1 Introduction

An emulsion is a colloidal dispersion of two immiscible liquids, where one phase is dispersed in another [1]. In the liquid phase, the main types of simple emulsions include oil-in-water (O/W) and water-in-oil (W/O) emulsions. Multiple emulsions are more complex systems, where the dispersed phase is by itself an emulsion. Multiple emulsions, in particular water–oil–water (W/O/W), have gained increasing interest due to their wide range of applications in controlled release of drugs, food formulation with reduced fat, encapsulation of active ingredients, and cosmetics [2, 3]. W/O/W emulsions are often obtained by emulsification of W/O into the secondary aqueous phase [4]. The main methods of generating W/O/W emulsion are one step and two step emulsification approaches. In the case of one step emulsification, strong mechanical agitation is required to induce phase inversion. At the initial stage W/O emulsion is formed, but a portion of emulsion shows phase inversion leading to formation of W/O/W emulsion. On the other hand, two–step emulsification techniques consist of making primary W/O emulsion using low HLB (hydrophilic-lipophilic balance) emulsifier(s) that strongly favors W/O and dispersing it in a secondary aqueous solution containing hydrophilic emulsifier [5]. One of the critical elements that determines the efficacy of this technique is the intrinsic stability of the internal W/O emulsion. It is worth mentioning that the presence of hydrodynamic perturbations during the second stage of emulsification must not lead to any significant breakdown of the primary W/O emulsion in order to obtain stable W/O/W emulsions [6].

A variety of apparatuses are used to produce W/O/W emulsions such as: high pressure homogenizers (HPH), blenders, microfluidizers, membranes, etc. These different apparatuses not only can induce the size reduction but also affect the emulsification capacity and adsorption of emulsifier at the interface [7, 8]. High pressure homogenizers are effective tools to produce fine droplets (nano-emulsions), which may not be easily obtained via mixers or rotor–stator homogenizers [9]. The difference in the emulsion droplet size is directly associated to the energy density. The higher the energy input/density, the smaller the droplet size [9]. However, sometimes such high energy can result in emulsion destabilization. A W/O/W emulsion’s stability against coalescence is mainly determined by compositional factors including the internal/external aqueous phase, hydrophobic/hydrophilic emulsifiers, and the type of oil phase [10, 11].

Internal aqueous phases often consist of molecules and compounds that are encapsulated for specific applications (for examples, drug, sugar, nutrients, and other active agents). External aqueous phases usually consist of emulsifiers (e.g. proteins, natural/synthetic active agents), hydrocolloids, and viscosity modifiers [12].

Emulsifiers play critical role in the stability of emulsions due to their tendency to be adsorbed at the oil–water interface. These surface-active agents are responsible for lowering the interfacial tension and facilitating the formation of emulsion droplets. The type of emulsifier can determine which phase is most likely to be the continuous phase and which one will be the dispersed phase. Therefore, using the wrong emulsifier could result in an inverted emulsion [5, 13]. For example, polyglycerol polyricinoleate (PGPR) which has low HLB value of 1.5 ± 0.5 strongly favors the formation of W/O emulsions and it is commonly used in formulation of W/O/W emulsions [5, 14]. While type of emulsifier is shown to be an important factor in the stabilization of W/O/W, the emulsifier concentration can also play a major role in the stability mechanism. Nollet et al. demonstrated that by increasing the concentration of PGPR in sunflower oil, the stability of W/O/W emulsion could be greatly improved leading to enhanced encapsulation of active ingredient (vitamin B12 in this case) [14].

