1. Introduction
Based on the main notions of the circular economy and the bioeconomy [1,2], the concept of using agricultural waste is discussed. The common objective is to minimize the generation of waste from economic or urban activities related to agriculture. The circular economy turns out to be attractive for understanding the sustainable challenges we face in terms of social, economic and environmental aspects. However, in the case of bio-waste, taking advantage of the immense amount of agricultural waste generated, the processes could become a complex and difficult operation [3]. This is especially true for the development of new materials from citrus fruit bio-waste.
Citrus fruits are believed to have originated from the warm southern slopes of the Himalayas in north-eastern India and northern Myanmar [4]. At present, citrus crops are among the most cultivated fruits in the tropical and subtropical regions of the world. Regarding the bio-waste issue, approximately one-third of citrus fruits are utilized for processing, which produces around 50–60% of organic waste [5].
With the growing importance that organic farming has acquired, both in developed and developing countries, there are no studies of these socio-economic realities [6]. Organic agriculture [7,8] has remained a haven against the invasion of agrochemicals and industrialization in the food supply chain. It represents less than 1% of global agriculture, specifically reported as 0.98% by Willer and Lernoud [9]. On the contrary, agriculture is the fastest-growing food sector in the world [10]. South America has a strong presence in the agriculture sector: Argentina (3,191,255 ha), Uruguay (930,965 ha) and Brazil (705,233 ha) [9,10,11]. Approximately 40% of the oranges produced globally are used in the production of different commercial products [12]. Due to processing, large amounts of waste products (bio-waste), such as peels from the juice industry, are generated and accumulated [13].
Considering this waste accumulation, different investigations propose the use of waste and bio-waste in order to obtain new materials, especially in sol-gel synthesis to obtain silica-based materials [13,14,15,16,17,18,19]. The sol-gel process can be described as the formation of an oxidic network through the polycondensation reaction of a molecular precursor in a liquid. The term sol refers to a dispersion of colloidal particles in a liquid medium where the stability of the colloids is due to both Brownian motion and small particle size. The term gel refers to a three-dimensional network of a solid phase interwoven with an entrapped and immobilized continuous liquid phase [18,19,20]. In our previous research, the sol-gel method was used as a versatile synthesis route characterized by the low temperatures at which inorganic materials and organic/inorganic hybrids were synthesized [21,22].
In this research, two main issues were addressed at the same time: the use of citric bio-waste and the obtention of materials using the sol-gel technique—looking for their use in heterogeneous catalysis as a bi-functional support system. Silica has been identified as an ideal support material for its strong hydrophilicity, acknowledged biocompatibility, shape and chemistry surface [23]. Two different strategies have been explored to combine bio-waste with the synthesis of silica-based materials. The first step was to obtain silica through acidic or alkaline hydrolysis by using acetic, citric, hydrochloric acids and an alkali (ammonium hydroxide). In the second step, lemon or orange peels were added to the obtained mixtures. The objective of this mixed synthesis was to find the influence of organic bio-waste on acids/alkalis, to partially replace them with organic orange or lemon peels, which could presumable provide citric acid, among other compounds. For this, different amounts of bio-waste were used in the various syntheses [24,25].
As a precursor of silica, tetraethyl orthosilicate (TEOS) was used, and its hydrolysis and condensation were studied, using absolute ethanol as a green solvent due to its renewability [26,27]. This solvent plays an important role in the synthesis of silica-based materials, both in the case of the reaction with TEOS, once they act as a homogenizer agent for substances with different solubilities that participate in the condensation reaction, and with lemon and orange peels, extracting compounds of interest from them [28,29,30]. All synthesized solids were characterized in-depth by integrating different physical-chemical techniques, such as scanning electron microscopy (SEM) and x-ray diffraction (XRD). The chemical compositions of the solids were investigated through Fourier transform infrared spectroscopy (FT₋IR) and the acidic properties by n-butylamine potentiometric titration.
With the physicochemical properties discussed in this research, silica-based materials synthesized with bio-residues could have the potential to be used as supports for heterogeneous reactions (whose analysis is reserved for future research).
