submicron emulsions containing fenugreek gum

submicron emulsions containing fenugreek gum

Accepted Manuscript Stability and physical properties of model macro- and nano/submicron emulsions containing fenugreek gum Olga Kaltsa, Neolea Spilio...

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Accepted Manuscript Stability and physical properties of model macro- and nano/submicron emulsions containing fenugreek gum Olga Kaltsa, Neolea Spiliopoulou, Stavros Yanniotis, Ioanna Mandala PII:

S0268-005X(16)30275-2

DOI:

10.1016/j.foodhyd.2016.06.025

Reference:

FOOHYD 3479

To appear in:

Food Hydrocolloids

Received Date: 31 March 2016 Revised Date:

25 May 2016

Accepted Date: 20 June 2016

Please cite this article as: Kaltsa, O., Spiliopoulou, N., Yanniotis, S., Mandala, I., Stability and physical properties of model macro- and nano/submicron emulsions containing fenugreek gum, Food Hydrocolloids (2016), doi: 10.1016/j.foodhyd.2016.06.025. This is a PDF file of an unedited manuscript that has been accepted for publication. As a service to our customers we are providing this early version of the manuscript. The manuscript will undergo copyediting, typesetting, and review of the resulting proof before it is published in its final form. Please note that during the production process errors may be discovered which could affect the content, and all legal disclaimers that apply to the journal pertain.

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2ο macroemulsion

Ultrasounds 1ο nanoemulsion

2ο nanoemulsion

+ Fenugreek Gum

5 month storage

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1ο macroemulsion

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+ Fenugreek Gum

ACCEPTED MANUSCRIPT Stability and physical properties of model macro- and nano/submicron emulsions containing fenugreek gum

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Olga Kaltsa, Neolea Spiliopoulou, Stavros Yanniotis, and Ioanna Mandala1

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Food Science & Nutrition Dept., Agricultural University of Athens, Iera Odos 75,

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11855, Athens, Greece.

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Abstract

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Nanoemulsions were made in two steps. Firstly, a less viscous, primary O/W

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emulsion was prepared using ultrasounds. In those emulsions, only whey protein

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isolate was used as an emulsifier, whereas the oily phase was olive oil. A stabilizer,

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fenugreek gum, was incorporated afterwards in the primary formulations resulting in

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the secondary emulsions of increased viscosity. Oil amount changed and its decrease

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from 20 to 5 % wt led to a reduced average droplet size and polydispersity index

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values in the primary emulsions. Nanoemulsions with the lowest polydispersity were

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produced at a high sonication time treatment of 12 min. Their droplet size was ~200

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nm. They showed increased viscoelastic properties and consistency leading to

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significantly increased stability compared to their coarse secondary emulsions

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produced by high shear mixing. Even the formulations with the lowest olive oil

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content investigated, 2.5% wt, presented an improved stability during a long-term

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storage of six months.

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Corresponding author: Ioanna Mandala ([email protected]), 75 Iera Odos, Votanikos, Athens, Tel.:+30 2105294692, Fax:+30 210 5294697

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ACCEPTED MANUSCRIPT 1. Introduction

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Emulsions can have very fine droplets of ten to a few hundred nanometers in

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diameter, namely nanoemulsions. They are designed to have a high kinetic stability

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considering that creaming or sedimentation velocity is proportional to the square of

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the particle size. Additionally, they have been praised for increased bioavailability of

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several bioactive compounds (McClements, 2005; Sonneville-Aubrun, Simonnet, &

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L’Alloret, 2004; Tadros, Izquierdo, Esquena, & Solans, 2004).

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In our study, virgin olive oil was used to form an oil in water emulsion. This is

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considered significant as many strategies and actions have been globally undertaken

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by several initiatives and authorities to overcome obesity pandemic, known as

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“globesity”. In particular, the World Health Organization suggestions towards fat

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include a consumption shift from saturated to unsaturated fats and the restriction of

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energy intake from fat (WHO, 2015).

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Fenugreek (Trigonella foenum-graecum L.) seeds are generally used as a spice but

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they also have medicinal properties. They contain 45% to 60% carbohydrate (mainly

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galactomannan), 6% to 10% lipid (mainly polyunsaturated fatty acids), and 20% to

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30% protein (4-hydroxyisoleucine being one of the major amino acids) (Rao,

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Sesikeran, Rao, Naidu, Rao, & Ramacjandran, 1996; Raghuram, Sharma, &

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Sivakumar, 1994). Over the last decade, the use of fenugreek gum has been increased

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in many food products, because of its considerable thickening, stabilizing, and

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emulsifying properties (Işıklı & Karababa, 2005). Additionally, fenugreek gum

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contains a low amount of protein. These proteinaceous moieties, at concentration as

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low as 0.1 wt %, impart an amphiphilic property to the gum, which can then act

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somehow like an emulsifier (Brummer, Cui & Wang, 2003; Youssef, Wang, Cui, &

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Barbut, 2009).

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In a previous study (Kaltsa,Yanniotis & Mandala, 2016) we have shown that

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fenugreek gum fractions with high galactomannan content (>80 %wt) may exhibit

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similar or improved stability properties in whey protein emulsions compared to other

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commercial galactomannans. However, when a high-energy homogenization process

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is used, such as ultrasonication, a severe degradation of commonly used

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polysaccharide stabilizers takes place, owed to extreme shearing. Hence,

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polysaccharides’ addition in the initial formulation is not suggested, as their

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degradation can reduce the viscosity of the continuous phase enhancing the

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ACCEPTED MANUSCRIPT destabilization process (Kaltsa, Michon, Yanniotis & Mandala, 2013; Kaltsa et al.,

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2016; Tiwari, Muthukumarappan, O'Donnell, & Cullen, 2010). Additionally,

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stabilizers can hinder the efficacy of the homogenization process. They increase the

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viscosity, which hinders the propagation of soundwaves, increases the cavitation

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threshold to higher amplitudes and reduces the shearing turbulence (Wooster,

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Golding, & Sanguansri, 2008).

