Theories of Emulsification

Theories of Emulsification
In the case of two immiscible liquids, the cohesive force between the molecules of each separate liquid exceeds the adhesive force between two liquids. This is manifested as interfacial energy or tension at the boundary between the liquids.  Therefore, to prevent coalescence and separation, emulsifying agents have been used.


Surfactant: Adsorbed at oil/water interface to form monomolecular film to reduce the interfacial tension. e.g., Tween and Spans. 


Hydrophilic colloids: Forming a multimolecular film around the dispersed droplet.  e.g., Acacia. 


Finely divided solids: They are adsorbed at the interface between two immiscible liquid phases to form particulate film. e.g., Bentonite and veegum. 


(a) Monomolecular adsorption:

The surface active agent (SAA) is a molecule that has two parts, one is hydrophilic and the other is hydrophobic. Upon the addition of SAA, they tend to form monolayer film at the oil/water interface. 


The functions of surface active agents to provide stability to dispersed droplets are as  follows: 


Reduction of the interfacial tension. 


Form a coherent monolayer to prevent the coalescence of two droplets when they approach each other. 


Provide surface charge which causes repulsion between adjusted particles. 


Bancroft rule 

As per the Bancroft rule, the emulsifying agent being used in an emulsion should be favorable to the external phase of the emulsion. 


So even though there may be a formula that is 60% oil and 40% water, if the emulsifier chosen is more soluble in water, it will create an oil-in-water system.


The Hydrophilic-Lipophilic Balance (HLB) of a surfactant can be used to determine whether it is a good choice for the desired emulsion or not. 


In Oil-in-water emulsions, use emulsifying agents that are more soluble in water than in oil (High HLB surfactants). 


In Water in Oil emulsions, use emulsifying agents that are more soluble in oil than in water (Low HLB surfactants). 


(b) Multimolecular adsorption

 

Polysaccharides

Amphoteric

Synthetic or semi-synthetic polymers

Colloids

Acacia

Agar

Alginic acid

Carrageenan

Guar gum

Karraya gum

Tragacanth

Gelatin

Carbomer resins

Cellulose ethers

Carboxymethyl chitin

PEN-n (ethylene oxide polymer)


Hydrophilic colloids form multimolecular adsorption at the oil/water interface. They have a low effect on the surface tension. 


• Their main function as emulsion stabilizers is to make a coherent multi-molecular film. This film is strong and resists the coalescence. They have, also, an auxiliary effect by increasing the viscosity of the dispersion medium. 


(c) Solid particle adsorption 

Finely divided solid particles are adsorbed at the surface of the emulsion droplet to stabilize them. Those particles are wetted by both oil and water (but not dissolved) and the concentration of these particles forms a particulate film that prevents the coalescence.


Finely divided solids

Bentonite 

Hectorite 

Kaolin 

Magnesium aluminium silicate 

Montmorillonite 

Aluminium hydroxide 

Magnesium hydroxide 

Silica

 Emulsion Stability 

The process by which an emulsion completely breaks is generally considered to be  governed by four different droplet loss mechanisms, i.e. 


• Brownian flocculation, 


• Creaming, 


• Sedimentation flocculation and disproportionation.

 

Mechanism leading to coalescence of an oil in water emulsion

Fig: Mechanism leading to coalescence of an oil in water emulsion 

Creaming – upward and downward 

• Creaming derives its name from the most commonly known example of a demulsification process.

 

• The separation of milk into its cream and skim milk components. Creaming is not an actual breaking but a separation of the emulsion into two emulsions, one of which  (the cream) is richer in the disperse phase than the other. Creaming is the principal process by which the disperse phase separates from an emulsion and is typically the precursor to coalescence. 


• The creaming rate (or settling rate for dispersed phases more dense than the  continuous phase) can be estimated from Stoke's equation:


υ = 2r2 (ρ − ρ0) g/9η


where υ is the creaming (settling) rate, r is the droplet radius, ρ is the density of the droplet, ρo is the density of the dispersion medium, η is the viscosity of the dispersion medium (continuous phase) and g is the local acceleration due to gravity. 


Flocculation 

• The aggregation of droplets to give 3-D clusters without coalescence occurring.  Importantly, all droplets maintain their own integrity and remain as totally separate entities. It results when there is a weak, net attraction between droplets and arises through various mechanisms.


• Flocculation may be subdivided for convenience into two general categories: that resulting from sedimentation aggregation and that from Brownian motion aggregation of the droplets. 


Disproportionation or Ostwald ripening 

• It is dependent on the diffusion of dispersed phase molecules from smaller to larger droplets through the continuous phase. 


• The pressure of dispersed material is greater for smaller droplets than larger droplets as per the Laplace equation. 


Coalescence 

• A few globules tend to fuse with each other and form bigger globules. 


• In this process, emulsifier film around the globules is destroyed to some extent. 


Breaking 


• Complete separation of phases, irreversible process. 


Phase Inversion 


In phase inversion o/w type emulsion changes into w/o type and vice versa. It is a  physical instability. 


• It may be brought about by the addition of an electrolyte, by changing the phase volume ratio by temperature changes, or by changing the chemical nature of the emulsifier  Phase inversion can be minimized by using the proper emulsifying agent in adequate concentration, and by storing the emulsion in a cool place.

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