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Article

Production of Biochar from Vine Pruning: Waste Recovery in the Wine Industry

1
PROMETHEUS, Unidade de Investigação em Materiais, Energia e Ambiente para a Sustentabilidade, Escola Superior Agrária, Instituto Politécnico de Viana do Castelo, Rua da Escola Industrial e Comercial de Nun’Alvares, 4900-347 Viana do Castelo, Portugal
2
INIAV—Instituto Nacional de Investigação Agrícola e Veterinária, Av. da República, Quinta do Marquês (Edifício Sede), 2780-157 Oeiras, Portugal
3
MARETEC—Marine, Environment & Technology Center, Secção de Ambiente e Energia, Departamento de Engenharia Mecânica, Instituto Superior Técnico, Av. Rovisco Pais N.° 1, 1049-001 Lisboa, Portugal
4
GOVCOPP, Unidade de Investigação em Governança, Competitividade e Políticas Públicas, Universidade de Aveiro, Campus Universitário de Santiago, 3810-193 Aveiro, Portugal
5
DEGEIT, Departamento de Economia, Gestão, Engenharia Industrial e Turismo, Universidade de Aveiro, Campus Universitário de Santiago, 3810-193 Aveiro, Portugal
*
Author to whom correspondence should be addressed.
Agriculture 2021, 11(6), 489; https://doi.org/10.3390/agriculture11060489
Submission received: 3 April 2021 / Revised: 21 May 2021 / Accepted: 24 May 2021 / Published: 25 May 2021

Abstract

:
The production of residual biomass, such as vine pruning, presents environmental problems since its elimination is usually carried out through the uncontrolled burning of the remaining materials and with the emission of greenhouse gases without any counterpart. The use of these residues to produce biochar presents several advantages. In addition to the more common energy recovery, other conversion ways allowing new uses, such as soil amendment and carbon sequestration, can be analyzed as options as well. In the present study, vine pruning biomasses are characterized to evaluate the behavior of the different constituents. Then, the different possible applications are discussed. It is concluded that materials resulting from the pruning of vineyards have excellent characteristics for energy recovery, with an increment of more than 50% in the heating value and almost 60% in the carbon content when carbonized. This recovery procedure contributes to creating new value chains for residual materials to promote sustainable practices in the wine sector.

1. Introduction

The use of biomass as a form of energy acquired a recent interest, despite being the oldest form of energy, accompanying developing mankind since the discovery of fire [1,2]. Obviously, in modern times, there are many innovations in improving fuels, but mainly concerning converting and valuing this form of energy [3,4]. While the use of biomass may have been limited to the direct combustion of branches and trunks in the early days of mankind, today, conversion includes improving fuels through thermochemical conversion technologies, such as torrefaction, pyrolysis and gasification, which are later more efficiently used in combustion recovery processes [5,6].
This recovery process may allow incorporating a set of materials that are not commonly used, mainly due to several unfavorable characteristics, such as high moisture content, excess of inert materials, low-density, and lower calorific value. These properties contributed to the exclusive use of materials presenting characteristics classified as good [7]. This segregation, besides the preference for some species, also includes the preference for specific parts, such as trunks, neglecting less favorable parts, such as branches, leaves, bark, or roots [8].
One of the sectors where the use and reincorporation of waste materials into supply chains can be presented as a necessity is the agro-industrial sector, now following sustainability and circular economy [9,10,11]. Within this so diverse sector, the wine industry emerges as an excellent field for developing this trend. First, due to the diversity of residual forms available, such as bagasse, stalks, or pruning materials, but also due to the quantities cyclically produced, which may cause environmental problems, such as CO2 emissions during uncontrolled waste burning, its disposal in landfills, or simple abandonment in piles [12,13,14].
The use of vine pruning materials in pyrolysis processes is a possibility that allows the resolution of several environmental problems, namely those related to managing the large volumes generated annually, but also adding some value to the materials, since its elimination results mostly in costs [15,16,17]. In this way, recovering these materials creates new value chains and introduces a circular economy perspective, contributing to the sector’s sustainability [18,19,20]. Biochar production converts the waste into materials with higher added value, higher energy density, which are not perishable by biological agents, hydrophobic, and even can be used to replace coal, serving as a mitigating agent for climate changes [21,22]. This biochar can also be used in soil amendment functions, taking advantage of its adsorption capacity to capture polluting elements or to fix nutrients, and serves as a sink, sequestrating carbon in the soil, and thereby contribute once again to mitigate climate changes [13,23].
This study aims to characterize vine pruning material, analyze its chemical composition, and understand the behavior of the materials when submitted to a pyrolysis process. Possibilities for use are also discussed, with a perspective of adding value to the materials and introducing circular economy processes in the wine industry by implementing new practices. We discuss how introducing these circular economy practices can lead to the sustainability of the sector, namely through the resolution of environmental problems and creating new value chains for waste materials.

