Research Article | Open Access
Rodrigo Heleno Alves, Thais Vitória da Silva Reis, Suzimara Rovani, Denise Alves Fungaro, "Green Synthesis and Characterization of Biosilica Produced from Sugarcane Waste Ash", Journal of Chemistry, vol. 2017, Article ID 6129035, 9 pages, 2017. https://doi.org/10.1155/2017/6129035
Green Synthesis and Characterization of Biosilica Produced from Sugarcane Waste Ash
In this study, ash from sugarcane waste was used in the synthesis of biosilica using alkaline extraction followed by acid precipitation. Different parameters that could influence the silica particle synthesis were evaluated. The ash and synthesized biosilica were characterized by a combination of spectroscopic and chemical techniques such as XRD, XRF, SEM, particle size analyser, N2 adsorption analysis, TGA, and FTIR. The best condition for biosilica production was achieved with fusion method and aging temperature of 80°C for 1 h during gel formation. X-ray powder diffraction pattern confirms the amorphous nature of synthesized silica. The purity of the prepared silica was 99% silica which was confirmed by means of XRF. The experimental data suggest that the sugarcane waste ash could be converted into a value-added product, minimizing the environmental impact of disposal problems.
Brazil is the global leader in the production of sugarcane, harvesting more than 600 million tonnes of it every year. The state of São Paulo, in the South-Central region, is the largest producer in the country and is responsible for 61% of Brazil’s sugarcane production .
The processing of sugarcane to produce sugar and ethanol generates various agricultural wastes, especially straw and bagasse. Each ton of sugarcane generates between 250 and 270 kg of bagasse and 200 kg of straw and tips .
About 50% of these residues are used in distillery plants as a source of energy; the remainder is stockpiled. The burning of the waste generates 1–4% ash. Considering the amount of sugarcane produced in this harvest, between 3 and 12 million tons of ash are produced each year.
Generally, the destination of biomass ash generated in the sugar industry is the disposal in landfills or used as fertilizer in the plantations. These practices have caused problems to public health and unwanted environmental impacts mainly associated with soil and water . Moreover, sugarcane waste ash can be used as a substitute for cement or sand in civil construction [4, 5].
The ash of the sugarcane waste contains high levels of silica . Silica is considered a value-added product for presenting numerous applications in various industries like rubber industry as a reinforcing agent, in tooth pastes as a cleansing agent, as an anticaking agent in salts, in cosmetics, and so forth . Thus, efforts have been done in order to find economical way to extract silica of waste ash materials.
The objective of this study was to evaluate the effect of different synthesis parameters to optimize conditions for obtaining biosilica from sugarcane biomass ash. This not only provides value addition but also solves the problem of large amount of ash disposal.
All the regents used were of analytical grade. Sodium hydroxide and acetic acid (analytical grade) were obtained from Merck (Darmstadt, Germany). The sample of ash derived from burning of the sugarcane waste was provided by the company COSAN S.A. (São Paulo, Brazil). Quantitative filter paper Whatman Number 41 was purchased from Whatman Plc (Kent, England). Oven (Fanen Orion 515 Model), muffle furnace (Quimis, Q-318 M24 Model), and mechanical shaker (Ethik Technology 430 Model) were used.
The synthesis of biosilica was carried out by different methods. A schematic flow chart for preparation of silica gel from sugarcane waste ash (SWA) is proposed as shown in Figure 1. The experimental conditions are summarized in Table 1.
| = mass of product formed; n.a = not totally amorphous; BS12 = aging temperature of 80°C.|
2.2.1. Preparation of Sodium Silicate Solution by Two-Step Process
Typically, 1.0 g of SWA was mixed with 1.3 g of NaOH in capsule and triturated to obtain a homogeneous mixture. This mixture was then calcined at 550°C for 1 h in a muffle furnace. After cooling to room temperature, the fusion products were ground and placed in beaker with 100 mL of distilled water. The suspension was stirred for 24 h (120 rpm) at room temperature. The resulting slurry of first step was submitted to hydrothermal treatment in an oven at different temperatures (90 and 100°C) and reaction times (1–24 h). The reaction products were filtered with a quantitative filter paper Whatman Number 41 and the filtered liquid (sodium silicate solution) was stored for biosilica preparation.
2.2.2. Preparation of Sodium Silicate Solution by One-Step Process
In a Teflon beaker, 1.0 g of SWA was mixed with 10 mL of 3 mol L−1 aqueous NaOH solution. The mixture was incubated at 100°C in oven for 3 h. At the end of the treatment, the mixture was filtered and the filtered liquid was allowed to cool to room temperature and was stored.
