If on the other hand there were excess of NaI in the
reactants, the surface would contain negative charge.
In the bulk of the particle, the two ions (Ag+
and I-)are exactly I equimolar proportions. In the medium (water)
where the particles are suspended, Na+ and NO3-
ions dominate, and some I – , H+, OH- ions are also apparent.
The negative charge on the surface of the particle
attracts positive ions from the solution, and repels negative ions. These I –
ions adsorbed at surface are known as potential determining ions. They
attract oppositely charged ions from the medium to the surface. Thus, Na+ are
concentrated in the immediate vicinity of the surface and tend to stick to the
surface, approaching it as closely as their hydration spheres permit. Na+ Ions
in this respect are called counterions or gegenions. They form a
compact layer called Stern layer.
NO3- ions are repelled, and together
with some Na+, I –, H+, OH- and Ag+
, due to thermal agitation of water, form a second diffuse layer called the Gouy-Chapman
layer. The combination of the two layers of oppositely charged ions
constitutes an Electric double layer.
The electric potential at the surface of the particle is
equal to the work against electrostatic forces required to bring a unit
electric charge from the bulk of the solution (infinity) to the surface of the
particle, and is known as surface potential or Electrothermodynamic
potential or Nernst Potential g0. On
moving away from the surface towards the bulk, the potential drops rapidly
across the Stern layer (Na ions screen further removal of other Na ions in the
diffuse part of the double layer).In the Gouy-Chapman layer, the drop of
potential is more gradual, tending to zero asymptotically as the composition of
cations and anions approach equilibrium. The thickness of the double layer has
been arbitrarily assigned the value of 0.37go.
(0.37 = 1/e). It usually ranges from 10 – 1000 Å and
decreases as the concentration of electrolytes in solution increases, more
rapidly for counter ions of high valence.
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