PaPer 468 Ital. J. Food Sci., vol. 27 - 2015 - Keywords: active packaging, antioxidant, biodegradable polymer, poly (butylene adipate co-terephthalate), thermoplastic starch - Development of an active bioDegraDable film containing tocopherol anD avocaDo peel extract J.c.f. fiDelis1, a.r.g. monteiro1*, m.r.s. scapim1, c.c.f. monteiro2, D.r. morais3, t. claus3, J.v. visentainer3 and f. Yamashita4 1State University of Maringa, Department of Food Engineering, Av Colombo, 5790 bloco 13 CEP 87030-900 Maringá, PR, Brazil 2State University of Maringa, Department of Design. Rua Dom Pedro II, 598, CEP 87200-055, Cianorte, PR, Brazil 3State University of Maringa, Department of Chemistry Av Colombo, 5790 bloco 13 CEP 87030-900 Maringá, PR, Brazil 4State University of Londrina, Department of Food Science. Rod. Celso Garcia Cid, Km 380, P.O.Box 10.011 CEP 86057-970- Londrina, PR, Brazil *Corresponding author: argmonteiro@uem.br AbstrAct thermoplastic starch (tPs) films and poly(butylene adipate co-terephthalate) (PbAt) (60/40 m/m) containing tOcO-70 (tocopherol/soybean oil 70/30 m/m) and avocado peel extract (ExA) were produced using blown film extrusion. the formulations of the 5 films (Fc/F1/F2/F3 and F4) were established through mixture design with constraints maintaining constant PbAt and tPs proportion, and varying the antioxidant concentrations. Adding antioxidants reduced the water vapour permeability (Kw) of the films, with formulation F2 presenting higher decrease in relation to Fc, 77.8%. the presence of ExA improved the mechanical properties of the films. the produc- tion of the films was determined to be viable after they presented good processability in a pilot extruder, as well as mechanical properties appropriate to production and utilization in industry. the presence of ExA and tOcO 70 provided the films with antioxidant activity; their application as active packaging requires further studies. http://argmonteiro%40uem.br Ital. J. Food Sci., vol. 27 - 2015 469 1. IntrOductIOn the fundamental function of food packaging is to delay the deterioration of the product in all physical, chemical, microbiological, sensory and nutritional aspects, ensuring the quality of the product until it is consumed (rEstuccIA et al., 2010). the oxidation of food sensitive substanc- es form hydroperoxides that decompose into al- dehydes, ketones, alcohols, acids, esters or hy- drocarbons, altering the color, texture, smell and taste, as well as reducing the shelf life (Mc- cLEMEnts and dEcKEr, 2000). Active packag- ing interacts with the food to increase its shelf life, and materials containing antioxidants are a promising alternatives used to develop new ac- tive packaging (bYun et al., 2010; PErEIrA dE AbrEu et al., 2012; PErEIrA et al., 2013). tocopherol is a liposoluble antioxidant that is widely applied in food as a primary antioxi- dant. tocopherol is highly stable when applied in films of polyethylene and polypropylene, even under severe extrusion conditions. (AL-MALAI- KA et al., 1999; AL-MALAIKA et al, 2001). recent studies regarding films elaborated from biode- gradable polymers with tocopherol have gener- ated positive results concerning antioxidant mi- gration when applied to food (bYun et al., 2010; GrAcIAnO-VErduGO et al., 2010; LÓPEZ et al., 2011; HWAnG et al., 2013; MArtIns et al., 2012). several active principles originating from plants have been applied as anti-oxidants (dI- cAstILHO et al., 2011; PErEIrA dE AbrEu et al., 2012; rubILAr et al., 2013), such as the avoca- do; the avocado is an oleaginous fruit native of tropical America (Mexico) that is rich in phenol derivatives. Only 69% of this fruit are edible, the remaining is constituted of stone and skin. the use of the skin to extract antioxidants may add value to the residue and minimize environ- mental issues. (WAnG et al., 2010) studied the antioxidant capacity of peels and seeds in various avocado species and concluded that these residues also contain large