Intan Soraya Che Sulaiman*a,
Mahiran Basri*a,
Hamid Reza Fard Masoumia,
Siti Efliza Asharia and
Maznah Ismailb
aNanodelivery Group, Department of Chemistry, Faculty of Science, Universiti Putra Malaysia, 43400 UPM Serdang, Selangor, Malaysia. E-mail: IntanSulaimanUPM@yahoo.com; mahiran@upm.edu.my
bLaboratory of Molecular Biomedicine, Institute of Bioscience, Universiti Putra Malaysia, 43400 Serdang, Selangor, Malaysia
First published on 5th July 2016
Clinacanthus nutans Lindau (C. nutans) is a well-known medicinal plant in South-East Asia that recently has attracted attention due to its therapeutic characteristics and cosmeceutical applications. However, delivering the beneficial attributes of the bioactive ingredients into a formulation is challenging due to poor solubility and low bioavailability of bioactive substances, which may hinder their effective transdermal delivery. Therefore, a nanoemulsion has been chosen to be a carrier in the encapsulation of bioactive ingredients of C. nutans extract for pharmaceutical and cosmeceutical formulations. In this work, a D-optimal mixture design was used to determine the optimal composition of a nanoemulsion-based system loaded with C. nutans leaves extract. The ultimate goal of the present work was to determine the optimum level of five independent variables (surfactant, oil, xanthan gum, bioactive extract, and water) in the optimal C. nutans nanoemulsion composition with minimum average droplet size. Under the optimal conditions, the predicted average droplet size was 99.99 nm. The actual response showed that the model was in good agreement with the predicted value with residual standard error (RSE) of 2.61%. The optimal nanoemulsion composition was observed to be stable under an accelerated stability study during storage at 25 and 45 °C for 90 days, centrifugal force and freeze–thaw cycles. Physicochemical characterization of the optimal nanoemulsion showed its suitability for transdermal application due to its stability against phase separation.
Consumers are increasingly environmentally conscious. Natural pharmaceutical and cosmetic products have gained tremendous attention compared to synthesized products for their fewer and less harmful side effects. Formulating a product with the beneficial attributes of the bioactive ingredients is a challenge due to various reasons such as poor solubility and low bioavailability of bioactive substances, which may hinder their effective transdermal delivery.10–12
In pharmaceutical and cosmeceutical formulations, encapsulation is currently under study for the production of an improved delivery system to gain an excellent end product. Emulsion is one of the delivery systems that use encapsulation. Oil-in-water (O/W) emulsion is a system that incorporates hydrophobic bioactive substances from a natural extract into the formulation. By definition, emulsion is a dispersion of one liquid phase in another immiscible liquid phase by using a mechanical device.13 Nanoemulsion is an emulsion with a very fine droplet size in the diameter range of 20–200 nm. Due to their very fine droplet size, nanoemulsions possess excellent stability against sedimentation or creaming, which appears to be a challenging issue in emulsion stabilization.14,15
Changing the size of a particle from a macro to nano dimension can change its property. Due to the large surface area of the system, low surface tension and low interfacial tension, O/W nanoemulsions containing bioactive substances can effectively penetrate and be uniformly deposited at target sites.10,15 In general for transdermal application of pharmaceutical and cosmeceutical products require the successful delivery of active ingredients through the skin's lipid barrier to reach the targeted lower layers. However the main resistance to transdermal transport is in a layer of cells joining the stratum corneum to the epidermis. Taking advantage of the nanosized molecule, the bioactive substances may pass through the pores and hair follicles of the skin and mucosal membranes, without disrupting normal tissues.16,17 Moreover encapsulation technique may able to protect unstable and sensitive bioactive substances against unwanted degradation.18 Furthermore, nanoemulsion are relatively non-toxic and safe and thus suitable for transdermal cosmetic application. Besides, nanoemulsions which are apparently transparent or translucent with low viscosity make them aesthetically pleasing, which is preferred in the pharmaceutical and cosmeceutical industries.14
D-Optimal mixture design is a systematic design, oriented for formulation optimization which contains many ingredients. The design is not only the actual amount of each of the single ingredient, but also its proportion in relation to other ingredients. In a mixture design approach, the total sum of all ingredients is equal to 100%.19 Each independent variable has effects on the experimental region and model making.20 This multivariate statistical technique required less sample preparation than the traditional method, and therefore D-optimal mixture design is more preferable among researchers.21,22 Nowadays, D-optimal mixture design has been adopted to optimize the cosmetic emulsions,23,24 self-emulsifying drug delivery systems,25 soap26 and lipstick27 formulation. Those studies demonstrated the advantages of D-optimal design in formulation and optimization of delivery systems. To date, application of C. nutans is limited in conventional formulation for treatment of herpes simplex and varicella zoster virus.6,28 However, no study has been conducted on its potential in nanotechnology for pharmaceutical and cosmeceutical application. In addition, there are no published works on the optimization of C. nutans formulation using any multivariate statistical technique.