2. Materials and Methods
The starting point to specifying the proposed objectives includes having the necessary material and carrying out an adequate design of the experiments. For the design of these steps, two levels of complexity were selected, when required. This means that some of the operating variables remain fixed. Thus, reliable results can be obtained with the fewest possible experiences [21,22].
Before starting with the sol-gel synthesis, the oranges and lemons were peeled (20 of each of them), and the peels were cut into small pieces and put on the stove for 3 days, at 70 °C. Once calcined, the peels become brittle, and it is easier to grind them to a small size, so they were ground in a mortar (Scheme 1). This size allows uniformity between the liquid gel and ground peels mixture. It should be noted that in 2020 a doctoral thesis was carried out with citrus peels without calcining (lemon, orange and mandarin) to obtain silica-based materials [31].
The sol-gel synthesis was carried out in a chamber with a nitrogen-controlled atmosphere at room temperature. First, a portion of the solvent, absolute ethanol (CH3CH2OH, Carlo Erba), and the corresponding catalyst for acid hydrolysis were placed into a beaker: acetic acid glacial (CH₃COOH, HPLC grade, J. T. Baker), citric acid (C6H8O7 anhydrous for synthesis, Merck) or hydrochloric acid (HCl, 37%, Merck). The same was done in the alkaline hydrolysis using ammonium hydroxide (NH4OH, Anedra analytical reagent). Then, the TEOS (Si(OC2H5)4, Aldrich 98%) was added, followed by the last portion of solvent and distilled water, respectively.
Each mixture, outside the nitrogen-controlled atmosphere, was placed on a magnetic stirrer at 500 rpm; the respective amounts of orange or lemon peels were added, maintaining stirring for 2 h. The mixture was left for 3 weeks at room temperature; then, the gel formed was dried at 100 °C for 1 h. The details of each synthesis are shown in Table 1, Table 2, Table 3 and Table 4 (considering the total volume of ethanol added). Each table details the ratios of the compounds and the amounts used of lemon and orange peels (25 and 50%) in relation to the pure silica mass—considering as 100% the 5 g of pure silica obtained with fixed volumes of 17 mL of TEOS and 21.8 mL and, as appropriate, 5 mL of CH₃COOH; 0.43 mL of C6H8O7; 7.5 mL of HCl (so proton concentration is the same in all cases) or 1.8 mL of NH4OH. The amounts of all the reagents were varied in order to maintain the relationship between the TEOS precursor, the acid and alkaline catalysts and the solvent, with which the same silica-based solids should be generated, but adding citrus peels.
The evaluation of the acidic properties was carried out by potentiometric titration with n-butylamine using a Metrohm 794 Basic Titrino titrator (Switzerland) with a double-junction electrode. For that, 0.025 mL/min of an n-butylamine solution in acetonitrile (0.025 N) was added to 0.025 g of sample, previously suspended in 45 mL of acetonitrile and keeping the stirring time constant (540 s) before adding the first drop and a waiting time of the drop of 60 s, while stirring constantly. FT₋IR spectrum was obtained using Bruker IFS 66 equipment (Germany). Pellets of the sample in KBr, at room temperature, were measured in a range between 500 and 4000 cm−1. SEM was applied to obtain different micrographs of the solids using the JEOL equipment, JSM-6390LV (Japan), with a voltage of 20 kV. Samples were supported on graphite and metalized with a sputtered gold film. Finally, XRD patterns were recorded by means of a PANalytical X’Pert Pro 3373/00 device with the following conditions: Cu Kα radiation (λ = 1.5417 Ǻ); Ni filter; 20 mA and 40 kV in the high voltage source; scanning angle (2θ) from 5° to 40°, scanning rate 2° (2θ)/min.
3. Results and Discussion
3.1. Digital Photographs
Among the basic principles of the sol-gel technique [32] is that it is an alternative to obtain non-metallic inorganic materials, such as glass and ceramics. This consists of the hydrolysis and condensation, originating from alkoxide precursors to form a polymeric network in the vitreous state, typically exhibiting a macroporous structure [33]. The gel is formed by a two-stage reaction: (1) hydrolysis and (2) polycondensation:
(1) The hydrolysis for gel formation is carried out using different alcohols as the solvent. This reaction is produced by the nucleophilic attack of the oxygen present in the water on the metal atom, forming silanols groups [34]. The solvent is the chemical compound that represents the largest proportion of the process.