2.2.3. Synthesis of Biosilica
In the as-obtained solution of sodium silicate, 3 mol L−1 acetic acid was added dropwise under constant stirring until pH 7. The silica gel formed was aged for at least 20 h at room temperature. After this time, the silica gel was washed with distilled water and filtered. The filtrate was stocked and the silica retained on the filter was dried for 24 h at 80°C [7–10].
2.2.4. Synthesis of Biosilica with Aging Process at 80°C
The sodium silicate solution was obtained using the two-step process described in Section 2.2.1. The conditions used in the second step were 90°C for 20 h. In the sodium silicate solution 3 mol L−1 acetic acid up was added to pH 7. The resulting gel mixture was aged at 80°C for 1 h (aging step). The gel was washed twice with 100 mL of distilled water, filtered (sodium acetate solution), and separated from solid (silica gel). The silica gel was dried at 135°C for 24 h . The sodium acetate solution was dried at 100°C to obtain sodium acetate as salt.
2.3. Characterization of Materials
The chemical composition of materials in the form of oxides was analysed by energy dispersive X-ray fluorescence spectrometry (XRF) (RX Axios Advanced, PANalytical, Phillips spectrometer) and wavelength dispersive X-ray fluorescence spectroscopy (WDXRF) (Rigaku Co. spectrometer, model RIX 3000). The mineralogical compositions of the samples were determined by X-ray diffraction analyses (XRD) with an automated Rigaku multiflex diffractometer with Cu anode using Co Kα radiation at 40 kV and 20 mA over the range (2θ) of 5–80° with a scan time of 0.5°/min. The crystalline phases present in the samples were identified with the help of ICDD (International Centre for Diffraction Data). The Fourier transform infrared spectroscopy (FTIR) spectra were recorded on ALPHA FTIR Spectrometer from Bruker, operating in attenuated total reflectance (ATR). The spectra were obtained using 200 cumulative scans, range 375 to 4000 cm−1. Scanning electron micrograph was obtained by a JEOL JSM-7401 scanning electron microscope, at a typical acceleration voltage of 3 KV. The particle size analysis was conducted by laser particle analyser Malvern MSS Mastersizer 2000 Ver. 5.54 (United Kingdom) (0.02–2000 μm) in isopropyl alcohol dispersing medium and pump speed of 2500 rpm. Adsorption-desorption isotherms were measured with Micrometrics TriStar volumetric adsorption analyser using nitrogen of 99.999% purity. Measurements were performed in range of relative pressure from 10E-6 to 0.99 liquid nitrogen on the samples degased for 2 h, under vacuum about 50 mTorr, at 200°C. The specific surface area and average pore diameter were evaluated using BET method. The total pore volume was estimated from the amount of nitrogen adsorbed at the relative pressure of 0.99. Thermogravimetric analyses were recorded in a thermogravimetric analyser TGA/SDTA 851 produced by Mettler Toledo. Dried samples (~10.0 mg) were analysed under dynamic nitrogen atmosphere with a flow of 100.0 mL min−1, using a alumina-port sample heated 1000°C with a heating rate of 5° or 10°C min−1. Determination of carbon and sulfur was done by LECO model TCHEN600. Other physical-chemical properties (bulk density, cation exchange capacity, pH, and pH of point of zero charge) have been described in a previous paper .
3. Results and Discussion
3.1. Characterization of Sugarcane Waste Ash
The chemical composition of sugarcane waste ash (SWA) is shown in Table 2. The major component was SiO2 content with 81.60 wt%., indicating that this material is suitable to use as a source of silica for producing sodium silicate solution. The compounds of aluminum, iron, potassium, and magnesium were found in amounts ≥1.3%. The other oxides were considered impurities for presenting content ≤1.00%. The percentage of carbon and sulfur was 0.16 and 0.04%, respectively.
|LI = loss on ignition at 1050°C for one hour.|
The sugarcane absorbs more silicon than any other cultivated plant. Sugarcane can remove from 500 to 700 kg Si ha−1 during their development . Monosilicic acid (H4SiO4) is the form of silicon used by plants, which is found in both liquid and adsorbed phases of silicon in soils [14–17].
The SWA diffractogram (Figure 2) indicated the presence of silica only in the crystalline phase (SiO2, ICDD01-085-0794). The peaks observed at 20.9°, 26.6°, 36.5°, 39.4°, 40.2°, 42.4°, 45.8°, and 50.2° are typical of quartz. The crystalline phase of silica in the sugarcane ash is related to the conditions of combustion (mainly time and temperature). At temperatures of 500–800°C or when the exposure to high temperature is small, the silica contained in the ash is predominantly amorphous. At temperatures greater than 800°C, the amorphous silica present in sugarcane is converted in crystalline silica polymorphs, such as quartz, cristobalite, and tridymite .
