I. Introduction
Biochar is a low-value by-product obtained by the thermochemical conversion of biomass into heat, power, fuels and/or chemicals using an oxygen-limited environment 1-3. The most common thermochemical processes are pyrolysis and gasification 2-4. Biochar material can be used in agriculture, carbon sequestration and wastewater treatment 2; this material is also effective in retaining nutrients and keeping them available to plants 5, thus by directly applying it into the soil, the conventional agricultural productivity and soil fertility may increase 6. However, the specific application of biochar depends on its physicochemical properties, which could change depending on the process used for obtaining it, i.e., operating conditions and biomass feedstocks; therefore, the understanding of chemical and physical properties of the biochar is crucial to find its most suitable applications 6,7.
Several characterization tests can be used to know the properties of biochar: the Brunauer-Emmet-Teller (BET) nitrogen gas physisorption method traditionally studies the morphological characteristics and physical properties of biochar; while Scanning Electron Microscopy (SEM) and Energy Dispersive EDX (x-ray spectrometry) are commonly used to observe the morphology and the surface of the biochar 7-9; and Fourier Transform Infrared Spectroscopy (FTIR) is frequently used to identify and qualitatively track changes in functional groups in biochar and soil samples 3.
Some authors have studied the effects of pyrolysis temperature on biochar properties. Jindo et al. (7 pyrolyzed rice husk, rice straw, and wood chips of apple tree and oak tree at temperatures between 400 °C and 800 °C. They found by BET and FTIR that an increase in process temperatures results in higher surface area, more development of aromatic compounds and a decrease in aliphatic groups. Ghani et al.10 evaluated the properties of biochar from waste rubber-wood-sawdust by pyrolysis between 450 °C and 850 °C, founding by BET analysis that the total surface is lower than 10 m2/g for lower temperatures and around 200 m2/g for higher temperatures. Kim et al.11 evaluated the properties of biochar from pitch pine produced by fast pyrolysis at different temperatures (300-500 °C); they obtained BET surface areas between 3.0 and 175 m2/g that increased with the pyrolysis temperature; from the FTIR spectra, they found that the O-H stretch peak (3600-3200 cm-1) decreases in the spectra for biochar. Azargohar et al.12 produced biochar from pyrolysis of agricultural waste (wheat straw and flax straw) and forest residues (sawdust), at temperatures between 400 °C and 550 °C; they found that increasing the pyrolysis temperatures resulted in ruptures on the biomass surfaces, caused by thermal cracking of their parent biomass; by FTIR analysis, they found that intensity of the peaks 33003400 cm-1 (-OH stretching), 2850-2950 cm-1 (-CH
stretching), and 1470 cm-1 (deformation vibration from alkanes) decreased with an increase in the pyrolysis temperature, which can be due to the improvement of aromatic structure in biochar. Finally, Shaaban et al.13 produced biochar from rubber wood sawdust at different temperatures and different holding times; the highest BET surface area (6.0 m2/g) corresponded to the highest temperature (700 °C) and the highest holding time (3 h).
Other authors have studied the properties of biochars obtained by different thermochemical processes, for instance, Brewer et al.14 studied the characteristics of biochar obtained from fast pyrolysis, slow pyrolysis and gasification (in a bubbling fluidized bed reactor) of corn stover, switchgrass and wood. The biochar surface areas were between 3.0 and 62.0 m2/g, and increased with the reaction residence time (fast pyrolysis < slow pyrolysis) and the temperature (pyrolysis < gasification). Luo et al.15 analyzed the effect of operation conditions, including heating temperature (200-700 °C), time (1-8 h), and atmosphere (air flow, air-limited and N2) on the physicochemical properties of biochar from pine sawdust, maize straw and sugarcane bagasse. They observed that the surface areas of the biochar significantly increased with temperature; in addition, operation under air condition or longer heating times (increased carbonization) tended to increase the micro-pore volumes and thus the surface areas of the biochar. Qian et al.16 analyzed the physicochemical properties of biochar derived from fluidized-bed gasification of switchgrass forage sorghum; in this case, biochar surface areas did not exceed 10 m2/g and FTIR observations suggested that raw material has more aliphatic structure than gasified char.
In this study, the morphology and physical properties of biochar obtained as by-product from downdraft gasification of Eucalyptus grandis, Acacia magnium and Gmelina arbórea are evaluated using BET, SEM, EDX and FTIR analyses. Such characterizations allowed predicting possible uses for these biochars. The selected forestry species present high silvicultural potential in Colombia 17, therefore, with this study, we expect to help promoting studies on thermal transformation of biomass, considering the potential in processes improvement when including biorefinery concepts regarding to low-value byproducts.