(2) The condensation begins as soon as the alkoxide groups are hydrolyzed. The concentrations of -OH and/or -OR end groups depend on the hydrolysis and condensation mechanisms. They are determined by the nature of the catalyst used [35]. Brinker and Scherer [26] studied the effect of pH on the morphology of the siliceous structures. They found that the change in the pH of the solution affects the rates of hydrolysis and condensation, respectively. Figure 1 shows the silica synthesized with acid hydrolysis using acetic acid. The first photograph (pure silica) shows the silica obtained without bio-waste, with its glassy structure, coming from a gel that slowly dried at room temperature.
Milea et al. [36] found that the sol-gel technique allows the preparation of a new glass composition with superior properties determined by the specific properties of the gel [37,38]. In the following, Figure 1a,b correspond to the silica-based materials with orange peel aggregates, and Figure 1c,d correspond to silica-based materials with lemon peels. It is important to note that in all cases, the added peels remained in the siliceous structure, mainly on the surface of the dry gel, due to condensation; this occurred as the gel dried. If Figure 1a and c are compared, it can be distinguished that with 50% orange or lemon peel, the silica-based solid turns yellowish and has a surface structure similar to pure silica. This layer of siliceous material is brighter and has a vitreous consistency. However, in the case of 25% orange and lemon peel added to the gel mixture, when drying, they are less shiny, although the surface is similar to 50% added bio-residues.
In the case of the 50% lemon or orange peel, the silica-based solid obtained forms two phases: one given by the compounds extracted by the solvents (ethanol and water) from the peels, varying the pH [25], and the other phase by the acid used in the synthesis. In the case of 25% peels, the effect is the same, although the pH is lower [28,39]. At this point, it is interesting to compare the gelation when the hydrolysis has already been carried out. Gelation is physically manifested by a drastic increase in the viscosity of the solution [40]. These changes in viscosity occur without causing the generation of chemical transformations or endothermic or exothermic changes [41]. The wet gel can be strengthened by aging and by the syneresis mechanism of Ostwald maturation [42]. The syneresis is characterized by the contraction of the gel network, produced by the expulsion or extraction of liquid. The gel that is a homogeneous substance becomes a segregation of solid components. Smaller particles have a higher solubility, which leads to their precipitation and the formation of larger ones [39]. During drying, the effect of citrus peels on the surface of the solids obtained indicates that the silicon skeleton becomes increasingly rigid. When the surface tension cannot deform the network, the gel body becomes too stiff. At this point, the likelihood of it breaking is higher [37,43], as can be seen in the photographs.
3.2. Potentiometric Titration Characterization
The acid properties of all the synthesized solids were studied through potentiometric titration with n-butylamine, which allows knowing the number of acid sites and their acid strength. To interpret the results obtained, the initial electrode potential (Ei) indicates the maximum acid strength of the surface sites, and the values of m eq/g solid, in which the plateau is reached, indicate the total number of acid sites. The acid strength of the surface sites can be classified according to the following ranges: very strong sites Ei > 100 mV, strong sites 0 < Ei < 100 mV, weak sites −100 < Ei < 0 mV and very weak sites Ei < −100 mV, respectively. It is important to clarify that this technique only indicates the mass acidity trend of the solids obtained [44]. The initial electrode potentials are shown in Table 5 and their respective potentiometric curves in Figure 2.
