1. Introduction
Up-to-date food cycle, except from the food itself, consists of various other important tasks which are necessary such as processing, post-treatment storage, packaging, distribution, retail and consumption [
1]. The transition from linear to circular bio-based economy is of utmost importance and new technologies that transform biological feedstock and/or resources into valuable products are required. The newly designed products should be renewable and cost effective to address the depletion of natural resources, the escalating global food demand and consumption as well as the severe climate change [
2]. In recent scientific studies, the development of bio-based materials, showcasing desired properties such as sustainability, resource efficiency and low carbon dioxide emissions is reported [
3]. The global output of plastics has reached an unprecedented value of 407 MMT (million metric tons), as already reported in the literature [
4], and the pandemic COVID-19 has contributed significantly to an increase of the aforementioned value. Petroleum-based plastics utilized in the packaging sector alone are accountable of approximately 44% of the overall value, indicating their major contribution to the environmental pollution [
4]. It should be mentioned though that various inherent properties including low cost, permeability, transparency, enhanced tensile and thermal performance and the ability to be easily sterilized has enabled the wide use of plastic materials in packaging applications [
5] so far, despite the great environmental concerns the last couple of decades. The combination of carbon-carbon bonds in the polymeric materials; which does not allow their ease treatment and disintegration after the end-life cycle; with their excessive use, has led to devastating effects on the environment, causing contamination and putting in danger all living organisms. The inability to be disintegrated in reasonable time in nature from factors such as UV irradiation leads to an accumulation of plastics into the environment as well as oceans. Approximately 8 MMT of plastics end up in the oceans each year [
6]. Currently, polymeric materials comprised of polyethylene, polypropylene, and poly(ethylene terephthalate) are extensively used in food packaging. These petroleum polymers despite their low weight and the ability to be easily transformed by extrusion in variable shapes do not showcase any sustainable characteristics. Their non-biodegradable nature contributes to the environmental pollution as has already been mentioned. Furthermore, the utilization of synthetic polymeric materials in food packaging has detrimental effects due to the release of carbon dioxide and other toxicants during the incineration process. Hazardous interactions between food and recycled or reused plastics have also been reported in the literature [
7].
The development of new packaging materials targeting to food-packaging applications requires in depth analysis in terms of biodegradability. Plastics can be classified in two distinct categories strongly dependent on their components as bio- or fossil-based. In both types, biodegradable, non-biodegradable components and their combination can be found. It should be mentioned that the final chemical structure of the materials determines their biodegradability and not the initial resource used [
8]. Bioplastics are therefore categorized as bio-based and nonbiodegradable, bio-based and biodegradable, and fossil-based and biodegradable respectively. Through this classification it is easily understood that not all bioplastics can be completely biodegradable and misinterpretations due to commercial purposes often occur.
The design and development of sustainable materials which are harmonized with the current environmental concerns and exhibit high quality, is vital for both industry and consumers. The scientific community has shifted its interest towards the production of edible and biodegradable materials that adhere to food quality and safety standards [
9]. Environmental contamination related to expired dairy products including milk, cheese whey, colostrum and additional dairy industry by-products derived from the processing procedures has not gained tremendous attention yet, and only limited reports make use of these by-products to form sustainable materials [
10]. The dairy byproducts may possibly lead to high-quality products further contributing to the circular economy.
In the case of food-grade components [
11], bio-based, bio-degradable and edible products can be made. Edible packaging is rapidly evolving as a sustainable/biodegradable substitute of conventional packaging, demonstrating advantageous characteristics. The shelf life of edible membranes can be further extended using various additives such as lipids, chitosan/chitin, gums, cellulose derivatives, animal or plant-based proteins and starches. Valuable characteristics involving bio-compatibility, non-toxicity, non-polluting, gas and moisture barrier properties, render the specific materials quite important for packaging-based applications [
12]. Furthermore, edible materials can be designed using proteins, polysaccharides and oils which are derived from feedstock and active chemicals such as antioxidants and/or antimicrobial agents. These reagents are used to further enhance their final properties making them ideal candidates in food science. The dual application of the above-mentioned materials, meaning packaging and consumption, without posing any threat on the human health is important, while by tuning the thickness of the films, different applications can be induced. The appropriate choice of edible packaging materials is related to the potential content/food to be packed and the processing technique [
13].