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The stability of whey prrotein nanoemulsions has been the topic of many studies

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lately (Adjonu, Doran, Torley, & Agboola, 2014a, b; Ali, Mekhloufi, Huang, &

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Agnely 2016; Ozturk, Argin, Ozilgen, & McClements, 2015; Teo et al., 2016; Zeeb,

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Herz, McClements, & Weiss, 2015). However, to our best of knowledge, there is no

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available information regarding nanoemulsion models containing fenugreek gum.

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The objective of this study is the investigation of nanoemulsion formation by

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changing the oil fraction, and ultrasonication processing time. In general low oil

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fractions (<10 %) favor the formation of nanoemulsions below 200 nm, while higher

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ones promote the formation of larger ones (Leong, Wooster, Kentish, & Ashokkumar,

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2009; Tabibiazar et al., 2015). Extended sonication time may also be useful in order to

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reduce the mean droplet diameter of nanoemulsions as in a longer process there is

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more time for the protein to orientate on the oil interface (Jafari Ηe, & Bhandari,

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2007). The stability of the final formulations (secondary model emulsions) produced

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by further dilution with fenugreek gum was evaluated and comparisons were made

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between nanoemulsions and their macroemulsion homologues produced by high-

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speed mixing.

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2. Materials and methods

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2.1. Materials

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Whey protein isolate (WPI) Lacprodan DI-9224 was kindly provided by Arla (Arla

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Foods Ingredients, Amba-Denmark). The composition of WPI powder in protein as

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stated by the manufacturer was protein 92 ± 2 %, and maximum amounts of fat 0.2 %,

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ash 4.5 % and lactose 0.2 %. Fenugreek gum powder Fenulife® was a kind gift from

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Frutarom(Londerzeel, Belgium) (moisture content 6.3 %, soluble fiber content 83.2

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%, mostly composed of galactomannan according to manufacturer and 3.2 % protein

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calculated by Dumas method (Kaltsa, Yanniotis & Mandala, 2016)). Virgin olive oil

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Altis (Elais Unilever, Greece) was purchased from a local store. Sodium azide was

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ACCEPTED MANUSCRIPT purchased from Fluka (Fluka Chemie AG, Buchs, Switzerland) and glacial acetic acid

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from Sigma–Aldrich.

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2.2. Solution preparation

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Whey protein stock solutions (10 g in deionized water in total weight 95, 90 or 80 g)

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were prepared by agitation with a magnetic stirrer for 90 min. Fenugreek gum (FGF)

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solutions 1, 1.5 and 2 %wt in deionized water were prepared by hot stirring in a water

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bath at 90 oC for 90 min. Thereafter, solutions were kept overnight at 5 oC to ensure

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complete hydration. Sodium azide 0.02 %wt was added to the aqueous solutions as an

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antimicrobial agent.

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2.3. Coarse emulsion preparation and screening

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Oil-in-water primary macro-emulsions were prepared by homogenizing 5, 10 or 20 g

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of oil phase with 95, 90 or 80 g of the WPI aqueous solutions accordingly. The initial

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step in preparing macro-emulsions involved the production of a coarse premix

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emulsion by homogenizing the oil and the aqueous phases using an Ultra Turrax (T25

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basic, Janke & Kunkel IKA Labortechnik, Staufen, Germany) for 2 min (13.500

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RPM) at room temperature. The coarse emulsions were further diluted with fenugreek

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gum solutions (2 %wt) in a ratio of 1:1 by weight. Ingredients were further mixed

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using a magnetic stirrer for 1 min in order to avoid recoalescence of the droplets and

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to yield to the secondary coarse emulsions. Emulsion preparation was conducted in

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neutral conditions in order to take advantage of the higher solubility of the protein.

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The pH of the resulting macro- and nano-emulsions was then adjusted to 3.8, which is

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typical for acidic food emulsions, with a few drops of glacial acetic acid.

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Nanoemulsions were produced by further homogenizing 10 ml of the primary coarse

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premixes with an ultrasonic homogenizer model Sonopuls 3200 (Bandelin Electronic

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Gmbh & Co, Berlin) equipped with a 3 mm in diameter titanium probe (MS 73). The

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tip was immersed 10 mm from the surface of the sample which was placed in a double

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jacketed flow-through vessel (model DG-3). The temperature was maintained at 30 ±

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1oC by circulating cold water with a pump. The amplitude was set at 40%. It was

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noticed that amplitude values higher than 40 % led to increased fluctuations of the

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samples in the vessel, which caused sample spilling. The processing time ranged

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between 1 up to 12 min. The experimental data at time intervals of 1, 2, 4, 8 and 12

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min showed that the nominal ultrasonic energy input (kJ), as a function of time,

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ACCEPTED MANUSCRIPT followed the following linear equation: Energy (kJ) = 1.88 x Time + 0.1524 (R2=1).

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The emulsification time, which resulted in both minimum droplet sizes and

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polydispersity index (PDI) for all oil concentrations used, was chosen for the

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incorporation of nanoemulsions in 2 %wt fenugreek solutions as mentioned above for

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macro-emulsions. All samples were prepared in triplicate.

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2.4. Droplet size measurement

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Droplet size distributions of the primary coarse emulsions were determined using a

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Mastersizer 2000 (Malvern Instruments, Malvern, UK). Emulsion droplets were

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characterized under high dilution conditions by dispersing the samples in deionized

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water. The refractive indices of water and olive oil were taken as 1.330 and 1.467,

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respectively, and the Mie theory was used for the analysis (Paximada, Tsouko,

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Kopsahelis, Koutinas, & Mandala, 2014). Average droplet sizes were characterized in

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terms of the volume mean diameter D50 and polydispersity (Span). All measurements

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were made at ambient temperature on three separately prepared samples.

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The mean droplet size (z-average diameter) and the polydispersity index (PDI) of

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nanoemulsions were measured using a dynamic light scattering instrument (Zetasizer

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Nano ZS, Malvern Instruments, Malvern, UK). Measurements were performed at

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25 °C in triplicate. Prior to measurement, the nanoemulsions were diluted (1:500)

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with deionized water to avoid multiple scattering during measurements.

