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Article

Potential of Mild Torrefaction for Upgrading the Wood Energy Value of Different Eucalyptus Species

by
Solange De Oliveira Araújo
1,*,
Duarte M. Neiva
1,
Angélica De Cássia Carneiro
2,
Bruno Esteves
3 and
Helena Pereira
1
1
Centro de Estudos Florestais, Instituto Superior de Agronomia, Universidade de Lisboa, Tapada da Ajuda, 1349-017, Lisboa, Portugal
2
Universidade Federal de Viçosa, Avenida Peter Henry Rolfs s/n, Viçosa 36571-000, Minas Gerais, Brazil
3
Instituto Politécnico de Viseu- Escola Superior de Tecnologia e Gestão de Viseu, Av. Cidade Politécnica, Viseu 3504-510, Portugal
*
Author to whom correspondence should be addressed.
Forests 2018, 9(9), 535; https://doi.org/10.3390/f9090535
Submission received: 8 August 2018 / Revised: 28 August 2018 / Accepted: 30 August 2018 / Published: 1 September 2018
(This article belongs to the Section Forest Ecology and Management)

Abstract

:
Torrefaction is a promising pre-treatment for improving the fuel quality of biomass. This study examined the effect of a mild torrefaction (from 160 to 230 °C) on the heating value, elemental composition, and thermogravimetric analysis of wood from eight Eucalyptus species (E. botryoides Sm., E. globulus Labill., E. grandis W.Hill ex Maiden, E. maculata (Hook.) K.D. Hill & L.A.S.Johnson, E. propinqua Maiden Deane, E. rudis Endl., E. saligna Sm., and E. viminalis Labill.). The higher heating values (HHV) increased from the initial average of 19 MJ kg−1 to 21 MJ kg−1 in the torrefied samples. The carbon content increased from 48.2% to 53.3% and the C/O ratio from 1.08 to 1.35. The torrefied wood samples showed more thermal stability with a shift of the mass loss peaks to higher temperatures and a higher residual mass at 450 °C of 36%, in comparison to 30% of the untreated samples. Torrefaction concentrated the biomass samples in the more energetic and thermal resistant components and decreased their sulfur and chlorine content, leading to a better combustion performance. The wood of the eight Eucalyptus species had a similar behavior and showed quality improvement. Therefore, torrefaction showed potential as a pre-treatment for eucalyptus biomass fuel improvement.

1. Introduction

Renewable energy plays a fundamental role in the reduction of fossil fuels consumption, and studies on alternative energy sources have increased exponentially [1]. The goal is to obtain cleaner energy sources of acceptable quality and with environmental, strategic, and socioeconomic benefits; e.g., reduction of pollutant emissions, higher energy security for countries depending on imported fossil fuels, poverty reduction, and access to energy in remote areas [2]. Biomass accounts for the largest fraction worldwide among the different renewable energy sources, although its use is still low compared with other sources [3]. Brazil is singled out in this context by International Energy Agency (IEA) [3], with approximately 16% of the world biomass use for power generation in the industry, followed by the US (9%) and Germany (7%).
Biomass may be used to meet a variety of energy needs, including electricity, home heating, vehicle fueling, and industrial process heating. The wood industries and homeowners are the major consumers of biomass energy, e.g., the timber and pulp and paper industries burn their own wood wastes to supply approximately 60% of their energy needs [4]. The potential environmental benefits from using well-managed biomass energy feedstocks as opposed to fossil fuels include lower emissions of certain pollutants and greenhouse gas emissions and CO2 neutrality. Biomass energy facilities can also help increase jobs in areas with resource-dependent economies, which are usually characterized by a slow economic growth [5,6].
However, the use of wood biomass to produce energy still has some limitations, mostly because of the physical properties of the wood itself. In general, raw biomass is characterized by a high moisture content, hygroscopic behavior, low energy density (the primary energy conversion technologies only reach 15% to 20% conversion efficiency), low density, and possible storage problems. Furthermore, transporting wood fuels over long distances is generally not economically feasible [5,7]. Some of the drawbacks of raw biomass can be mitigated by pretreatments. A number of conversion methods have been proposed, of which torrefaction has attracted more attention in recent research because of its increasing application potential [8].
Torrefaction is a thermochemical process that is carried out at relatively low temperatures between 200 °C and 300 °C. In this range, the thermochemical degradation of lignocellulosic materials is moderate, with hemicelluloses as the most easily degraded structural component. This thermal treatment ensures a more homogeneous material with higher energy density, maintaining in average 90% of the energy and 70% of the mass content in relation to the raw material [9].
Therefore, torrefaction is a promising technique to improve the performance of biomass for energy utilization. However, the number of studies is still limited, specifically regarding the thermochemical behavior of different lignocellulosic materials and wood species. Among them, the Eucalyptus species are especially interesting because some are already important industrial raw materials; e.g., E. globulus Labill.—for the pulping industry, and many are potential pulp and timber species or biomass crops [10,11]. In this study, the torrefaction of eight eucalyptus species was studied.