2. Materials and Methods

2.1. Sampling and Material Preparation

The biomass of vine pruning was collected during December 2020 in vineyards located in the Ponte de Lima region (North Portugal). The material was subsequently cut into portions with dimensions close to 3 cm, as shown in Figure 1, to facilitate drying and grinding.
For biochar production, we used a BARRACHA (model K-3) high-temperature furnace, which uses electrical resistances for generating heat. This furnace also presents a built-in thermal controller that enables programming four temperature stages with respective residence times. The preparation of the samples was made with the aid of conventional aluminum paper used to wrap the material into a cylindrical shape. Because the aluminum paper has two distinct sides, it should be noted that the opaque part of the sheet must be directed towards the outside so that during the carbonization process, the heat is not reflected.
The definition of temperature stages and a scheme of the programmable stages are presented in Table 1. Temperatures were chosen based on the definition presented by Nunes (2020) [24], while the residence times were selected based on the studies by Ribeiro et al. (2018), Sá et al. (2020) and Nunes et al. (2021) [20,25,26]. Figure 2 shows the material wrapped in the aluminum foil and the material after the biochar production phase.

2.2. Laboratory Characterization Tests

To carry out the laboratory characterization tests, the procedures described in the following reference standards were used:
  • ISO 17225-1: 2014—Solid biofuels—Fuel specifications and classes—Part 1: General requirements.
  • ISO 16948: 2015—Solid biofuels—Determination of total content of carbon, hydrogen and nitrogen.
  • ISO 16967: 2015—Solid biofuels—Determination of major elements—Al, Ca, Fe, Mg, P, K, Si, Na and Ti.
  • ISO 16968: 2015—Solid biofuels—Determination of minor elements—Ar, Cd, Cobalt, Cr, Copper, Hg, Mn, Mo, Ni, Pb, Sb, V and Zn.
  • ISO 16994: 2016—Solid biofuels—Determination of total content of sulfur and chlorine.
  • ISO 18125: 2017—Solid biofuels—Determination of calorific value.
  • ISO 21404: 2020(en)—Solid biofuels—Determination of ash melting behavior.
  • ASTM E870—82(2019)—Standard Test Methods for Analysis of Wood Fuels (with reference documents: ASTM D1102—84(2021)—Standard Test Method for Ash in Wood; ASTM E871—82(2019)—Standard Test Method for Moisture Analysis of Particulate Wood Fuels; ASTM E871—82(2019)—Standard Test Method for Moisture Analysis of Particulate Wood Fuels)—Determination of proximate analysis by thermogravimetry.