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2.5. Emulsion stability

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The storage stability (at 5 οC) of macro- and nanoemulsions was determined by

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obtaining backscattering profiles with a Turbiscan 2000 device (Turbiscan 2000,

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Formulaction, Toulouse). For unstable macro emulsions the serum percentage was

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calculated (Zinoviadou, Scholten, Moschakis, & Biliaderis, 2012). In stable samples

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(macro- and nano/submicron emulsions), the average value of the backscattering (BS)

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measurement at the middle zone of the cell (between 30 and 40 mm of sample height)

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has been plotted as a function of ageing time and BS variation (dBS) during 10 days

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of storage. Calculations were conducted as described in Kaltsa et al. (2013).

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2.6. Emulsion rheology

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Viscosity measurements were performed with a hybrid rheometer DHR (TA

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Instruments, New Castle, DE, US) equipped with plate-plate geometry (upper plate

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ACCEPTED MANUSCRIPT diameter 50 mm, gap 1 mm) to obtain flow curves between 0.1 to 1000 s-1 at 25 ±

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0.01 oC by circulating water from a peltier. The total measurement time was 900 s. All

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measurements were performed in triplicate and data reported as average and standard

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deviations.

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The linear viscoelastic region (LVR) was assessed at 6.28 rad/s (= 1 Hz) by strain

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sweep experiments; for all samples a constant deformation of γ = 0.1 % was used,

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which was within the linear viscoelastic region of all the samples. Deviation from the

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linear viscoelastic region occurs when the sample starts to permanently deform,

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implying the destruction of the transient network structure. Small deformation

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oscillatory measurements were performed for the evaluation of the viscoelastic

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properties, G′ (storage modulus), G″ (loss modulus), and tanδ (G″/G′) (Steffe,

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1996; Metzger, 2006), over the frequency range of 0.1–100 rad/s at 25 °C.

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3. Results and discussion

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3.1. Droplet size

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The droplet mean diameter (D50) of primary coarse emulsions ranged between

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9.48 and 13.76 µm (Table 1). Although emulsion diameter usually increases when

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increasing oil concentration (Christensen et al., 2001), only a slight change in the

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mean diameter was observed for samples containing 20 %wt olive. Nevertheless, no

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significant differences were observed compared to emulsions containing lower

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amounts of olive oil (p>0.05). No significant differences were observed either

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considering the polydispersity of samples since Span values ranged between 1.46 up

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to 2.48 (Table 1). This allows us to assume that the emulsification time and protein

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isolate concentration used, were sufficient to equally minimize the droplet size in all

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formulations examined regardless of the oil content.

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It is well known that WPI, as a protein, is a surface-active molecule that has the

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tendency to adsorb at interfaces and undergoes structural rearrangement. However, its

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solubility and emulsifying properties depend on pH. As mentioned above, emulsion

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preparation was conducted at neutral conditions in order to take advantage of higher

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solubility of the protein. In our study, the whey protein used, presented a minimum of

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93.6 % solubility (data not shown) at pH 5, which is near the typical value of whey

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proteins’ pI ~ 4.5 (Pelegrine and Gasparetto, 2005) and should be mentioned that only

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undenatured whey proteins remain soluble throughout all pΗ range

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ACCEPTED MANUSCRIPT Αt neutral pH values, oil droplets with whey protein absorbed at the interface possess

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a negative charge and are strongly repelled. On the contrary, at pH values near pI, the

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surface charge diminishes and repulsive forces are weakened, leading to enhanced

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attraction of the droplets. At even lower pH whey proteins take on a net positive

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electrical charge. They can then interact with charge-carrying polysaccharides (e.g.

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pectin, xanthan, carrageenan, chitosan) and extensive interactions may take place

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either increasing or decreasing the stability of the emulsion. In our case, the reduction

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of pH did not induce any instability, as fenugreek gum, like all other galactomannans,

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does not carry any electrostatic charge to interact with the positively charged WPI on

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droplet interface. However, proteinaceous moieties in fenugreek gums may impart an

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amphiphilic property to the gum, which enables it to act somehow like an

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emulsifier (Brummer et al., 2003; Youssef et al., 2009; Kaltsa et al., 2016).

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Primary coarse emulsions were subjected to sonication in order to achieve further

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droplet size reduction. As shown in Fig. 2a, a sharp decrease in the droplet size was

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achieved within 1 min of sonication, hence the z-average diameter ranged between

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323 - 288 nm depending on the oil content. Thereafter, the droplet size was

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moderately reduced at increased sonication times up to 12 min. In more detail, the z-

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average diameter of samples containing 5 and 10 %wt oil did not show any

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considerable droplet reduction after 1 or 2 min of sonication accordingly, whereas a

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longer time of 8 min was necessary that samples containing 20 % wt oil reach a

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droplet size plateau.

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Regarding the polydispersity of sonicated emulsions, it is shown that the PDI

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decreased, when the sonication processing time increases (Fig. 2b). Although the PDI

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values for samples containing 5 and 10 %wt oil, was 0.434 and 0.51 respectively after

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1 min of sonication whereas the PDI values were considerably higher in samples

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containing 20% olive oil. More specifically, emulsions containing 20 %wt olive oil

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were characterized by

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polydispersity of the droplets (Tiwari, Hihara, & Rawlins, 2014). However, results

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should be treated with caution since DLS measurements can be considered reliable

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when values of PDI <0.5 are obtained.

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At low oil fractions 5 and 10 %, PDI values were unvarying after 4 or 8 min

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accordingly. However, PDI values reduction under sonication time increase was

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remarkable in samples containing 20% olive oil. Actually, the lowest PDI value was

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observed at 12 min of sonication in emulsions containing 20% of olive oil.

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PDI values greater than 0.9, indicative of the strong

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ACCEPTED MANUSCRIPT Considering the above findings, a sonication time of 12 min was selected in order to

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further add the FGF gum, as that time resulted in the lowest PDI values for all

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samples produced.

