1. Introduction
In the era of concern for the natural environment around us, finding ways to reduce the extraction of fossil fuels, from which traditional plastics are also made, is crucial. This can be supported by the production of modern biodegradable materials based on plant raw materials, which in many cases can provide an alternative to plastics [
1]. Such materials are appreciated by the public; previous research has confirmed their usefulness in many areas, e.g. packaging, disposable tableware, car upholstery components, structural boards and beams, etc. [
2,
3]. Various plant based raw materials rich in cellulose, pectin and proteins can be used to manufacture such materials, as research has confirmed [
4]. This opens up new possibilities for the application of such plant raw materials, the management of which is difficult or economically unjustifiable. Among such raw materials is apple pomace, which is a massive by-product of processing apples into juice. It is estimated that more than 20 million tonnes of apple pomace are produced worldwide each year [
5]. Factors supporting their use include large-scale production and a chemical composition that is favourable, both for the production of food and non-food raw materials [
6]. On average, apple pomace contains cellulose (7-22%), lignin (15%-20%), starch (14%-17%), pectin (4-14%), and small quantities of protein [
7,
8]. Due to its pectin, sugar and insoluble fibre content, much of it is used for the production of nutritional supplements or animal feed [
9]. Pomace can also be processed into pellets and used as fuel [
10,
11]. Apple pomace is also used as a natural organic fertiliser [
12]. The remainder of the apple pomace produced is usually composted (intensive fermentation processes take place in this raw material), which is not beneficial to the environment and, in particular, to groundwater [
13,
14]. This particularly argues for an even wider use of apple pomace, especially for non-food purposes.
One interesting area in which apple pomace could potentially be used is the packaging industry, which is currently focused on the search for innovative biodegradable materials. Interest in pomace as feedstock for biodegradable materials is still low and is mainly limited to the use of pomace as an additive of a few percent. Studies have been carried out, among others, on biodegradable active film packaging in which apple pomace or apple pomace extracts acted as an antioxidant released during food storage [
15,
16]. Attempts have also been made to enrich TPS starch with apple pomace [
17]. Overall, researchers mainly point to the positive aspects of incorporating apple pomace (and other types of pomace) into a polymer matrix [
18,
19]. Reports from scientific literature indicate that pelletisation of apple pomace is feasible, so it is possible to thicken apple biomass to obtain a compact structure [
20]. Other authors report that increasing the functionality of similar products is possible by obtaining pectin bonds (gel) in the product, but this requires strictly defined heating as well as cooling conditions. The same authors also claim that the pectin contained in apple pomace enables the formation of membranes and allows mixing with other polymers. It has also been found that monosaccharide content in the pomace allows pomace molecules to stick together, but the resulting material is hygroscopic and, consequently, can quickly lose its mechanical properties in the presence of water [
21].
Literature review confirms that apple pomace can be used as an additive in the manufacture of biocomposites. However, the literature lacks precise information on how and under what conditions the particles of this raw material are combined during compaction. Based on data from the literature, it also appears that one of the main problems in producing a biodegradable material from apple pomace is obtaining adequate strength of such a material. Author [
22] argue that this is usually related to poor bonding quality between the particles that make up the pomace. This is particularly the case when biocomposites are produced by pressure compacting. For this reason, many authors attempt to increase press force, which improves strength properties of the materials obtained, allowing more efficient use of van der Waals forces in the material being pressed [
23]. However, in order to achieve the right mechanical properties, the use of Van der Walls forces alone requires adequate material fragmentation and relatively high contact forces, up to 500 MPa [
20], to allow material molecules to approach one another sufficiently. When such contact forces are applied, unit energy required to produce the material increases significantly, which is mainly related to intermolecular friction [
24].