3. Results and Discussion

The materials resulting from vine pruning are normally used as firewood for heating and as fuel in bakery and restaurant ovens [27]. In Portugal, for example, traditionally, it is the preferred fuel for piglet roasters restaurants in the Bairrada region [28]. However, given the considerable volumes of biomass produced annually throughout the country, it is very difficult to collect and use it, given the dispersion of wine production throughout the territory, which is usually abandoned, or else eliminated by burning the leftovers [29,30]. Despite the recognized properties as a fuel, previously reported in several works, such as those by Duca et al. (2016), Torreiro et al. (2020), Nunes et al. (2020) or Atelge et al. (2020), where several characterizations of materials and different forms of energy recovery, such as anaerobic digestion, pyrolysis or gasification, are presented, still exists a deep lack of knowledge concerning creating value chains using these materials and about the best options to manage the amounts yearly generated [31,32,33,34].
The results obtained in the thermogravimetric analysis for vine pruning samples, dry and carbonized material, are presented in Table 2.
After drying in a laboratory oven for 12 h at 90 °C, the sample material showed an average value of 3.67 ± 0.16%. The volatile content showed an average value of 77.80 ± 0.08%. The ash content showed an average value of 1.42 ± 0.01%. The fixed carbon content showed an average value of 19.58 ± 0.20%. The moisture content after carbonization of the samples showed an average value of 1.34 ± 0.04%. The volatile content showed an average value of 33.90 ± 0.67%. The ash content showed an average value of 7.28 ± 0.07%. The fixed carbon content showed an average value of 58.82 ± 0.69%.
The thermogravimetric analysis (Figure 3) demonstrated that the moisture content changes to residual values, reaching a minimum value of 1.34%, in line with the results obtained by Ren et al. (2013), with values below 2.00% for temperatures of 300 °C, or in work by Barzegar et al. (2020), which obtained 1.90% moistures for the same conditions [35,36]. As expected, the volatile content had a significant reduction, going from the initial 77.80% to a value of 33.90%. This result is justified by the loss of mass verified since this occurs mainly due to the volatilization of hemicellulose, which is the compound responsible for forming most of the volatile organic compounds and structural water [37,38,39,40]. As the ash consists essentially of nonvolatilizable metal oxides, the increase observed in its content is justified with the verified mass loss since it is proportional [41,42]. With the release of oxygenated compounds, the fixed carbon content increased from 19.58% to 58.82%. This increase in the fixed carbon content is one of the advantages of the thermochemical conversion process since it allows the obtention of a material with higher carbon content and greater viability for energy recovery, but also because of the possibility that it opens for other uses, namely in soil amendment, due to the adsorbent capacity that biochar presents, and which has been widely studied [43,44,45].
The results obtained for CHNO analysis are presented in Table 3.
The C content for the dry samples showed an average value of 46.28 ± 1.09. The H content showed an average value of 6.28 ± 0.22. The N content showed an average value of 0.54 ± 0.26%. The O content showed an average value of 46.89 ± 1.55. The C content for the biochar samples showed an average value of 73.53 ± 0.13%. The H content showed an average value of 4.64 ± 0.05%. The N content showed an average value of 1.200 ± 0.02%. The O content showed an average value of 20.62 ± 0.16.
The trend of evolution of the CHNO contents after the carbonization of the material (Figure 4) demonstrated consistency with previous studies, and the consonance with the behavior revealed by other forms of biomass, with the values of the C content showing a significant increase, from 46.28% to 73.53%, while, in the opposite direction, the O content drops from the initial 46.89% to 20.62%, after the carbonization process. These results are in line with the recognized elimination of oxygenated products resulting from the degradation of hemicellulose [13,46,47,48]. The N content showed a slight increase, from 0.54% to 1.20%, associated with its concentration, justified by the average weight loss of 78.31 ± 1.00% observed, while the H content showed a slight decrease, from the initial 6.28% to 4.64%, associated with its contribution to forming volatile organic compounds [49]. In addition, the analysis of the H/C and O/C ratios, which show a sharp decrease, indicates increased calorific value, since after being projected in a van Krevelen diagram, biochar will present a position closer to the origin of the graphic when compared to the projection of the ratios obtained with the CHO contents for the dry samples of vine pruning.