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Nanoemulsions with an average size droplets of 207 nm and a narrow polydispersity

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(~ 0.2) at oil fraction 5% wt can be seen (Fig. 2a, b). This size is slightly higher than

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that reported by Adjonu et al. (2014a), who prepared WPI nanoemulsions of 160 nm,

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which could be attributed to slightly lower oil fraction used (4 %wt). Lower droplet

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sizes reaching 75 nm have been referred by using bovine serum albumin (BSA) in the

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presence of polyethylene-glycol (PEG) (Tabibiazar et al., 2015).

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An increase in the oil fraction to 10 or 20% led to higher droplet sizes (~280 nm) and

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PDI values (~0.38), although no significant differences were observed after 12 min of

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sonication (p>0.05) (Table 1).

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3.2. Screening of FGF concentration for secondary coarse emulsion preparation

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Initially, a screening procedure was conducted in order to assess the FGF

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concentration required to obtain stable secondary coarse emulsions containing 2.5, 5,

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or 10 %wt olive oil in the final formulation. The curves of creaming (% Serum)

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versus storage time of coarse emulsions containing 0.5 up to 1 %wt FGF are shown in

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Fig. 3.

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The oil phase content significantly affected the serum percentage values (p<0.05). As

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can be seen the stability of emulsions was improved by increasing the oil content from

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2.5 to 10 %wt (Fig. 3a, b,c).

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For emulsions containing 0.5 %wt FGF the serum percentage decreased from 71.3 to

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~ 9.5 % when the oil content changed from 2.5% to 10%wt, while for those

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containing 0.75 %wt FGF, a reduction from 42.2 to 3.2 % was noticed for the same

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oil content change. Stability improvement by increasing the oil content is well known.

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It is associated to the increase in packing fraction of oil droplets, which leads to

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enhanced interdroplet interactions and viscosity and to more structured emulsions

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(Dickinson & Golding, 1997; Sun & Gunasekaran, 2009; Nikiforidis, Biliaderis, &

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Kiosseoglou, 2012). However, the oil concentrations used are far from the droplet

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close packing limits. In fact, creaming becomes inhibited altogether when the oil

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volume fraction φ is as high that the droplets become close-packed, which is φ ~ 0.6

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for monodisperse spheres (Dickinson, 2009).

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ACCEPTED MANUSCRIPT Polysaccharides employed as thickeners of emulsions confer long term emulsion

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stability and prevent creaming through viscosity modification of the aqueous

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continuous phase (Dickinson, 2003). In our case, the addition of 1 %wt FGF resulted

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in the formation of stable coarse emulsions, which did not show any phase separation

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during 10 days of storage. Therefore, this concentration was used in subsequent

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formulations and comparisons were made between coarse and nanoemulsion

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emulsions. Huang, Kakuda, & Cui (2001), who compared the stability of emulsions

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containing different hydrocolloids, have also shown that long term stability without

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phase separation could be achieved by the use of higher concentration of fenugreek,

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guar and locust gums (1-1.5 %wt), attributed to a droplet movement restriction caused

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by the continuous phase viscosity increase.

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3.3. Emulsion rheological properties

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The Power law model was adopted to describe the viscosity properties of coarse and

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nanoemulsion analogues, as the same model was applied to describe the shear

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thinning behavior of extruded fenugreek gum solutions (Chang & Cui, 2011).

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Table 2 summarizes the estimated consistency (k) and flow behavior (n) values of

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prepared secondary coarse and nanoemulsions containing 1 %wt FGF and various

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amounts of olive oil. All model emulsions prepared were highly pseudoplastic with

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flow coefficient (n) values varying from 0.29 to 0.35.

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Consistency and flow behavior values were both influenced by the oil content and the

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preparation method used, but the greatest changes were noticed at 10% oil. At 2.5% or

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5% oil content differences among the samples were not significant in most cases

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(Table 2).

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Considering the coarse emulsions, an increase of oil content from 2.5 to 10 %wt

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increased the consistency of the samples as well, from ~7.4 to 11.7 Pa-sn. This

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change of the oil fraction causes an upward shift of the flow curves to higher

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viscosities, attributed to the increased packing of the oil droplets. This leads to

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enhanced droplet interactions, thus to more viscous emulsions (Sun & Gunasekaran,

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2009). Significant differences were observed among all coarse emulsions regardless

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of their oil content (p<0.05). Nevertheless, this was also observed in nano-emulsions,

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for which, k values increased from 8.59 to 15.69 Pa-sn. The decrease of the droplet

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size within the submicron scale resulted in an increase of the k values by 16 up to 34

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% depending on oil concentration. However, it may be noticed that no significant

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ACCEPTED MANUSCRIPT differences are found between the viscosity values (k) of submicron emulsions

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containing 2.5 and 5 %wt olive oil (p>0.05).

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The oil fraction increase also led to an enhancement of the pseudoplastic character in

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both coarse and nano-emulsions, as evidenced by the decrease in flow behavior values

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(n). Flow behavior values ranged between 0.333 – 0.352 and 0.288 – 0.324 for coarse

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and nanoemulsions respectively. Similar values were reported for 1 %wt fenugreek

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solutions by Wu et al. (2009), indicating the predominant role of fenugreek on

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emulsion pseudoplasticity, as found in a previous study (Kaltsa et al., 2016).

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Nanoemulsions were more pseudoplastic in all cases, regardless of the oil

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concentration (p<0.05).

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Dynamic oscillatory shear tests were used to characterize the viscoelastic properties of

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coarse and nano-emulsions containing 1 %wt FGF. The storage (G’) and loss (G”)

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modulii measured, are shown in Fig. 4(a-c). Loss tangent (tanδ) was also used to

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assess the elastic or viscous character predominance in the samples as shown in the

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same figure.

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Overall, samples exhibited frequency-dependent storage and loss modulus values,

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which increased during frequency ramp from 0.1 to 100 rad/s. In all emulsions, G”

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was dominant over G’ in low frequency region, thereby showing a liquid like

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behavior. This implies that the most of the input energy cannot be stored at this low

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frequency region, thus it dissipates through viscous flow. At higher frequencies

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(approximately > 1 rad/s) a cross-over occurs and a solid-like behavior is observed for

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all emulsion preparations (G’>G”). Additionally, the crossover point of the modulii is

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shifted at lower frequencies in the viscoelastic spectra of nanoemulsions.

