Open Access
Issue
OCL
Volume 19, Number 2, Mars-Avril 2012
Page(s) 111 - 119
Section Dossier : Fonctionnalités des huiles
DOI https://doi.org/10.1051/ocl.2012.0438
Published online 15 March 2012

© John Libbey Eurotext 2012

Introduction

Emulsions are generally obtained by shearing two immiscible fluids, leading to the fragmentation of one phase into the other. The fragments (droplets) adopt a spherical shape whose typical size varies between 100 nm and several tens micrometers. The two immiscible liquid phases are generally oil and water, for which the surface tension (energy of contact) is nonzero. Emulsions can be classified on the basis of the organization of the two immiscible phases. If the oil droplets are dispersed in the water phase, then it is called an Oil-in-Water (O/W) emulsion, whereas the inverse is known as a Water-in-Oil (W/O) emulsion. The material within the droplets is usually referred to as the dispersed or internal phase, whereas the material that makes up the surrounding liquid is called the continuous or external phase. The fabrication of emulsions requires the presence of surface-active (amphiphilic) molecules, whose chemical structure comprises both hydrophilic and lipophilic moieties. They thus tend to adsorb and concentrate at the boundary between the oil and water (called “interface”) at the droplets surface. Molecules made of a linear hydrocarbon chains (between 10 and 20 methyl segments) and a polar head group, commonly named surfactants, fall into this class of molecules. Biopolymers like proteins or some polysaccharides may also be used as surface-active species. Their functional role in emulsions is crucial since (i) they facilitate the emulsification process, (ii) they prolong the shelf life of the emulsions (see below) and (iii) they determine the emulsion type (O/W or W/O) according the well known Bancroft rule (“the phase in which the surfactant is preferentially soluble tends to become the continuous phase”) (Leal-Calderon et al., 2007).

The surface tension (σ) is a measure of the cohesive energy arising from the imbalance of forces between the molecules at an interface. When two immiscible phases are in contact with each other, then the molecules at the interface experience an imbalance of forces. This will result in an increase of the free energy at the interface. This excess free energy can be quantified as the amount of energy required to create a new surface or as the force that acts perpendicular and inward from the boundaries of the surface to reduce the area of the interface. The unit of interfacial tension in the SI system is N.m−1. From a thermodynamic point of view, emulsions are out-of-equilibrium (metastable) systems because of surface tension. As such, they tend to evolve over time towards the total phase separation of the two immiscible phases. As a matter of fact, the kinetic stability of emulsions is strongly dependent on its formulation, and especially on the type and concentration of the dispersed phase and of the surface-active species. Because the shelf life of these materials may become significant (from weeks to years) they are suitable for various commercial applications.

Emulsions of the O/W type are widely used because of their ability to safely transport and deliver hydrophobic substances through an aqueous continuous phase. All kinds of surface treatments are based on emulsion technology: painting, paper coating, road surfacing, etc. Because homogeneous mixtures of two immiscible fluids may be obtained, hazardous solvents may be avoided when transporting hydrophobic substances. Once the emulsion is spread, water evaporates and is released into the atmosphere, while the dispersed phase concentrates, leading to the formation of a hydrophobic film. Moreover, emulsion technology significantly simplifies the handling and pouring of many hydrophobic substances. Indeed, at ambient temperature some materials may be almost solid, whereas by dispersing them in water, they remain fluid. Typical examples are bitumen used for road surfacing or silicon oil used to ensure water-tightness in bathroom fittings. Emulsions are also involved in food and cosmetic industry because of the large variety of rheological properties and sensory profiles that may be achieved. Moreover, they are also efficient drug carriers (medicines, food, and pesticides) for various biological targets.

The ingredients of emulsions self-organize under the effect of physical (intermolecular or interdroplet forces, phase separations), chemical (formation of covalent bonds) and biological (fermentation, etc.) factors. Because emulsions are metastable systems, their initial microstructure evolves over time during storage and/or transportation as a result of thermal treatments, mechanical stresses, physical coarsening and biological action. An important challenge for emulsion science is therefore to understand and control the evolution of colloidal interactions, microstructure and rheological properties during processing, storage, transportation, application and even ingestion (food emulsions).

All the industrial applications have already led to an important empirical control of emulsions from their preparation to their destruction. The scientific background of emulsions has also progressed over the last decades and in this tutorial review we aim to give an overview of some recent advances, emphasizing the functionality of the ingredients, the control of the rheological properties through the formulation or upon application of a shear, and the coarsening (ageing) mechanisms.