II. Materials and methods
A. Wood gasification
Biochar samples were obtained as by-product from downdraft gasification of Eucalyptus grandis (BC-EG), Acacia magnium (BC-AM) and Gmelina arbórea (BC-GA). The processes were carried out at atmospheric pressure, using biomass with similar shapes and sizes (chips with sizes between 4 and 10 mm). The gasifying agent was air with a superficial velocity of 0.1 m/s for all experiments. The complete description of the experimental process and the physicochemical characterization of biomass have been described in (17). The maximum temperature reached in the gasification processes was approximately 700 °C. Cold gas efficiencies between 25.8 % and 30.9 % were obtained. The lowest gas heating value obtained was between 2.5 and 3.0 MJ/ Nm3 with a mainly composition of CO, CO2, CH4, H2 and N2, with average concentrations of 13 %, 16 %, 2 %, 4 %, and 64 vol%, respectively 17.
B. Biochar characterization
1) Surface area: The surface areas and pore size distribution of all materials were determined by the BET method from N2 isotherms measured at 75.2 K using a Quantachrome Autosorb Automated instrument. Each experiment used 100 mg of solid biochar.
2) Scanning Electron Microscopy: The samples were analyzed by high-resolution scanning electron microscopy (HRSEM) in a JEOL 7600F electron microscope with an acceleration of 30 kV and a theoretical resolution of 1 nm. For this analysis, a solid sample homogeneously dispersed in pure ethanol was deposited on a Cu grid, previously covered with a thin layer of biochar. In addition, the analysis of elements was carried out by X-ray energy dispersive system spectroscopy (EDS), using a Si (Li) model INCA, Oxford.
3) Fourier Transform Infrared (FTIR): Infrared spectra of the biochar were recorded at room temperature and 2.0 cm-1 resolution on a IRAffiniti-1 Shimadzu spectrometer. Each sample for FTIR analysis was prepared by grinding and mixing 1 mg of the biochar with 200 mg of IR-grade KBr, and then the sample was pressed into a pellet using a hydraulic press. The FTIR spectrum of the pellet was recorded over a wavenumber range of 650 cm-1 - 4000 cm-1.
III. Results and discussion
A. BET surface area and porosity
The main surface characteristics of biochar are listed in Table 1. According to the average pore size, all samples can be classified as mesoporous materials because their pore sizes are between 2 and 50 nm.
Sample | BET Surface area (m2/g) | Average pore diameter (nm) | Total pore volume (cm3/g) |
BC-AM | 50.0 | 4.25 | 0.052 |
BC-GA | 2.0 | 47.0 | 0.020 |
BC-EG | 30.0 | 5.3 | 0.040 |
Biochar derived from Acacia magnium (BC-AM) had the highest surface area (50.0 m2/g), while the biochar derived from Gmelina arbórea (BC-GA) had the lowest surface area (2.0 m2/g) (Table 1). Some authors have obtained surface areas in the same order of magnitude for biochar obtained from gasification processes. For instance, Qian et al.16 obtained biochar with surface areas between 0.7 and 60 m2/g from switchgrass, sorghum straw and red cedar; and Brewer et al.14 obtained biochar with surface areas between 24 and 31 m2/g from corn stover and switchgrass. Taking into account that the surface area of BC-AM is 96.4 % greater than BC-GA, and 38.2 % higher than BC-EG, it is expected that the BC-AM presents a greater adsorption capacity, considering that the adsorption capacity is expected to increase with the surface area. In future studies, the BC-AM biochar-sorption capability of selected contaminants, such as dyes in aqueous systems, will be evaluated.
B. SEM-EDX
Figure 1 shows the SEM micrographs of biochar obtained by gasification. In general, no sample revealed a definite shape, being BC-GA the most amorphous with poorly defined micrographs showing weak pores. This is consistent with its higher average pore diameter observed by BET analysis (Table 1). Table 2 shows the localized carbon and oxygen content of the samples determined by EDX-SEM analysis.
The SEM-EDX analysis showed that the BC-AM had the best development of pores (better-defined pores), with smaller pores than those developed by the other two biochars; while the BC-EG had larger developed pores, less defined and less uniform compared with the pores developed by BC-AM; and the BC-GA had uneven and weak pores that appear to be larger than the other samples (Fig. 1 and Table 2). These results are consistent with the BET results, in which BC-AM had greater surface area and smaller pore size than the other samples, while the BC-GA had the lowest surface area and a larger pore size (Table 1). The sample with the highest carbon content and the lowest oxygen content was the BC-GA. This result can be explained by physical properties of raw material (forest species) used as feedstock for the gasification process.