Therefore, addition or activation of natural adhesive substances contained in plant products in order to naturally reinforce the materials obtained seems to be a more promising method. The extrusion process which, as a result of temperature and pressure, can modify the structure of both starch based and non-starch based raw materials, may be used for this purpos [
25]. Such experiments have not been performed so far and, therefore, they fill the gap in biocomposite research. In the case of apple pomace, pectin is the most promising gluing component. Other interesting components are lignin and cellulose, found in the composition of apple pomace, which can also reinforce biocomposites. Despite their presence in apples, studies carried out to date have shown relatively low strength of materials made exclusively from apple pomace [
26]. Therefore, a promising addition could be the introduction of starch as a reinforcing substance. In its crystalline form, starch forms an amorphous structure under the influence of temperature and in the presence of a plasticiser, which significantly facilitates moulding, while acting as a binding agent as well. Depending on the type of plasticiser used and the ratio of amylose to amylopectin contained in the starch, different properties of processed starch can be obtained [
27]. Research into the use of starch as an additive in the manufacture of apple pomace films was carried out by Gustafsson et al. [
28]. Unfortunately, their research is difficult to relate to solid materials. The production of films takes advantage of the phenomenon of dissolution of components contained in pomace. In the process of pressure moulding, the bonding of molecules by using pressure and temperature forces is exploited.
Given the above, the aim of the present study was to investigate the basic properties of biocomposites obtained from extruded apple pomace reinforced with potato starch.
2. Materials and Methods
2.1. Materials
The research material was wet apple pomace (moisture content 60% (±2%)) purchased on the local market (Greenherb, Łancut, Poland). Before being used, the pomace was stored under refrigeration at a temperature of +1°C. The basic chemical composition of the pomace was: raw ash 2.4%, total protein 5.47%, crude fat 3.92%, crude fibre 58.25% of dry mass. SP potato starch was purchased from a local producer (Superior, Poland). Primary chemical composition of the starch was as follows: crude ash 0.4%, total protein 0.06%, crude fat 0.05%, amylose 21.2, amylopectin 79.1% of dry mass.
2.1.1. Pre-Treatment of apple pomace and biocomposite production
The pomace was rinsed in water at 16 °C to remove soluble compounds. After draining excess water in a piston press, moisture content of the pomace was 50 % (±0.2%). The pomace with this moisture content was pretreated in a high temperature extruder. The purpose of this method was to prejellify the starch and pectin contained in the pomace and to homogenise the apple pomace. A modified single-screw extruder (Insta Pro 600) with an L:D ratio of 12:1, retrofitted with electric heaters, was used in the tests. Temperature distribution in the extruder was, respectively: 120/100/80/80 °C. The resulting extruded (EAP) apple pomace was dried in a convection dryer to a moisture content of 10%. The dry material was crushed in a beater shredder (Bak, Poland) equipped with 1 mm hole diameter sieves. The final material was obtained by sieving the dry apple pomace in a sifter through 0.5 mm hole sieves. The mixes used in the tests were prepared in a ribbon mixer by adding water to dry matter to obtain a raw material with a moisture content of, respectively: 10, 12 and 14% (±0.2%). A detailed test plan showing the raw material composition of the biocomposites is shown in
Table 1. The material thus obtained was conditioned in a sealed container for 1 h at room temperature.
The material obtained in this way was then compacted by hot pressing on a test stand, which consisted of a hydraulic press (FR - 5014, manufacturer: Farys, Poland) with a maximum pressure of 150 kN. Electrically heated plates were installed on the piston pin and at the bottom of the press, with heaters with a total power of 1.600W installed inside the plates. The temperature was controlled by heater controllers with the accuracy of ± 0.1 °C. Plate wall thickness was 15mm (±0.1 mm) on both sides of the heater. A metal mould was inserted between the plates, which allowed a 81 cm
2 sample to be moulded/compressed to a thickness of 5mm (± 0.1 mm) (
Figure 1).
The weight of a single sample poured into the mould at a time was 80 g. The value of stress during the pressing process that was applied during the tests was 20 MPa. The biocomposite moulding tests were carried out at the temperature of 140°C (±0.1°C). The pressing time for each sample was 4.5 minutes.
2.2. Mechanical Properties
Strength tests were carried out in accordance with ISO 178:2019 [
29]. The standard describes testing of mechanical properties of plastics. The basic assumption underlying this standard is homogeneity of the material. In order to carry out the strength tests, the AXIS 500 stress testing device with an FA 500N load cell was used. Samples in the form of a 5×15×90mm rectangular beam were placed on two supports (distance between the supports: 40 mm), and then subjected to a static bending load (
Figure 2). The bending force was concentrated in the sample symmetry axis. The strength test was continued until the sample broke. The bending head displacement rate was calculated according to the following equation:
Where: a - deformation rate of the outer fiber (mm×min-1), l - distance between supports, h - sample thickness.