2. Materials and Methods

2.1. Materials

Six-year-old trees from eight eucalyptus species (Eucalyptus botryoides Sm., E. globulus Labill., E. grandis W.Hill ex Maiden, E. maculata (Hook.) K.D. Hill & L.A.S.Johnson, E. propinqua Maiden Deane, E. rudis Endl., E. saligna Sm., and E. viminalis Labill.) were collected from an arboretum located in the fields of the School of Agriculture (ISA), University of Lisbon (ULisboa), at Tapada da Ajuda, Lisboa, Portugal (38°42′ N; 09°10′ W). The trees were harvested, and the lower stem log from the base to 1.3 m of height was taken and then sawn into boards, were cut with 60 × 7.5 × 2 cm3 (in axial, tangential, and radial directions). The boards were air dried to moisture content between 12% and 15%.

2.2. Methods

The wood boards were torrefied with gradual heating from 160 to 230 °C by the Portuguese company Santos & Santos Madeiras (S&S) under the registered trademark Atlanticwood, a thermo-modification process. Depending on the treatment temperature and wood, the conditioning phase takes 5–15 h. The specific characteristics of the process (reactor and temperature gradient) are under industrial secrecy.
The higher heating value (HHV) was determined (ABNT 1984) [12] using an Adiabatic Bomb Calorimeter (Model IKA300, IKA, Staufen, Germany). For this analysis the samples were oven-dried at 103 °C ± 2 °C until a constant mass was reached.
Ash content was determined by Technical Association of the Pulp and Paper Industry, TAPPI standard method T15 os-58. The elemental composition was determined using the ASTM D5373-08 (2008) [13] with a Perkin-Elmer II 2400 (Shelton, CT, USA) element analyzer. The composition regarding carbon, nitrogen, and hydrogen (CHN) was determined, as well as Ca, Mg, K, Cl, and S, while the oxygen percentage was calculated as (100 − (ash + carbon + hydrogen + sulphur + nitrogen)) difference.
Thermogravimetric analysis (TGA) and derivative thermogravimetry (DTG) measurements were carried out using a differential thermal analyzer DTG-60H (Shimadzu, Kyoto, Japan) in a dynamic nitrogen atmosphere (gas flow of 50 mL min−1) with a temperature range of 10 to 900 °C using a 10 °C/min−1 heating rate, using 2 mg ± 0.1 mg samples in a platinum container. The thermogravimetric curve (TG) and the curve of the first derivative of the mass loss (DTG) were recorded. From the TG curves, the mass loss was calculated in the following temperature ranges: 50 to 100 °C, 100 to 150 °C, 150 to 200 °C, 200 to 250 °C, 250 to 300 °C, 300 to 350 °C, 350 to 400 °C, and 400 to 450 °C. The residual mass at 450 °C was also calculated.

