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 CHEMICAL ENGINEERING TRANSACTIONS  
 

VOL. 43, 2015 

A publication of 

The Italian Association 
of Chemical Engineering 
Online at www.aidic.it/cet 

Chief Editors: Sauro Pierucci, Jiří J. Klemeš 
Copyright © 2015, AIDIC Servizi S.r.l., 
ISBN 978-88-95608-34-1; ISSN 2283-9216                                                                               

 

Effect of Rosemary Oil and an Emulsion of Essential Oils on 
Structure and Physical Properties of Chitosan Film 

Elena Torrieri*,a, Silvana Cavellaa, Paolo Masia,b 
a Food and Agricultural Department -University of Naples Federico II –Naples, Italy  
bCAISIAL-Centre of Food Innovation and Development in the Food Industry University of Naples Federico II – Naples, Italy 
elena.torrieri@unina.it 
 
The objective of this work was to study the effect of Rosemary oil (Resemary Officinalis) and an emulsion at 
68 % of EOs (EA3) on chitosan (CH) film forming dispersion (FFD) and CH films properties. FFD were 
characterized in terms of rheological properties and particle size distribution. In order to study the impact of 
EOs into the CH matrix, microstructure (SEM), film thickness, equilibrium moisture content (EMC) and water 
vapour permeability (WVP) of the dried film were evaluated. Results showed that oil concentration did not 
affect particle size distribution whereas the type of EO have an effect on the particle size dimension. The 
rheological properties of the FFD were significantly affected by the presence of the EOs. While a continuous 
structure was observed for the CH film, the presence of EOs caused discontinuities associated with the 
formation of two phases in the matrix: lipid droplets embedded in a continuous polymer network. The 
dimension of the oil droplet were higher in the film respect to the FFD. Moreover, it was showed that the 
higher the EOs content, the higher the film thickness and the lower the film moisture sorption capacity. The 
WVTR of CH film has an average value of 2.3x10-3 g m-2 s-1. The study revealed that an active chitosan film 
could be obtained by using the EA3 emulsion of EOs.  

1. Introduction 

Active packaging technologies involve interactions between the food and the packaging material to extend the 
shelf life of foods while maintaining their quality and safety. These materials are designed to deliberately 
incorporate ‘active’ components intended to be released into the food or to absorb substances from the food 
(Regulation (EC) No 1935/2004; regulation (EC) No 450/2009). Recently, given the increasing health 
concerns of consumers, current packaging research has focused on the use of natural compound, such as 
essential oil, as active agents in active edible coating materials to preserve and prolong the shelf life of food 
as meat, fish or minimally processed fruit (Azevedo et al., 2014; Bonilla et al., 2014; Fuenmayor et al., 2013; 
Higueras et al., 2014; Raybaudi-Massilia et al., 2008; Valencia-Chamorro et al., 2009). Among the most 
common oils that have been proven antimicrobial properties against spoilage microorganisms the main are 
Cilantro oil, Coriander oil, Oregano oil, Rosemary oil, Sage oil, Clove (bud) oil and Thyme oil (Burt, 2004). 
Chitosan has been studied extensively in the food industry due to its excellent film-forming, antimicrobial, 
physical and mechanical properties (Elsabee and Abdou, 2013) and an active antimicrobial film based on 
chitosan has been recently developed (Lago et al., 2014). The functional properties of edible film depend on 
the type of constituents and also on their interaction (Giancone et al., 2008, 2011). According to the 
application of EOs, it is also important to evaluate their effects on the physical and structural properties of the 
resulting film (Sánchez-González et al., 2010). About the role of EOs on film functional properties the results 
reported on literature are still contradictory, in particular regarding the effect of the oil on the water barrier 
properties of the film. However, it has been reported that a major role can play the type of polysaccharide or 
the type of oil added and their interaction on the effective structure of the film and thus on the diffusivity of the 
water. In fact, if by adding the oil the matrix results more open, an higher diffusion of water in the matrix can 
be expected and thus a negative impact on the water barrier properties expected (Perone et al., 2014). The 

                                

 
 

 

 
   

                                                  
DOI: 10.3303/CET1543005 

 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 

Please cite this article as: Torrieri E., Cavella S., Masi P., 2015, Effect of rosemary oil and an emulsion of eos oils on structure and physical 
properties of chitosan film, Chemical Engineering Transactions, 43, 25-30  DOI: 10.3303/CET1543005

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composition of the film and the interaction between the constituent (polysaccharides, oil, emulsifier) began a 
critical aspect to design active film with desired properties (Perone et al., 2014).  In this work the relation 
between structure and properties of chitosan film obtained with rosemary oil and an emulsion of EOs at 68 % 
has been investigated.  