The discrete particle diameter distribution and the cumulative distribution of SWA were shown in Figure 3. The diameters corresponding to the cumulative distribution in the contents of 10.0%, 50.0%, and 90.0% (, , , resp.) and Sauter mean diameter () presented the following values: 12.170, 62.528, 208.140, and 26.084 μm, respectively. The range of the estimated particle size was between 0.893 and 563.677 μm.
3.2. X-Ray Diffraction Analysis of Biomass Ash-Based Products
Tests were performed using different experimental conditions in order to determine the optimal conditions of synthesis for obtaining the biosilica. The broad X-ray diffraction peak at theta equal to 22 degrees confirms the formation of amorphous silica, in general . The results are summarized in Figures 4 and 5. The yield of the synthesis was estimated using the mass of the actual product obtained (Table 1).
In the set of experiments at 100°C (Table 1, BS1–BS7 samples, Figure 4), XRD showed that the extracted silica is predominantly amorphous for BS2 to BS5 samples. For shorter reaction time (1 h) there was no gel formation (BS1 sample). A difference in the patterns of diffraction was recognized after 24 h of hydrothermal treatment due to the formation of only crystalline material (BS6 sample). There was no gel formation in BS7 sample, and therefore it did not form silica. This fact suggests that the alkaline fusion method should be applied to transform the high crystalline silica content of SWA in sodium silicate solution prior to the hydrothermal step.
In the set of experiments at 90°C (Table 1, BS8–BS12, Figure 5), essentially noncrystalline (amorphous) biosilica was formed (except BS8 sample) with yield directly proportional to the time of hydrothermal treatment. XRD of BS8 sample show amorphous silica along with some crystalline silica.
The greatest silica yield (91%) was obtained for the synthesis with aging process at 80°C (BS12 sample). Furthermore, the gelation time presented a drastic reduction (at least 20 h for 1 h) and the synthesis was reproducible. Aside from biosilica xerogel, 1.663 g of sodium acetate can also be derived from synthesis through evaporation of the aqueous solution (Figure 1). Thus, besides the mineralogical analysis, other characterizations were carried out for the silica gel obtained by this experimental procedure.
3.3. Characterization of Biosilica Gel
3.3.1. Physical and Chemical Characteristics
X-Ray fluorescence showed that the produced biosilica had high purity (99.1%), free of MgO, P2O5, TiO2, SO3, MnO, Ta2O5, and As2O3 that were present in the sugarcane waste ash (Table 2). Also, minor amounts of Na2O, Al2O3, and Cl and traces of Fe, K, Ca, Ni Cu, and Zn were found in synthesized material. Some impurities were resulting from the sodium hydroxide used in the synthesis. The high purity was obtained after washing the silica gel (B12 sample) repeatedly with deionized water to remove sodium salt [8–10].
The other physical-chemical properties of biosilica and the ash that served as raw material are shown in Table 3. The pH of the leached of the ash is slightly acid and the pH of silica gel is slightly alkaline. To produce silica, it is necessary to add acid to silicate solution. When acid was added to silicate solution (pH > 11), silica gel started to form rapidly as soon as pH 10 was reached and formed a rigid gel at pH ~ 7.0. The incomplete neutralization or the presence of residual OH- may be responsible for slightly alkaline pH of the leached biosilica. The surface of the biosilica has a negative charge in aqueous solution because the pH value is above the pH in the point of zero charge indicating that is a material with cationic exchange capacity. The bulk density of the biosilica was lower than 1.3 g cm−3, showing that this product is classified as lightweight material. This property may be beneficial for the use of the prepared gel in many environmental and industrial applications .
|CEC = cationic exchange capacity; = point of zero charge.|
3.3.2. Morphology Analysis of Silica Gel
The surface morphology of the biosilica was obtained using SEM images with different magnifications (Figure 6). The silica particles with size between <1 to 100 μm were grouped into clusters, forming an irregular and cohesive surface. In addition, smooth surfaces were also observed. The agglomeration of particles forming clusters is a result of alkaline treatment and the lack of uniformity is a result of the laboratory grinding process.
3.3.3. Thermogravimetric Analysis
The thermogravimetry profiles of sugarcane waste ash (SWA), biosilica (BS), and biosilica repeatedly washed with water (BSW) are shown in Figure 7. For the BS and BSW sample, the first mass loss (33–90°C) is ascribed to moisture loss . The second mass loss (90–180°C) corresponds to the loss of physically adsorbed water from the surface . The third step (180–530°C) was related to the loss of the organic structure (CH3COONa) and the loss of the chemically adsorbed water bonded to Si-OH (silanol) through the hydrogen bond [21, 22]. The fourth weight loss (530–1000°C) is due to the surface dehydroxylation reaction . For the SWA, only a mass loss of 1.20% probably related to moisture loss was observed.