The test was completed when the sample deformation reached 5%, which meant a deformation of 7 mm.
Based on the tests performed, the bending strength and Young's modulus were determined.
Bending strength R
g as the highest stress value was calculated according to the following relationship:
where:
Fg – bending force (the greatest force recorded during bending);
l – distance between supports (constant value in our case);
Wg – bending strength index;
Wg for a beam with a rectangular cross-section:
Where:
b – beam width;
h – beam height.
Next, Young's Modulus (YM) was calculated using the following relationships:
where:
F0,2 – bending force corresponding to a deformation equal to 0.2% of the total deformation of the extreme fibers of the beam;
l – distance between supports (constant value in our case);
f0,2 – deflection arrow corresponding to a deformation equal to 0.2% of the total deformation of the extreme fibers of the beam;
f0,2 for a beam with a rectangular cross-section:
ε = 0,2%
Iy – moment of inertia of the cross-section;
Iy for a beam with a rectangular cross-section:
2.3. Colour Analysis
Colour analyses were carried out on the basis of images of the sample surface taken with a STX OPTA-TECH stereo microscope equipped with a 5 megapixel (Mpix) camera, (manufacturer: OPTA-TECH, Warsaw, Poland). The area photographed was illuminated with a circular LED illuminator with the colour temperature of 7000 K. The camera was calibrated before photographing by performing the white balance on a Minolta reference plate, no. 1863310. The colour tests were performed using CorelDRAW X7 Version 17.1.0.572 software, where the L*a*b* space was selected for the analysis of colour changes. The individual letters stand for: L*-brightness; a*- colour from green to magenta; b*- colour from blue to yellow.
2.4. Scanning Electron Microscope (SEM)
A HITACHI S-3400N scanning electron microscope (SEM), (manufacturer: Hitachi, Tokyo, Japan) w was used to take images of the fractures and the outer surface of the samples. The following parameters were set in the microscope: accelerating voltage of 20 kV and low vacuum of 70 Pa.
2.5. Thermogravimetry Analysis (TGA) and Derivative Differential Thermal Analysis (DTA)
The samples tested were subjected to a thermogravimetric analysis using TGA and DTA methods. The tests were carried out on a TGAQ50 V20. 13. Build 39 thermogravimetric analyser. The TGA tests were carried out for analytical samples weighing app. 10 mg. Sample mass changes were measured in an inert atmosphere (N2). Temperature change took place at a rate of 10°C×min-1. The temperature change range was from 30 to 795°C. As a result of the performed analyses, a so-called thermogravimetric curve (TGA) was obtained in the following system: sample mass – temperature. The differential thermal analysis (DTA) was carried out in parallel to the TGA measurements. As a result, the derivative of the thermogravimetric curve of mass versus temperature was obtained. In this way, the temperature dependent change in reaction rate is shown. The maxima on the differential curve define the points at which the rate of temperature decrease due to reaction progress and the rate of temperature increase are maximum. Application of the DTA method facilitates the analysis of thermal effects including determination of the temperature of onset and extremes of the thermal effect. A summary of the TGA/DTA curves for each sample is shown in the chart.
2.6. FTIR infrared spectrum analysis
The (FTIR) infrared spectrum analysis was performed with the FTIR Nicolet 8700 spectrophotometer (producer: Thermo Electron Corporation, USA). The spectra were recorded with the resolution of 2 cm-1 in the range of 400–4000 cm-1. The tests were performed at room temperature.