2. Material and methods 

2.1. Material 

Medium molecular weight Chitosan (CH MMW) with a degree of deacetylation higher than 75 – 85 %, acetic 
acid puriss. p.a., rosemary essential oils (Rosemary Officinalis- REO) and Tween 80 were purchased from 
Sigma-Aldrich (Milan, Italy). EA3 Emulsion (68 % of essential oils, 0.8 % Polisorbate Tween 80, 0.8 % Myverol 
18-92, 1 % Citric Acid, 3 – 5 % CaCl2) was provided from Kerry Ingredients & Flavours (Bergamo, Italy). The 
composition of EA3 EO were: Coriander (>10%), Clove (>10%), Caraway (10%), Cardamon (>10%), White 
Thyme (5-10%), Cinnamon Distilled Fraction (Nutmeg (5-10%), Black Pepper (2-5%), Anise (2-5%), Anise 
(<2%), Sage (<2%), Oregano (<2%), Mint (<2%).  

2.2 Emulsion and Film making procedure 

CH 1% (w/v) was prepared by dispersing chitosan powder in acetic acid solution (1%, v/v) at room 
temperature for 12 hours. Then, the dispersion has been centrifuged for 4 min at 5,000 rpm to eliminate the 
solid impurity suspended. Then, essential oils emulsion (EA3) or a mixture of REO and tween - 80 (4:1) were 
added to polymer solutions to reach a final concentration of 0.5 %, 1 %, and 2 % (w/v). CH-EA3 and CH-REO-
tween-80 mixtures were emulsified for 4 min at 15,500 rpm at room temperature using a rotor-stator 
homogenizer (Ultra TurraxR, T 18, IKA, Milan, Italy) and then the solutions were de-aerated under vacuum for 
15 minutes to prevent pinhole formation. 20 ml of FFD were poured onto levelled 56.7 cm2 polystyrene Petri 
dishes and allowed to dry at 20° C and 50 % relative humidity (RH) for 48 h under air circulation. The dried 
films were peeled from the dishes and stored at 20°C and 50 % relative humidity prior to testing.  
 
2.3. Characterization of the FFD 
The particle size analysis of the FFDs was carried out by means of a laser diffractometer (Mastersizer 3000, 
Malvern Instruments, Worcestershire, UK). The samples were diluted in deionised water at 1,800 rpm until an 
obscuration rate of 10 % was obtained. Mie theory (Merkus, 2009) was applied considering a refractive index 
of 1.48 and absorption of 0.001 for essential oils emulsion samples (EA3) and 1.48 and 0.01 for REO 
samples. Three replications for formulation were made. The tenth, fiftieth and ninetieth percentile (D10, D50, 
D90), has been calculated and indicated the percentage of particles with dimension inferior to the value 
reported. 
Flow curves were obtained using of a strain controlled rheometer (RFS II, Rheometric Inc. Piscataway, NY), 
fitted with a coaxial cylinders. The viscosity versus shear rate was recorded at 25 °C. The shear rate ranged 
between 0.04-103 s-1. 

2.4. Characterization of the film 

Microstructure of film samples was examined using an LEO EVO 40 scanning electron microscope (Zeiss, 
Oberkochen, Germany). Film thickness was measured using a micrometer model HO62 with a sensitivity of ±2 
µm (Metrocontrol Srl, Casoria, NA, Italy). The moisture content of samples was determined by the gravimetric 
method. film samples were oven-dried at 105°C and accurately weighed at regular time intervals until constant 
weight was reached. Three measurements were performed for each sample. The moisture content was 
expressed as grams of water over grams of total weight (g/100g). Water vapour transmission rate  (WVTR) of 
films was evaluated by gravimetric test according to ASTM E96 (1993) by means of a Fisher or Payne 
permeability Cup (Carlo Erba, Milan, Italy) at 25 °C (RH%= 0 – 85 %).  

3.  Results  

3.1. Characterization of the FFD 

Particle size of EA3 dispersion without and with polymer showed monomodal particle size distributions, and 
CH-EA3 dispersion showed bigger particle dimension respect to EA3 emulsion. Whereas for REO essential oil 
the particles dimension are reduced once they are dispersed into chitosan. Moreover, the particle size 
distribution changes by bimodal in absence of chitosan to monomodal in its presence. The D10, D50, D90 values 
are reported in Table 1.  

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Table 1:  Particle size dimension of CH-EA3 and CH-REO   

Samples 
 (wt%) D10 (μm) D50 (μm) D90 (μm) 

CH-EA3 mean value and standard deviation 
0,5 1.92 (0.27) 3.02 (0.26) 4.87 (0.15) 

1 1.99 (0.24) 3.25 (0.48) 5.83 (1.59) 

1,5 1.82 (0.39) 2.85 (0.53) 4.55 (0.99) 

EA3 1.20 (0.01) 2.75 (0.01) 4.68 (0.01) 
CH-REO  

0,5 0.120 (0.020) 0.263 (0.053) 0.566 (0.107) 

1 0.128 (0.018) 0.295 (0.055) 0.672 (0.099) 

1,5 0.130 (0.006) 0.283 (0.012) 0.596 (0.017) 

REO  0.325 (0.022) 0.620 (0.040) 3.11   (0.711) 
 
 
The typical flow curves for CH and CH-EOs FFD are shown in Figure. 1. Flow curves showed a shear-thinning 
behaviour for all samples. At the contrary of what expected (Vargas et al., 2011; Floury et al., 2000; Otsubo et 
al., 1994), as the oil content increases the viscosity decreases. The minor effect of concentrations of REO 
samples on viscosity can be explained by the lower size of REO particles.   
 