Overall composition and fabrication

The behavior of emulsions is determined by the three phases of the system: the fat or oil phase, the interfacial phase and the aqueous phase. Understanding the structural properties of emulsions requires a precise knowledge of the behaviors of these three phases, both individually and cooperatively. In O/W emulsions based on lipids, the dispersed phase is mainly composed of triglycerides that may be partly or totally crystallized depending on the temperature. The aqueous phase may contain ions, biomolecules such as polysaccharides or proteins, etc. which may exert stabilizing or destabilizing effects.

The interface may be composed of proteins, amphiphilic polymers and/or small surfactants. The surface-active species that can be used is restricted by regulations, cost considerations and practical factors, such as ease of utilization reliability of source and compatibility with other ingredients. Common stabilizers used in the food, cosmetic and pharmaceutical industries to formulate emulsions are:

  • amphiphilic proteins like whey protein isolates, caseinates, soy protein isolates;

  • amphiphilic polysaccharides like modified starch, locust beam gum, gum Arabic, etc.;

  • low-molecular weight surfactant molecules like “Spans” (sorbitan fatty acid esters), “Tweens” (ethoxylated sorbitan esters), fatty acids, mono- and di-glycerides;

  • phospholipids like egg, soy or dairy lecithin.

Being metastable, emulsions are not formed spontaneously once the ingredients are put in contact. Instead, their manufacturing generally requires the application of an intense shear. A variety of methods have been developed to prepare emulsions which can be classified as either turbulent or laminar flow techniques. Turbulent flow techniques are based on mechanical devices generating turbulence and cavitation phenomena that allow breakup of the dispersed phase and lead to the formation of tiny droplets. Among these techniques, we can mention high-pressure homogenizers, microfuidizers or turbulent blade-type mixers (Leal-Calderon et al., 2007). Laminar flow techniques rely on the application of low shear rates in highly viscous emulsions. In this regime, the applied stress , where η is the emulsion viscosity, must be large enough to produce droplet elongation and further break-up according the so-called Rayleigh instability (Mabille et al., 2000). Droplet fragmentation is possible at low shear rates provided the average emulsion viscosity is large enough.

A conventional emulsion typically has droplets with mean radii between 100 nm and 100 μm. Conventional emulsions are optically opaque because the droplets have similar dimensions to the wavelength of light and so they scatter light strongly. A nanoemulsion is an emulsion that contains very small droplets, i.e. mean radii between 10 to 100 nm. One of the main attractions of nanoemulsions over conventional emulsions is that they tend to be optically transparent. Consequently, they can be used to incorporate lipophilic bioactive molecules into transparent, aqueous-based products or beverages without altering too much their appearance. Nanoemulsion delivery systems may also protect the encapsulated bioactives against environmental stresses (e.g. pH, oxygen, and degradation by enzymes), and increase the bioavailability of the encapsulated bioactives because of their small droplet size and high surface-to-volume ratio (McClements, 2011). Nanoemulsion-based delivery systems are well established in the pharmaceutical domain where they improve the oral bioavailability and biological efficacies of lipophilic drugs (Shah et al., 2010). Nanoemulsions are attracting much interest in the food and nutraceutical industries owing to their potential to incorporate and maximize the health benefits of lipophilic functional components within food products (e.g. ω-3 fatty acids, α-tocopherol, lycopene, lutein, coenzyme Q10, etc.).

Ageing: coalescence and Ostwald ripening

Once formed, the shelf life of emulsions may vary from a few hours to years depending on formulation and process parameters. Figure 1 illustrates the main mechanisms of physical emulsion instability. Some instabilities involve droplet aggregation and are generally reversible; others, related to droplet size evolution, are irreversible (Leal-Calderon et al., 2007). Reversible flocculation may lead emulsions to cream (O/W emulsions) or sediment (W/O) depending on the overall density mismatch between the droplets and the continuous phase. Meanwhile, irreversible droplet size increase may occur through two different mechanisms: Ostwald ripening and coalescence.

thumbnail Figure 1.