The oxygen content of a fuel is a determining factor for the efficiency of its conversion during combustion. The availability of oxygen in the fuel increases the combination with hydrogen to produce water, which subsequently lowers the temperature of the flame. As shown in Figure 5, pyrolysis causes a reduction in the oxygen content and increases the carbon content without, however, significantly altering the hydrogen content. As saw earlier, the pyrolysis process, like what happens with the biomass torrefaction process, leads to the volatilization of one of the constituent compounds of biomass, which is hemicellulose, mainly in the temperature range between 220 °C and 320 °C, as described by Nunes et al. (2020) [24]. When this temperature is exceeded, accelerated cellulose decomposition begins. However, the procedure is similar and continues to lean towards the elimination of oxygen [50,51].
This reduction in the oxygen content significantly improves the combustibility of the biochar, but this may not even be the greatest advantage and the best way to enhance this material since, as recent studies indicate, its use as a soil amendment to take advantage of its adsorbent properties for the removal of polluting elements, or even the fixation of nutrients, can be an advantage with a more positive impact than energy recovery [52,53]. Another possibility that emerges from incorporating biochar in soils is related to the carbon sequestration capacity, contributing to the mitigation of climate changes since it is a negative emission technology [54,55].
The results obtained in the determination of S and Cl are shown in Table 4.
For dried samples, the S content showed an average value of 185 ± 5 ppm. The Cl content showed an average value of 41.0 ± 50.7 ppm. For carbonized samples, the S content showed an average value of 183 ± 4 ppm. The Cl content showed an average value of 5.2 ± 3.9 ppm.
It is very common for different forms of biomass to have low sulfur contents, as is evidenced in several studies, such as those by Arias et al. (2008) and Simonic et al. (2020) [56,57]. The result obtained proves this trend since the value obtained is low, being in line with the values allowed, for example, by the ENplus® standard, which is 0.04% [58]. Chlorine, on the other hand, can appear in abundant quantities, being one of the agents responsible for the corrosion of combustion equipment that most contributes to damage and maintenance stops [59,60]. However, a recent study by Sá et al. (2020) proved that chlorine could be eliminated from the final product through thermochemical conversion processes, as seen in the results obtained, in which from the initial 0.0041%, it changed to 0.0005%, that is, to a practically null value, as is presented in Figure 6 [26].
The results obtained for HHV and LHV are shown in Table 5.
The HHV of the dry samples showed an average value of 18.95 ± 0.002 MJ/kg. LHV showed an average value of 17.58 ± 0.002 MJ/kg. The HHV of carbonized samples presented an average value of 29.78 ± 0.007 MJ/kg. The LHV presented an average value of 28.78 ± 0.007 MJ/kg.
In previous works, such as those carried out by San José et al. (2013), where developing a novel conical combustor for thermal exploitation of vineyard pruning wastes is presented, the results obtained to follow the values obtained in the present work [61]. Also, in the work of Bilandzija (2012), who assesses the energy potential of several fruits pruned biomass in Croatia, including vine pruning, the average values of HHV and LHV for dry materials are confirmed [62]. The use of biowastes is a topic with growing and current interest, namely due to introducing the concepts of circular economy and sustainability in the wine industry and the agrarian environment in general. Several recent studies address the theme and present results on characterizing materials, even comparing variations between the different vine varieties used, as is the case of the works by Sun et al. (2020), Acquadro et al. (2020), Bisaglia & Romano (2018) or Loupit et al. (2020) [63,64,65], but also in the perspective of new valuation methodologies, as is the case presented by Allesina et al. (2018), which addresses using vine pruning as fuel in small-scale gasifiers [66], or the case presented by Margaritis et al. (2020), which deals with the impact of torrefaction on the characteristics