 

Figure 1: Viscosity (Pa s) of chitosan film added with EOs as function of shear rate (s-1) 

3.2. Characterization of the film 

Characteristic SEM images of cross section of the films are shown in Figure 2. The oil droplets were uniformly 
distributed along the thickness but its sizes are not homogenous and it are bigger than in the FFD.  

 

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Figure 2: SEM micrographs of 1 % Chitosan  film at 0% EA3  (A), 0.5% oil  (B), 1.5 % oil (C), and of 1 % 
Chitosan  film at 0.5 % REO (D), 1.5 % REO oil (E). 
 
As reported in Table 2, the addition of EOs led to an increase of films thickness. The films made from CH-
REO, which showed a smaller particle sizes, were thinner than the others. 
In general, equilibrium moisture content (EMC) at aw equal to 0.5 decreased as EO was incorporated into 
chitosan-based film (Table 2). Chitosan-based films containing REO essential oil had less equilibrium moisture 
content than those containing EA3 essential oils when the same level of essential oil was present (0.5, 1 %) in 
each film. Lipid fraction caused to formation of covalent bonds between the functional groups of chitosan 
chains, leading to a decrease in the availability of hydroxyl groups and limiting polysaccharide–water 
interactions by hydrogen bonding and resulting in a decrease of moisture content value of edible films.  
Chitosan film had a WVTR value of 2.3x10-3 g m-2 s-1 (Table 2). EA3 did not have a significant effect on the 
WVTR of chitosan film. Different results have been obtained when REO has been added to chitosan film. The 
WVTR of chitosan film  increased to almost 50 % when REO has been added. The higher particle size of REO 
in CH film by disrupting the compact structure of the polymer can enhance moisture passing through the films 
and thereby increase the water vapour transmission rate values of the films. Moreover, as suggested by 
Perdones et al. (2014), possible interactions of the EO compounds with CH, as also deduced from water 
sorption data and SEM results, make the matrix more open to the transport of water molecules, despite the 
theoretical increase of the hydrophobic nature of the matrix due to the presence of lipids. Anyway, the 
differences between CH film with EA3 and REO EOs can be attributed to the different dimension of the oil 
particle in the film. Thus, the good stability of the emulsion during casting is very important for the WVTR of 
the film. 

4. Conclusions 

EOs concentration did not showed any effect on the particle size dimension in chitosan FFD.  All the 
dispersion CH-EA3 showed bigger particle dimension respect to EA3 emulsion, whereas for REO essential oil 
the particles dimension are reduced once they are dispersed into chitosan. The oil had a significant effect of 
viscosity of FFD that decreased as oil concentration increased. The structure of the CH film has been well 
observed by SEM images: A continuous structure was observed for the CH film while  the presence of EOs 
caused discontinuities associated with the formation of two phases in the matrix: lipid droplets embedded in a 
continuum polymer network. The oil droplets were uniformly distributed along the thickness but its sizes were 
not homogenous and it were bigger than in the FFD. The addition of EOs led to an increase of films thickness 
and a decreased of moisture content as the oil concentration increased. EA3 did not have a significant effect 

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on the WVTR of chitosan film, but the WVTR of chitosan film increase of almost 50 % when REO has been 
added. Chitosan is a promising biopolymer for active food packaging and chitosan-EA3 film showed better 
properties that chitosan-REO film. 
 
 
Table 2:  EMC (0.5 aw), WVTR, WVP and thickness of Chitosan film with different concentration of EO  
  

Samples 
(EOs wt %) 

EMC 
(gw/gdm) 

Thickness 
(μm) 

WVTR x 10-3  
(g m-2 s-1) 

CH-EA3 

0 22 (2) 46 (9) 2.6 (0.4) 

0,5 15 (2) 63 (5) 2.19 (0.03) 

1 13 (1) 86 (4) 2.04 (0.05) 

1,5 10 (1) 97 (9) 2.28 (0.07) 

CH-REO  

0 22 (2) 46 (9) 2.6 (0.4) 

0,5 12 (1) 53 (4) 5.6 (0.1) 

1 10 (1) 65 (5) 5.2 (0.6) 

1,5 9   (1) 69 (4) 4.3 (0.9) 
 

 

 
Acknowledgements 
This work was supported by VIVOPACK project (MISE, Industria 2015, Bando PII Made in Italy). 

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