Open Access Article
Nadia N.
Nikolova
a,
Stefan K.
Baier
bc and
Vivek
Sharma
*a
aDepartment of Chemical Engineering, University of Illinois Chicago, Chicago, IL 60607, USA. E-mail: viveks@uic.edu
bMotif Foodworks, Boston, MA, USA
cSchool of Chemical Engineering, The University of Queensland, Brisbane, QLD 4072, Australia
First published on 14th January 2026
Mayonnaise is a dense oil-in-water emulsion with over 65% oil, vinegar (or lime juice), and egg as an emulsifier or stabilizer. Conventional mayonnaise, an animal-based (AB) formulation, has flow behavior suitable for dispensing, spooning, spreading, consuming, and use as a salad dressing, dip, and base for sauces. Emulating its texture, flavor, stability, rheology, processability, and sensory attributes is challenging with egg-free recipes that often include plant-based (PB) proteins and hydrocolloids, such as xanthan gum, guar gum, and starch in the aqueous phase. Here, we contrast the rheological responses of commercially available AB and PB mayos under oscillatory strain to assess their linear and nonlinear viscoelastic properties and to assess why the addition of hydrocolloids provides an egg-free alternative with suitable shelf-life and processability. Also, responses assess texture and the first-bite impression and help contrast the mouthfeel that encompasses holistic and dynamic sensations throughout consumption. All mayos display gel-like responses in oscillatory shear at low strain and liquid-like responses beyond the yield stress. All AB mayos show a strain overshoot in the plots of loss modulus against strain, which is absent in the response of vegan mayos that use polysaccharides as hydrocolloids. We contrast the apparent yield stress values from the shear flow curve, the onset of strain softening in the elastic modulus beyond a critical strain, and dripping experiments. Hydrocolloids and proteins with dissimilar interfacial and bulk properties contribute to the contrasting moduli, yielding, and strain overshoot response of real and vegan mayo.
Egg influences the emulsification, flavor, emulsion stability, and rheology of real mayonnaise. Egg yolk contains an abundance of amphipathic lipids, proteins, and lipoprotein complexes (livetin, phosvitin, lipovitellin, and lipovitellenin), whereas egg white is rich in proteins (ovalbumin, ovotransferrin, ovomucoid, ovomucin, and lysozyme).21 The plant-based (PB) alternatives incorporate ingredients like aquafaba or soy milk, which contain plant proteins that are expected to serve as emulsifiers, and provide nutrition, flavor, and rheological response.1,2,22–24 Plant proteins tend to be mainly globular, with four sub-classifications based on solubility criteria: albumins (in water), globulins (in dilute salt solutions), prolamins (in aqueous ethanol solutions), and glutelins (in dilute acid/alkaline solutions, but insoluble in water).24 As egg proteins, which are also globular, tend to be more water-soluble and better emulsifiers, the egg-free recipes sometimes supplement PB proteins with lipids to facilitate emulsification and enhance emulsion stability.25 Often, PB emulsions incorporate small molecules to enhance the flavor profile and hydrocolloids, such as starches or polysaccharides, to influence interfacial and suspending liquid properties, enhancing emulsion stability and tuning rheology and processability.26–30 A rational formulation design requires a fundamental understanding of how ingredients influence the mayo microstructure, dynamics of dispersed drops and macromolecules, flows within the suspending fluid, and the deformation and flow of interfaces.6,7,31–36 Our review of the current state-of-the-art in modeling drop deformations and emulsions rheology37 lists the many unresolved challenges that arise in understanding the influence of non-Newtonian suspending fluids and interfaces on emulsion rheology.6,31–37 Despite considerable literature on the shear rheology response of animal-based and low-fat mayos,3,16,38–44 the rheology of vegan mayos remains relatively uncharted.4,17,22,45,46 Although we ultimately aim to elucidate and design ingredient-dependent rheology for emulsions, here we focus on characterizing the contrasting rheology of commercially available AB and PB mayos.