4. Conclusion
Research has shown that it is possible to produce a biocomposite from (EAP) apple pomace reinforced with (SP) potato starch. It was found that the pomace processed by extrusion in combination with the starch allows the production of a biocomposite with a compact structure and a smooth surface, as shown by SEM microscopic images. The colour of extruded apple pomace biocomposites is dark brown and darkens with growing starch content. Furthermore, it was found that the addition of (SP) potato starch in each case contributed to improving strength parameters of the biocomposites obtained. The study showed that the strongest materials were the biocomposites produced with the highest share of SP starch and with extreme moisture contents of 10% and 14%. This may suggest that two technologies can be adopted in the manufacture of such biodegradable materials. The first is the "dry" one, where materials are bonded mainly by pressure and the van der Waals forces present in the material. In this case, non-jellified starch can act as a natural reinforcement, with some of the jellified starch and pectin providing an additional natural binder. The other technology, promoting an increase in moisture content, where the vast majority of the starch is jellified and the pectin presumably interacts with the gel, also contributing to strengthening of the biocomposite. The advantage of the second method lies in obtaining a smoother surface using a moisture content of 14%. On the other hand, better temperature resistance will be obtained by manufacturing the product from raw material with a moisture content of 10%, as confirmed by the TGA tests. Finally, FTiR studies reveal that the transmittance value is higher for biocomposites obtained from raw material with a moisture content of 10%. The hydroxyl bond values also increase with the addition of starch. The research shows that extruded apple pomace combined with potato starch is a promising raw material that can be used to produce biodegradable materials that do not require a high stress transfer, e.g. household items, plates, cups, etc. For a wider application of apple pomace, however, further development of this technology towards the search for even more advanced biodegradable additives is necessary.
Author Contributions
Conceptualization, A.E., T.Ż.; methodology, A.E. T.Ż.; software, A.E, T.Ż; formal analysis, A.E T.Ż. A.K.; investigation, T.Ż, A.E.; resources, A.E T.Ż.; data curation, T.Ż.; writing—original draft preparation, A.E., T.Ż. R.K., A.K.,; writing—review and editing, A.E., T.Ż. R.K, A.K.; visualization, T.Ż.; supervision, A.E.; project administration, A.E.; funding acquisition, A.E, T.Ż. All authors have read and agreed to the published version of the manuscript.
Figure 1.
Technological diagram for preparation of the raw material and moulding of biocomposites: 1 - single-screw extruder, 2- convection dryer, 3 - hammer mill, 4 - band mixer, 5 - hydraulic press with a matrix for forming samples.
Figure 1.
Technological diagram for preparation of the raw material and moulding of biocomposites: 1 - single-screw extruder, 2- convection dryer, 3 - hammer mill, 4 - band mixer, 5 - hydraulic press with a matrix for forming samples.
Figure 2.
Bending strength tests.
Figure 2.
Bending strength tests.
Figure 2.
Influence of potato starch (SP) addition and raw material moisture content on parameter changes: (a) bending strength, (b) Young Modulus (YM), (c) water contact angle, (d) color component L*, (e) color component a*, (d) color component b*.
Figure 2.
Influence of potato starch (SP) addition and raw material moisture content on parameter changes: (a) bending strength, (b) Young Modulus (YM), (c) water contact angle, (d) color component L*, (e) color component a*, (d) color component b*.
Figure 3.
Figure 3: Biocomposites from extruded apple pomace (EAP) and: (a) - 40, (b) - 30, (c) - 20, (d) - 10 and (e) - 0% addition of potato starch (SP). Moisture content in the raw material 12%.
Figure 3.
Figure 3: Biocomposites from extruded apple pomace (EAP) and: (a) - 40, (b) - 30, (c) - 20, (d) - 10 and (e) - 0% addition of potato starch (SP). Moisture content in the raw material 12%.
Figure 4.
SEM scanning microscopy images of the biocomposites: (a, b) - "breakthrough" of the sample; (c)-starch granules of non-gelatinized starch, d-gelatinized starch, (d) and e and (f)- surface area comparisons of samples produced at 10 and 14% raw material moisture. Samples( a-d): starch addition 40%, raw material moisture 10%).
Figure 4.
SEM scanning microscopy images of the biocomposites: (a, b) - "breakthrough" of the sample; (c)-starch granules of non-gelatinized starch, d-gelatinized starch, (d) and e and (f)- surface area comparisons of samples produced at 10 and 14% raw material moisture. Samples( a-d): starch addition 40%, raw material moisture 10%).
Figure 5.
The course of (mass loses) (a) and (derivative mass change biocomposites) (b) curves of biocomposites from (EAP) extruded apple pomace and (SP) starch.
Figure 5.
The course of (mass loses) (a) and (derivative mass change biocomposites) (b) curves of biocomposites from (EAP) extruded apple pomace and (SP) starch.
Figure 6.
Figure 3: FTIR infrared spectrum of biocomposites from extruded apple pomace (EAP) and: (a) - 40, (b) - 30, (c) - 20, (d) - 10 and (e) - 0% addition of potato starch (SP). Moisture content in the raw material 14%.