quantities of phenol compounds, among other antioxidants. rOdrÍGuEZ-cArPE- nA et al. (2011) used avocado peel and seed ex- tracts to inhibit lipid oxidation in meat products. Active packaging can be manufactured using ecofriendly materials, such as biodegradable polymers. starch has been used as an alterna- tive to produce biodegradable films, but the ma- terials present a low mechanical strength and are hygroscopic (MALI et al, 2005; rEn et al., 2009; scAPIM, 2009). the conversion of starch into thermoplastic starch (tPs) involves heat- ing and shearing with a plasticizer agent, such as glycerol. the materials produced from blends of ther- moplastic starch and other biodegradable poly- mers may be used to develop low-cost biodegrad- able packaging with better mechanical and bar- rier properties (brAndELErO et al., 2012; OLIVA- tO et al., 2011; rEn et al., 2009; scAPIM, 2009). Poly(butylene adipate co-terephthalate) (PbAt) is a biodegradable polyester with mechanical prop- erties similar to the those of polyethylene films with resistance to fat and humidity and temper- ature variations (bAsF, 2013). Previous stud- ies have studied biodegradable materials pro- duced using blends of thermoplastic starch and PbAt (brAndELErO et al., 2012; OLIVAtO et al., 2011; rEn et al., 2009; scAPIM, 2009). the ob- jective of this study was to characterize and as- sess the mechanical and structural properties of biodegradable films composed of thermoplastic starch, PbAt and antioxidants (tocopherol and bark extract avocado) seeking better interaction among these compounds in order to suggest fur- ther studies on the application of these films in active packaging. 2. MAtErIALs And MEtHOds 2.1. Materials the film production utilized native cassava starch (Indemil com. Ind. Ltda, brasil), glycerol (synth P.A, brasil), poly(butylene adipate co-tere- phthalate) (Ecoflex®, bAsF chemical company, brasil) and tOcO-70 (tocopherols solution/soy- bean oils 70/30 m/m) (danisco, brasil). the av- ocado fruits (Persea americana Mill) were utilized at an intermediate maturity stage as moderate- ly tender and green peel derived from são Pau- lo state after being purchased in Maringá Pr. 2.2. Production and characterization of avocado peel extract the peels were separated from fruits, cut into 2-cm squares, dried in a greenhouse at 60°c for 24 h, ground in an analytical mil and sieved. the extracts were prepared according to sAn- tOs et al. (2011) with some modifications. the previously dried and ground peels were soaked in ethanol at 95% v/v (proportion 1/10 m/v) with stirring for 4 h. the solution was vacuum filtered and concentrated via rotary evaporation at 40°c. the dry extracts (ExA) were stored in amber flasks at -18°c, under nitrogen atmos- phere (n 2 ) until the analyses. the compounds in ExA were characterized and quantified using ultra-High Performance Liquid chromatography coupled to Electro- spray Ionization Mass spectrometry in nega- tive ion mode (uPLc-EsI(-)-Ms) (Acquity uPLc- tQd, Waters, EuA). Approximately 10.0 mg of dry ExA and 1.0 mg of standard in HPLc grade methanol were injected (3 µL) into uPLc-EsI(- )-Ms equipped with an Acquity column uPLc bEH c18 (2,1 x 50 mm) with 1.7 µm particles at 30°c. A gradient elution at 0.20 mL/min with solvent A (formic acid at 0.1%, in Milli-Q water) and b (methanol) was used with the following 470 Ital. J. Food Sci., vol. 27 - 2015 method: from 95% of A and 5% of b to 100% b in 8.00 min, and the system was stabilized at 10.00 min. the spectra were acquired under the following conditions: capillary and cone stress of -3000 V and -30 V, respectively, with a source temperature of 150°c and a temperature of de- solvation of 350°c. 2.3. Preparation of the biodegradable films We produced 5 different types of biodegrada- ble films, where the film control (Fc) was used as a reference and was composed of starch/ glycerol/PbAt the proportions 42/18/40 (w/w/w). In the other films concentrations