of vine pruning fuel [67]. Regarding the pyrolysis or carbonization process, there are also several works already in existence, such as those by Tag et al. (2016), Azuara et al. (2017), Dunnigan et al. (2018), Hoffmann et al. (2019) and Sun et al. (2020), and that validate the results obtained here [23,63,68,69,70]. As can be seen in Figure 7, the heating value for carbonized materials increases by more than 50%. This demonstrates the advantages of using a thermochemical conversion process such as pyrolysis to valorize these residual materials, both for the potential energy generated and associated logistical advantages. Such logisticl advantages include reduction of volume, energy densification and ease of storage, since the materials, being hydrophobic, can be stored outside, and because they do not rot or are subject to biological activity, as demonstrated in the work of Nunes et al. (2021) [20].
The results obtained concerning the mass loss for the carbonized samples of vine pruning are shown in Table 6.
The mass loss presented an average value of 78.31 ± 1.00%. The values verified in the mass loss are in agreement with the values presented in previous works, such as those by Tag et al. (2016) or Nunes et al. (2020) [23,33]. The values presented in the referred works are included in the range 75–80% for process temperatures of 400 °C and equivalent residence time.
The results for major elements are shown in Table 7.
The Al content showed an average value of 60.55 ± 12.12 ppm. The Ca content showed an average value of 7445.35 ± 465.69 ppm. The Fe content showed an average value of 34.00 ± 4.52 ppm. The Mg content showed an average value of 1359.30 ± 54.46 ppm. The p content showed an average value of 1095.81 ± 18.26 ppm. The K content showed an average value of 8244.37 ± 197.87 ppm. The Si content showed an average value of 152.65 ± 35.60 ppm. The Na content showed an average value of 421.79 ± 22.45 ppm. The Ti content showed an average value of 3.01 ± 0.47 ppm.
The results obtained in determining the content of major elements for the carbonized samples of vine pruning are shown in Table 8.
The Al content showed an average value of 81.09 ± 10.82 ppm. The Ca content showed an average value of 14,154.86 ± 337.54 ppm. The Fe content showed an average value of 54.56 ± 6.00 ppm. The Mg content showed an average value of 2324.90 ± 10.62 ppm. The P content showed an average value of 2291.92 ± 27.94 ppm. The K content showed an average value of 16,772.98 ± 373.72 ppm. The Si content showed an average value of 178.81 ± 7.61 ppm. The Na content showed an average value of 421.37 ± 9.73 ppm. The Ti content showed an average value of 4.45 ± 0.83 ppm.
The results for minor elements are shown in Table 9.
The As content showed an average value of 0.73 ± 0.17 ppm. The Cd content showed an average value of 0.44 ± 0.14 ppm. The Co content showed an average value of 0.31 ± 0.11 ppm. The Cr content showed an average value of 0.29 ± 0.25 ppm. The Cu content showed an average value of 24.93 ± 1.89 ppm. The Mn content showed an average value of 41.34 ± 2.18 ppm. The Ni content showed an average value of 0.39 ± 0.28 ppm. The Pb content showed an average value of 0.16 ± 0.13 ppm. The Zn content showed an average value of 35.81 ± 41.73 ppm.
The results obtained in determining the content of minor elements for the carbonized samples are shown in Table 10.
The As content showed an average value of 2.79 ± 0.165 ppm. The Cd content showed an average value of 0.02 ± 0.046 ppm. The Co content showed an average value of 0.04 ± 0.072 ppm. The Cr content showed an average value of 0.04 ± 0.072 ppm. The Cu content showed an average value of 45.85 ± 0.768 ppm. The Mn content showed an average value of 86.94 ± 1.212 ppm. The Ni content showed an average value of 0.08 ± 0.135 ppm. The Pb content showed an average value of 0.73 ± 0.141 ppm. The Zn content showed an average value of 52.89 ± 2.581 ppm.
Figure 8 and Figure 9 show, respectively, the evolution of major and minor elements present in the analyzed vine pruning biomass. As can be seen, and in line with the average loss of mass observed in the tests, there is a tendency for metallic elements to concentrate since they are not eliminated during the volatilization process that occurs during pyrolysis. The same trend was confirmed by the work of Kraiem et al. (2016) or Picchi et al. (2013) [71,72]. This issue is extremely important, mainly because these elements, which will be found essentially in the form of metal oxides, are the main ones responsible for the phenomena of fouling and slagging that occur in energy recovery systems. Hence, its characterization is particularly important [73].