According to the literature, Gmelina arbórea has the lowest bulk density among the studied species 17. This promotes heat transfer during the gasification process because lower ratios of air/fuel are achieved (i.e., fewer amount of biomass in the same volume of reactor); thus, the process tends to combustion, increasing both temperature and reaction velocity. The highest carbonization degree is reflected in an increase in the carbon composition and a decrease in the oxygen composition of the biochar. A decrease in oxygen composition increases the surface hydrophobicity of the biochar 13.
Sample | C | O | Na | K | Ca |
BC-AM | 81.63 | 18.07 | 0.11 | 0.09 | 0.1 |
BC-GA | 88.36 | 9.12 | - | 1.33 | 0.89 |
BC-EG | 87.51 | 10.25 | - | 0.41 | 0.54 |
A higher surface hydrophobicity could become a desirable attribute of a biochar for processes such as removing of contaminants from aqueous matrices; however, high surface areas are also desirable for such application 3, and according to Table 1, the BC-GA had the lowest BET surface area among the studied species. Therefore, considering BC-GA for sorption applications will probably require additional biochar activation processes to improve the BET surface area. On the other side, the presence in the biochar of minerals as Na, K and Ca (Table 2) is considered an important characteristic for biochar applications such as soil amendment, since they are nutrient elements for plant growth 16,18. Among the tested samples, the highest mineral composition was found for the BC-GA; this result is consistent with the composition of C and O, which results from the increase in gasification temperature, which increases volatilization of light compounds of raw material and reaction with the carbon during gasification, reducing the oxygen content of char and thus increasing the mineral contents 16. Therefore, we can conclude that among the analyzed samples, BC-GA is the most suitable for soil remedial applications.
C. FTIR Spectra
Figure 2 shows the FTIR spectra in the 4000-2500 cm-1 and the 1800-1000 cm-1 range for the three biochars obtained under similar gasification conditions.
The FTIR spectra shows that the frequency range between 3600 cm-1 and 3200 cm-1 reveal the peaks corresponding to OH bonds (Fig. 2). The relative small size of these peaks is attributed to loss of moisture due to the high temperatures reached in the gasification process 11. Clear peaks commonly attributed to hemicellulose and cellulose (i.e., 3200-3000 cm-1 for OH or 3100-3000 cm-1 for CH) are absent in all the biochar samples, which lead us to conclude that the hemicellulose and cellulose present on the raw material (wood) degradated at the gasification temperatures 19. This is an expect result because the degradation of hemicellulose and cellulose generally take place at temperatures between 200-300 °C and 300-400 °C, respectively 11. Peaks between 1400 cm-1 and 900 cm-1 are generally attributed to lignin, mainly due to rings of type C=C 19; these peaks are slightly more pronounced than those found for hemicellulose and cellulose, which can be attributed to the degradation of lignin at temperatures between 200 °C and 700 °C 12.
The peaks observed between 2850-2970 cm-1 are attributed to aliphatic functional groups (CH bonds), and are poorly pronounced in the analyzed samples, because the degradation of aliphatic compounds occurs at high gasification temperatures, leading to the formation of aromatic compounds 12. The peaks observed between 1750 cm-1 and 1650 cm-1 are attributed to the acid axial deformation C=O, primarily aldehydes and ketones formed by dissociation of cellulose and hemicellulose 12. In the range of 16001580 cm-1, the observed bands are linked with aromatic C=C and C=O, associated with ketones and quinones 19. The FTIR analysis allowed us to conclude that the gasification process leads to the degradation of cellulose and hemicellulose, while some aromatics related with lignin remain in the biochar samples. According to 3, such characteristics could improve the biochar application as soil amendment.
From biorefinery concepts and aiming to improve low-value byproducts in the gasification process, the silvicultural potential of Colombia could focus on producing species such as Acacia magnium or Gmelina arbórea to use them in the gasification process (for syngas or energy production), due to the potential use of the solid biochar by-product in different applications, i.e., absorption or soil amendment.
IV. Conclusions
According to the characterization of biochar obtained by fixed-bed gasification of Eucalyptus grandis, Acacia magnium and Gmelina arbórea, we can conclude that such biochar can be suitable for different specific applications. SEM micrographs revealed the best development of pores in BC-AM, while BET analysis showed lower average pore diameter (4.25 nm) and higher surface area (50.0 m2/g) in BC-AM than in BC-EG or BC-GA; thus, the biochar obtained from Acacia magnium is expected to be the most suitable for absorption applications, even when adsorption capacity could be improved by additional activation processes. Based on the SEM-EDX analysis, we can conclude that due to the presence of minerals such as K, Na and Ca, biochars could be used as a soil amendment.