Schematic representation of the different instabilities in emulsions. A) creaming or sedimentation due to the density mismatch between the drops and the continuous phase; B) flocculation (aggregation) followed by creaming (O/W emulsions); C) Ostwald ripening (Diffusion of dispersed molecules from small droplets to large ones across the continuous phase, because of the difference in Laplace Pressure); D) coalescence (the drops recombine ultimately leading to the total phase separation of the two immiscible phases).

If the average diameter in the emulsion is lower than approximately 1 μm, the droplets are submitted to thermal (Brownian) motion that delays gravity induced phase segregation phenomena. However, creaming or sedimentation is accelerated if the droplets undergo flocculation. For instance, high levels of salt are known to promote aggregation in emulsions by screening the repulsive interaction between the droplets. Above a critical salt concentration, the electrostatic repulsion is no longer sufficient to overcome the attractive van der Waals forces (Israelechvili, 1985). Protein-stabilized emulsions appear to be more stable to high salt levels than conventional emulsions because the presence of a thick protein layer induces a long-range steric repulsion (Israelachvili and Wennerström, 1992; Dimitrova et al., 2004). Two emulsions droplets may also attract each other when surrounded by smaller species. This attraction is purely entropic in origin: when the two large droplets approach, the small species may be expelled, leading to an uncompensated pressure within the depleted region. The so-called depletion attraction scales with the osmotic pressure of the small species and also with the size of the depleted volume in between the two large interacting droplets (Asakura and Oosawa, 1958). Various types of tiny colloidal species may produce depletion flocculation, when present in large excess in the continuous phase: polymer coils (Meller and Stavans, 1996), surfactant aggregates (micelles) (Aronson, 1989; Bibette et al., 1990), or proteins (Dickinson et al., 1997).

Coalescence occurs when two droplets collide and finally merge. At a microscopic scale, a single coalescence event between two drops in contact proceeds through the nucleation of a channel that reaches a critical size, above which it becomes unstable and grows. For a coalescence event to occur, an energy barrier has to be overcome (Kabalnov and Wennerström, 1996). Its origin is still a matter of debate but it is now well admitted that the activation energy may be determined by several interfacial parameters: surface forces, surface tension, dilatational elasticity, spontaneous curvature, etc. (Kabalnov and Wennerström, 1996; Leal-Calderon et al., 2007). When coalescence is the main destabilization mechanism, the time evolution of the average droplet size is self-accelerated and the size distribution broadens (Schmitt et al., 2004).

Ostwald ripening (OR) consists of the net transport of oil from small droplets to larger ones through the continuous phase. OR in O/W emulsions occurs via the molecular dissolution of oil in the continuous phase. It is driven by the dependence of the oil solubility with droplet size:(1)where C(r) is the solubility of the emulsified oil, C(∞) is the oil solubility close to a planar interface, r is the droplet radius, σ is the interfacial tension, Vm is the oil molar volume and R is the ideal gas constant. Equivalently, this means that the chemical potential, μ(r), of the dispersed phase depends on the droplet radius, r:(2)where μ(∞) is the chemical potential at a planar interface. The second term in the rand-hand side of eq. 2 represents the energy due to the additional pressure within the droplets with respect to the continuous phase, also known as Laplace pressure (2σ/r). Thus OR arises from the difference in chemical potential between small and large emulsion droplets.

The theoretical models developed by Lifshitz-Slesov (1961) and Wagner (1961) predict a linear relationship between the cube of the average emulsion radius <r> and time, the slope of which is:(3)where D is the molecular diffusion coefficient of the dispersed molecules in the continuous phase and ρ is the density of the dispersed phase. The theory also predicts that the size distribution remains narrow and self-similar over time, that is the same distribution is obtained when plotted as a function of r/<r>.

OR can be slowed down by dissolving in the dispersed phase a second oil with much lower water solubility (Higuchi and Misra, 1962). The concept is based on the entropy of mixing that opposes OR (Kabanov, 2001). When a mixed oil emulsion undergoes OR, the soluble oil has greater mobility. Over time, the larger droplets become enriched with the soluble oil whereas smaller droplets become enriched with the insoluble compound. This situation creates an osmotic pressure mismatch that tends to drive the soluble oil back to the smaller droplets, thus compensating the effect of OR. In an ideal mixture, the chemical potential of the soluble oil is given by:(4)where xi is the mole fraction of insoluble oil in the droplet. The Laplace pressure term in the rand-hand side of this equation is always positive. Compared with eq. 2, the additional term represents the entropy of mixing, which is negative for any fraction xi. It can be deduced from eq. 4 that an emulsion can be stabilized against OR provided the fraction of the insoluble compound is large enough. According to Kabalnov’s theoretical treatment (2001), the entropic stabilization is obtained when the osmotic pressure of the insoluble compound is comparable to Laplace pressure. The minimum amount of insoluble compound to be incorporated is thus:(5)where <r0> is the initial average droplet diameter of the emulsion. Considering “reasonable” numerical values, namely σ = 10−2 N.m−1, Vm= 10−3 m3.mol−1, <r0> = 0.5 μm, the molar fraction of insoluble oil xi,min has a value of 1.6% at T = 298 K.