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Entanglements of macromolecular solutions can result in such behavior according to

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Ross-Murphy (1984). Moreover, when G’ is higher than G’’ over most of the

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frequency range investigated, the formation of a weak three-dimensional network of

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ordered chain segments can be evident. The same behavior was observed in

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nanoemulsions of higher oil content (Fig. 4c). However, as the tanδ values were

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higher than 0.3 over the entire frequency range (Fig. 4), emulsions maintain a viscous

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character (Mandala et al., 2004). Only for a tanδ > 0.1, a weak gel behavior is

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ascribed, whereas a strong gel is evident at tanδ values less than 0.1 (Wang & Cui,

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2005). These findings can be explained by the fact that galactomannans, even at low

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concentrations, are capable of forming highly viscous solutions due to their high water

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binding capacity. Galactomannans, such as fenugreek and guar gum, do not form gels

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ACCEPTED MANUSCRIPT on their own, whereas for locust bean gum, high concentrations and

subzero

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temperatures (Dea et al., 1977) or a long storage are required to form gels

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(Richardson, Clark, Russell, Aymard, & Norton, 1999). According to Wu, Cui, Eskin

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& Goff (2009) fenugreek gum solutions with concentration ranging between 0.5 -2

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%wt present a liquid like behavior at lower frequencies (G”>G’) and a solid-like at

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higher ones. Moreover, in another study, the mechanical spectra of 1 %wt fenugreek

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gum aqueous dispersions showed a change of behavior depending on the molecular

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weight. Fenugreek gum fractions with higher molecular weight (Mw≥ 18.3x105

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g/mol) showed a concentrated polymer solution pattern, exhibiting modulus crossover

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(G’>G’’) at high angular frequencies, as in our case, whereas those of lower Mw

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presented a dilute polymer solution pattern, as evidenced by modulii values (G’’>G’)

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and absence of crossover (Funami et al., 2008).

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The droplet packing caused by oil fraction increase and sonication resulted in

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emulsion thickening as evidenced by the enhancement of G’ and G’’ values (Sun &

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Gunasekaran, 2009).

330

At the same time, a decrease of loss tangent occurred, revealing the increase of the

331

solid like behavior. Minor differences in the storage, loss modulus and tanδ were

332

detected between formulations with low amounts of oil (2.5 and 5 %wt). Obviously,

333

findings of dynamic properties are in-line with those obtained in respect with the flow

334

behavior of the emulsions.

335

3.4. Stability of coarse and nano- emulsions containing 1 %wt FGF

336

Coarse and nanoemulsion formulations at 1 %wt FGF did not exhibit any phase

337

separation within the period tested (10 days, 5οC), as back-scattering values were

338

constant during storage (Fig. 5). According to Mie theory the back scattering intensity

339

increases by a decrease of the particle size of the droplets, when their diameter is

340

greater than 500 nm while the opposite applies for those of smaller size e.g.

341

nanoemulsions. It can be noticed that the initial BS intensity values are affected by oil

342

content and emulsification method. According to several studies BS intensity is a

343

value influenced by the size and density of the oil particles in emulsions. It is

344

enhanced by the increase of the oil droplet number and by decreasing their size or the

345

size of the flocs present (Palazolo, Sorgentini, & Wagner, 2004 and 2005). In our case

346

the increase of the oil fraction from 2.5 to 10 %wt increased the initial BS values of

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ACCEPTED MANUSCRIPT coarse emulsions from 40.3 to 61.6 % and those of nanoemulsions from 45.6 to 71.8

348

%.

349

Concerning storage time, in coarse emulsions containing 5 and 10 %wt oil, a

350

reduction of approximately ~4 % in BS (dBS) was noticed within 10 days of storage,

351

while it reached a value of 11.4 % decrease in samples containing 2.5 %wt oil (Fig.

352

5c). The BS change (dBS) was lower in nanoemulsions and ranged between ~ 1-1.9

353

%, hence an improvement in the stability in terms of the coalescence-flocculation was

354

achieved, attributed to droplet size reduction and thickening of the samples as

355

discussed above.

356

Normally, an increase in BS should have been noticed with storage time, in the case

357

of nanoemulsions, as a consequence of coalescence or flocculation phenomena

358

occurring during storage as previously observed in other studies (Porras, Solans,

359

González, & Gutiérrez, 2008; Wulff-Pérez, Torcello-Gómez, Gálvez-Ruíz, & Martín-

360

Rodríguez, 2009). In our case, the reason for a back scattering decrease could be

361

explained by the fact that nanoemulsions may have undergone flocculation during the

362

incorportation of FGF solution and subsequent pH adjustment from 6.5 to 3.8 passing

363

through the isoelectric point of proteins. The net negative charge that the oil droplets

364

posse at high pH values is suppressed by the decrease of pH values near the pI of the

365

protein (4.8), thus a few droplets of an average diameter 200 - 300 nm could easily

366

form flocs, the size of which could be detected by the Turbiscan wave length.

367

Considering a long storage of five months, as demonstrated in Fig. 6 and 7, coarse

368

emulsions prepared with 2.5 %wt oil were the least stable, since phase separation

369

(serum) occurred as evidenced by a sharp BS decrease near zero values at the bottom

370

of the tube (Fig. 6). Phase separation of that sample is also shown in Fig. 7. For the

371

rest of the samples, BS decreased gradually along

372

coalescence-flocculation phenomena indicated by higher BS values on day 0 (purple

373

line) and lower ones one day 150 (red line).

374

4. Conclusions

375

Low oil content model emulsions were developed and stabilized by FGF addition.