Alternatively, sodium caseinate (NaCN), a milk protein, can form an elastic layer around the oil droplets and favor the formation of O/W and as a result it is commonly used in the outer water phase of W/O/W [15]. For example, Jahaniaval et al. evaluated the physicochemical and functional properties of soluble NaCN fractions as a function of both pH (~ 3–8) and temperature (~ 50–100 °C). The authors found that NaCN emulsification capacity is highly dependent on the pH and temperature of solution as these factors directly influence the NaCN concentration and confirmation around the oil droplets, and consequently the emulsion stability [16]. In addition to the effects of emulsifier type and concentration on the properties of emulsion, the weight ratio of W/O can also alter the stability and creaming behavior of W/O/W through altering the rheology of media. In two separate studies looking at O/W and W/O/W emulsion systems using food-grade emulsifiers, it was highlighted that as the fraction of disperse phase increases the viscosity increases and as a result reduces the chance of coalescence [17, 18].

Furthermore, adsorption of fine particles including micro/nanoparticles at the interface is shown to affect W/O/W emulsion stability through altering the rheological properties of the system (e.g. elasticity and rigidity of interface) [19,20,21].

Despite many efforts to understand the stability of multiple emulsions, a study investigating the effects of altering emulsifier concentration and portion of primary W/O emulsion on emulsion stability, in combination with these particular food-grade emulsifiers in the soybean oil phase, has not yet been conducted. This study shows for the first time that increase in droplet size is governed by different mechanisms as the concentration of W/O changes in the system. Additionally, this work illustrates that using even three different emulsifiers still yields a stable emulsion with similar droplet sizes and therefore indicates that our method/process can be generalized to other emulsion systems.

The significant impacts of processing techniques on droplet size distribution, creaming behavior, and system stabilization/destabilization, are also are lacking in the literature. To fill this gap, we investigated the effects of: (i) portions of primary W/O emulsion (25 wt%, 40 wt%, 50 wt%); (ii) the concentration of hydrophilic emulsifier; NaCN, in the external aqueous phase (0.3 wt%, 0.6 wt%, 0.9 wt%); (iii) the type of hydrophilic emulsifiers used; and (iv) the different processing techniques used (ultrasonic vs. high pressure homogenization) on the formation and stability of W/O/W emulsions. In this work, different methods for generation of multiple emulsions along with relevant characterization tools (such as microscopy, size analysis, rheometry, etc.) for monitoring the emulsion stability will be presented. Then, the emulsion stability analysis including droplet size measurements, creaming index, and viscosity measurements under different experimental conditions will be conducted and the results will be compared with the literature. The results of this study can aid with the design of multiple emulsions with desired droplet sizes and rheological properties which can be directly used in formulation of low-fat food and encapsulation of active ingredients.

2 Materials and methods

2.1 Materials

Different chemicals including NaCN, Cremophor EL, Tween 60, sodium chloride, soybean oil and (Hydroxypropyl)methyl cellulose (HPMC) were obtained from Sigma-Aldrich. Polyglycerol polyricinoleate (PGPR) was obtained from Palsgaard. All materials were used without further purification.

2.2 Emulsion preparation

W/O/W emulsions were prepared using a two-step process. The formation and stability of W/O/W emulsions under various experimental conditions were evaluated. The experimental parameters include: portions of primary W/O emulsion (25 wt%, 40 wt%, 50 wt%), concentration of hydrophilic emulsifier; NaCN, in the external aqueous phase (0.3 wt%, 0.6 wt%, 0.9 wt%), type of hydrophilic emulsifier; and the emulsification process (ultrasonic vs. high pressure homogenizer). For example, in one of the formulations (i.e. W/O concentration = 50 wt% and W/O ratio = 20/60), 20 g water containing sodium chloride (40 mg) was dispersed in the oil phase consisting of soybean oil (58.3 g), PGPR (1.5 g) and HPMC (0.2 g). The mixtures were homogenized at 700 W using a Vibra-cell Ultrasonic liquid processor (Sonics & Materials, Inc) at 37 °C for 30 min to obtain the primary W/O emulsions. The second step involved the dispersion of primary emulsions into the aqueous solution containing hydrophilic emulsifier (e.g. NaCN, Tween 60, Cremophor EL) using the same homogenizer for the duration of 15 min. The schematic of W/O/W emulsion preparation is illustrated in Fig. 1. To control the temperature and prevent dramatic increases in temperature during the emulsification, an ice-water bath was used. The total weight of W/O/W emulsion samples were kept constant at 160 g.