3.3.4. FTIR Analysis
The FTIR spectra of sugarcane waste ash (SWA), biosilica (BS), and biosilica after washing repeatedly with deionized water (BSW) are shown in Figures 8(a), 8(b), and 8(c), respectively. For all samples, the bands observed at about 450–455 cm−1 and 1050–1070 cm−1 were attributed to the Si-O-Si symmetric and asymmetric stretching, respectively [8, 23–25].
According to the literature, the bands observed at 400, 520, 690, and 780 cm−1 for SWA sample were due to Si-O-M (metal impurities bonding), Al-O-Si bending vibrations, Si-O-Al deformation, and Si-O stretching indicating the presence of crystalline quartz, respectively [21, 22, 26, 27]. These results are in agreement with chemical analysis (Table 2) and XRD patterns (Figure 2).
The appearance of absorption bands at 550 and 560 cm−1 assigned to the (Si)-Al-O stretching indicated the presence of small content of aluminum in BS and BSW samples . Also, this is in agreement with chemical analysis.
The presence of band about 790–797 cm−1 for BS and BSW samples was due to Si-O-Si symmetric stretching [21, 29]. The bands at 615, 645, 925, 1415, and 1560 cm−1, for BS sample, were due to the presence of sodium acetate (CH3COONa), which is impurity of the synthesis process . The absence of these peaks in BSW sample confirmed once again that the repeated washing step removes completely soluble salts of synthesized silica gel.
The band at 957 cm−1 for BSW sample is due to the presence of silanol group Si-OH bending vibration absorption [27, 29]. According to the TGA thermogram (Figure 7), BS sample also has the silanol group in its structure; however the silanol band was probably overlaid by the C-C stretching band at 925 cm−1. Table 4 shows FTIR assignments of the peaks observed in Figures 8(a), 8(b), and 8(c).
|SWA = sugarcane waste ash; BS = biosilica; BSW = biosilica washed with water.|
3.3.5. N2 Adsorption-Desorption Isotherms
Figure 9 presents the nitrogen adsorption/desorption isotherms measured at 77 K for the sugarcane waste ash and biosilica. The sugarcane waste ash exhibits a typical type II isotherm of nonporous materials according to the IUPAC classification (Figure 9(a)) [31, 32].
The isotherm obtained for BS (Figure 9(b)) was attributed to type IV, which is associated with a complex mesoporous structure where the distribution of pore size and shape were not well defined. In addition, the multilayer adsorption might occur in the middle relative pressure range. The desorption cycle of the isotherm displays a H2 type of the hysteresis loop, which is often associated with a complex mesoporous structure where the distribution of pore size and shape is not well defined [33, 34].
The surface area of all the materials was evaluated using BET method and the pore size by BJH method (isotherms with hysteresis), and their textural properties are summarized in Table 5. It is seen that the sugarcane waste ash shows low specific surface area and porosities. The synthesized silica showed high specific area with dimensions and pore volume within the specifications of mesoporous materials, which can also be proved by type IV isotherms, characterizing its mesoporosity in Figure 9.
| = specific area; = total pore volume; = average pore diameter.|
Pure amorphous silica was successfully extracted at a 99.1% yield from sugarcane waste ash generated by a two-stage heating process followed by precipitation by acidification of the sodium silicate solution, so obtained. The XFR, FTIR, and XRD data gave clear evidence to the high purity of amorphous silica extracted from sugarcane waste ash. The use of the one-step process did not result in the formation of biosilica. Experimental results show that optimum conditions for producing biosilica were 90°C for 20 h in the hydrothermal treatment of two-step method, aging temperature of 80°C, and an aging time of 1 h. The mesoporous structure of silica makes it a potential catalytic (or catalyst support) or adsorbent material.
Conflicts of Interest
The authors declare that there are no conflicts of interest regarding the publication of this paper.
The authors are grateful to Conselho Nacional de Desenvolvimento Científico e Tecnológico (CNPq) and Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES) for financial support, Dr. Paola Corio and Dr. Jonnatan J. Santos (Institute of Chemistry, USP) for SEM and FTIR-ATR analysis, Dr. M. A. Logli for nitrogen adsorption desorption isotherms analysis, and COSAN S. A. (São Paulo, Brazil) for supplying the sugarcane waste ash.
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