Substances isolated from blood and glandular fluid, namely proteins, that vary in terms of molecular weight, concentration, and function are used in such applications. The use of dairy products has been extended beyond consumption and can be utilized in different fields as packaging [
14]. The expired dairy products contribute significantly to the environmental pollution but still contain a variety of proteins that either offer defense against enteropathogens or are necessary to produce new dairy products [
15]. Large amounts of proteinaceous waste, particularly whey and caseins, are produced from the dairy wastes. In bovine milk, caseins constitute approximately 80% of the total protein, concluding for it being the most abundant type of proteins [
16]. Even though almost half of the whey generated globally is recovered and used in various products, including meals, supplements, and medications huge quantities are discarded without any prior processing [
17]. Inherent characteristics of milk proteins, such as high barrier and film properties, make them ideal for biomaterial synthesis [
18]. In recent years, the preparation of protein membranes from dairy waste has attracted the interest of several scientific groups. Laetitia M. Bonnaillie et al. [
19] synthesized casein/glycerol/citric pectin membranes to study the structure and mechanical properties by adding a polysaccharide and a plasticizer. Muhammad Rehan Khan et al. [
20] highlighted the impact of active ingredients on the composition of materials and lifespan of products, considering the presence of active ingredients in the casein matrix.
In the present study chitosan, casein, glycerol and squid ink were utilized for the development of the films. Chitosan was selected because of the attractive properties such as, antimicrobial properties, biodegradability, film forming properties it has [
21]. Casein was used because of its excellent barrier and film forming properties while it is also biodegradable and non-toxic [
22]. Τhe combination of the two biopolymers was carried out both to combine the excellent properties of the materials and to overcome the brittle nature of casein membrane. The squid ink was used to impart antimicrobial and antioxidant properties to the prepared films [
23]. Casein protein was isolated from expired cow milk, by the precipitation method followed by the preparation of the relative membranes under different ratios of casein. For comparison reasons membranes of pure chitosan, chitosan and casein as well chitosan, casein and glycerol were prepared. For the final membranes according to the reagents used abbreviations of the type A
xB
yC
zD
w are used where A, B, C and D are the compounds (chitosan, casein, glycerol and squid ink respectively) and x, y, z and w the relative %wt ratios.
2. Materials and Methods
2.1. Materials
Sigma–Aldrich (St. Louis, MO, USA) was the supplier of low molecular weight chitosan (75–85% deacetylated), glycerol, acetic acid (99,8%), methanol (99,8%), ethanol (99,8%), sodium hydroxide (98%) and diethyl ether. The expired milk was supplied from the national dairy industry DODONI S.A. and the squid ink was purchased from the local market.
2.2. Extraction of Casein
For the casein extraction from expired dairy product, a beaker containing 500 ml of expired milk, was heated till to reach 55 oC. In another beaker, 500 ml of acetic acid solution (approximately 10 % v/v), was heated under the same conditions (temperature and time). The foam formed on the surface of the milk was carefully removed and the acetic acid solution was added in beaker, dropwise, to adjust the pH at approximately 4.6, which is the isoelectric point of casein. To obtain the solid, the mixture was filtrated with filter paper. The solid sample was washed several times with distilled water and was placed in another beaker which contained enough amount of ethanol able to cover the solid. Filtration took place again with filter paper to collect the solid sample. The protein sample was washed with 250 ml solution of ethanol/diethyl ether in a ratio of 1:1 and once more with 100 ml of diethyl ether. The extracted sample was left to dry at room temperature.