In practice, the main factor determining the rate of OR is the water solubility of the oil phase, C(∞). This is why, OR is not usually a concern for emulsions based on oils with very low water solubility such as long chain triglycerides. Instead, OR may occur rapidly for fine emulsions (<r> <<1 μm) prepared using oils with a significant water-solubility like short chain triglycerides, essential oils, etc. (Wooster et al., 2008). In this latter case, OR can be arrested by dissolving for instance a long chain triglyceride within the oil phase prior to the emulsification at a mole fraction given by eq. 5.

Interdroplet interactions in the presence of protein-polysaccharide mixtures

Proteins and polysaccharides play a key role in the stabilization of food emulsions. Mixtures of both biopolymers can be found in the ingredients of a wide range of products like mayonnaise or ice cream. Proteins are primarily used as emulsifying agents. Polysaccharides are used to inhibit gravity-induced creaming and further phase separation in W/O emulsions during long-term quiescent storage. The main effect of polysaccharides is based on the viscosity increase of the aqueous continuous phase located in the gaps between the dispersed droplets. This is certainly a realistic explanation at low oil volume fractions, where the well-dispersed droplets can be separately immobilized in an entangled polysaccharide network, and the buoyancy force acting on each droplet is insufficient to overcome the yield stress of the surrounding gel. For moderately concentrated emulsions (say 30 vol. % oil), this explanation has to be revised because the evolving microstructure of the emulsion is highly heterogeneous (Moschakis et al., 2006). Indeed, in concentrated O/W emulsions, the mechanism by which hydrocolloid thickeners control creaming phenomena involves the interconnected depletion-flocculated network of oil droplets.

The overall stability and texture of food emulsions containing biopolymer mixtures depends not only on the intrinsic properties of the individual ingredients, but also on the nature and strength of the protein-polysaccharide interactions. In some cases, protein and polysaccharide interactions may synergistically improve the overall emulsion stability. When attractive forces arise between them, complexation results and the protein-polysaccharide complexes that may adsorb at the oil/water interface and efficiently stabilize oil-in-water emulsions (Neirynck et al., 2007). When protein-stabilized emulsions are subjected to heat treatment, for pasteurization or sterilization purposes, they generally tend to aggregate because of protein denaturation and bridging and the resulting emulsions become flocculated. However, incubation of protein-polysaccharide mixtures at high temperature may result in covalently linked amphiphilic conjugates whose adsorption at the droplet surfaces enhances the repulsive steric interactions. The resulting emulsions exhibit no sign of droplet aggregation after prolonged heating and remain stable against creaming (Diftis and Kiosseoglou, 2006).