Fig. 1
figure 1

Schematic of W/O/W emulsion preparation: a ultrasonic liquid processing and b high pressure homogenization (HPH)

Additionally, we compared the effect of different processing techniques on the emulsion stability. In the second approach, the primary W/O emulsion was made using IKA T-10 homogenizer at 15,000 rpm for 3 min. The resulting emulsion was further cooled in the room temperature and then homogenized using high pressure homogenizer (HPH, IKA) at 1000 bars for 8 cycles. The same procedure was used to prepare the final W/O/W emulsions.

2.3 Optical microscopy

An optical microscope was used to observe the multiple emulsion samples and their stability against coalescence under different experimental conditions. A drop of emulsion sample was deposited on a glass slide and then enclosed with a coverslip. In few cases, the samples were slightly diluted with DI water to improve the imaging quality. The morphology of emulsion droplets was further monitored via light microscope (Olympus, USA). Water-soluble dye was added to the primary W/O emulsion to help with monitoring the encapsulation of inner water droplets during the second emulsification step (i.e. W/O/W).

2.4 Determination of average droplet size of W/O/W emulsions

The average droplet size and size distribution of W/O/W emulsions were measured using Malvern MasterSizer MSE (Malvern Instruments). The droplet size distribution was measured in W/O/W emulsion after different storage times at the room temperature. To ensure the homogeneity of the samples before taking the measurements, the emulsion samples were agitated gently. The measurements were conducted under continuous agitation while using refractive index of 1.48 for soybean oil with the obscuration range set in the range of 5% and 15%. To ensure the accuracy of our results, each measurement was repeated three times and the results were compared with the microscopy images, accordingly. The surface weighted mean diameter (D[2, 3]) was calculated based on the following equation [22]:

$$D_{{\left[ {3,2} \right]}} = \frac{{\sum n_{j} d_{j}^{3} }}{{\sum n_{j} d_{j}^{2} }}$$
(1)

Here \(d_{j}\) and \(n_{j}\) are the diameter and number of droplets with size \(d_{j}\), respectively. It should be noted that the estimation of average diameter based on D[2, 3] agrees more closely with the microscopy images than those obtained from D[3, 4] (i.e. volume weighted mean diameter) and as such D[2, 3] is reported. Additionally, the polydispersity of size distribution can be extracted as follows [17]:

$${\text{Span}} = \frac{{d_{0.9} - d_{0.1} }}{{d_{0.5} }}$$
(2)

where \(d_{0.9}\), \(d_{0.5}\), and \(d_{0.1}\) account for the point in the size distribution in which 90%, 50%, and 10% of the total volume of sample are contained.

2.5 Stability tests for W/O/W emulsions as a function of storage time

The stability of multiple emulsion samples was evaluated based on the observation of two separate phases: the cream layer and the serum layer at the top and bottom of the vials in ambient conditions, respectively. The creaming index (i.e. HL/HE%; where HL and HE are the height of serum layer and total emulsion height, respectively) for different emulsion samples was calculated as a function of storage time. In this case, the higher creaming index value is indicative of emulsion with inferior stability.

2.6 Viscosity measurements

The rheological tests were conducted using an ARG2 rheometer (TA Instruments). Cone and plate geometry was used due to its compatibility with these emulsion systems. The viscosity of prepared emulsion samples was measured using cone contact angle of 2°, 40 mm diameter, and with the 1000 \(\mu m\) gap. The temperature was set to 23.00 ± 0.15 °C and the shear rate was varied between 0.2 and 150 s−1. For comparison purposes, the viscosity was reported at the shear rate of 15 s−1. For system calibration, water which has a known viscosity was used. The data was collected after the system reached equilibrium and the measurements were replicated three times to confirm the repeatability of our results.