The oscillatory shear rheometry provides two primary measures of moduli: storage or elastic modulus, G′, and loss or viscous modulus, G″, obtained by varying the strain amplitude, γ, at a constant oscillation frequency, ω, or vice versa, as summarized in Fig. 1.7,47 The G′ variation captures the elastic or the solid-like response, as the measured stress, σ12 is in phase (δ = 0) with the applied strain, γ. The G″ variation captures the dissipative, liquid-like response, with the σ12 as out of phase (δ = π/2) with γ. The moduli G′ and G″ appear nearly constant for sour cream at low strain as shown in Fig. 1a, which corresponds to the linear viscoelastic (LVE) regime.48 Small amplitude oscillatory shear (SAOS) measurements utilize frequency sweeps at small strain to capture the characteristic LVE responses of complex fluids, with frequency-dependent moduli displaying the influence of elasticity, dynamics, and dissipation by the weakly perturbed microstructure of complex fluids.7 Nonlinear VE response measured in so-called LAOS measurements (and the MAOS regime is in a transition regime or asymptotically nonlinear regime), and in a more generalized framework, G′(ω) and G″(ω) measured using SAOS represent only the first harmonic of a richer response function.49–51 Using examples from food systems, Fig. 1b–d illustrate the G′(ω) and G″(ω) data obtained for a representative VE liquid (cellulose gum solution),52 VE solid (pectin),53 and mayonnaise as a gel-like material.3Fig. 1e–h show that amplitude sweep at a constant ω reveals the four key behavior types for the moduli G′(γ) and G″(γ) illustrated by for tomato homogenate,54,55 fibrin gel,56,57 low-fat mayonnaise,41 and a starch gel:58 shear strain thinning (SST), shear strain hardening (SSH), weak strain overshoot (WSO), and strong strain overshoot (SSO) (also referred to as type I, II, III, and IV, respectively).41,49–61 Strain thinning is alternatively referred to as strain softening and strain hardening as strain stiffening.
![]() | ||
| Fig. 1 Illustrations of rheological behavior displayed by food as soft matter (or edible soft matter) in oscillatory shear rheometry. (a) Strain sweep at fixed frequency for Daisy-brand sour cream,48 illustrating three regimes: small, medium, and large amplitude oscillatory shear (SAOS, MAOS, and LAOS). Frequency sweep obtained using SAOS with three typical characteristics: (b) viscoelastic liquid-like response of 1 wt% of cellulose gum in an aqueous solution;52 (c) viscoelastic solid-like response of Ca2+ F-pectin gel;53 (d) gel-like response of real mayonnaise with 80% oil fraction.3 Four key types of nonlinear responses revealed via strain sweep (in LAOS experiments): (e) shear strain thinning (SST) for high-pressure treated tomato homogenate.54 (f) Shear strain hardening (SSH) for fibrin gel.56,57 (g) Weak strain overshoot (WSO) for a 20 wt% oil AB mayo thickened with 6 wt% waxy corn starch.41 (h) Strong strain overshoot (SSO) for 10 wt% waxy rice cultivar starch gel.58 | ||
Real mayonnaise has nearly frequency-independent moduli in the LVE regime, as shown in Fig. 1d.3 The perceived “gel” texture is captured below a critical strain, as shown in Fig. 1g. In the strain sweep, the loss modulus G″(γ) of AB mayonnaise exhibits an overshoot, displaying the WSO response. A structural breakdown of the gel network occurs above a critical strain, and the elastic modulus G′(γ) for this jammed-dense emulsion displays a yield point. Thus, mayonnaise, like many food products, exhibits yield stress, σy which also contributes to the product's texture and mouthfeel during consumption and its flow behavior during dispensing, dipping, or spreading.9,62–64 A wide range of yield stress values, from σy ∼ 20 Pa to σy ∼ 200 Pa, has been reported for commercially available and homemade mayonnaise.3,16,38–43 Unfortunately, as there is no single agreed-upon method for estimating or measuring yield stress, the reported values vary considerably depending on the type of flow experiment being performed.8,9,11,63–66 We previously characterized the apparent σy and shear thinning behavior of AB and PB mayos