4. Conclusions

The wine sector is responsible for generating high volumes of waste, which until the present date, has not been treated in a way to be recovered. The uses of this type of waste are rare, in addition to the traditional ones, essentially as firewood, with the elimination of the remaining volumes carried out using, normally, the uncontrolled burning of these materials, without using the generated energy. In this way, using a process such as pyrolysis to recover residues from vine pruning creates a product with higher added value, allowing its use as fuel, but also in soil amendment, and even for carbon sequestration, contributing to the mitigation of climate changes. The results obtained confirm the quality of the fuel produced, revealing a significant increase in the heating value and the carbon content. This perspective on the use and recovery of waste resulting from the wine industry fits in with the assumption of policies to introduce processes based on the circular and regenerative economy to implement sustainability principles in the sector.

Author Contributions

Conceptualization, A.I.F., A.C.R., A.M.R. and L.J.R.N.; methodology, A.I.F., A.C.R., J.C.O.M. and L.J.R.N.; validation, A.I.F., A.C.R., A.M.R., J.C.O.M. and L.J.R.N.; formal analysis, A.I.F., A.C.R., A.M.R. and L.J.R.N.; investigation, A.I.F., A.C.R., A.M.R. and L.J.R.N.; resources, A.C.R. and L.J.R.N.; data curation, A.I.F., A.C.R., A.M.R. and J.C.O.M.; writing—original draft preparation, A.I.F., A.C.R. and L.J.R.N.; writing—review and editing, A.C.R., A.M.R., J.C.O.M. and L.J.R.N.; visualization, A.I.F. and L.J.R.N.; supervision, L.J.R.N. and J.C.O.M.; project administration, L.J.R.N. and J.C.O.M. All authors have read and agreed to the published version of the manuscript.

Funding

This research results from the project TECH—Technology, Environment, Creativity and Health, Norte-01-0145-FEDER-000043, supported by Norte Portugal Regional Operational Program (NORTE 2020), under the PORTUGAL 2020 Partnership Agreement, through the European Regional Development Fund (ERDF). L.J.R.N. was supported by proMetheus, Research Unit on Energy, Materials and Environment for Sustainability—UIDP/05975/2020, funded by national funds through FCT—Fundação para a Ciência e Tecnologia.

Institutional Review Board Statement

Not applicable.

Informed Consent Statement

Not applicable.

Data Availability Statement

The data presented in this study are available per request to the corresponding author.

Acknowledgments

The authors would like to acknowledge the companies YGE—Yser Green Energy SA and AFS—Advanced Fuel Solutions SA, both in Portugal, for the execution of the laboratory tests.

Conflicts of Interest

The authors declare no conflict of interest.