2.3. Membrane Synthesis
For the Chi
32Cas
32Gly
20SqInk
16 membrane synthesis, in a beaker containing 50 mL of distilled water, 2 % (w/v) of extracted casein and 0.4 % (w/v) of sodium hydroxide were added. The mixture was transferred in an ice bath and it was sonicated using and ultrasonicator (UP100H, 100W, 30kHz, Hielscher Ultrasonics) for 5 min and then allowed to stir until completely dissolved. While stirring, 2 % (w/v) of chitosan was added in the solution followed by the addition of 2 % (v/v) acetic acid. The new solution was left to stir for approximately 10 min. In the same beaker 0.5 ml of glycerol was added followed by the addition of 1 % (w/v) squid ink. The final solution contains 1 g (2 % w/v) extracted casein, 1 g (2 % w/v) chitosan, 0.63 g (1.26 % w/v) glycerol and 0.5 g (1 % w/v) squid ink. It is then transferred to polystyrene dishes to evaporate the solvent and form the hydrogel membrane. For the preparation of all other materials, pure chitosan, pure casein, Chi
50Cas
50, Chi
33Cas
67 and Chi
38Cas
38Gly
24, similar was followed by not including the additional step or steps on the aforementioned method. The abbreviations and quantities used in all the experiments are listed in
Table 1.
2.4. Attenuated Total Reflectance-Fourier Transform Infrared Spectroscopy (ATR-FTIR)
ATR-FTIR analysis was conducted with a SHIMADZU IRSpirit fourier transform infrared spectrophotometer (1, Nishinokyo Kuwabara-cho, Nakagyo-ku, Kyoto 604-8511, Japan). The ATR objective featured a ZnSe prism with a 250 μm contact area on the studied samples. The prism allowed for a penetration depth of around 2.0 µm (@1000 cm−1) and enabled measurements starting from 650 cm−1.
2.5. X-Ray Diffraction (XRD)
The samples' crystallinity was examined using a PANalytical X'PertPRO diffractometer (Enigma Business Park, Grovewood Rd, Malvern WR14 1XZ, United Kingdom) using Cu/Kα radiation. The diffractometer is equipped with an X'Celerator detector running at 40 kV voltage and 40 mA current. The membranes underwent scanning within the 2θ range from 2° to 60°.
2.6. Thermogravimetric Analysis (TGA)
TGA analysis was carried out utilizing a Setsys Evolution-Setaram (7, rue de l'Oratoire 69300 Caluire-et-Cuire France) TGA, TG-DSC, and TG-DTA analyzer. The procedure involved placing roughly 30 mg of the sample into a platinum crucible, adjusting the heating and nitrogen (N2) flow rates, and then conducting the test. Throughout all experiments, the heating rate remained constant at 10 K/min, and the N2 flow rate at 25 ml/min within the temperature range from room temperature to 700 °C.
2.7. Dynamic Mechanical Analysis (DMA)
The films’ dynamic mechanical behavior was examined using a dynamic mechanical analyzer (DMA Q800, TA Instruments, 159 Lukens Drive New Castle, DE 19720, USA) in film tension mode. To evaluate the storage modulus (E′) and the loss factor (tan δ), a temperature range from -70 °C to 120 °C, at a rate of 3 K/min, along with a frequency of 1 Hz, was applied.
2.8. Mechanical Properties
The membranes' tensile characteristics were assessed following ASTM D638 standards, employing a custom horizontal tensile testing stage manufactured by ADMET (51 Morgan Drive | Norwood, MA 02062, USA). Specimens in type V dumbbell shapes were prepared and subjected to testing at a strain rate of 0.1 min−1 until failure. Each membrane type underwent testing at least three times by making the required type V dumbbell shaped specimens. The elongation of these specimens was tracked using a linear variable differential transformer (LVDT), while the load was measured through a 44.5 N load cell (or a 445 N load cell for the pure specimens). The elongation values were transformed into engineering strain by dividing each specimen's initial effective length, while the load values were transformed into engineering stress by dividing by the specimen's cross-sectional area.
2.9. Scanning Electron Microscopy (SEM)
The surface morphology of the samples was observed using a JEOL JSM-6510 LV SEM Microscope (Ltd., Tokyo, Japan) equipped with an X-Act EDS detector from Oxford Instruments, Abingdon, Oxford shire,UK (an acceleration voltage of 20 kV was applied) with possibility to function under low vacuum conditions. Before examination, all membranes were sputter-coated with gold/palladium for 45 s to prevent sample charging during observation with SEM.