3 Results and discussion

3.1 Effect of primary emulsion concentration on the formation and stability of W/O/W emulsions

We evaluated the effect of altering the portion of primary W/O emulsion on the stability of multiple emulsions. Figure 2 shows the microscopy images of W/O/W emulsions prepared with the ultrasonic liquid processor along with their corresponding droplet size distribution. Based on the results, it can be inferred that the emulsion with the highest portion of W/O (i.e. 50 wt%, Fig. 2a) is more stable against coalescence with narrower droplet size distribution. On the other hand, further reduction in the percentage of primary emulsion led to formation of larger droplets with broader size distribution (25 and 40 wt% W/O, Fig. 2b and c). The average droplet size increased from 4 ± 0.6 to 9 ± 2.5 μm with a decrease in the concentration of W/O from 50 wt% to 25 wt%. Additionally, the microscopy images of diluted emulsions depicted in Fig. 3a and b clearly confirm the formation of multiple emulsions as indicated from the presence of an inner aqueous phase. It is also shown that the oil phase can contain one and/or multiple water droplets depending on the emulsion type. These results agree well with the literature, showing the formation of multiple emulsions using microscopy techniques [23, 24]. We note that the higher stability at the higher concentration (50 wt%) of primary emulsion can be associated with increased solution viscosity due the larger volume fraction of dispersed phase [17]. To investigate how the rheology can play role in the stability of emulsions, the apparent viscosity of solutions at different portions of W/O were measured, accordingly. Based on the results shown in Fig. 4, it is clear that an increase in the portion of primary W/O emulsion, leads to an enhancement of solution viscosity. For example, the viscosity increases from 1.4 ± 0.19 to 4.7 ± 0.21 Pa.s as the W/O concentration altered from 25 wt% to 50 wt%. The increase in the emulsion viscosity reduces the chance of droplet–droplet collision and slows down the coalescence and destabilization kinetics. The enhanced emulsion stability with the increase in the solution viscosity has been reported for different multiple emulsion systems and support our results presented herein [22, 25].

Fig. 2
figure 2

Optical microscopy images and droplet size distribution of prepared W/O/W emulsions (NaCN = 0.3 wt%) with different portions of primary emulsion: a W/O = 50 wt%, b W/O = 40 wt%, c W/O = 25 wt%

Fig. 3
figure 3

Microscopy images of diluted W/O/W emulsions (NaCN = 0.3 wt%) with different portions of primary emulsion: a W/O = 50 wt%, b W/O = 40 wt%. The arrows show the colored water droplets entrapped in the oil phase

Fig. 4
figure 4

Viscosity of W/O/W emulsions (NaCN = 0.3 wt%) with different portions of primary emulsion (25, 40, and 50 wt%) measured under ambient condition

Next, we calculated the creaming index (HL/HE%; where HL and HE are the height of serum layer and total emulsion height, respectively) of these emulsions at different storage times under ambient conditions. The results summarized in Fig. 5 show that the emulsion with the lower percentage of primary W/O emulsion possesses higher creaming index (~ 21% vs. 12% for 25 wt% and 50 wt% W/O after 1-day storage, respectively) with inferior stability than those with higher W/O percentage. The creaming index results agree well with the microscopy images and the droplet size measurements shown in Figs. 2 and 3. The increase of water phase can also induce greater instability, possibly due to the increased frequency of coalescence and bridging at higher water volume fraction. The increase in the creaming index and further emulsion destabilization at the longer storage times originate from higher rates of flocculation and coalescence [26].