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Figure 1. Samples collected for the characterization and biochar production tests.
Figure 1. Samples collected for the characterization and biochar production tests.
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Figure 2. (a) Material wrapped in the aluminum foil; (b) produced biochar.
Figure 2. (a) Material wrapped in the aluminum foil; (b) produced biochar.
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Figure 3. Evolution of moisture, volatiles, ashes and fixed carbon contents after carbonization of vine pruning.
Figure 3. Evolution of moisture, volatiles, ashes and fixed carbon contents after carbonization of vine pruning.
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Figure 4. Evolution of CHNO contents after carbonization of vine pruning.
Figure 4. Evolution of CHNO contents after carbonization of vine pruning.
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Figure 5. Triangular diagram representing CHO contents. As can be seen, the content of CHO for vine pruning is similar to those found by Nunes et al. (2020) and Sá et al. (2020), both for dry and carbonized samples [26,33]. Vine pruning and biochar are the samples analyzed in the present work; samples 1 to 6 and samples 7 to 12 are, respectively, dry samples and carbonized samples from previous referred studies, as follows: 1 and 7—rice husks; 2 and 8—almond shells; 3 and 9—kiwi pruning; 4 and 10—olive pomace; 5 and 11—Pinus pinaster; and 6 and 12—Eucalyptus globulus.
Figure 5. Triangular diagram representing CHO contents. As can be seen, the content of CHO for vine pruning is similar to those found by Nunes et al. (2020) and Sá et al. (2020), both for dry and carbonized samples [26,33]. Vine pruning and biochar are the samples analyzed in the present work; samples 1 to 6 and samples 7 to 12 are, respectively, dry samples and carbonized samples from previous referred studies, as follows: 1 and 7—rice husks; 2 and 8—almond shells; 3 and 9—kiwi pruning; 4 and 10—olive pomace; 5 and 11—Pinus pinaster; and 6 and 12—Eucalyptus globulus.
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Figure 6. Evolution of S and Cl contents after carbonization of vine pruning.
Figure 6. Evolution of S and Cl contents after carbonization of vine pruning.
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Figure 7. Evolution of HHV and LHV after carbonization of vine pruning.
Figure 7. Evolution of HHV and LHV after carbonization of vine pruning.
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Figure 8. Evolution of the contents of major elements after the carbonization of vine pruning.
Figure 8. Evolution of the contents of major elements after the carbonization of vine pruning.
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Figure 9. Evolution of minor elements content after carbonization of vine pruning.
Figure 9. Evolution of minor elements content after carbonization of vine pruning.
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Table 1. Scheme of the programmable stages according to the temperature and residence time.
Table 1. Scheme of the programmable stages according to the temperature and residence time.
StagesCarbonization StepsTemperature (°C)Residence Time (min)Heating Rate (°C.min−1)
1Initial heating/pre-dryingTroom–180305
2Post-drying and intermediate heating180–3400603.7
3Carbonization40090-
4Cooling400–50 °CUntil can safely open the furnace-
Table 2. TGA results.
Table 2. TGA results.
Moisture (%)Volatiles (%)Ashes (%)Fixed Carbon (%)
DryBiocharDryBiocharDryBiocharDryBiochar
Sample 13.741.3577.8333.331.427.3019.5159.36
Sample 23.771.3777.8434.511.417.3319.4658.16
Sample 33.511.3077.7233.851.427.2219.7858.94
Average3.671.3477.8033.901.427.2819.5858.82
Standard deviation0.140.030.070.590.010.060.170.61
Confidence0.160.040.080.670.010.070.200.69
Table 3. CHNO results.
Table 3. CHNO results.
C (%)H (%)N (%)O (%)
DryBiocharDryBiocharDryBiocharDryBiochar
Sample 147.1273.556.364.690.711.20945.7920.53
Sample 246.4873.626.424.600.621.21346.4720.55
Sample 345.2373.406.054.620.281.17548.4220.78