3. Results

The higher heating values of the untreated and torrefied wood samples of the different eucalyptus species are compiled in Table 1. Overall, the results show that there is an energy gain with the torrefaction process for all species, i.e., the mean calorific value of the torrefied wood was 21 MJ kg−1, while that of the untreated wood was 19 MJ kg−1. The increase in calorific value by torrefaction was on average 7.4% when compared with the untreated samples. The highest values were found for E. botryoides, E. grandis, and E. rudis (9.3%, 9.9%, and 10.8% respectively), while E. maculata presented the lowest value (2.2%).
The results of the elemental analysis are presented in Table 2. There was a clear effect of the torrefaction in the elemental analysis for the eight eucalyptus woods, which presented a similar trend of an increase in carbon and a decrease in oxygen along with a slight decrease in hydrogen with heating. The largest carbon increase between treated and untreated wood was for E. rudis (16%), E. botryoides (14%), E. grandis, and E. maculata (11%). In contrast, E. globulus (6%), E. saligna (8%), and E. propinqua (9%) had the lowest C increase. The oxygen content of the torrefied woods decreased in all of the samples by an average of 11% with E. botryoides, E. grandis and E. rudis achieving the more pronounced drops (above 12%) and E. globulus the lowest variation (5.3%). The hydrogen content was only slightly reduced; i.e., on average H corresponded to 6.0% of the untreated wood samples and 5.8% of the torrefied samples.
The N content of the eucalyptus woods was low, on average 0.22% and 0.26% for untreated and torrefied samples, respectively. The ash content was low and slightly increased in the torrefied samples: on average 0.60% in untreated and 0.85% in torrefied wood samples. The contents for Ca, K, Mg, and S were low in both the original wood and in the torrefied samples. The chlorine content dropped in nearly all of the samples with torrefaction. The largest decrease was measured for E. rudis (0.4% vs. 0.2%), while for the other species the decrease was about 0.25%. The chlorine content only increased in the E. grandis wood.
Figure 1 shows the TG and DTG curves for the untreated and torrefied woods of the different eucalyptus species (for the 150 to 450 °C temperature range) and Table 3 reports the mass loss observed at different temperature ranges. The first step, which corresponded primarily to the loss of physically absorbed water and some low-molecular weight compounds, is evident in the range of 50 to 200 °C (Table 3).
The mass losses were overall negligible until 250 °C, and were slightly higher in the case of untreated wood samples. Degradation was substantial in the 250 to 300 °C range being lower for the torrefied wood samples with an average of 19% and 13% for untreated and torrefied samples, respectively. The same occurred in the 300 to 350 °C range when most of the thermochemical degradation occurred: on average 28% and 20% for the untreated and torrefied samples, respectively. Overall the mass losses in the range of 250 to 400 °C were 54% and 62% for the torrefied and untreated samples, respectively.
The TGA curves show that the untreated wood has a higher thermal degradation than the heat-treated wood; i.e., a lower thermal stability than the torrefied material. For the untreated samples, compared to treated ones, the mass loss began at lower temperatures and the bulk of the mass loss also occurred at a lower temperatures, with higher mass loss that resulted in a lower yield of the residual material. The residual mass at 450 °C was higher for the torrefied samples (36% vs. 30% for the untreated samples).
When comparing the studied eucalyptus species’, it is possible to verify that they all showed a similar behavior in the thermogravimetric analysis, with small visual differences in the TGA/DTG thermograms. In general, the highest peaks of thermal degradation occurred between 300 and 400 °C. In the untreated samples, a first peak occurred at approximately 300 °C and the maximum peak occurred at 340 to 350 °C; in the torrefied samples, the first peak decreased or disappeared.