using torsional rheometry4 and determined the apparent extensional yield stress, σye, and dispensing behavior using dripping experiments.4 Though all mayos displayed yielding, shear thinning, and two regimes in pinching (intermediate power law and terminal linear variation of radius with time), most real mayos showed higher σy and σye values compared with vegan mayos.4 Even for real and vegan mayos that displayed comparable rate-dependent viscosity, implying that manufacturers can employ similar processing equipment and parameters, we found striking differences in the dispensing behavior and the extensional rheology response.4 However, our previous publication and the state-of-the-art published literature lack a comparative characterization of the oscillatory shear response of AB and PB mayos, even though in industrial practice, the oscillatory shear responses are often characterized, mapped and correlated to consumer-perceived desirables and distinctions in texture, consistency, viscosity, dispensing, spreadability, first bite impression, mouthfeel, and cohesion.50,67–73
The magnitude of complex viscosity, |η*(ω)| obtained as a function of fixed low or high strain and variable frequency, ω can be compared to the shear rate-dependent variation in viscosity, η(
). Complex fluids, such as entangled polymer solutions and melts, display a fortuitous agreement η(
) = |η*(ω)|ω=
, also known as the Cox–Merz rule, for |η*(ω)| obtained using small-amplitude oscillatory shear (SAOS) measurements in the linear viscoelastic regime (LVE). For polymeric materials, the Cox–Merz rule (and time-temperature superposition) enables acquisition of flow curves over an extended shear rate range, even though elastic instabilities and instrument limitations plague such measurements in drag-driven or pressure-driven rheometers.74–76 The empirical Cox–Merz rule appears to hold for some food materials containing dispersions of starches, polysaccharides, and pectin.77–79 However, it does not typically apply to concentrated and dense food systems, including tomato pastes,80 dispersions of waxy maize81 and tapioca starch,82 wheat flour dough,83 yogurt, condensed milk and cream cheese,84 mayonnaise,84,85 and other spreads such as apple butter, mustard, and margarine.85 In 1991, Doraiswamy et al.75 introduced an empirical extension of the Cox–Merz rule for complex fluids with a yield stress, and incorporated elastic, viscous, and yielding phenomena via a limiting recoverable strain. The modified Cox–Merz rule,75 also known as the Rutgers–Delaware rule (as suggested by Krieger86), i.e. η(
) = |η*(γ0ω)|
=γ0ω superimposes (η(
)) and the nonlinear viscoelastic response (|η*|(γ0ω)) computed at an effective shear rate, using as a shift factor the critical strain defined at the point of yielding. Doraiswamy et al.75 argued that even though the response to large-amplitude oscillatory shear involves many harmonics, the first harmonics determine all the parameters in their model. Here, we contrast the linear and nonlinear viscoelastic regimes and examine the response of AB and PB mayos using the conventional and the extended Cox–Merz rules.
The paper presents a rheological matchup of commercially available real and vegan mayos, with the typical fat content exceeding 70% by volume. Oscillatory shear tests evaluate moduli, gel strength, yield stress, and post-yielding behavior as a function of strain and frequency. The magnitude of the complex viscosity is compared with the rate-dependent viscosity to assess the applicability of the conventional and the extended Cox–Merz rules. Thereafter, the yield stress values estimated from oscillatory shear are compared with those deduced from shear flow curves and dripping experiments. We anticipate that the experimental protocols and distinctions described here will aid in deciphering how replacing AB proteins with PB proteins and additives, such as starch and polysaccharides that can influence interfacial properties and suspending liquid (or matrix) rheology, affect the overall flow behavior and sensory perception of mayos and other multi-ingredient edible soft matter.