Average46.2873.536.284.640.541.2046.8920.62
Standard deviation0.960.110.200.050.230.021.370.14
Confidence1.090.130.220.050.260.021.550.16
Table 4. S and Cl results.
Table 4. S and Cl results.
S (ppm)Cl (ppm)
DryBiocharDryBiochar
Sample 118118692.71.3
Sample 218417913.86.5
Sample 319018316.47.7
Average18518341.05.2
Standard deviation53.544.83.4
Confidence5450.73.9
Table 5. HHV and LHV results.
Table 5. HHV and LHV results.
HHV (MJ/kg)LHV (MJ/kg)
DryBiocharDryBiochar
Sample 118.9529.8417.5828.84
Sample 218.9529.7117.5828.72
Sample 318.9529.7817.5828.78
Average18.9529.7817.5828.78
Standard deviation0.0020.0060.0020.006
Confidence0.0020.0070.0020.007
Table 6. Determination of mass loss of carbonized samples of vine pruning.
Table 6. Determination of mass loss of carbonized samples of vine pruning.
Initial Mass (g)Final Mass (g)Mass Loss (%)
Sample 1229.1847.1179.44
Sample 2261.7060.0177.07
Sample 3257.0455.4978.41
Average249.3154.2078.31
Standard deviation17.596.551.00
Confidence19.907.411.00
Table 7. Major elements results for dry samples.
Table 7. Major elements results for dry samples.
Al
(ppm)
Ca
(ppm)
Fe
(ppm)
Mg
(ppm)
P
(ppm)
K
(ppm)
Si
(ppm)
Na
(ppm)
Ti
(ppm)
Sample 174.546972.4631.151303.741101.958120.49188.82407.252.71
Sample 253.667722.3738.571386.391077.508444.39137.45413.723.48
Sample 353.447641.2132.291387.781107.988168.23131.67444.392.83
Average60.557445.3534.001359.301095.818244.37152.65421.793.01
Standard deviation12.12411.544.0048.1216.14174.8631.4619.840.41
Confidence13.71465.694.5254.4618.26197.8735.6022.450.47
Table 8. Determination of the content of major elements of carbonized samples.
Table 8. Determination of the content of major elements of carbonized samples.
Al
(ppm)
Ca
(ppm)
Fe
(ppm)
Mg
(ppm)
P
(ppm)
K
(ppm)
Si
(ppm)
Na
(ppm)
Ti
(ppm)
Sample 191.8014,219.5860.642331.452317.6116,937.31182.17422.195.15
Sample 273.4014,415.4850.932329.092268.3616,988.84183.20412.394.52
Sample 378.0713,829.5252.112314.152289.8016,392.79171.07429.533.68
Average81.0914,154.8654.562324.902291.9216,772.98178.81421.374.45
Standard deviation9.56298.295.309.3824.69330.266.738.600.74
Confidence10.82337.546.0010.6227.94373.727.619.730.83
Table 9. Minor elements results for dry samples.
Table 9. Minor elements results for dry samples.
As
(ppm)
Cd
(ppm)
Co
(ppm)
Cr
(ppm)
Cu
(ppm)
Mn
(ppm)
Ni
(ppm)
Pb
(ppm)
Zn
(ppm)
Sample 10.580.580.400.4823.1639.640.630.2914.51
Sample 20.880.340.200.3426.4843.440.410.1014.53
Sample 30.730.390.320.0425.1540.950.130.0978.40
Average0.730.440.310.2924.9341.340.390.1635.81
Standard deviation0.150.130.100.221.671.930.250.1136.88
Confidence0.170.140.110.251.892.180.280.1341.73
Table 10. Determination of the content of minor elements in carbonized samples of vine pruning.
Table 10. Determination of the content of minor elements in carbonized samples of vine pruning.
As
(ppm)
Cd
(ppm)
Co
(ppm)
Cr
(ppm)
Cu
(ppm)
Mn
(ppm)
Ni
(ppm)
Pb
(ppm)
Zn
(ppm)
Sample 12.960.070.110.1145.4787.530.220.8355.52
Sample 22.730.000.000.0046.6387.580.030.7751.59
Sample 32.690.000.000.0045.4485.700.000.5951.55
Average2.790.020.040,0445.8586.940.080.7352.89
Standard deviation0.1460.0400.0640.0640.6791.0710.1190.1252.281
Confidence0.1650.0460.0720.0720.7681.2120.1350.1412.581
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Nunes, L.J.R.; Rodrigues, A.M.; Matias, J.C.O.; Ferraz, A.I.; Rodrigues, A.C. Production of Biochar from Vine Pruning: Waste Recovery in the Wine Industry. Agriculture 2021, 11, 489. https://doi.org/10.3390/agriculture11060489

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Nunes LJR, Rodrigues AM, Matias JCO, Ferraz AI, Rodrigues AC. Production of Biochar from Vine Pruning: Waste Recovery in the Wine Industry. Agriculture. 2021; 11(6):489. https://doi.org/10.3390/agriculture11060489

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Nunes, Leonel J. R., Abel M. Rodrigues, João C. O. Matias, Ana I. Ferraz, and Ana C. Rodrigues. 2021. "Production of Biochar from Vine Pruning: Waste Recovery in the Wine Industry" Agriculture 11, no. 6: 489. https://doi.org/10.3390/agriculture11060489

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