Comparing the potentiometric curves of the synthesis with acid hydrolysis (Figure 2a–c)—samples that use acetic, citric and hydrochloric acid—the presence of free electrons in the acid gave a higher acidity (Figure 2c). Comparing the use of 50 and 25% orange peels in acid hydrolysis versus pure silica (with acetic acid), KZ1 gives an Ei of 128 mV for pure silica versus 110 mV for 50% (KZ2) and 132 mV for 25% (KZ3) (Table 5). Citric and hydrochloric acid showed similar behavior to acetic acid when silica-based solid synthesized with orange and lemon peels were analyzed (Figure 2b,c). For basic hydrolysis, the use of NH4OH generated the lowest value in both cases of 50 and 25% of the bio-waste. In the case of lemon peel, for both 50 and 25%, the Ei values (Table 5) and the potentiometric curves (Figure 2d) followed the same trend as those obtained for orange peels.
Among the constituents of lemon, approximately 70% correspond to citric acid, while folic and ascorbic acid are the predominant constituents in orange [31]. The incorporation of bio-waste in the structure of silica prepared by acid hydrolysis maintains the same Ei as the initial one, or decrease for all cases, since the acidity of the acids used as catalysts was greater than that of the bio-waste (compare Ei of Table 5 in the KZ11-Z13 series for orange and in the KZ11-KZ15 series for lemon). Although lemon was more effective in maintaining the high number of acidic sites for the samples synthesized with hydrochloric acid (compare the two series in Figure 2c), this trend did not hold for the samples synthesized with acetic or citric acid. Furthermore, at this point, one can see that none of the bio-residues contributed new strong acid sites to the final material because the acidity of pure silica was “diluted” by the incorporation of orange or lemon peels.
When ammonium hydroxide was used, the acidic sites of the bio-waste were neutralized by the ammonia. Therefore, when the bio-waste amount was only 25%, the acidity of the bio-waste was neutralized and, hence, the obtained Ei of KZ18 (38 mV) and KZ20 (96 mV) was lower than pure silica KZ16 (107 mV). On the other hand, when the bio-waste amount was 50%, the acidity of the obtained silica slightly increased in comparison with the pure silica, as can be seen in the Ei values of KZ17 (112 mV) and KZ19 (116 mV), which can be understood as a contribution of the bio-residue to the final material acidity, slightly increasing it.
3.3. SEM Characterization
The pH of the catalyst determines the texture of the solid product, as can be seen in Figure 3. The morphology caused by acid hydrolysis (KZ1, KZ6 and KZ11) is laminar and typical of sol-gel silica. Curran and Stiegman [45] studied the morphology of siliceous structures at very high acidic concentrations; below the isoelectric point, dry xerogels become mesoporous. This is due to the protonation of silanols (-SiOH) to produce (-SiOH2+), which are leaving groups and increase the rate of condensation. First, hydrated monomers obtained from the hydrolysis of precursors undergo condensation reactions, forming silicate polymer chains and then small nuclei. These grow through silica monomer and polymer bonding, forming primary particles, usually 5–7 nm in mean diameter. Then, primary particles aggregate, producing larger SiO2 particles that grow up to a stationary critical size [46]. In contrast, alkaline hydrolysis (KZ16) gives clusters of spheres because it is slower hydrolysis (formation of branched polymers or spherical aggregates). As expected, the use of only one alkoxide combined with appropriately chosen amounts of reagents allows for deep control over the nucleation and growth processes, leading to spherical and highly monodisperse nanoparticles [47].
Regarding the SEM micrographs, Figure 4 shows the samples prepared with HCl as a catalyst. It was possible to observe a similarity to the characteristic laminar format of silica regardless of the amounts of orange or lemon that were added to the synthesis. In this case, hydrolysis with the strong acid can form, on the one hand, only silica and, on the other, leach the shells, as can be seen in the micrographs. Zarib and Abdullah [48] obtained a smooth surface and a rough surface together in the silicate particle. This was when rice husk was used as a bio-waste.
The NH4OH sample, which can be seen in Figure 5, had a rounded shape and its particles formed clusters of variable sizes, which may be due to the action of orange and lemon aggregates that modify the pH of the synthesis. An agglomeration of nanoparticles of silica-based material and bio-waste was observed due to the three-dimensional hydrophilic networks on the surface of the solids [49]. Other researchers have synthesized silica with low surface microspheres from wheat husk ash with an alkaline and acid precipitation process [50].