376

Stable coarse formulations were achieved upon the addition of 1 wt % FGF in all

377

cases of oil content (2.5, 5 or 10 %wt). Emulsion stability was further ameliorated by

378

preparing nano/submicron emulsions by ultrasonic homogenization. Nanoemulsions

379

with the smallest droplet diameter (~200 nm) and PDI (~0.2) were produced at the

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the sample tube due to

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ACCEPTED MANUSCRIPT lowest oil content after 12 min of sonication. Droplet size reduction in the

381

nano/submicron scale influenced the viscoelastic properties of the emulsions, as more

382

structured and viscous samples were obtained. All nano/submicron emulsions

383

exhibited higher stability during storage compared to coarse models due to a droplet

384

size reduction and their enhanced viscoelastic properties. Our results demonstrate that

385

the presence of nanosized droplets is mostly beneficial in the case of producing very

386

low oil content (2.5 % wt) model emulsions, as long term stability is still evident.

387

Acknowledgements

388

This research has been co-financed by the European Union (European Social Fund –

389

ESF) and Greek national funds through the Operational Program “Education and

390

Lifelong Learning” of the National Strategic Reference Framework (NSRF) –

391

Research Funding Program: Heracleitus II. Investing in knowledge society through

392

the European Social Fund.

393

The authors would like to thank Frutarom Belgium N.V. for kindly donating

394

FenuLife® extract.

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References

396

Adjonu, R., Doran, G., Torley, P., & Agboola, S. (2014a). Formation of whey protein

397

isolate hydrolysate stabilised nanoemulsion. Food Hydrocolloids, 41, 169-177. Adjonu, R., Doran, G., Torley, P., & Agboola, S. (2014b). Whey protein peptides as

399

components of nanoemulsions: A review of emulsifying and biological

400

functionalities. Journal of Food Engineering, 122, 15-27.

RI PT

398

Ali, A., Mekhloufi, G., Huang, N., & Agnely, F. (2016). β-lactoglobulin stabilized

402

nanemulsions—Formulation and process factors affecting droplet size

403

and nanoemulsionstability. International Journal of Pharmaceutics, 500(1–2),

404

291-304.

SC

401

Brummer, Y., Cui, W., & Wang, Q. (2003). Extraction, purification and

406

physicochemical characterization of fenugreek gum. Food Hydrocolloids, 17,

407

229–236.

M AN U

405

408

Chang, Y. H. & Cui, S.W. (2011). Steady and dynamic shear rheological properties of

409

extrusion modified fenugreek gum solutions. Food Science and Biotechnology

410

20(6) 1663-1668.

Christensen, K.L. L, Pedersen GP, & Kristensen HG. (2001). Technical optimization

412

of redispersible dry emulsions. International Journal of Pharmacy, 212, 195-

413

202.

TE D

411

Dea, I.C.M., Morris, E. R., Rees, D. A., Welsh, E.J., Barnes, H. A., & Price J. (1977).

415

Associations of like and unlike polysaccharides: Mechanisms and specificity in

416

galactomannans, interacting bacterial polysaccharides, and related systems.

417

Carbohydrate Research, 57, 249–272.

419

Dickinson E. (2003). Hydrocolloids at interfaces and the influence on the properties

AC C

418

EP

414

of dispersed systems. Food Hydrocolloids, 17(1), 25-39.

420

Dickinson, E. (2009). Hydrocolloids in emulsions stability. In G. O. Phillips & P. A.

421

Williams (Eds.), Handbook of Hydrocolloids (pp. 23-47). FL: CRC Press.

422

Dickinson, E., & Golding, M. (1997). Rheology of sodium caseinate stabilized oil-in-

423

water emulsions. Journal of Colloid and Interface Science, 191, 166–176.

424

Funami, T., Kataoka, Y., Noda, S., Hiroe, M., Ishihara, S., Asai, I., Takahashi, R., &

425

Nishinari, K. (2008). Functions of fenugreek gum with various molecular

426

weights on the gelatinization and retrogradation behaviors of corn starch—1:

427

Characterizations of fenugreek gum and investigations of corn starch/fenugreek 14

ACCEPTED MANUSCRIPT 428

gum composite system at a relatively high starch concentration; 15 w/v%. Food

429

Hydrocolloids, 22(5), 763-776.

430

Huang, X., Kakuda, Y., & Cui, W. (2001). Hydrocolloids in emulsions: particle size

431

distribution and interfacial activity. Food Hydrocolloids, 15(4-6), 533-542.

432

Işıklı, N. D., & Karababa, E. (2005). Rheological characterization of fenugreek paste (çemen). Journal of Food Engineering, 69, 185–190.

RI PT

433 434

Jafari, S. M., He, Y., & Bhandari, B. (2007). Production of sub-micron emulsions by

435

ultrasound and microfluidization techniques. Journal of Food Engineering, 82,

436

478–488.

Kaltsa, O., Michon, C., Yanniotis, S., & Mandala I. (2013). Ultrasonic energy input

438

influence οn the production of sub-micron o/w emulsions containing whey

439

protein and common stabilizers. Ultrasonics Sonochemistry, 20(3), 881-891

440

Kaltsa, O., Yanniotis, S., & Mandala, I. (2016). Stability properties of different

M AN U

441

SC

437

fenugreek galactomannans in method. Food Hydrocolloids, 52, 487–496.

442

Leong, T. S. H., Wooster, T. J., Kentish, S. E., & Ashokkumar, M. (2009).

443

Minimising oil droplet size using ultrasonic emulsification. Ultrasonics

444

Sonochemistry, 16, 721–727.

Mandala, I. G , Savvas, T. P, & Kostaropoulos, A. E. (2004). Xanthan and locust bean

446

gum influence on the rheology and structure of a white model-sauce. Journal of

447

Food Engineering, 64(3), 335-342.

449

McClements, D.J. (2005). Food emulsions: Principles, practice, and techniques (2nd ed.). Boca Raton: CRC Press.

EP

448

TE D

445

Metzger, T.G. (2006). Handbook of Rheology. Hannover: Vincentz Network.

451

Nikiforidis, C. V., Biliaderis, C. G., & Kiosseoglou, V. (2012). Rheological

452 453

AC C

450

characteristics and physicochemical stability of dressing-type emulsions made of oil bodies–egg yolk blends. Food Chemistry, 134(1), 64–73.

454

Ozturk, B., Argin, S., Ozilgen, M., and McClements, D. J. (2015). Formation and

455

stabilization of nanoemulsion-based vitamin E delivery systems using natural

456

biopolymers: Whey protein isolate and gum arabic. Food Chemistry, 188, 256-

457

263.