2.10. Water Vapor Transmission Rate Measurements-Water Diffusion Coefficient Calculation
The water vapor transmission rate (WVTR [g/(cm
2*s
1)]) for all the obtained membranes was calculated according to the ASTM E96/E 96M-05 method at 38 °C and 95% RH, using a custom-made apparatus. The calculated WVTR values were converted into water vapor diffusivity (D
wv) values according to theory and relative equations which are described in detail in a previous publication by our group [
24].
2.11. Oxygen Transmission Rate Measurements-Oxygen Permeability Calculation
The oxygen transmission rate (OTR) values (cc O
2/m
2/day) for each membrane was assessed following ASTM D 3985 standards (23 °C and 0% RH). An oxygen permeation analyzer (O.P.A., 8001, Systech Illinois Instruments Co., Johnsburg, IL, USA) was utilized for these measurements. Subsequently, using the derived OTR values, the oxygen permeability coefficient values (PeO
2) were calculated, employing the theoretical framework and equations described thoroughly in a prior publication by our group [
24].
Author Contributions
Synthesis experiment design, Andreas Karydis-Messinis, Christina Kyriakaki , Eleni Triantafyllou, Dimitrios Moschovas and Apostolos Avgeropoulos; characterization measurements and interpretation, Andreas Karydis-Messinis, Christina Kyriakaki , Eleni Triantafyllou , Kyriaki Tsirka , Christina Gioti, Dimitris Gkikas, Konstantinos Nesseris , Dimitrios A. Exarchos, Spyridoula Farmaki, Aris Giannakas , Constantinos E. Salmas, Theodore E. Matikas, Dimitrios Moschovas and Apostolos Avgeropoulos; experimental data analysis and interpretation Andreas Karydis-Messinis, Christina Kyriakaki, Eleni Triantafyllou, Dimitrios Moschovas and Apostolos Avgeropoulos; overall evaluation of this work, Apostolos Avgeropoulos, Andreas Karydis-Messinis and Dimitrios Moschovas ; TGA, Christina Gioti; Tensile measurements, Kyriaki Tsirka ATR-FTIR Theodore E. Matikas, Dimitrios A. Exarchos and Spyridoula Farmaki SEM measurements, Dimitrios Moschovas and Apostolos Avgeropoulos ; WVTR and OTR Aris Giannakas and Constantinos E. Salmas.
Figure 1.
FTIR spectra of (a) pure casein, (b) pure chitosan, (c) Ch50Cas50, (d) Ch33s67, (e) Chi38Cas38Gly24 and (f) Chi32Cas32Gly20SqInk16.
Figure 1.
FTIR spectra of (a) pure casein, (b) pure chitosan, (c) Ch50Cas50, (d) Ch33s67, (e) Chi38Cas38Gly24 and (f) Chi32Cas32Gly20SqInk16.
Figure 2.
XRD diffractograms of (a) pure casein, (b) pure chitosan, (c) Ch50Cas50, (d) Ch33Cas67, Chi38Cas38Gly24 and (f) Chi32Cas32Gly20SqInk16.
Figure 2.
XRD diffractograms of (a) pure casein, (b) pure chitosan, (c) Ch50Cas50, (d) Ch33Cas67, Chi38Cas38Gly24 and (f) Chi32Cas32Gly20SqInk16.
Figure 3.
TGA thermograms of (a) pure chitosan, (b) Ch50Cas50, (c) Ch33Cas67, (d) Chi38Cas38Gly24 and Chi32Cas32Gly20SqInk16.
Figure 3.
TGA thermograms of (a) pure chitosan, (b) Ch50Cas50, (c) Ch33Cas67, (d) Chi38Cas38Gly24 and Chi32Cas32Gly20SqInk16.
Figure 4.
Storage modulus plots of (a) pure chitosan, (b) Ch50Cas50, (c) Ch33Cas67, (d) Chi38Cas38Gly24 and Chi32Cas32Gly20SqInk16.
Figure 4.
Storage modulus plots of (a) pure chitosan, (b) Ch50Cas50, (c) Ch33Cas67, (d) Chi38Cas38Gly24 and Chi32Cas32Gly20SqInk16.
Figure 5.
Tan delta plots of (a) pure chitosan, (b) Ch50Cas50, (c) Ch33Cas67, (d) Chi38Cas38Gly24 and (e) Chi32Cas32Gly20SqInk16.