3.4. XRD Characterization
The structure of the synthesized materials was determined using the XRD technique. This conventional technique has been increasingly used in similar studies for mixed matrices using bio-waste, such as the work developed by Worathanakul et al. [51] in which bagasse ash was used as a silica source for zeolite synthesis, another alternative source for the production of valuable materials and chemicals.
Figure 6 shows the x-ray diffraction diagrams of the silica obtained using TEOS as a precursor employing the acids (acetic, citric and hydrochloric) and the alkali (ammonium hydroxide) as catalysts. The amorphous structure of silica xerogels was confirmed by the broad peaks in the interval around 15–30° 2θ, as reported by Czarnobaj [52], and by the band located around 23° 2θ, which is the typical diffraction of this type of silica [53,54].
Figure 7 presents the XRD diagrams of the synthesized silica-based solids with 50%, and 25% orange and lemon peels with acidic and alkali hydrolysis. The similarity of the diagrams with the silica without the addition of bio-waste indicates that the surface of the solids obtained was mostly silica-based solids.
3.5. FT₋IR Characterization
FT₋IR spectroscopy has been widely used for the characterization of materials synthesized by the sol-gel method [51,55]. This made it possible to perform an in-depth analysis to understand the relationships between the properties of the material—including its structure at the atomic level—and the IR spectrum. As the structure evolved in the silica xerogel, a three-dimensional network of interconnected tetrahedral units formed. FT₋IR allows, depending on the width and position of the bands, the characterization of the material by interpreting its composition and structure. In this study, the region of 4000–500 cm−1 was used.
Figure 8 shows the complete FT₋IR spectrum of the samples obtained by synthesis with TEOS as a precursor and acetic acid (KZ1), citric acid (KZ6) and hydrochloric acid (KZ11) as acid catalysts and ammonium hydroxide (KZ16) as the alkaline catalyst. Table 6 shows the characteristic absorption bands of silica obtained with acetic acid as a catalyst.
Figure 8 and Table 6 show bands at 500, 800, 950, 1080 and 1200 cm−1 (the five last bands), which are characteristic bands of silica, corresponding to vibrations of silicon-oxygen bonds. These bands can be classified by the movement (to roll, bend and stretch) of the oxygen atom related to the silicon atoms [56]. The symmetric and asymmetric stretching modes of the Si-O-Si bonds can be assigned to bands at 1166 and 1079 cm−1, respectively. The vibration at 797 cm−1 is associated with the symmetric stretching of the Si-O bond or vibrational modes of structure rings. The bands centered at 948 and 1864 cm−1 were assigned to the vibration of the Si-O bonds (silanols) and are characteristic of silica xerogel [57]. The band located around 566 cm−1 was attributed to the deformation of cyclotetrasiloxanes (four-membered siloxane rings). This molecule can constitute a large fraction of the oligomeric species present in TEOS-derived systems because they are stable during the hydrolysis processes [58].
The broad band located at 3000 to 3700 cm−1 was assigned to the OH species due to stretching vibrations of hydrogen-bonded water molecules on the surface of silica [59], to silanols bound to molecular water and to free silanols on the surface of the gel [60,61]. The band located at 1639 cm−1 was assigned to the deformation of molecular water and resulted from the angular deformations of H-O-H bonds in H2O. The description made for the KZ1 silica sample is common for the other three pure silica forms (KZ6, KZ11 and KZ16).
Figure 9 shows the FT₋IR spectra of the silica-based materials obtained with 50% and 25% orange and lemon peels with acid and alkaline hydrolysis. As previously mentioned, changes in the position and shape of the absorption bands can be related to structural changes, which can occur with different solvent compositions (such as water and ethanol), leading to a variation in the hydrolysis and condensation reactions.
For Figure 9a, the band appearing at 2932 cm−1 (marked as I) can be assigned to the symmetric and asymmetric stretching of the C-H bonds in the residual groups CH3-OH and CH3-O-Si [60]. In this same figure, two absorption bands are observed at 1409 and 1518 cm−1 (marked as II and III, respectively) due to the CH3 groups provided by the organic material (bio-waste); these bands are characteristic of a hydrophobic form of silica. The description made for the KZ2 sample is common for the other silica-based solids synthesized with 50% and 25% orange and lemon peels.