| Sample name | Fat (g) per tbsp (g) [wt%] | Ingredients influencing rheology and emulsion stability |
|---|---|---|
| Hellmann's real mayonnaise | 11/14 [79%] | Whole eggs, egg yolk |
| Sir Kensington's classic mayonnaise | 11/14 [79%] | Egg yolks |
| Kraft real mayonnaise | 10/13 [77%] | Eggs, egg yolks |
| Hellmann's plant-based mayo | 8/14 [57%] | Modified potato starch, corn starch |
| Sir Kensington's classic vegan mayo | 10/13.5 [74%] | Chickpea, acacia gum, xanthan gum |
| Chosen Foods classic vegan mayo | 10/14 [71%] | Chickpea, faba bean, sunflower lecithin, xanthan gum, acacia gum, guar gum, mustard flour |
| Follow Your Heart original vegenaise | 9/14 [64%] | Soy protein, brown rice syrup, mustard flour |
Torsional rheometry measurements were performed on an Anton Paar MCR 302 rheometer at 25 °C. Roughened 25 mm parallel plates were created by applying a 600-grit adhesive-back sandpaper (McMaster-Carr Part #47185A51) to the smooth plates with a 1 mm sample testing gap. Amplitude sweep tests were performed within the low frequency range, at ω = 1 rad s−1, over a range of strain γ = 0.01% to γ = 100%. The amplitude setting for the frequency sweep experiments was chosen to be within the linear viscoelastic (LVE) regime of each sample. The frequency sweep range was ω = 0.01 rad s−1 to ω = 100 rad s−1 to probe long and short time oscillations. Flow curves were obtained by ramping up from
= 0.01 s−1 to
= 1000 s−1. To reduce the effects of deformation history from sample loading, a 10-minute wait time was implemented to allow time for restructuring and relaxation. The sample was replaced after each trial. Drop size distribution was obtained using a Bruker TD-NMR (time-domain) drop size analyzer.
. The G′ and G″ exhibit strain-independent values
and
, respectively, at low strain (γ < γc) for all real and vegan mayos. As moduli exhibit strain independence for γ < γc, the behavior indicates a linear viscoelastic (LVE) response. Here G′(γ) > G″(γ), implying that the mayos appear solid-like under small deformations or stress. The real mayonnaise emulsions exhibit an elastic modulus at low strain or gel strength,
, whereas the
values for vegan mayo emulsions vary over a considerable range, from
to
. Beyond the LVE regime, i.e., for γ > γc, the samples exhibit a significant drop in the G′ value or show yielding. The values of G′ and G″ intersect at crossover strain, γx shown using the vertical dotted lines. Indeed, a transition from elastic-dominated to the viscous-dominant bulk response occurs above γx. As elastic modulus displays strain softening above γc, and the moduli shift from a solid-like response, with G′(γ) > G″(γ) to a liquid-like response with G′(γ) < G″(γ) response above γx, either strain can be referred to as a yield point. The corresponding plots for strain-dependent variation of tan
δ is included as Fig. SF1 in the supplementary document. Fig. 2 shows that the vegan mayos yield at a lower strain, independent of the criteria used. A close comparison of the strain-dependent variation of storage modulus, G′ and loss modulus, G″ for Hellmann's real and vegan mayos reveals a nearly matched magnitude and strain-dependent variation, reminiscent of close agreement displayed by variation of their viscosity with shear rate.4 In contrast, Sir Kensington's real and vegan mayos display noticeable differences in the onset of yielding in the strain-dependent variation of G′(γ) and the contrasting response of the loss modulus, G″(γ). The paired comparison of strain variation of G′(γ) and G″(γ) of AB and PB mayos for these two brands are included in the two plots of Fig. SF2 in the supplementary document.
Fig. 2a–c show that the loss modulus, G″ for the real mayonnaise increases for γ > γc (≈ 10%) and then decreases with larger strain. Thus, the strain sweep reveals that all real mayonnaises or AB mayos exhibit weak strain overshoot (WSO), in agreement with previous studies (see Fig. 1 for example).41 The extent of this strain-hardening, or strain overshoot, is weaker and less pronounced for Hellmann's and Follow Your Heart vegan mayos (see Fig. 2d and f). As these are the two PB mayos that contain hard granules from corn, potato, and/or brown rice, the WSO arises, possibly due to droplet interface interactions that resist flow past other drops and granules at lower strains. In contrast, the oil droplets can deform and flow past other drops and the deformable granules at high strain. Alternatively, the strain-hardening bump could be interpreted as a contribution from the gel-like microstructure, which breaks down after a certain strain. This phenomenon has been observed in other studies of strain-dependent rheological response of foams and emulsions.87,88 The two PB samples, Sir Kensington's and Chosen Foods (Fig. 2e and f), that contain polysaccharide additives such as acacia gum, xanthan gum, and guar gum display shear strain-thinning (SST) response (similar to the response of polysaccharide solutions for the relevant concentrations60 and tomato homogenates54,55) as both moduli G′ and G″ decrease with increasing strain after an initial strain-independent regime.