Therefore, the main objectives of this study were to produce and develop an optimal novel composition of C. nutans O/W nanoemulsion using D-optimal mixture design with minimum surfactant concentration and to identify the effect of the main components to the system. The physicochemical properties and stability of the optimal prepared nanoemulsion were determined.
:
GSO, various ratios of oil mixture (PKOE
:
GSO) 9
:
1, 8
:
2 and 7
:
3 was added to the basic compositions. The composition of the 0.1% bioactive-loaded systems was added into the oil phase containing T80
:
S80, and 2-phenoxyethanol. The mixture was heated up to 70 °C until homogenized before subjected to centrifugal force for 15 min at 4000 rpm. Evaluation under cross-polarized light was made to observe possible phase separation. The best amount of oil mixture was observed as 9
:
1 in the composition formulation.| Independent variables, Xj | Lower limit, Lj | Upper limit, Uj |
|---|---|---|
| Surfactant, A | 7 | 13 |
| Oil, B | 5 | 15 |
| Xanthan gum, C | 0.5 | 1 |
| Bioactive extract, D | 0.05 | 0.1 |
| Water, E | 70.1 | 86.65 |
By using Design Expert software (Version 7, Stat. Ease Inc., Minneapolis, USA), the design matrix was generated. According to the D-optimal mixture design, the input variables are non-negative proportionate amounts of mixture, therefore the sum must be equal to one, as shown below,
| ∑Xj = 1 and 0 ≤ Xj ≤ 1 |
:
1. GSO was chosen to blend with PKOEs as its providing a good source of linoleic acid. Linoleic acid is an essential fatty acid that can enhance the absorption of bioactive extract and also can be used as carrier oil.30–32 The bioactive material was a mixture of ethyl acetate and ethanol extracts of C. nutans leaves (1
:
1). The blend of hydrophilic (Tween 80) and lipophilic (Span 80) non-ionic surfactants at ratios 8.2
:
1.8 were chosen to obtain better solubilization and stability of the dispersion system developed. Initially, the aqueous and oil phase mixtures were prepared separately and heated up to 70 °C. Once each mixtures were homogenized, the oil phase consisting of T80
:
S80, PKOEs
:
GSO, bioactive, and 0.8% (w/w) 2-phenoxyethanol was gradually added drop wise to the aqueous phase (xanthan gum and deionized water) and stirred with Ultra Turax high shear homogenizer (T25 digital, IKA-Werk, Germany) for 15 min at 6000 rpm. The emulsions were then cooled down to room temperature (25 ± 0.5 °C) by mixing, using an overhead stirrer (RW20 digital, IKA-Werk, Germany) at 250 rpm speed for 30 min.
:
200) with deionized water before being filled into a cuvette capillary cell to avoid multiple scattering effects. Measurements were performed with an angle of 177 at room temperature (25 ± 0.5 °C).
:
1 (PKOE
:
GSO) was chosen as the best amount of oil mixture to be used in the formulation.
| Experiment No. | A | B | C | D | E | Particle size (nm) | |
|---|---|---|---|---|---|---|---|
| Actual | Predicted | ||||||
| 1 | 7.031 | 5.005 | 0.672 | 0.100 | 86.392 | 137.7 | 138.65 |
| 2 | 9.773 | 8.408 | 0.990 | 0.099 | 79.930 | 164.84 | 163.86 |
| 3 | 12.998 | 9.857 | 0.650 | 0.100 | 75.595 | 126.33 | 124.54 |
| 4 | 12.979 | 12.554 | 0.780 | 0.092 | 72.794 | 176.9 | 179.17 |
| 5 | 12.998 | 15.000 | 0.501 | 0.055 | 70.646 | 228.9 | 229.42 |
| 6 | 7.756 | 15.000 | 1.000 | 0.050 | 75.394 | 604.2 | 603.58 |
| 7 | 7.225 | 14.744 | 1.000 | 0.100 | 76.131 | 827.3 | 824.14 |
| 8 | 13.000 | 5.084 | 0.753 | 0.072 | 80.290 | 40.12 | 41.69 |
| 9 | 7.031 | 5.005 | 0.672 | 0.100 | 86.392 | 139 | 138.65 |
| 10 | 7.000 | 8.495 | 0.500 | 0.071 | 83.134 | 232.03 | 231.62 |
| 11 | 7.225 | 14.744 | 1.000 | 0.100 | 76.131 | 820.1 | 824.14 |
| 12 | 12.997 | 15.000 | 0.999 | 0.089 | 70.116 | 237.3 | 237.88 |
| 13 | 9.644 | 14.998 | 0.670 | 0.100 | 73.788 | 376.9 | 375.56 |
| 14 | 9.402 | 5.001 | 0.500 | 0.050 | 84.246 | 87.63 | 84.90 |
| 15 | 7.756 | 15.000 | 1.000 | 0.050 | 75.394 | 604.33 | 603.58 |
| 16 | 13.000 | 10.150 | 1.000 | 0.055 | 74.996 | 143.05 | 140.98 |
| 17 | 9.708 | 11.843 | 0.716 | 0.050 | 76.883 | 237.85 | 241.68 |
| 18 | 12.998 | 15.000 | 0.501 | 0.055 | 70.646 | 230.6 | 229.42 |
| 19 | 9.402 | 5.001 | 0.500 | 0.050 | 84.246 | 83.26 | 84.90 |
In order to examine the suitability and significance of the final model, an analysis of variance (ANOVA) was employed using Design Expert software (Table 3).