458

Palazolo, G. G., Sorgentini, D. A., & Wagner, J. R. (2005). Coalescence and

459

flocculation in o/w emulsions of native and denatured whey soy proteins in

460

comparison with soy protein isolates. Food Hydrocolloids, 19(3), 595-604.

15

ACCEPTED MANUSCRIPT Palazolo, G. G., Sorgentini, D. A, & Wagner, J. R. (2004). Emulsifying properties

462

and surface behavior of native and denatured whey soy proteins in

463

comparison with other proteins. Creaming stability of oil-in-water

464

emulsions. Journal of the American Oil Chemists' Society, 81(7), 625-632.

465

Paximada, P., Tsouko, E., Kopsahelis, N., Koutinas, A. A., & Mandala, I. (2016).

466

Bacterial cellulose as stabilizer of o/w emulsions. Food Hydrocolloids, 53, 225-

467

232.

RI PT

461

Pelegrine, D. H. G, and Gasparetto, C. A. (2005). Whey proteins solubility as

469

function of temperature and pH. LWT - Food Science and Technology, 38(1),

470

77–80.

SC

468

Porras, M., Solans, C., González, C., & Gutiérrez, J. M. (2008). Properties of water-

472

in-oil (W/O) nano-emulsions prepared by a low-energy emulsification method.

473

Colloids and Surfaces A: Physicochemical and Engineering Aspects, 324(1–

474

3), 181-188.

M AN U

471

475

Raghuram, T. C., Sharma, R. D., & Sivakumar, B. (1994). Effect of fenugreek seeds

476

on intravenous glucose disposition in non-insulin dependent diabetic patients.

477

Phytotherapy Research, 8, 83–86.

Rao, P. U., Sesikeran, B., Rao, P. S., Naidu, A.N., Rao, V. V., &. Ramacjandran, E. P.

479

(1996). Short-term nutritional and safety evaluation of fenugreek. Nutrition

480

Research, 16, 1495–1505.

TE D

478

Richardson, P. H., Clark, A. H., Russell, A. L., Aymard, P., & Norton, I. T. (1999).

482

Galactomannan gelation: A thermal and rheological investigation analysed

483

using the cascade model. Macromolecules, 32, 1519–1527.

485 486 487 488 489

Ross-Murphy S.B. (1984). Rheological methods. In H.W.-S. Chan (Ed.), Biophysical

AC C

484

EP

481

Methods in Food Research. (pp. 137-139). Oxford: Blackwell.

Sonneville-Aubrun, O., Simonnet, J.T., & L’Alloret, F. (2004). Nanoemulsions: a new vehicle for skincare products. Advances in Colloid Interface, 108,. 145–149.

Steffe, J.F. (1996). Rheological Methods in Food Process Engineering. (2nd ed.). East Lansing: Freeman Press.

490

Sun, C., & Gunasekaran, S. (2009). Effects of protein concentration and oil-phase

491

volume fraction on the stability and rheology of menhaden oil-in-water

492

emulsions stabilized by whey protein isolate with xanthan gum. Food

493

Hydrocolloids, 23(1), 165-174.

16

ACCEPTED MANUSCRIPT Tabibiazar, M., Davaran, S., Hashemi, M., Homayonirad, A., Rasoulzadeh, F.,

495

Hamishehkar, H., & Mohammadifar, M. A. (2015). Design and fabrication of a

496

food-grade albumin-stabilized nanoemulsion. Food Hydrocolloids, 44, 220-228.

497

Tadros, T., Izquierdo, P., Esquena, J., & Solans C. (2004). Formation and stability of

498

nano-emulsions. Advances in Colloid and Interface Science, 108–109, 303–318.

499

Teo, A., Goh, K.K.T., Wen, J., Oey, I., Ko, S., Kwak, H.-S., & Lee, S.J. (2016).

500

Physicochemical properties of whey protein, lactoferrin and Tween 20

501

stabilised nanoemulsions:

502

Chemistry, 197(A), 297-306.

504

of

temperature,

pH

and

salt.

Food

Tiwari, A., Hihara, L., & Rawlins, J. (2014). Intelligent coatings for corrosion control. (1st ed.). Boston: Butterworth-Heinemann.

SC

503

Effect

RI PT

494

Tiwari, B. K., Muthukumarappan, K., O'Donnell, C. P. & Cullen, P. J. (2010).

506

Rheological Properties of Sonicated Guar, Xanthan and Pectin Dispersions.

507

International Journal of Food Properties, 13(2), 223-233.

M AN U

505

508

Wang Q. & Cui S.W. (2005). Understanding the Physical Properties of Food

509

Polysaccharides. In S. W. Cui (Ed.), Food Carbohydrates.Chemical, Physical

510

Properties and Applications, pp. 161-195.New York: CRC Press.

512

WHO.

Global

Strategy on

Diet,

Physical

Activity and

Health.

(2015).

TE D

511

http://www.who.int/dietphysicalactivity/diet/en/ Accessed 22/03/2016. Wooster, T. J., Golding, M., & Sanguansri, P. (2008). Impact of oil type on

514

nanoemulsion formation and Ostwald ripening stability. Langmuir, 24(22),

515

12758-12765.

EP

513

Wu, Y., Cui, W., Eskin, N. A. M., & Goff, H. D. (2009). An investigation of four

517

commercial galactomannans on their emulsion and rheological properties. Food

518

AC C

516

Research International, 42(8), 1141-1146.

519

Wulff-Pérez, M., Torcello-Gómez, A. Gálvez-Ruíz, M. J., & Martín-Rodríguez, A.

520

(2009). Stability of emulsions for parenteral feeding: Preparation and

521 522 523

characterization of o/w nanoemulsions with natural oils and Pluronic f68 as surfactant. Food Hydrocolloids, 2(4), 1096-1102.

Youssef, M. K., Wang, Q., Cui, S.W., & Barbut, S. (2009). Purification and partial

524

physicochemical

characteristics

525

Hydrocolloids, 23(8), 2049-2053.

of

protein

free fenugreek gums.