All the characterizations used and discussed above portray the first part of a broad study, in which we highlight the initial stage of understanding the morphology and behavior of silica supports synthesized using different amounts of bio-waste and acidic and basic catalysts in order to analyze the influence that such bio-residues have on the reaction to obtain the silica-based solid support. Based on this knowledge, and also based on previous studies on the same topic [24,25], orange and lemon bio-waste can provide acidity for the reaction with the precursor TEOS. There is an indication that it would be possible to partially replace the acid catalysts used in this synthesis by bio-waste, but not completely, as they subtly reduce the acidity of the mixed materials when compared to pure silica—since the acidity of the acids used is greater than the amount of acidic compounds that are extracted from the citrus peels in the mixed matrices.
4. Conclusions
In this study, we synthesized new materials using the sol-gel method, a simple and fast technique that allowed the inclusion of bio-waste into silica matrices, proposing a first stage for the development of new silica-based supports that can be used in heterogeneous catalysis. The analyses of the influence of the orange and lemon peel percentages in the acidity and morphology of siliceous solids revealed promising results, suggesting that the bio-waste used can provide acidity to partially replace the acid catalysts investigated in acid hydrolysis—since the values obtained using 25 and 50% of bio-waste are similar to those of pure silica—but it is not possible to replace them completely. In addition, the mixed materials also showed the ability to maintain the siliceous structure. This is an important step for future studies in order to replace, for example, strong inorganic acids with a renewable raw material (bio-waste), which has a lower cost and suitable morphology. Research based on sustainability aspects is increasingly important and necessary in the current model of production and consumption in which we live. The chemistry required for a circular model will materialize only through a new attitude toward research, chemical engineering and the design of new processes and products.
Conceptualization, P.G.V. and V.G.Z.; conduct of the experiments and characterization techniques, K.Z., K.I. and M.B.C.M.; prepared and wrote the draft of the manuscript, P.G.V.; supervision and editing of the final version, P.G.V. All authors have read and agreed to the published version of the manuscript.
This research received no external funding.
Not applicable.
Not applicable.
More data can be obtained by request to the authors.
The authors would like to thank UNLP, CONICET, AUGM, CNPq and Capes for the financial support, at the service of FT₋IR of CINDECA, Dra. R. Arreche, Dra. V. Palermo, Tco Qco L. Osiglio and G. Kürten for their collaboration in this study.
The authors declare no conflict of interest.
Publisher’s Note: MDPI stays neutral with regard to jurisdictional claims in published maps and institutional affiliations.
Figure 1. Silica gel obtained with CH₃COOH: (a) 50% orange peel; (b) 25% orange peel; (c) 50% lemon peel; (d) 25% lemon peel.
Figure 2. Potentiometric curves of the synthesized solids: (a) Acid hydrolysis: acetic acid (KZ1, KZ2, KZ3, KZ4, KZ5); (b) citric acid (KZ6, KZ7, KZ8, KZ9, KZ10); (c) hydrochloric acid (KZ11, KZ12, KZ13, KZ14, KZ15); (d) alkali hydrolysis: ammonium hydroxide (KZ16, KZ17, KZ18, KZ19, KZ20).
Figure 3. SEM micrographs of synthesized silica-based solid by acid (KZ1, KZ6 and KZ11) and alkali (KZ16) hydrolysis. Magnification ×4000 (scale bar: 2 µm).
Figure 4. SEM micrographs of the silica-based solid synthesized using HCl with orange and lemon peels. Magnification ×1000 (scale bar: 10 µm).
Figure 5. SEM micrographs of the silica-based solid synthesized using NH4OH with orange and lemon peels. Magnification ×1000 (scale bar: 10 µm).
Figure 7. XRD diagram of all synthesized silica-based solids. (a) All solids synthesized with 50% orange peel. (b) All solids synthesized with 50% lemon peel. (c) All solids synthesized with 25% orange peel. (d) All solids synthesized with 25% lemon peel.