Bulk rheological properties of concentrated emulsions

Since emulsions are dispersions of deformable droplets, they can span droplet volume fractions from zero to almost one. Much effort has been spent in studying the rheology of diluted emulsions. At low volume fraction, emulsions consist of spherical droplets and such systems flow easily and exhibit shear-thinning behavior. A significant change in the rheological behaviour is observed if the droplets are concentrated up to volume fractions higher than the fraction φ* corresponding to the random close packing of hard spheres. For randomly packed monodisperse spheres, φ*=0.64. Above φ*, the droplets can no longer pack without deforming (figure 2); although being composed of fluids only, emulsions resemble an elastic solid as they do not flow under they own weight. The elasticity arises because the repulsive droplets have been concentrated up to a sufficiently large volume fraction that permits the storage of interfacial energy (Princen, 1986; Princen and Kiss, 1986). Two compressed droplets will begin to deform before their interfaces actually touch, due to the intrinsic repulsive interactions between them. Emulsions minimize their total free energy by reducing the repulsion, which may have different origins, at the expense of creating some additional surface area by stretching the droplet. The excess surface area of the droplets determines the equilibrium elastic energy stored by the interfaces. When a small sinusoidal shear stress, τ, is applied to an emulsion, the resulting strain, γ, is proportional to τ, with τ=G γ. The shear modulus, G, is determined by the additional excess surface area created by shear deformation. This latter is frequency-dependent and can be considered as the sum of two contributions. The in-phase contribution, G′, is linked to the stored energy (solid-like behavior), while the π/2 out-of-phase contribution, G′′, is related to the dissipated energy (fluid-like behavior). Both moduli are increasing functions of the droplet fraction. In concentrated emulsions, the elastic modulus is significantly higher than the loss modulus, reflecting the essentially solid nature of the materials. Interestingly, when normalized by half the Laplace pressure (σ/<r)>), the rescaled data of G’ and G” all fall onto single master curves, whatever the average droplet size of the emulsions as shown in figure 3 (Mason et al., 1995). The scaling with Laplace pressure confirms that the origin of elasticity results from the storage of energy due to the stretching of the interfaces. Moreover, the scaling with the droplet fraction indicates that the elasticity of these compressed droplets depends only on the packing geometry.

thumbnail Figure 2.

Evolution of the rheological properties in monodisperse emulsions as a function of the droplet volume fraction, φ.

thumbnail Figure 3.

Evolution of the shear moduli G’ and G”, normalized by Laplace pressure, as a function of the droplet volume fraction, φ, for monodisperse emulsions.

Proteins adsorbed at the oil-water interface are tightly packed and may experience strong lateral attractive interactions. They form bi-dimensional layers at the interface with intrinsic 2D viscoelastic properties. As a consequence, droplet deformation is controlled not only by Laplace pressure but also by the 2D interfacial viscoelastic properties. This is why the dimensionless shear elastic modulus G’/(σ/<r>) of protein-stabilized emulsions is generally larger than for low-molecular-weight surfactant-stabilized emulsions (Dimitrova et al., 2001; Bressy et al., 2003; Derkatch et al., 2007).

Emulsions based on crystallizable oils

Very often the dispersed phase in emulsions is composed of totally or partially crystallized oils. For instance, this is the case of dairy emulsions. Upon cooling, the spherical and smooth surface of the warm dispersed droplets which is controlled by surface tension evolves into a rough and rippled surface due to the formation of irregularly shaped/oriented crystals. In such conditions, the droplets are prone to the so-called “partial coalescence” phenomenon (Boode and Walstra, 1993). Crystals located nearby the oil/water interface can protrude into the continuous phase and when such crystals are present within the thin film separating two droplets, they may pierce it and bridge the surfaces, causing the droplets to coalesce (figure 4). If the crystallized fraction within the globules is sufficient, the intrinsic firmness of the fat network hinders relaxation to the spherical shape driven by surface tension after each coalescence event. As time passes, large clusters appear and grow by the accretion of any other primary droplet or cluster until a rigid network made of partially coalesced droplets is formed, in which the original droplet shape remains recognizable.

thumbnail Figure 4.

Scheme of the partial coalescence process. Fat crystals protruding from the interface pierce the film in between two adjacent droplets. Shape relaxation is inhibited because of the intrinsic firmness of the solid fat network.

Large surface-active species like proteins are highly efficient in stabilizing partially crystallized droplets against partial coalescence. The emulsions then exhibit long-term kinetic stability in quiescent storage conditions and can even be submitted to high shear forces without being destroyed. Instead, surfactants with short molecular chain length generally do not provide a sufficient degree of stabilization and the emulsions may become lumpy a few hours after their preparation. Addition of small amounts of surfactant in protein-stabilized emulsions is a common way to monitor the sensitivity towards partial coalescence (Thivilliers et al., 2008; Fredrick et al., 2010). The displacement of proteins from the oil interface by added surfactants (Mackie et al., 1999) contributes to emulsion instability and induces sensitivity to partial coalescence.