The changes in elastic and loss modulus as a function of strain amplitude and frequency shown in Fig. 2 and 3 provide insights into gel strength, yielding, microstructural changes, and contributions to the flow response. The continuous phase forms thin films between the deformable dispersed phase droplets in the jammed, dense emulsion, resulting in a foam-like polyhedral packing. As strain is applied, the drops deform in alignment with the flow, causing the bulk behavior to transition from elastic to viscous. Additionally, the magnitude and variation of G′ and G″ can also indicate heuristic and sensory properties described as initial texture perception, firmness, and gel strength of a soft material like mayonnaise.18,89 The gel strength of real mayonnaises in this study (G′ = 1000 Pa) corresponds to previous measurements of commercial and model mayonnaise emulsions.3,90,91 In contrast, the vegan mayos exhibit a broader range of the elastic moduli values (G′ = 100 Pa to G′ = 2000 Pa) implying it is more challenging to predict and control the apparent gel strength consistently compared to AB mayonnaise. Although the evaluation using moduli data from amplitude sweep measurements consistently shows all real mayos have higher apparent yield stress than vegan mayos, the moduli measured in response to oscillatory frequency sweep in the LVE regime shows mixed results, with some vegan mayos showing higher modulus values.
Table 2 provides metrics to assess size variation and also includes the composition, expressed as percent moisture and fat. Hellmann's real, Sir Kensington's real, and Follow Your Heart vegan appear to have relatively high fat fractions, suggesting their rheology has a similar microstructural origin: a continuous phase in the form of a network of thin films between deformable dispersed-phase droplets, resulting in a foam-like polyhedral packing.2 The elastoviscoplastic response, characterized by a yield stress, strain-dependent elastic and viscous moduli, and shear-thinning behavior, is therefore reporting the integrated response of the foam-like network and the drops to applied stress.37,101–105 In Table 1, we list fat content per tablespoon (wt%) for all samples based on their labels, and the simplest estimates of volume fraction for the four mayos included in Table 2 are in reasonable agreement with the labels. Therefore, we can estimate that Kraft real and Sir Kensington's vegan mayos also have ϕ > 70% and are jammed-dense emulsions. However, as the Hellmann's plant-based mayo has a relatively low fat fraction (54%), the elasticity and yielding response are not just due to the foam-like architecture but are deeply influenced by the dynamics of the modified starch present at the interface and in the suspending liquid.
| Sample description | Diameter (µm) | Composition | ||||
|---|---|---|---|---|---|---|
| D2.5 (2.5%) | D50 (50%) | D97.5 (97.5%) | δD (stdev) | Moisture (%) | Fat (%) | |
| Hellmann's real mayo | 1.61 | 2.71 | 4.56 | 0.74 | 17 | 78 |
| Hellmann's plant based mayo | 1.96 | 3.05 | 4.74 | 0.70 | 41 | 54 |
| Sir Kensington's classic mayo | 1.02 | 1.78 | 3.14 | 0.53 | 14 | 82 |
| Follow Your Heart-original vegan | 1.64 | 3.51 | 7.52 | 1.47 | 23 | 72 |
Table 2 lists the drop diameters D2.5, D50, and D97.5, below which, respectively, 2.5%, 50%, and 97.5% of the drops in the distribution fall. Here, D50 provides a measure of the median size, whereas D2.5 and D97.5 represent the fines and large drops at the tail ends of the distribution. Of the two Hellmann's mayos, the vegan mayo appears to have greater polydispersity and larger drop sizes. The average drop sizes for Follow Your Heart vegan mayo are larger than the other three, whereas Sir Kensington's real mayonnaise has the smallest drop sizes. Fig. 4 shows the corresponding drop size distribution obtained from the analysis of hindered diffusion in these NMR studies: Sir Kenginston's mayonnaise has the narrowest size distribution. Table 2 and Fig. 4 indicate that Follow Your Heart mayo has the widest size variation.