Figure 8. FT₋IR spectrum of the pure silica obtained by synthesis with TEOS as a precursor and acetic acid (KZ1), citric acid (KZ6), hydrochloric acid (KZ11) and ammonium hydroxide (KZ16).
Figure 9. FT₋IR spectrum of the synthesized silica. (a) All silica synthesized with 50% orange peel. (b) All silica synthesized with 50% lemon peel. (c) All silica synthesized with 25% orange peel. (d) All silica synthesized with 25% lemon peel.
Conditions employed in silica synthesis using acetic acid as a catalyst.
Sample | Precursor | Solvent | Acid | Water | Bio-Waste |
---|---|---|---|---|---|
KZ1 | TEOS | EtOH | CH₃COOH | H2O | Pure silica |
17.0 mL | 21.8 mL | 5.0 mL | 5.0 mL | 5.0 g | |
KZ2 | TEOS | EtOH | CH₃COOH | H2O | 50% orange peel |
8.5 ml | 10.9 mL | 2.5 mL | 2.5 mL | 2.5 g | |
KZ3 | TEOS | EtOH | CH₃COOH | H2O | 25% orange peel |
12.8 mL | 16.3 mL | 3.75 mL | 3.75 mL | 1.25 g | |
KZ4 | TEOS | EtOH | CH₃COOH | H2O | 50% lemon peel |
8.5 mL | 10.9 mL | 2.5 mL | 2.5 mL | 2.5 g | |
KZ5 | TEOS | EtOH | CH₃COOH | H2O | 25% lemon peel |
12.8 mL | 16.3 mL | 3.75 mL | 3.75 mL | 1.25 g |
Conditions employed in silica synthesis using citric acid as a catalyst.
Sample | Precursor | Solvent | Acid | Water | Bio-Waste |
---|---|---|---|---|---|
KZ6 | TEOS | EtOH | C6H8O7 | H2O | Pure silica |
17.0 mL | 21.8 mL | 0.43 mL | 5.0 mL | 5.0 g | |
KZ7 | TEOS | EtOH | C6H8O7 | H2O | 50% orange peel |
8.5 ml | 10.9 mL | 0.20 mL | 2.5 mL | 2.5 g | |
KZ8 | TEOS | EtOH | C6H8O7 | H2O | 25% orange peel |
12.8 mL | 16.3 mL | 0.30 mL | 3.75 mL | 1.25 g | |
KZ9 | TEOS | EtOH | C6H8O7 | H2O | 50% lemon peel |
8.5 mL | 10.9 mL | 0.20 mL | 2.5 mL | 2.5 g | |
KZ10 | TEOS | EtOH | C6H8O7 | H2O | 25% lemon peel |
12.8 mL | 16.3 mL | 0.30 mL | 3.75 mL | 1.25 g |
Conditions employed in silica synthesis using hydrochloric acid as a catalyst.
Sample | Precursor | Solvent | Acid | Water | Bio-Waste |
---|---|---|---|---|---|
KZ11 | TEOS | EtOH | HCl | H2O | Pure silica |
17.0 mL | 21.8 ml | 7.5 mL | 5.0 mL | 5.0 g | |
KZ12 | TEOS | EtOH | HCl | H2O | 50% orange peel |
8.5 ml | 10.9 mL | 3.8 mL | 2.5 mL | 2.5 g | |
KZ13 | TEOS | EtOH | HCl | H2O | 25% orange peel |
12.8 mL | 16.3 mL | 5.6 mL | 3.75 mL | 1.25 g | |
KZ14 | TEOS | EtOH | HCl | H2O | 50% lemon peel |
8.5 mL | 10.9 mL | 3.8 mL | 2.5 mL | 2.5 g | |
KZ15 | TEOS | EtOH | HCl | H2O | 25% lemon peel |
12.8 mL | 16.3 mL | 5.6 mL | 3.75 mL | 1.25 g |
Conditions employed in silica synthesis using ammonium hydroxide as a catalyst.