Figure 6.
Figure 3: FTIR infrared spectrum of biocomposites from extruded apple pomace (EAP) and: (a) - 40, (b) - 30, (c) - 20, (d) - 10 and (e) - 0% addition of potato starch (SP). Moisture content in the raw material 14%.
Table 1.
Empirical test plan.
Table 1.
Empirical test plan.
Sample. nomber |
Index* |
Apple pomace (EAP) [wt %], |
Starch [wt %] |
Moisture [%] |
1 |
p60_s40_m10 |
60 |
40 |
10 |
2 |
p70_s30_m10 |
70 |
30 |
10 |
3 |
p80_s20_m10 |
80 |
20 |
10 |
4 |
p90_s10_m10 |
90 |
10 |
10 |
5 |
p100_s0_m10 |
100 |
0 |
10 |
6 |
p60_s40_m12 |
60 |
40 |
12 |
7 |
p70_s30_ m12 |
70 |
30 |
12 |
8 |
p80_s20_ m12 |
80 |
20 |
12 |
9 |
p90_s10_ m12 |
90 |
10 |
12 |
10 |
p100_s0_ m12 |
100 |
0 |
12 |
11 |
p60_s40_m14 |
60 |
40 |
14 |
12 |
p70_s30_ m14 |
70 |
30 |
14 |
13 |
p80_s20_ m14 |
80 |
20 |
14 |
14 |
p90_s10_ m14 |
90 |
10 |
14 |
15 |
p100_s0_ m14 |
100 |
0 |
14 |
Table 2.
Anova variance analysis results, SS sum of squares, df degree of freedom, MS sum of mean squares, F statistics, p value of test probability, L linear, Q square.
Table 2.
Anova variance analysis results, SS sum of squares, df degree of freedom, MS sum of mean squares, F statistics, p value of test probability, L linear, Q square.
Source of variation |
Bending strength (MPa); R2= 0.762; Pure error MS==0.848 |
|
|
SS |
|
df |
|
|
MS |
|
F |
|
|
p |
1, Moisture (°C) |
L |
12.908 |
1 |
12.908 |
15.218 |
0.0005 |
Moisture (°C) |
Q |
8.5 |
1 |
8.5 |
10.022 |
0.0035 |
2, Starch (wt%) |
L |
74.721 |
1 |
74.721 |
88.093 |
0 |
Starch (wt%) |
Q |
5.8 |
1 |
5.8 |
6.838 |
0.0138 |
Interaction 1Lvs 2L |
|
4.375 |
1 |
4.375 |
5.158 |
0.0305 |
Lack of fit |
|
7.713 |
9 |
0.857 |
1.01 |
0.4537 |
Pure error |
|
25.446 |
30 |
0.848 |
|
|
Total SS |
|
139.463 |
44 |
|
|
|
|
Young’s modulus (MPa); R2= 0.871; Pure error MS=00036 |
1, Moisture (°C) |
L |
0.002 |
1 |
0.002 |
5.509 |
0.0257 |
Moisture (°C) |
Q |
0.027 |
1 |
0.027 |
74.898 |
0 |
2, Starch (wt%) |
L |
0.565 |
1 |
0.565 |
1573.495 |
0 |
Starch (wt%) |
Q |
0.05 |
1 |
0.05 |
138.238 |
0 |
Interaction 1L vs.2L |
|
0.005 |
1 |
0.005 |
14.932 |
0.0006 |
Lack of fit |
|
0.086 |
9 |
0.001 |
26.562 |
0 |
Pure error |
|
0.011 |
30 |
0.0004 |
|
|
Total SS |
|
0.74 |
44 |
|
|
|
Water contact angle ( °); R2=0.881; Pure error MS=0.866 |
1, Moisture (°C) |
L |
173.761 |
1 |
173.761 |
220.634* |
0 |
Moisture (°C) |
Q |
67.254 |
1 |
67.254 |
85.396* |
0 |
2, Starch (wt%) |
L |
6201.76 |
1 |
6201.76 |
7874.695* |
0 |
Starch (wt%) |
Q |
333.206 |
1 |
333.206 |
423.089* |