Fig. 5
figure 5

Creaming Index (%) at different storage times while using different portions of primary W/O emulsion (NaCN = 0.3 wt%): 25 wt%, 40 wt%, and 50 wt%

To further evaluate the possible mechanism behind the increase in the droplet size, we plotted D3ave as a function of time (D3ave vs. t) for the samples with different portions of primary W/O emulsion (see Fig. 6). The linear correlation between D3ave vs. t for the case of 25 wt% W/O further indicates that the increase in droplet size is mainly governed by Ostwald ripening [27]. Nevertheless, at higher portions of W/O (i.e. 40 wt% and 50 wt%) D3ave showed insignificant dependency to t (storage time) and therefore such a small increase in the size can originate from simple droplet–droplet interactions and further droplets coalescence. We also evaluated the effects of NaCN concentration on the droplet size distribution and emulsion stability against creaming to better understand how the concentration of emulsifiers alters the integrity of W/O/W emulsions.

Fig. 6
figure 6

D3ave as a function of time (D3ave vs. t) for the samples with different portions of primary W/O emulsion (NaCN = 0.3 wt%): 25 wt%, 40 wt%, and 50 wt%

3.2 Effect of NaCN concentration on the formation and stability of W/O/W emulsions

NaCN is shown to be a potential candidate for stabilization of W/O/W emulsions. NaCN is often used as the hydrophilic emulsifier and can impact the stability of W/O/W emulsion in the presence of a hydrophobic emulsifier such as PGPR [28]. Based on the concentrations of NaCN and PGPR in the emulsion the coverage of droplets with emulsifiers and droplet–droplet interactions can be easily influenced resulting in formation of emulsions with different size distribution and creaming stability [29].

We monitored the stability of W/O/W emulsion as a function of NaCN concentration, while keeping other conditions the same (W/O = 50 wt%). Figure 7 reveals that with increase in the concentration of NaCN in the external aqueous phase from 0.3 wt% to 0.9 wt%, the average droplet size slightly increases, and size distribution becomes broader. This trend is consistent with the higher creaming index values observed at the higher NaCN concentration (see Fig. 8). It should be noted that this result may seem counter-intuitive, as increasing NaCN concentration in the solution should lead to higher coverage of oil droplets and therefore favor the formation of smaller droplets [28].

Fig. 7
figure 7

Microscopy images of W/O/W emulsions with different concentrations of NaCN in the external aqueous phase (W/O = 50 wt%): a NaCN = 0.3 wt% b NaCN = 0.6 wt% and c NaCN = 0.9 wt%

Fig. 8
figure 8

Creaming Index (%) at the different storage times for different concentrations of NaCN in the external aqueous phase: 0.3 wt%, 0.6 wt% and 0.9 wt%

Nevertheless, we believe that formation of larger droplets in our emulsion system can be attributed to the disruption of the PGPR layer with increase in NaCN concentration at the W/O interface (since NaCN can diffuse in and out of the external aqueous phase). In the next section we aim to gain a deeper understanding of system stability, and evaluate the effects of emulsifier type as well as processing techniques (ultrasonic liquid processing vs. high pressure homogenization) on droplet size and size distribution in W/O/W emulsions.

3.3 Effect of hydrophilic emulsifier type and processing techniques on the droplet size distribution of W/O/W emulsions

Emulsifier type can play significant role in altering the properties of emulsions. Milk protein (e.g. NaCN studied herein) can adsorb and unfold at the oil–water interface and increase the droplet surface coverage [30]. The correct selection of emulsifier results in the formation of a stable emulsion with desired physicochemical and functional properties. For example, Zamani et al. showed that replacing Tween 20 with whey protein microgels (WPMs) in the emulsion can significantly improve the stability and prevent phase separation due to the enhancement of viscoelastic properties of emulsion (elastic modulus and yield stress) [19].