| Source | Sum of squares | DF | Mean square | F-Value | p-Value | Significance |
|---|---|---|---|---|---|---|
| Model | 1 059 782.80 |
11 | 96 343.89 |
9225.19 | <0.0001 | Significant |
| Linear mixture | 920 620.95 |
4 | 230 155.24 |
22 037.98 |
<0.0001 | |
| AB | 7205.60 | 1 | 7205.60 | 689.96 | <0.0001 | |
| AC | 21 339.10 |
1 | 21 339.10 |
2043.28 | <0.0001 | |
| AD | 1629.37 | 1 | 1629.37 | 156.02 | <0.0001 | |
| AE | 2912.40 | 1 | 2912.40 | 278.87 | <0.0001 | |
| BD | 1150.64 | 1 | 1150.64 | 110.18 | <0.0001 | |
| BE | 572.98 | 1 | 572.98 | 54.86 | 0.0001 | |
| CE | 917.77 | 1 | 917.77 | 87.88 | <0.0001 | |
| Residual | 73.11 | 7 | 10.44 | |||
| Lack of fit | 35.34 | 2 | 17.67 | 2.34 | 0.1918 | Not significant |
| Pure error | 37.77 | 5 | 7.55 | |||
| Cor total | 1 059 855.90 |
18 |
The computed F-value of the model (9225.19) indicated that the model design was significant. This result showed that predicted and actual values revealed good correspondence between them, and the model developed can be used to adequately describe the relationship between the variables to the response and to predict the particle size of optimal C. nutans nanoemulsion. Regression coefficient for the final reduced model is presented in Table 4.
| Source | Coefficient estimate | Regression coefficient | Particle size |
|---|---|---|---|
| A – surfactant | 2018.91 | Standard deviation | 3.23 |
| B – oil | 386.85 | PRESS | 1161.79 |
| C – xanthan gum | 17 139.05 |
R2 | 0.9999 |
| D – bioactive extract | −2366.40 | Adjusted R2 | 0.9998 |
| E – water | 108.89 | Predicted R2 | 0.9989 |
| AB | −3265.49 | Adequate precision | 304.663 |
| AC | −48 123.31 |
||
| AD | −165 054 |
||
| AE | −2423.56 | ||
| BD | 101 121.90 |
||
| BE | 241.33 | ||
| CE | −13 410.46 |
The final equation for the model obtained was shown in eqn (1). The greatest effect on the response was caused by factor C (xanthan gum). This could be due to the presence of hydrocolloid gum such as xanthan gum can affect the non-Newtonian behavior of emulsions.34 This phenomenon was a consequence of a decrease in the non-Newtonian behavior of emulsion during which an overlap of xanthan gum concentration in the aqueous phase was reached.34,35 As stabilizer added to the emulsion, xanthan gum acts by modifying the viscosity of the aqueous phase.36 By increasing the viscosity of the continuous phase, the emulsion stability was enhanced and thus retarded the droplets movement.37 As the result, the particle size of the molecules decreased with increasing amount of xanthan gum. Some studies reported that addition of xanthan gum to the emulsion may minimize droplet mobility and decreases collision numbers. Hence, it provided enough time for surfactant to adsorb on droplets and stabilize them from coalescence.35,38 However, at certain concentration of xanthan gum, the depletion flocculation occurs. After this overlapping concentration, increasing amount of xanthan gum will promote creaming through mechanism of depletion.35 Therefore the particle size of molecules after this concentration started to increase. Fig. 1 represents that the polynomial regression model was in good agreement with the experimental results. The predicted R2 of 0.9989 was in reasonable agreement with the adjusted R2 of 0.9998. The signal to noise ratio of 304.663 indicated an adequate signal; thus the model can be used to navigate the design space in order to predict the particle size of C. nutans nanoemulsion.