) = |η*(ω)|ω=
) that uses the LVE data (for γ0 = 0.1% is not applicable. The plots of |η*|(γ0ω) overlap at large strains with each other and with η(
), implying that the nonlinear response, observed after yielding, is quite similar and comparable. All mayos thus display the behavior (η(
) = |η*(γ0ω)|) anticipated by the extended Cox–Merz rule, also known as the Rutgers–Delaware rule. In such cases, the strain is large enough to significantly perturb the microstructure, as seen in Fig. 5 with strains of γ0 = 30% and γ0 = 40%.
In 1983, Bistany and Kokini85 showed that a two-parameter modification of the Cox–Merz rule, η*(ω) = C[η(
)]α|
=ω with the exponent, α (ranging from 0.74 to 1.4) and a pre-factor, C (ranging from 0.160 to 9.52) captures the rate-dependent variation in apple butter, mustard, mayonnaise, and margarine. Berland and Launay suggested using α = 1 for wheat flour doughs83 and this worked well for tapioca starch dispersions.82 All empirical relationships are helpful if their range, domain and circumstances of validity are respected. However, the Rutgers–Delaware rule (aka the extended Cox–Merz rule) proposed by Doraiswamy et al.75 is built on a stronger conceptual basis by accounting for a limiting recoverable strain that has a maximum value corresponding to the strain at which the transition from solid-like to liquid-like response (yielding) occurs. Recent studies by Shim et al.106 offer a fundamental and valuable perspective using recovery rheology, which involves decomposing the strain into recoverable and unrecoverable parts. Shim et al.106 find that the Rutgers–Delaware rule applies when the maximum imposed strain is high enough to yield the sample, where most of the strain is unrecoverable. Further exploration into microstructural recovery and recoverable elastic strain of mayonnaise will be detailed in a future study.
σ = σy + K n | (1) |
Fig. 6b and e consider yielding as manifested in oscillatory shear and the determination of yield stresses. As discussed earlier in the context of Fig. 2, the elastic modulus displays strain softening above the critical strain, γc for all real and vegan mayos, and moduli show a shift from a solid-like (G′(γ) > G″(γ)) to a liquid-like (G′(γ) < G″(γ)) response above the crossover strain, γx. Either of the two strains can be used to identify the yielding point and determine an apparent yield stress; both values are listed in Table 3. In the first case, yielding is indicated by the drop-off of the storage modulus from the linear regime. Using the moduli
and
observed at γc and γx, respectively, provide the two yield stress estimates, determined with the equation shown below, where
:
![]() | (2) |
| Sample |
σ
y ( ) [Pa] |
γ c [—] | σ y (γc) [Pa] | γ x [—] | σ y (γx) [Pa] | ||
|---|---|---|---|---|---|---|---|
| Real: Hellmann's | 1167 | 135 | 6.8 | 72 | 70.0 | 170 | 159 |
| Real: Sir Kensington's | 1077 | 151 | 14.6 | 133 | 73.9 | 174 | 142 |
| Real: Kraft | 853 | 161 | 10 | 74 | 68.9 | 123 | 123 |
| Vegan: Hellmann's | 1407 | 58 | 4.6 | 58 | 59.0 | 156 | 114 |
| Vegan: Sir Kensington's | 1707 | 89 | 1 | 15 | 55.8 | 109 | 98 |
| Vegan: Chosen Foods | 155 | 27 | 2.15 | 2.8 | 54.9 | 15 | 78 |
| Vegan: Follow Your Heart | 2387 | 161 | 2.15 | 46 | 37.5 | 121 | 152 |
Fig. 6c and f show a montage of dispensing and pinching, outlining solid-like and liquid-like regimes. The images are snapshots from an earlier study,4 in which we determined the extensional yield stress, σye, using dripping into air with gravity-based rheometry protocols.108–111 Experimentally, the mayo was dispensed at a very slow flow rate, resulting in a nearly solid-like cylinder being extruded. Once the mass of the extrudate divided by the local area exceeded the yield stress, locally the material yielded and then underwent rapid pinching, as seen in Fig. 6c and f. The mass of the drop was directly measured after pinch-off, and the yielding event was considered at the onset of pinching, 0.9R0, where R0 is the radius of the nozzle. Then, the extensional yield stress was determined using eqn (3), accounting for the weight of the droplet and the cross-sectional area of the flowing, pinching filament.