Based off the findings of Zamani et al. we replaced the NaCN with other types of emulsifiers including Tween 60 and Cremophor EL (W/O = 50 wt%, emulsifier concentration = 0.3 wt%). The droplet size analysis along with creaming behavior analysis showed small differences between these different cases. The two emulsion samples containing Tween 60 and Cremophor EL vs. the sample of NaCN showed slightly smaller droplet size with narrower size distribution possibly due to their enhanced surface activity at the interface (see Fig. 9). For example, the average droplet sizes for NaCN, Tween 60, and Cremophor EL were 4 ± 0.6 μm, 3.1 ± 0.5 μm, and 2.4 ± 0.4 μm, respectively. This slight dependency of emulsion stability and droplet size to the types of hydrophilic emulsifier could be due to: (i) greater stability of the primary emulsion where PGPR prevents coalescence due to its high droplet surface coverage; and/or (ii) the synergetic effect of hydrophilic emulsifier with the hydrophobic one at this specific experimental condition (e.g. concentration, temperature, and etc.). However, in our study, although the type of emulsifier did not influence the emulsion stability to a great extent, but it may still be important for other emulsions systems including high internal phase emulsions (HIPE) and O/W/O [31, 32].

Fig. 9
figure 9

Average droplet size of W/O/W emulsions while using different hydrophilic emulsifiers including: NaCN, Tween 60 and Cremophor EL (W/O = 50 wt% and emulsifier concentration = 0.3 wt%)

Finally, we evaluated the effect of processing techniques (ultrasonic liquid processing vs. high pressure homogenization) on the emulsion stability against creaming and examined the droplet size distribution while using NaCN as the emulsifier. As shown in Fig. 10, the use of HPH instead of the ultrasonic liquid processor adversely affected the emulsion stability and droplet size distribution. The emulsion prepared with HPH showed fast creaming and significant phase separation even during one day of storage time. These results are not surprising and worth discussing in more detail. Since HPH is a high-energy emulsification method, it can destabilize the primary W/O and/or the whole W/OW emulsions given these systems are very sensitive to the energy input [3, 33].

Fig. 10
figure 10

Droplet size distribution of W/O/W emulsions prepared via using different processing techniques: a ultrasonic liquid processor and b high pressure homogenizer (HPH). Experimental conditions: W/O = 50 wt% and NaCN = 0.3 wt%

We believe this is also the main reason why HPH in comparison with the ultrasonication method leads to the formation of emulsions with inferior stability and significantly broader size distribution (see Fig. 10a and b). Another possible scenario could be the adverse effects of HPH on the properties of ingredients (e.g. emulsifier) present in the emulsions. For example, HPH can affect the adsorption kinetics of emulsifiers at the interface and alter the rheological properties of multiple emulsion.

4 Conclusion

In this research study, we examined the effects of sodium caseinate (NaCN) concentration, a type of hydrophilic emulsifier, portions of primary W/O emulsion, and the emulsification process on the formation and stability of W/O/W emulsions. The analysis of W/O/W emulsions revealed that the sample with higher concentration of primary W/O emulsion (50 wt% vs. 40 wt% and 25 wt%) possessed narrower droplet size distribution and a lower creaming index. In this case, the average droplet size decreased from 9 ± 2.5 μm to 4 ± 0.6 μm as W/O concentration increased from 25 wt% to 50 wt%. The higher stability of the emulsion at W/O = 50 wt% is attributed to the enhancement in the emulsion viscosity (larger volume fraction of dispersed phase) and slower rate of droplet coalescence. Increasing the NaCN concentration from 0.3 wt% to 0.9 wt% resulted in the formation of larger droplets possibly due to the destabilization of primary W/O emulsion through the disruption of the polyglycerol polyricinoleate (PGPR) layer by NaCN at the interface. Additionally, we evaluated the effects of different hydrophilic emulsifiers in the external aqueous phase and our results demonstrated that Cremophor EL and Tween 60 vs. NaCN lead to the formation of smaller droplet sizes, possibly due to their enhanced surface activity at the interface. Finally, the use of high pressure homogenization (HPH) instead of ultrasonic liquid processing to generate W/O/W samples adversely affected the emulsion stability and led to formation of droplets with a broad size distribution. Our findings will help with the design of emulsion systems for desired applications using food-grade emulsifiers.