Figure 5.
Tan delta plots of (a) pure chitosan, (b) Ch50Cas50, (c) Ch33Cas67, (d) Chi38Cas38Gly24 and (e) Chi32Cas32Gly20SqInk16.
Figure 6.
Indicative stress vs strain plots of (a) pure chitosan, (b) Ch50Cas50, (c) Ch33Cas67, (d) Chi38Cas38Gly24 and Chi32Cas32Gly20SqInk16.
Figure 6.
Indicative stress vs strain plots of (a) pure chitosan, (b) Ch50Cas50, (c) Ch33Cas67, (d) Chi38Cas38Gly24 and Chi32Cas32Gly20SqInk16.
Figure 7.
SEM images of (a) pure casein, (b) pure chitosan, (c) Ch50Cas50, (d) Chi33Cas67, (e) Chi38Cas38Gly24 and (f) Chi32Cas32Gly20SqInk16.
Figure 7.
SEM images of (a) pure casein, (b) pure chitosan, (c) Ch50Cas50, (d) Chi33Cas67, (e) Chi38Cas38Gly24 and (f) Chi32Cas32Gly20SqInk16.
Table 1.
Abbreviations and compositions of the prepared hydrogel membranes.
Table 1.
Abbreviations and compositions of the prepared hydrogel membranes.
Sample code |
Chitosan (w/v %) |
Casein (w/v %) |
Glycerol (w/v %) |
Squid Ink (w/v %) |
Chi32Cas32Gly20SqInk16 (%wt:32/32/20/16)
|
2 |
2 |
1.26 |
1 |
Chi38Cas38Gly24 (%wt:38/38/24)
|
2 |
2 |
1.26 |
- |
Chi33Cas67 (%wt:33/67)
|
2 |
4 |
- |
- |
Ch50Cas50 (%wt:50/50)
|
2 |
2 |
- |
- |
Pure Chitosan (%wt:100)
|
2 |
- |
- |
- |
Pure Casein (powder)
|
- |
100 |
- |
- |
Table 2.
Mechanical properties of the prepared hydrogel membranes.
Table 2.
Mechanical properties of the prepared hydrogel membranes.
Specimen |
Stress (MPa) |
Strain (%) |
% change in stress* |
% change in strain* |
Pure Chitosan Reference system
|
102.82 ± 6.97 |
6.77 ± 3.01 |
Reference system |
Chi50Cas50 |
51.60 ± 2.00 |
7.66 ± 1.70 |
-49.82 |
+13.15 |
Chi33Cas67 |
36.84 ± 2.02 |
2.61 ± 0.07 |
-64.17 |
-61.45 |
Chi38Cas38Gly24 |
15.36 ± 0.63 |
38.42 ± 0.22 |
-85.06 |
+467.50 |
Chi32Cas32Gly20SqInk16 |
12.18 ± 1.85 |
23.74 ± 3.56 |
-88.15 |
+250.66 |
Table 3.
Water vapor transmission rate (WVTR) and water diffusivity (D) of the hydrogel membranes Pure Chitosan (a), Ch50Cas50 (b), Ch33s67 (c), Chi38Cas38Gly24 (d) and Chi32Cas32Gly20SqInk16 (e).
Table 3.
Water vapor transmission rate (WVTR) and water diffusivity (D) of the hydrogel membranes Pure Chitosan (a), Ch50Cas50 (b), Ch33s67 (c), Chi38Cas38Gly24 (d) and Chi32Cas32Gly20SqInk16 (e).
Samples |
WVTR [gr/(cm2*s)] |
Dwv (cm2/s) |
Pure Chitosan |
7.69367E-07(6.48778E-08) |
1.10E-04(1.98E-05) |
Ch50Cas50 |
9.55637E-07(4.27094E-07) |
3.33E-04(0.79E-04) |
Chi33Cas67 |
7.79506E-07(5.03817E-07) |
5.16E-04(1.04E-04) |
Chi38Cas38Gly24 |
1.92141E-06(3.3557E-07) |
8.20E-04(1.69E-04) |
Chi32Cas32Gly20SqInk16 |
1.53178E-06(3.217612E-07) |
8.51E-04(8.76E-05) |