The model obtained is shown in regression eqn (1).
Y = 83 778.50A − 6323.40B + 564 763.61C + 214 014.35D − 54.23E − 119 220.74AB − 1 756 950.25AC − 6 026 012.61AD − 88 482.76AE + 3 691 892.72BD + 8810.94BE − 489 606.91CE
| (1) |
In order to assess the effect of each variable on the particle size of C. nutans nanoemulsion, the three-dimensional (3D) surface and contour (2D) plots were examined. The plots presented in Fig. 4 demonstrate the influence of surfactant, oil, and xanthan gum on the response. The other two independent parameters (bioactive extract and water) were kept constant. Decreasing the surfactant concentration increased the particle size of the nanoemulsion. This might have been due to a low level of emulsifier concentration that led to the incomplete surface coverage of oil; hence, oil droplets coalesced and led to an increase in particle size.39 Surfactants can reduce interfacial tension, therefore with insufficient amounts of surfactant oil was less homogenized in the aqueous phase, which increased particle size.40
In contrast, decreasing the oil concentration seemed to decrease of the particle size of emulsion from 524.23 nm to 126.69 nm. This could be due to a lower collision rate between oil droplets, which reduces the possibility of coalescence.41 Sufficient emulsification results in smaller particle sizes.42 Xanthan gum, however behaves differently. By increasing xanthan gum concentration, particle sizes decreased but at a certain level, particle size starts to increase. The same observation was reported by Krstonošić et al. (2015) and Rodd et al. (2000) in the presence of xanthan gum as an emulsifier.34,43 As mentioned earlier, decrease in non-Newtonian behavior of emulsion happened because xanthan gum reached overlap concentration in which individual polymer molecules begin to physically interact. Therefore, after that concentration, the flocculation occurs and the droplets form a weak-gel network. Thus, promoted a large particle size to be produced.34,43
The 3D surface and 2D plots presented in Fig. 5 demonstrate the influence of the bioactive extract on the response. Direct interactions can be observed in the presence of the bioactive extract. Increasing the amount of the bioactive extract results in a significant increased of particle size from 275.84 nm to 439.32 nm. Therefore, the incorporation of bioactive extract into the particles will result incremental increased of particle size.44
![]() | ||
| Fig. 5 The 3D surface and 2D plot demonstrate the influence of bioactive extract (D) on the particle size of nanoemulsion; and oil (B) and water (E) are kept constant. | ||
![]() | (2) |
| Variables | Particle size (nm) | RSE (%) | |||||
|---|---|---|---|---|---|---|---|
| Surfactant (%) | Oil (%) | Xanthan gum (%) | Bioactive (%) | Water (%) | Actual | Predicted | |
| 9 | 7.5 | 1 | 0.075 | 82.745 | 145.17 | 145.348 | 0.12 |
| 10.2 | 9.5 | 0.73 | 0.075 | 79.495 | 173.20 | 172.974 | 0.13 |
| 10.4 | 10 | 0.74 | 0.075 | 78.785 | 177.50 | 182.236 | 2.60 |
| 10.7 | 10.5 | 0.76 | 0.075 | 77.965 | 187.80 | 188.474 | 0.36 |
| 11 | 11 | 0.77 | 0.075 | 77.155 | 191.70 | 193.626 | 0.99 |
| 11.2 | 11.5 | 0.8 | 0.075 | 76.425 | 199.60 | 202.78 | 1.57 |
| 11.5 | 12 | 0.85 | 0.075 | 75.575 | 210.03 | 209.34 | 0.33 |
The RSE% indicated no significant difference between the actual and predicted values, proving that a good model was obtained.
However, smaller particle sizes may be obtained with higher surfactant levels but the optimum formulation would have the surfactant at a minimum. High level of surfactant will exposed the skin to irritation as well as increases the cost of production.