Sample | Precursor | Solvent | Alkali | Water | Bio-Waste |
---|---|---|---|---|---|
KZ16 | TEOS | EtOH | NH4OH | H2O | Pure silica |
17.0 mL | 21.8 ml | 11.8 mL | 5.0 mL | 5.0 g | |
KZ17 | TEOS | EtOH | NH4OH | H2O | 50% orange peel |
8.5 ml | 10.9 mL | 5.9 mL | 2.5 mL | 2.5 g | |
KZ18 | TEOS | EtOH | NH4OH | H2O | 25% orange peel |
12.8 mL | 16.3 mL | 8.8 mL | 3.75 mL | 1.25 g | |
KZ19 | TEOS | EtOH | NH4OH | H2O | 50% lemon peel |
8.5 mL | 10.9 mL | 5.9 mL | 2.5 mL | 2.5 g | |
KZ20 | TEOS | EtOH | NH4OH | H2O | 25% lemon peel |
12.8 mL | 16.3 mL | 8.8 mL | 3.75 mL | 1.25 g |
Initial electrode potential (Ei) values of the silica-based solid synthesized.
Sample | Ei (mV) | Sample | Ei (mV) |
---|---|---|---|
KZ1 | 128 | KZ11 | 632 |
KZ2 | 110 | KZ12 | 582 |
KZ3 | 132 | KZ13 | 604 |
KZ4 | 89 | KZ14 | 585 |
KZ5 | 117 | KZ15 | 604 |
KZ6 | 275 | KZ16 | 107 |
KZ7 | 72 | KZ17 | 112 |
KZ8 | 104 | KZ18 | 38 |
KZ9 | 118 | KZ19 | 116 |
KZ10 | 187 | KZ20 | 96 |
FT₋IR of silica synthesized with acetic acid (KZ1).
Bands | Wavenumber (cm−1) | Band Assignment | Functional Group |
---|---|---|---|
1 | 3437 | ν OH 1 | O-H bonded |
2 | 1864 | νβ (Si-O) 2 | Si-OH |
3 | 1639 | δ H-O-H 3 | H-O-H |
4 | 1166 | νS (Si-O-Si) 4 | Si-O-Si |
5 | 1079 | νa (Si-O-Si) 5 | Si-O-Si |
6 | 948 | νβ (Si-O) 2 | Si-OH |
7 | 797 | νs (Si-O) 6 | Si-O-Si |
8 | 566 | ν (Si-O) 1 | SiO2 |
1 ν: vibration stretching; 2 νβ: symmetric vibration stretching; 3 δ: deformation vibration; 4 νS: symmetric deformation vibration; 5 νa: anti-symmetrical vibration stretching; 6 νs: symmetrical vibration.
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Abstract
This study focused on the use of citrus bio-waste and obtention of silica-based materials through the sol-gel technique for promoting a greener and more sustainable catalysis. The sol-gel method is a versatile synthesis route characterized by the low temperatures the materials are synthesized in, which allows the incorporation of organic components. This method is carried out by acid or alkali hydrolysis combined with bio-waste, such as orange and lemon peels, generated as co-products in the food processing industry. The main objective was to obtain silica-based materials from the precursor TEOS with different catalysts—acetic, citric and hydro-chloric acids and ammonium hydroxide—adding different percentages of lemon and orange peels in order to find the influence of bio-waste on acids/alkali precursor hydrolysis. This was to partially replace these catalysts for orange or lemon peels. The solids obtained were characterized with different techniques, such as SEM, FT₋IR, potentiometric titration and XRD. SEM images were compared with pure silica obtained to contrast the morphology of the acidic and alkali hydrolysis. However, until now, few attempts have been made to highlight the renewability of reagents used in the synthesis or to incorporate bio-based catalytic processes on larger scales.
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1 Department of Chemistry, Federal University of São Carlos, São Carlos 13565-905, SP, Brazil;
2 Centro de Investigación y Desarrollo en Ciencias Aplicadas “Dr. Jorge J. Ronco” CINDECA, CONICET-CIC-UNLP, Facultad de Ciencias Exactas, Universidad Nacional de La Plata, La Plata 1900, Argentina;
3 Department of Chemistry, Federal University of São Carlos, São Carlos 13565-905, SP, Brazil;