Thermally induced partial coalescence

Partial coalescence may be provoked in quiescent conditions upon application of a specific thermal treatment called “Tempering”. Tempering consists of applying a temperature cycle that produces partial melting of the crystal mass (warming step), followed by recrystallization (cooling step). Tempering is known as an efficient way to transform an initially fluid cream into a material with thick or solid consistency (Boode et al., 1991). Thivilliers et al. (2006) observed a significant increase in the emulsion firmness in triglyceride (anhydrous milk fat and cocoa butter)-in-water emulsions stabilized by sodium caseinate/surfactant mixtures. Owing to temperature cycling, the initially fluid emulsions turned into hard gels that became trapped into a deep metastable state as they could be stored for several weeks without any appreciable change. The gel structure formed after a long interval of tempering was a continuous network of partially aggregated fat droplets. The progressive increase of the bulk elastic modulus G’ during tempering was interpreted within the frame of percolation theory. The results suggest that partial coalescence involves irreversible bridging between a crystallized patch in one droplet surface and a melted patch on an adjacent droplet surface (figure 4). Consequently, the rate of partial coalescence reaches a maximum value for a well-defined solid fraction within the oil phase. It was also shown that the coalescence rate and thus the gelling kinetics were controlled by the oil solid fraction, the average droplet size and the surfactant-to-protein molar ratio.

Gelling in emulsions has also been studied in model crystallisable droplets made of alkanes or paraffin oils with high melting temperature. Following the pioneering work of Golemanov et al. (2006), Kahn et al. (2007) have investigated two possible routes to produce emulsion gels in quiescent conditions, both of them exploiting the crystallized state of the droplets (figure 5). One is due to partial coalescence which induces formation of a rigid network of interconnected droplets. This scenario occurs preferentially when the average droplet size is large. The second route occurs without film rupturing (no coalescence) and is provoked by a restriction of the internal dynamics (“jamming”) due to surface roughness. This latter situation is preferentially observed in emulsions with small average droplet diameter.

thumbnail Figure 5.

Two possible configurations for gelled materials based on crystallizable droplets: partial coalescence and jamming. When partial coalescence occurs, the elasticity arises from the network of interconnected droplets, whereas in the jamming process the elasticity is due to the fact that the individual droplets cannot slide one against each other because of surface roughness (flow hindering).

Shear-induced partial coalescence

Shear forces due to processing may induce dramatic and irreversible changes in the structure of materials comprising semi-solid droplets. For instance, the fabrication of viscoelastic aerated foods like whipped creams or ice creams is based on the application of intense mechanical agitation which promotes the formation of an interconnected droplets network (van Aken, 2001; Drelon et al., 2006). Shear-induced partial coalescence is also exploited to separate fat from the aqueous phase of native dairy creams in order to obtain butter. Many cosmetic products are oil-in-water emulsions containing semi-crystalline waxes and the texture of such materials is controlled by the instabilities occurring under shear. The evolution scenario depends on the formulation, temperature, and shear history of the sample.

Many papers in the literature have reported destabilization of emulsions made of partially and/or fully crystallized droplets submitted to shear (Hinrichs and Kessler, 1997; Davies et al., 2000; Xu et al., 2005; Guery et al., 2006). Thivilliers-Arvis et al. (2010) provided insight into how semi-solid oil-in-water emulsions may become destabilized by partial coalescence when subjected to moderate shear flows. They designed observation methods to visualize oil-continuous regions that result from coalescence of droplets. Quantitative relations between the composition of the droplets (in terms of solid fraction) and the parameters that characterize the instability onset (magnitude, duration or frequency of the applied strain) were obtained. With these tools, they identified two mechanisms for the propagation of coalescence through the network of partially coalesced droplets. The evolution of the primary emulsions according one of them is mainly determined by the rate of partial coalescence. Emulsions prone to fast coalescence undergo gelling before massive macroscopic clumping occurs. Instead, in emulsions exhibiting low coalescence rates, randomly distributed clumps are formed and grow over time (figure 6). The coalescence rate and thus the destabilization pathway depend on the crystal size and/or protrusion at the oil/water interface, both properties being controlled by the average droplet size and by the protein-to-surfactant molar ratio.

thumbnail Figure 6.

Two possible pathways for the shear-induced evolution in emulsions based on crystallizable oils: (A) formation of a gel that spans over the whole volume and (B) nucleation/growth of randomly distributed clumps (adapted from Thivilliers et al., 2010).