![]() | (3) |
The weight of the drop, the length or volume of the drop, and the timescale for pinch-off were higher for AB mayos, implying these tests visualize and illustrate differences that could manifest on dipping and dispensing.
Table 3 lists the values of yield stress, estimated using the following four distinct methods across varying experiments for all mayos: the shear flow curve (using the HB fit), strain sweep in oscillatory shear (using a choice of either critical strain or crossover strain, and the associated modulus), and dripping-into-air (DiA: relying on the interplay of yield stress and gravity for the onset of neck pinching, with capillarity playing a role before pinch-off). Yield stress, or the apparent yield stress, provides a pragmatic parameter for comparing materials and describing the stark change in viscosity or flow behavior that occurs with varying stress. However, the frequency chosen for oscillatory shear, the deformation history in dripping, the presence or absence of thixotropy for shear and extension, and the choice of protocols can all influence the absolute value of the apparent yield stress.1,8,9,11,64,108,112–114 Regardless of the experimental method or the yielding criteria, vegan mayo samples showed lower yield stress than real mayonnaise samples.
In Table 3, the first column shows the elastic modulus magnitude from the LVE regime, observed before yielding, while the second column displays the yield stress. The apparent yield stress for Hellmann's real mayonnaise (
, γc = 6.79%) of σy = 72 Pa is larger than the corresponding value of σy = 58 Pa observed for the Hellmann's vegan mayo (yield point at
, γc = 4.63%), calculated using eqn (1). Alternatively, the yield stress shown in the second-to-last column was determined from the crossover point between the elastic and viscous moduli or the transition from solid-like G′ > G″ to liquid-like G″ > G′ behavior. The crossover point was determined by linear interpolation of the two neighboring data points of each modulus, followed by using the crossover modulus and crossover strain values in eqn (2). Table 3 also includes the values of extensional yield stress, σye. To compare its value to yield stress manifested in shear rheometry, the last column entry is scaled by
, as a von Mises yield criteron predicts σye = βσy with
though
to
are observed in experiments.4,109,111,115 While shear rheology captures the response to shear flows involving velocity gradients perpendicular to the flow direction arising during pumping through tubes and orifices, or during spreading and dipping, extensional flows associated with streamwise velocity gradients that arise in dispensing, swallowing, and oral coating, making the extensional rheology response crucial for understanding oral processing, creaminess and cohesion.19,28,116 Extensional rheology response is said to be more closely correlated with consumer-relevant performance in real-use scenarios such as squeezing or dolloping from a bottle, and spreading or spreadability.8,10,19,20,41,42,77,109,110,116 Given the trends displayed by shear and extensional yield stress datasets, it appears plausible that the yield stress and the magnitude and the variation of the moduli can also indicate initial texture perception, the first-bite impression, firmness, and gel strength of soft materials like mayonnaise.18,89 On similar lines, it can be said that the change in elastic and loss modulus as a function of strain or frequency imbibe insights into gel strength, yielding, microstructural changes, contributions to flow response, and heuristic and sensory properties.
At the high ϕ limit, for emulsions with similar interfacial, dispersed, and suspending fluid properties (all rheologically Newtonian), smaller drop sizes and narrower drop-size distributions are expected to yield higher yield stress, σy and elastic modulus.35,37 However, σy asymptotically reaches a value set by capillary stress (ratio of surface tension to the drop size) at the highest ϕ or fat fraction, making emulsions with nearly monodisperse drops quite insensitive to volume fraction deep in the jammed-dense regime, ϕ > 70%.35,37 Such explanations are inadequate for real formulations like mayos, as these theoretical and phenomenological arguments do not account for the non-Newtonian rheology of the interfacial and suspending fluids, and the physicochemical properties of the molecular, macromolecular, or particulate additives present in drops, thin films, and at interfaces, which affect emulsification, emulsion stability, and rheology.4,35,37,92,117 Mayonnaise also traditionally contains mustard seed particles, and vegan mayos often contain additives like starch granules and polysaccharides. Among real mayos, the use of whole egg or addition of egg albumin provides for a more viscoelastic matrix (e.g. in Hellmann's real). In contrast, in vegan mayo, proptein–polysaccharide interactions can play a role.