tOcO-70 and ExA were determined using a mixture design with constraints (table 1), were proportion of starch/glycerol/PbAt was main- tained at 42/18/40 (m/m/m). the results were analyzed using the stAtIstIcA 7.0 software (statsoft, EuA). the films were processed in the technolo- gy Laboratory of Food science and technolo- gy department of state university of Londri- na (uEL - brazil). the antioxidant compounds were mixed with glycerol. Initially, the pellets were produced in a pilot twin screw extrud- er (bGM, model d-20, brazil) equipped with screws measuring 20 mm in diameter and 680 mm in length. the speed of the screws was set at 100 rpm, and the temperature profile in all five heating zones was 90/120/120/120/120°c. the film was produced in a pilot single-screw extruder (bGM, model EL-25, brazil) equipped with a screw measuring 250 mm in diameter. the speed was maintained at 35 rpm, and the temperature profile in all four heating zones and in the matrix for balloon formation was 90/120/120/130/130°c. 2.4. Biodegradable Films 2.4.1. Thickness (δ) and density (ρ) the thickness (δ) of the films was determined using a digital micrometer (0.001 mm resolution, Mitutoyo, Japan). twelve random points on each film formulation were assessed. For the densi- ty (ρ), the average masses of 10 square samples (25 mm x 25 mm) of film were calculated after being conditioned in desiccators with anhydrous calcium chloride for 20 days. 2.4.2. Water vapour permeability (KW) the films were conditioned at 64±2% rH and 25±2°c for 72 h. the film samples were fixed to a circular opening of a permeation cell (area of 60 mm2) with silicone grease. the interior of the cell was filled with magnesium chloride saturated solution (33% rH) and was stored at 25±2°c in a desiccator that contained sodium nitrate saturated solution (64% rH) to main- tain a 31% rH gradient across the film. the sample were weighed every 3 h during 72 h of testing time. the changes in the weight of the cell or mass gain (m) were plotted as a function of time (t). the slope of each line was calculat- ed using linear regression, and the water va- pour permeation ratio (Kwr) was obtained us- ing Equation (1): Kwr = (m/t).(1/A) where m/t is the angular coefficient of the curve and A is the sample permeation area. the Kw was calculated as Equation (2): Kw= Kwr.st/sp(rH 1 -rH 2 ) where st is the mean sample thickness (m), sp is the water vapour saturation pressure at the assay temperature (Pa), rH1 is the relative hu- midity of the desiccator and rH2 is the relative humidity in the interior of the permeation cell. the tests were conducted in triplicate. 2.4.3. Sorption isotherms the sorption isotherms of the films were deter- mined according to the methodology described by scAPIM (2009) using the following relative humidities at 25°c: 11.3, 33, 43.2, 52.9, 64.5, 75.3, 84.3 and 90.2%. the isotherms were modeled according to the Guggenheim-Anderson-de boer (GAb) model (Equation 3) using the Quasi-newton method in statistica 7.0. X w = where X W (g of water/g of dry matter) is the rel- ative humidity of balance, m 0 is the water con- tent in the monolayer (g of water/g of solids), a w is the water activity, and c and K are constants from the GAb model that represent the sorp- tion heat in the first layer and sorption heat of the multilayer. table 1 - Formulation of biodegradable films according to mixture design and the constraints. Films component (m/m/m) Film formulation Starch + Glycerol ExA TOCO-70 + PBAT x 1 x 2 x 3 FC 1.000 - - F1 0.994 0.006 - F2 0.992 - 0.008 F3 0.986 0.006 0.008 F4 0.993 0.003 0.004 ° x 1 + x 2 + x 3 = 1 Ital. J. Food Sci., vol. 27 - 2015 471 2.4.4. Determination of solubility (β) and diffu- sion (Dw) coefficients the method used to calculate the solubility coef- ficient (β) was proposed by LArOtOndA et al. (2005) using the first order derivative of the GAb. this model is correlated with the water activity and water vapor pressure (P s ) at 25°c according to Equation 4. where β(g/g.Pa)is the solubility coefficient, c, K, and m 0 are the GAb model parameters and Ps (Pa) is the water vapor pressure at 25°c. the a w was the average of the relative humidity gradi- ent used in Kw(g/m.Pa.day) (item 2.4.2). the coefficient of water vapor diffusion (dw) was calculated according to Equation 5 using the values of β and Kw, as determined in section 2.4.2, where ρ is the film density: PVA dw= Kw/ρ.