Droplet crystallization may also have a strong impact on the digestion of lipids in food emulsions. The digestion of lipids is not only important in nutrient delivery and intestinal absorption but also plays a key role in satiation and regulation of energy intake (Feinle et al., 2002; Mattes, 2007). The digestion is an interfacial process initiated by the adsorption of lipolytic enzymes to the surface of emulsified lipid droplets. The process is initiated in the stomach by gastric lipases and continues in the duodenum upon the action of pancreatic lipase and co-lipase in the presence of surface-active bile salts (Carrière et al., 1993; Armand et al., 1997; Fave et al., 2004). All ingested lipids turn into emulsions, either during the food manufacturing process or via oral/digestive processing during food consumption. Generally, the pancreas produces an excess of lipase relative to the amount of ingested fat (Carrière et al., 2005; Armand, 2007). Therefore the rate of lipolysis is controlled, not by the amount of enzyme but by its ability to reach the interface of emulsified substrates. This in turn is controlled by the physicochemical characteristics of the oil–water interface, such as interfacial composition and surface area (Armand et al., 1997; Fave et al., 2004; Carrière et al., 2005; Armand, 2007). The surface area of the emulsion droplets is a key parameter affecting the rate of lipid digestion (Fave et al., 2004; Golding and Wooster, 2010). The rate of lipolysis is directly proportional to the area available for lipase adsorption, which scales as the inverse size of the emulsion droplets (Lundin et al., 2008). Golding et al. (2011) have demonstrated that the differences in fat absorption profile achieved by controlling emulsion structural stability during digestion provide a basis for examining the physiological effects of food structure on lipid metabolism. It was found that the major factor controlling the rate of fat digestion in vitro was the droplet surface area available for lipase adsorption, which was governed by emulsion instability. The rate of fat absorption in vivo was only affected by large changes in the droplet surface area (through coalescence), and only if these changes remained until the droplets reached the small intestine. This was most evident in emulsions that had undergone extensive partial coalescence under gastric conditions. Partial coalescence resulted in a dramatic reduction in triglyceride absorption, in part because the network of fat crystals provided the agglomerates with an internal scaffold to resist re-dispersion as they passed through the pylorus (region of the stomach that connects to the small intestine).

Conclusion

Emulsions are out-of-equilibrium materials governed not only by thermodynamic conditions but also by the entire process history. The basic knowledge about the physicochemical properties and kinetic evolution of emulsions is progressing but the inherent complexity of such materials is permanently raising novel fundamental questions at the frontier between physics, chemistry and biology. Many emulsions based on lipids in food, cosmetic and pharmaceutical industries are designed to interact with human body. The behavior of emulsions once ingested, spread on skin or introduced in the bloodstream trough parenteral administration is far to be fully understood and consolidating knowledge in that field would certainly improve their performance (in terms of therapeutic, nutritional, organoleptic, properties). Controlling the fate of emulsions in body is certainly one the most challenging issues of emulsion science within the next years or decades.

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To cite this article: Leal-Calderon F. Emulsified lipids: formulation and control of end-use properties. OCL 2012; 19(2): 111–119. doi : 10.1051/ocl.2012.0438

All Figures

thumbnail Figure 1.

Schematic representation of the different instabilities in emulsions. A) creaming or sedimentation due to the density mismatch between the drops and the continuous phase; B) flocculation (aggregation) followed by creaming (O/W emulsions); C) Ostwald ripening (Diffusion of dispersed molecules from small droplets to large ones across the continuous phase, because of the difference in Laplace Pressure); D) coalescence (the drops recombine ultimately leading to the total phase separation of the two immiscible phases).

In the text
thumbnail Figure 2.

Evolution of the rheological properties in monodisperse emulsions as a function of the droplet volume fraction, φ.

In the text
thumbnail Figure 3.

Evolution of the shear moduli G’ and G”, normalized by Laplace pressure, as a function of the droplet volume fraction, φ, for monodisperse emulsions.

In the text
thumbnail Figure 4.

Scheme of the partial coalescence process. Fat crystals protruding from the interface pierce the film in between two adjacent droplets. Shape relaxation is inhibited because of the intrinsic firmness of the solid fat network.

In the text
thumbnail Figure 5.

Two possible configurations for gelled materials based on crystallizable droplets: partial coalescence and jamming. When partial coalescence occurs, the elasticity arises from the network of interconnected droplets, whereas in the jamming process the elasticity is due to the fact that the individual droplets cannot slide one against each other because of surface roughness (flow hindering).

In the text
thumbnail Figure 6.

Two possible pathways for the shear-induced evolution in emulsions based on crystallizable oils: (A) formation of a gel that spans over the whole volume and (B) nucleation/growth of randomly distributed clumps (adapted from Thivilliers et al., 2010).

In the text

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