Food

17

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Zeeb, B., Herz, E., McClements, D. J., & Weiss, J. (2015). Reprint of: Impact of

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alcohols on the formation and stability of protein-stabilized nanoemulsions.

528

Journal of Colloid and Interface Science, 449, 13-20. Zinoviadou, K. G., Scholten, E., Moschakis, T., & Biliaderis, C. G. (2012). Properties

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of emulsions stabilised by sodium caseinate–chitosan complexes. International

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Dairy Journal, 26(1), 94-101.

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ACCEPTED MANUSCRIPT Caption of Figures

534

Figure 1. Volume weighted size distributions of primary emulsions as affected by oil

535

concentration.

536

Figure 2. Droplet size (a) and polydispersity index (PDI) (b) of emulsions as a

537

function of sonication time and oil concentration. Diamonds correspond to 5 %,

538

squares 10 % and triangles to 20 % oil.

539

Figure 3. Stability of coarse emulsions containing as affected by oil (diamonds, 2.5

540

%wt, squares 5 %wt and triangles 10 %wt) and FGF concentration (open symbols: 0.5

541

%wt, closed symbols: 0.75 %wt and “x”, all other emulsions containing 1 %wt).

542

Different letters indicate significant differences among samples (p<0.05).

543

Figure 4. Effect of oil content on storage (G’, closed symbols) and loss modulus (G”,

544

open symbols) of emulsions containing a) 2.5 %wt (diamonds), b) 5 %wt (squares)

545

and c) 10 %wt (triangles) olive oil. Black symbols indicate coarse emulsions and red

546

ones nanoemulsions. Black circles correspond to loss tangent (tanδ) of course

547

emulsions and red circles of nanoemulsions

548

Figure 5. Stability of emulsions containing 2.5 (diamonds), 5 (squares) and 10 %wt

549

oil (triangles): a) Coarse emulsions, b) Nanoemulsions and c) Back scattering

550

variation (dBS) after 10 days of storage (5 oC).a-d Different letters indicate significant

551

differences among samples (p<0.05).

552

Figure 6. Back scattering profiles of coarse and nano- emulsions containing 1 %wt

553

FGF during storage (5 oC).

554

Figure 7. Stability of coarse and nano- emulsions containing 1 %wt FGF after 5

555

months of storage (5 oC).

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ACCEPTED MANUSCRIPT Caption of Tables

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Table 1. Droplet size (volume median diameter (D50) and z-average diameter) and

558

polydispersity (Span and PDI) of primary emulsions as affected by olive oil

559

concentration and emulsification method applied.

560

Table 2. Estimated consistency (k) and flow behavior (n) values of coarse and nano-

561

emulsions

various

amounts

of

olive

oil

and

1

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FGF.

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Figure 1 7

5

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6

5%

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10000

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a ab

c

0.4

10%

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a

ab

a

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12

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a 100

14

20%

a

c

a

ab

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d

a

a

c b

bc

0.6

10%

ab a

PDI (-)

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c

b

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Figure 2

z-average diameter (nm)

565

a

0.0 0

2

4 6 8 10 Sonication time (min)

12

14

22

ACCEPTED MANUSCRIPT 566

Figure 3 100

80

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b

40

20

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c

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567

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Figure 4

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100

G', G" (Pa)

G', G" (Pa)

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10

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100

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0.1 1 10 Angular frequency (rad/s)

100

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570

24

ACCEPTED MANUSCRIPT

Figure 5 100

80

Back scattering (%)

60

40

60

12 Nanoemulsions 10

40

2

4

6 8 Storage days

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10

12

8 c

6 bc

4

20

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dBS (%)

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2.5

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573

25

ACCEPTED MANUSCRIPT

Figure 6

Oil content (%wt)

10

80%

80%

60%

60%

60%

40%

40%

40%

20%

20%

20%

0mm

0%

50mm

0d

EP

Back Scattering 100% 80% 60% 40% 20% 0% 0mm

150d

50mm

0mm

0% 50mm

150d

0mm

0d

Back Scattering 100%

152d

0d

Back Scattering

80%

80%

60%

60%

40%

40%

20%

20%

0mm

50mm

100%

0%

0% 150d

0d

Back Scattering 100%

80%

0%

Nano-emulsions

Back Scattering 100% BS variation

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26

ACCEPTED MANUSCRIPT Figure 7 2.5 % wt

5 % wt

10 % wt

Coarse emulsion Nanoemulsion

Coarse emulsion Nanoemulsion

Coarse emulsion Nanoemulsion

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577 578

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ACCEPTED MANUSCRIPT 580

Table 1 Oil concentration (%wt) 5

10

20

D50 (µm)

9.73a ± 3.3

9.48a ± 4.09

13.76a ± 3.96

Span (-)

1.81a ± 0.23

2.68a ± 1.08

1.46a ± 0.54

207.3a ± 1.0

288.7b ± 17.6

267.3b ± 8.5

0.219a ± 0.006

0.381b ± 0.021

0.386b ± 0.009

Nano- emulsions Z-average diameter (nm)

581

a-b

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PDI (-)

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Coarse emulsions

Different superscripts per parameter indicate significant differences among samples (p<0.05).

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Table 2 k (Pa-sn)

n (-)

2.5

7.40a ±0.45

0.352d ±0.006

5

8.31b ± 0.32

0.343d ± 0.011

10

11.72c ±1.05

0.333c ±0.003

2.5

8.59b ±0.71

5

9.09b ±0.35

10

15.69d ±0.24

Oil content (%wt)

584

a-d

585

2

0.324bc ±0.006 0.320b ±0.001 0.288a ±0.012

SC

Nanoemulsions

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Coarse emulsions

Different superscripts indicate significant differences among samples (p<0.05).

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R values range between 0.987-0.994.

29

ACCEPTED MANUSCRIPT Highlights •

Low oil content macro and nanoemulsion models were prepared containing fenugreek gum



Droplet size decrease enhanced the rheological properties of nanoemulsions



Nanosized droplets are mostly appreciated for emulsions with the lowest oil

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content (2.5 %)