The conformation- and interaction-dependent rheological properties of rheology modifiers such as cellulose gum and xanthan gum that are polyelectrolytes, show sensitivity to acid and electrolyte concentrations, and therefore are affected by the amount of lemon juice (or vinegar) and salt in recipes.3,19,26,28,29,41,60 Recent studies show that modified starch granules and protein-based microgel particles can populate the oil–water interfaces in vegan mayos, suggesting that their stability and rheology can be mechanistically similar to those of Pickering emulsions.46,94,118,119 Focused investigations are needed to characterize and elucidate the influence of drop size distribution, microstructural differences and ingredients like hydrocolloids and plant proteins on the various features of the rheological response of mayos and similar jammed, dense emulsions. The comparison of the Hellmann's real and vegan mayos shows that the shear thinning response in the flow curve and weak strain hardening (WSO) in the strain-amplitude sweep in oscillatory shear can be made similar despite a significant difference in fat content and protein types. Despite the fat content of ϕ > 70%, vegan mayos containing polysaccharides in the suspending liquid phase and possibly at the o/w interfaces show an absence of an overshoot or WSO response.
= 50 s−1, the frequency-dependent response at matched deformation rate could be expected to correlate with thickness perception. However, this is only the first bite impression of texture during eating or consumption.18 In reality, oral processing is complex and involves a broad and dynamic range of shear rates, often spanning from
< 1 s−1 (saliva mixing and coating) to
> 103 s−1 (mastication and swallowing) and a broad range of oscillatory strain and strain rates. The deformation rate continuously changes as the interfacial gap narrows during lubricated squeeze flow in the oral cavity, and the flow field exhibits both shear and extensional characteristics. Thus, real-life mouthfeel would be better captured across a range of shear rates, referring to the viscosity profile within such a range to comprehensively assess the in-mouth performance of food products, with complementary deductions made using tribological and extensional rheology measurements and by accounting for the role played by dissolution, dilution and digestion brought about by the continuous addition of saliva.116,123 Furthermore, mechanistic insights into how interfacial properties—such as interfacial tension, film elasticity, and adsorption kinetics—influence emulsion stability, drop deformation, and ultimately rheological and tribological responses would enhance and inform ingredient selection to optimize processing and sensory performance.
Though the variation in G′ and G″ (and the flow curves) due to the choice of ingredients likely alters the consumer's overall experience and perception of “creaminess” and “thickness”,69,72,73,124 these sensory attributes only partially correlated with the rheological and tribological response.18,68,70,71,125,126 Creaminess is a complex interaction between food and saliva in the mouth that results in the coalescence of dispersed oil droplets and a change in the suspending fluid fraction and properties, thereby altering the fluid and flow properties.18,123,127 “Thickness”, “stringiness”, and “gloopiness” are heuristic perceptions of flow behavior, often illustrated and estimated using simple, handy or kitchen flow experiments like dripping from a ladle, dispensing from a bottle, stretching a liquid bridge between a thumb and index finger, between a dipped fry and mayo, or between a fruit and chocolate syrup; all include the influence of shear and extensional rheology and free surface flows. These consumer perceptions of flow behavior likely correlate with the strain-dependent and frequency-dependent changes in the oscillatory shear measures (G′ and G″), as ultimately all connect to the role of dispersed macromolecules, drops, and particles, colloidal forces, and microstructural deformation. We infer that oscillatory shear enables characterization of three key features of flow behavior of mayo and other yield stress formulations – the apparent yield stress (from strain amplitude sweep), apparent shear thinning (from complex viscosity as a function of effective shear rate), and strain-dependent softening or stiffening (from G′ and G″ at a fixed frequency). Yield stress, gel strength, rate or frequency dependent viscosity, and power law index, determined from oscillatory shear rheology provide pragmatic metrics for contrasting processability and sensory attributes.
All the datasets and plots included in the attached contribution, “Rheological matchup of real and plant-based mayo: gel strength, strain overshoot, and yielding, plus the extended Cox–Merz rule,” are available via request to the corresponding author.
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