β ρ.β 2.4.5. Mechanical properties the mechanical properties (ultimate tensile strength and elongation at rupture) were assessed according to AstM d 882-91 (AstM, 1996) us- ing a texturometer (stable Micro systems, mod- el tA.tX2i, England) with a 30-mm distance be- tween the clutches and a traction speed of 500 mm/min. the samples were 80 mm long and 6 mm wide; they were conditioned under 64.5% rH at 25°c for seven days before the analyses. For each formulation, 10 repetitions were performed. 2.4.6 Microstructures analysis the analyses were conducted using scanning electron microscope (shimadzu, model ss-550n, Japan) based on the methodology descripted by scAPIM (2009). the samples were immersed in liquid nitrogen and fractured with the aid of tweezers before being conditioned in a desicca- tor with calcium chloride to remove any humid- ity for three weeks. the samples were subse- quently overlaid with two golden covers through a metallizer (shimadzu Ic-50 Ion coater, Japan). After preparation, the samples were visualized through electronic scanning microscope to have its fracture area surface analyzed. 2.4.7. Antioxidant capacity of avocado peel ex- tract and films the analyses were carried out according to the method described by sErPEn et al., (2012). sample of 10.0 mg of avocado peel extract and each film formulation was reacted with 5 mL of 2.2-diphenyl-1- picrilhidrazil (dPPH•) in etha- nol/water (50/50, v/v) over 1, 2, 3 and 4 hours under magnetic stirring and protection from light. Afterward, the blend was centrifuged for 1 min at 300-400 rpm (8 G) and the absorb- ance of the supernatant was measured through a spectrophotometer (thermoscientific, mod- el Genesys 10 uV, usA) at 525 nm. Methanolic solutions of (±)-6-hydroxy-2,5,7,8-tetramethyl- cromano-2-carboxylic acid (trolox) in different concentrations were used to obtain the calibra- tion curve for 5 mL (y = 29.448x + 5.4989, r² > 0.99) with the oxidant capacity expressed in µmol of trolox equivalents (Et)/g for each film formulation. 3. rEsuLts And dIscussIOn 3.1. Antioxidant compounds and antioxidant capacity of avocado peel extract. the following antioxidant compounds were identified and measured in the avocado peel ex- tract: citric acid (133±10 µg/100 g extract), cat- echin hydrate (82±3 µg/100 g extract), malic acid (75±2 µg/100 g extract), epicatechin (62±3 µg/100 g extract) and tartaric acid (11.8±0.1 µg/100 g extract). Prior studies have revealed positive results for active packaging developed using plant extracts with compositions similar to ExA (dIcAstILHO et al., 2011; LÓPEZ et al., 2011; PErEIrA dE AbrEu et al., 2012). the antioxidant capacities of ExA and tOcO- 70 were 188±8 mmol Et/g o and 162±8mmol Et/g, respectively. WAnG et al. (2010) assessed different avocado species and concluded that both the seed and peel contain copious quan- tities of phenolic compounds and high antiox- idant capacities. the authors found variations from 38 to 189.8 µmol of Et/g in peels from dif- ferent species; the peel contributes 38% of the antioxidant capacity of the entire fruit. there- fore, the extraction concentrated the relevant compounds, presenting an antioxidant capaci- ty more than a thousand times higher than that reported by (WAnG et al., 2010). 