Taking into account the constraints of Table 6, the optimum formulation of C. nutans nanoemulsion was obtained with a composition of 5% of oil, 8.13% of surfactant, 1% of xanthan gum, 0.1% of bioactive extract, 0.8% of preservative and 84.97% of water. Under the optimum compositions, the predicted average droplet size is 99.99 nm, whereas the actual size was 97.38 nm. The actual response showed that the model is in good agreement with the predicted value with a residual standard error (RSE) of 2.61%.
| Name | Goal | Lower limit | Upper limit | Importance |
|---|---|---|---|---|
| Constraints | ||||
| Surfactant | Minimize | 7 | 13 | 3 |
| Oil | In range | 5 | 15 | 3 |
| Xanthan gum | In range | 0.5 | 1 | 3 |
| Bioactive | Maximize | 0.05 | 0.1 | 5 |
| Water | In range | 70.92 | 87.19 | 3 |
| Particle size | In range | 90 | 100 | 5 |
TEM images (Fig. 6) confirmed the spherical shape of oil droplets in a colloidal system and encapsulation of the bioactive extract in the oil droplets. Apart from that, the particle size measured using TEM is in accordance with the size procured from photon correlation spectroscopy.
Two rheological experiments (steady state and oscillatory) were employed for a better understanding of the behavior of respective nanoemulsion. The C. nutans nanoemulsion had a shear-thinning behavior in both experiments. Fig. 7 represents result of the steady state experiment; shear stress versus shear rate. This direct interaction indicated the present of pseudoplastic behavior in the system,48 which fitted with the power law model shown in following eqn (3);
| τ = kγn | (3) |
Thermogravimetric analysis (TGA) has been employed to study the degradation temperature of nanoemulsion. The TGA thermogram (Fig. 9) demonstrated three distinct transformation regions, with a mass loss observed in the system. The first change occurred at the range of 60 °C to 185 °C due to the loss of water from the surface. This is followed by the second change at the temperature range of 225 to 350 °C due to the loss of water in the micelle structure. At very high temperatures, approximately 350 to 440 °C, decomposition of oil occurs, due to the combustion of organic-bound carbon in the oil. With rapid heating, the transformations over higher temperatures occur in shorter times but over broader temperature ranges.51
The nanoemulsion prepared under optimum compositions was defined to be stable upon centrifugal force test and freeze thaw cycles (Table 7). With different storage conditions for 90 days (room temperature and 45 °C), no phase separations were observed, indicated the stability of the nanoemulsion.
| Stability test | Storage stability (days) | Centrifugation | Freeze thaw cycle (3 cycles) | |||||||
|---|---|---|---|---|---|---|---|---|---|---|
| 1 | 30 | 60 | 90 | |||||||
| Temperature (°C) | 25√ | 45√ | 25√ | 45√ | 25√ | 45√ | 25√ | 45√ | √ | √ |
The stability of the end product under extreme storage conditions is important to ensure the ability of the final formulation to tolerate under market storage. For better understanding of the stability assessment for optimal formulation at room temperature (25 °C), the particle size, polydispersity index and zeta potential changes during observation period for 90 days was recorded (Fig. 10 and 11). Even though, the particle sizes of the colloidal system slightly increased in time during the storage period however still remaining in the nano-sized range (less than 200 nm). This phenomenon could be attributed to Ostwald ripening and coalescence. Coalescence can be preventing by a stabilizer while Ostward ripening will continuously occur. Ostward ripening is defined as the process in which large particles grow at the expense of the smaller particles due to the higher solubility of smaller ones.52 The pH value for optimal nanoemulsion was 5.27 ± 0.01. This pH value is compatible with the pH of human skin which ranges from 5 to 6.53 Conductivity tests can be used to determine the ability of the emulsion to conduct electricity. High conductivity values will lead to less lamellar water and more free water in the system.54 Moreover, high conductivity indicates that the aqueous phase is the continuous phase in the system. Thus, the type of nanoemulsion can be determined as either oil in water (O/W) or water in oil (W/O). In this study, C. nutans nanoemulsion was confirmed as an O/W nanoemulsion due to its high conductivity value of 1227 μS cm−1. Furthermore, oil in water formulation was more favourable in formulation of cosmetic product due to its characteristic such as less greasy and less cost. Fig. 12 illustrates the FT-IR spectra of C. nutans nanoemulsions in different storage conditions. The spectra clearly show that the freshly prepared nanoemulsion (2 days) and the nanoemulsions for one year storage at 25 °C and 45 °C have no significant difference. This indicated the stability of C. nutans extract in developed nanoemulsions system showing no decomposition of the compounds against long term storage (one year) at different temperatures (25 °C and 45 °C).
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| Fig. 12 FT-IR spectra of C. nutans nanoemulsions. (a) Freshly prepared (2 days), (b) one year storage at 25 °C and (c) one year storage at 45 °C. | ||
| This journal is © The Royal Society of Chemistry 2016 |