0 |
Interaction 1L vs.2L |
|
231.673 |
1 |
231.673 |
294.168* |
0 |
Lack of fit |
|
924.457 |
9 |
102.717 |
130.426* |
0 |
Pure error |
|
23.627 |
30 |
0.788 |
|
|
Total SS |
|
7955.739 |
44 |
|
|
|
L*; R2= :0.733; Pure error MS=:0.055 |
1, Moisture (°C) |
L |
0.702 |
1 |
0.702 |
12.670* |
0.0013 |
Moisture (°C) |
Q |
18.432 |
1 |
18.432 |
332.810* |
0 |
2, Starch (wt%) |
L |
42.955 |
1 |
42.955 |
775.598* |
0 |
Starch (wt%) |
Q |
1.165 |
1 |
1.165 |
21.042* |
0.0001 |
Interaction 1L vs.2L |
|
8.853 |
1 |
8.853 |
159.847* |
0 |
Lack of fit |
|
24.643 |
9 |
2.738 |
49.440* |
0 |
Pure error |
|
1.661 |
30 |
0.055 |
|
|
Total SS |
|
98.411 |
44 |
|
|
|
a*; R2= 0.719; Pure error MS=0.00095 |
1, Moisture (°C) |
L |
0.197 |
1 |
0.197 |
206.465* |
0 |
Moisture (°C) |
Q |
0.188 |
1 |
0.188 |
196.878* |
0 |
2, Starch (wt%) |
L |
5.73 |
1 |
5.73 |
6011.003* |
0 |
Starch (wt%) |
Q |
8.265 |
1 |
8.265 |
8669.272* |
0 |
Interaction 1L vs.2L |
|
0.045 |
1 |
0.045 |
47.596* |
0 |
Lack of fit |
|
5.602 |
9 |
0.622 |
652.913* |
0 |
Pure error |
|
0.029 |
30 |
0.00095 |
|
|
Total SS |
|
20.056 |
44 |
|
|
|
b*; R2= 0.711; Pure error MS=0.0065 |
1, Moisture (°C) |
L |
0.853 |
1 |
0.853 |
130.809* |
0 |
Moisture (°C) |
Q |
1.439 |
1 |
1.4394 |
220.546* |
0 |
2, Starch (wt%) |
L |
30.543 |
1 |
30.543 |
4681.378* |
0 |
Starch (wt%) |
Q |
0.761 |
1 |
0.761 |
116.587* |
0 |
Interaction 1L vs.2L |
|
0.111 |
1 |
0.111 |
17.004* |
0.0003 |
Lack of fit |
|
13.479 |
9 |
1.498 |
229.550* |
0 |
Pure error |
|
0.196 |
30 |
0.0065 |
|
|
Total SS |
|
47.382 |
44 |
|
|
|
Table 3.
Summary of percentage mass loss during TGA analysis.
Table 3.
Summary of percentage mass loss during TGA analysis.
Sample |
Mass losses (%) |
Temperature at 5% mass losses (°C) |
Temperature at 50% mass losses (°C) |
I 30-150°C |
II 150-250°C |
III 250-350°C |
IV 350-600°C |
|
Total 30-600 °C |
p60_s40_m10 |
3.37 |
15.79 |
54.15 |
0 |
|
73.31 |
166,5 |
314,1 |
p70_s30_m10 |
4.02 |
24.28 |
20.91 |
22.49 |
|
71.70 |
153,2 |
322,7 |
p80_s20_m10 |
4.22 |
24.77 |
18.85 |
29.13 |
|
76.97 |
142,1 |
325,6 |
p90_s10_m10 |
3.55 |
26.39 |
14.75 |
26.64 |
|
71.33 |
158,5 |
330,1 |
p60_s40_m14 |
3.19 |
15.64 |
54.49 |
0 |
|
73.32 |
171,4 |
301,1 |
p70_s30_m14 |
2.93 |
20.41 |
49.91 |
0 |
|
73.25 |
158,5 |
315,5 |
p80_s20_m14 |
4.09 |
25.17 |
16.75 |
24.52 |
|
70.53 |
150,1 |
329,7 |
p90_s10_m14 |
3.71 |
25.69 |
15.88 |
26.30 |
|
71.58 |
159,3 |
328,1 |
p100_s0_m10 |
4.15 |
32.09 |
33.75 |
0 |
|
69.99 |
149,3 |
325,9 |
|
|
|
|
|
|
|
|
|