3.2. Films characterization 3.2.1. Sorption isotherms the films all exhibited practically constant water sorption until 60% ur, and above 60% 472 Ital. J. Food Sci., vol. 27 - 2015 an increase in sorption occurred (Fig. 1) due to the hydrophilic nature of the starch. Accord- ing to tALJA et al. (2008), for relative humidi- ties above 60%, a replacement of starch-starch and starch-glycerol interactions with starch- water and water-glycerol interactions may oc- cur, justifying the increase in water sorption from the humidity. Adding tOcO-70 and ExA decreased the hy- drophilicity of the films under ur above 75% while formulations F2, F3, F4 and F1 present- ed reductions of 34, 21, 11 and 10%, respec- tively, concerning water sorption in the con- trol film (Fc). the formulation containing only tOcO-70 (F2) presented the lowest water sorp- tion in high relative humidities most likely due to the compatibility between the tocopherol and the soybean oil present in the compound with the starch and PbAt blend (brAndELErO et al., 2012). the GAb model was satisfactorily adjusted to the experimental isothermal data, and the de- termination coefficients (r²) varied from 0.89 to 0.99 (table 2). the constant values of sorption for the multilayer (K) are correlated with the isothermal behavior in relative humidity above 65% (Fig. 1); specifically, the higher the water sorption for the films in that area are, the high- er the K values are. 3.2.2. Water vapour permeability (KW), the coef- ficient of solubility (β), the coefficient of diffusion (Dw), the thickness (δ) and the density (ρ) the films containing antioxidants presented values for the water vapour permeability (KW), the coefficient of solubility (β) and the coeffi- cient of diffusion (dw) lower than for the con- trol film (Fc) (table 3) due to the hydrophobic nature of ExA and tOcO-70. Film F2 contained only tOcO-70 and presented the lowest hydro- phobicity, with a decrease of 77.8% in relation to the control formulation (cF). considering that the hydrophilicity of the cassava starch is a ma- jor obstacle for its application in packages, the addition of antioxidants may also contribute to improve this characteristic (AVÉrOus and bO- QuILLOn, 2004; brAndELErO et al., 2011; OLI- VAtO et al., 2011; rEn et al., 2009). According to the model generated using the mixture design (r2=0.83) that was correlated with the KW in accordance with the film com- ponents (Fig. 2), the films containing only one type of antioxidant present a reduced KW that has proven to be more effective than the blends. this behavior may be verified using the pos- itive interaction model +5.x 2 .x 3 ; specifically, when the film contains both antioxidants (x 2 = avocado extract; x 3 = tOcO-70), an increase in Kw occurs. brAndELErO et al. (2012) verified that the presence of soybean oil in the AtP/PbAt blends facilitated an interaction between the carboxyl group of the fatty acids and the PbAt, as well as film compaction promoted by the starch, which explains why formulation F2 presented the low- est β e dw coefficients. both ExA and tOcO-70 acted as compatibilizers, helping polymers in- teract and enabling the formation of a more compact structure that gives the molecules less Fig. 1 - Water sorption isotherms of biodegradable films at 25 °c. table 2 - Parameters for the GAb equation at 25°c for the biodegradable films. Parameters Films formulations for GAB model FC F1 F2 F3 F4 m 0 0.0348 0.0370 0.0394 0.0399 0.0465 C 168.52 159.57 150.49 163.361 139.76 K 1.02 0.97 0.86 0.91 0.87 R² 0.97 0.99 0.89 0.94 0.96 table 3 - Water vapour permeability (KW), thickness (δ), density (ρ), coefficient of solubility (β) and coefficient of diffusion (dw) for the biodegradable films. Formulation KW (x10-6) Δ ρ β (x10-5) Dw (x106) (g/m.Pa.day) (µm) (g/cm³) (g/g.Pa) (m²/day) FC 14.51±0.47 196±37 1.278 4.50 0.25 F1 6.75±0.46 149±19 1.475 4.12 0.11 F2 3.21±0.52 146±13 1.165 3.24 0.08 F3 6.03±0.81 130±17 1.279 3.69 0.13 F4 7.53±0.98 161±17 1.153 3.95 0.17 Ital. J. Food Sci., vol. 27 - 2015 473 space to move, as shown by the coefficient of dif- fusion. these additives also provide lower hydro- philicity, as the coefficient of solubility indicates. Possibly, such improvement in the interaction of polymers promoted by the presence of antioxi- dants contributed to the lower thickness of the films since all of the formulations with an anti- oxidant presented reduced thickness compared with the control formulation, Fc, with higher mean value, 196±37µm, and F3 with the lower mean value, 130 ±17µm. 3.2.3. Mechanical properties According to the model generated using the mixture design (r2=0.77) to correlate the me- chanical properties with the film components, the avocado extract (ExA) had a larger effect than tOcO-70 concerning the tensile strength (Fig. 3) and the elongation of the films (Fig. 4). According to OLIVAtO et al. (2012), both citric and malic acids promote reticulation (crosslinking) between thermoplastic starch Fig. 2 - Permeability of water vapour of films according to starch/PbAt, ExA and tOcO-70 contents. Fig. 3 - tensile strength of the films according to starch/ PbAt, ExA and tOcO-70 contents. Fig. 4 - Film elongation at break according to starch/PbAt, ExA and tOcO-70. and PbAt, making the films resistant toward traction. ExA contains both acids in its com- position, improving the mechanical properties of the films. 3.2.4. Antioxidant capacity of biodegradable films According to the model generated while us- ing the mixture design (r2=0.98) and correlat- ing the antioxidant capacity with the film com- ponents, the effect of the avocado peel extract (ExA) on the antioxidant capacity of the films was higher than that of tocopherol (tOcO- 70) (Fig. 5). the antioxidant capacity of the ExA extract and the tOcO-70 solution are similar, howev- er, the films containing ExA presented a higher antioxidant capacity compared to the films con- taining tOcO-70, most likely due to the higher thermal stability of the ExA. 474 Ital. J. Food Sci., vol. 27 - 2015 3.2.5. Desirability function As observed in the analyses of Kw the presence of tOcO-70 provided better result when com- pared with formulation Fc, with 77.8% decrease. However, by assessing the contour surfaces of the mechanical properties and the antioxidant capacity, it is possible to observe the occurrence of a tendency to have these characteristics im- proved when ExA is more present than tOcO- 70. the desirability function indicated that the formulation that maximizes the ultimate tensile strength, elongation at rupture, and the antiox- idant capacity while minimizes the permeability to water vapor (Kw) is a film whose composition should consist of 98.95% starch + PbAt + glyc- erol, 0.556% EXA, and 0.494% tOcO-70. After these results, further studies are going carry out with the same composition defined by desira- bility function. 3.2.6 Microstructure In the surface and film fracture micrographs neither pores, non-gelatinized granular nei- ther starch nor phase separation were detect- ed, thereby indicating good interactions be- tween the components of the films for all for- mulations. 4. cOncLusIOns the production of biodegradable films com- posed of thermoplastic starch, PbAt and anti- Fig. 5 - Antioxidant capacity of the films according to starch/ PbAt, ExA and tOcO-70 contents. oxidants (tocopherol and avocado peel extract) is viable since the films presented good pro- cessability in a pilot extruder, as well as the ap- propriate mechanical properties for industrial production and applications. the presence of ExA provided the films with antioxidant activi- ty enabling their application as active packag- ing. It is required to conduct further studies to test the application of this blend of polymers and antioxidants in biodegradable and active packaging for products rich in lipids, such as hamburguers, nuggets, peanuts and soy, to verify the occurrence of antioxidant action of the package produced using such film on the product stored. still, we suggest the develop- ment of a film with composition established through the desirability function to carry out the application tests. 5. 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