4. Discussion

The calorific values found in this work for the untreated eucalyptus woods fall within previous literature’s values, as reported for E. globulus (17.6 to 19.8 MJ kg−1), E. botryoides (19.9 MJ kg−1), E. grandis (18.8 to 19.9 MJ kg−1), E. maculata (18.8 to 19.6 MJ kg−1), and E. saligna (18 to 19.5 MJ kg−1) [14,15].
The torrefaction increased the calorific values of the wood samples to 21 MJ kg−1 (Table 1). This effect is in accordance with previous reports e.g., the heating value increased from 19 MJ kg−1 to 21 or 23 MJ kg−1 in torrefied woods [16]. In eucalyptus wood treated at 220 °C, 250 °C, and 280 °C, the increase was 4%, 10%, and 16%, respectively [9].
The higher energy content in the torrefied wood samples was related to the chemical changes that occurred during the heat treatment where the higher energetic components were concentrated [17]. In fact, the torrefied wood samples increased their C content and decreased their O content, resulting into C/O ratios of 1.35 in comparison with 1.08 for the untreated samples (Table 2). This was reported for several cases with a higher C content increase for the more severe torrefaction conditions [18,19,20]. For eucalyptus wood, 24% more C content and 26% less O content were found after torrefaction at 280 °C for 3 h [21].
The carbon increase was related mostly to the degradation of hemicelluloses during the torrefaction process, while lignin (the component with the highest carbon content) remained mostly unaltered [22]. Moreover, the thermal behavior of wood during heating (Figure. 1) showed a first mass loss at the lower-temperature range (the first peak of the DTG curve), which corresponded to the decomposition of the hemicellulose fraction. As the temperature rose, the chemical reactions became more complex and cellulose degradation occurred near 350 °C (the second peak of the DTG curve). Similar results were obtained from the TGA analysis of other kinds of biomass [23,24,25].
The torrefied wood samples showed an overall higher thermal stability compared to the untreated samples (Table 3), with a shift of the mass loss to higher temperatures. The higher residual mass at 450 °C was also indicative of the thermal stability of the torrefied samples in comparison to the untreated woods. This was in accordance with the fact that the torrefied samples were concentrated in cellulose and lignin, which were more heat resistant [20,26,27].
Biomass fuels exhibit different rates of fouling depending on their ash content and composition, which may influence fouling and slagging [27]. For instance, the N content is important in the formation of pollutant emissions, while S and Cl may cause fouling and slagging [28]. The untreated and the torrefied wood samples were at the same 0.01% level of S, and all were under the limits set in EN (European Norm) 15289 [29]. In general, the heat treatment reduced the S and Cl contents (Table 2), thereby decreasing the associated risks.
The mild torrefaction used in this study confirmed an improvement in the biofuel properties of all tested eucalyptus species, which showed no noticeable differences between them. Therefore, the torrefied woods of the different eucalyptus species may be considered a rather homogeneous biofuel. All of the heat-treated wood samples had calorific values higher than the minimum value required by ISO (International Organization for Standardization) 17225-1 [30].

5. Conclusions

A mild torrefaction process considerably improved the thermal properties of eucalyptus wood biomass by increasing their C/O ratio by 20% and their calorific value by 10%.
Torrefaction concentrated the biomass samples in more energetic and thermal resistant components and decreased their sulfur and chlorine contents, leading to a better combustion performance.
The wood of the eight Eucalyptus species had a similar behavior and quality improvement, which allows for their use as mixed feedstocks. Therefore, the torrefaction showed its potential as a pre-treatment for biomass fuel improvement.

Author Contributions

Conceptualization, S.O.A. and H.P; Funding acquisition, H.P. and A.C.C.; Investigation, S.O.A., D.M.N., A.C.C., B.E.; Resources, A.C.C., B.E. and H.P.; Supervision, H.P.; Writing—original draft, S.O.A., D.M.N. and H.P.; Writing—review & editing, S.O.A., D.M.N., A.C.C., B.E. and H.P.

Funding

This research was funded by CNPq (National Council for Scientific and Technological Development) through a grant awarded to the first author 236389/2012-2 and Forest Research Centre (CEF) which is a research unit funded by FCT (Fundação para a Ciência e a Tecnologia, Portugal) through the strategic project UID/AGR/0239/2013. This study was also partially funded by FCT through project EucPlus-New processes and uses for eucalyptus woods (PTDC/AGR-CFL/119752/2010).

Acknowledgments

The authors wish to thank the Federal University of Viçosa, CAPES (Coordination for the Development of Higher Level Personnel) and acknowledge the help of Sofia Knapic for providing the samples and Jorge Gominho for general assistance. The authors are thankful to the Santos & Santos industry which is part of the group Catarino for the heat treatment of the wood samples.

Conflicts of Interest

The authors declare no conflicts of interest.

References

  1. Chen, W.H.; Kuo, P.C. Torrefaction and co-torrefaction characterization of hemicellulose, cellulose, and lignin as well as torrefaction of some basic constituents in biomass. Energy 2011, 36, 803–811. [Google Scholar] [CrossRef]
  2. Carneiro, A.C.O.; Santos, R.C.; Oliveira, A.C.; Pereira, B.L.C. Conversão direta da madeira em calor e energia. In Bioenergia & Biorrefinaria-Cana-de-Açúcar & Espécies Florestais; Santos, F., Colodette, J., de Queiroz, J.H., Eds.; UFV: Viçosa, Brazil, 2013; pp. 355–378. [Google Scholar]
  3. International Energy Agency. World Energy Outlook 2012; International Energy Agency: Paris, France, 2012. [Google Scholar]
  4. Balat, M.; Ayar, G. Biomass energy in the world, use of biomass and potential trends. Energy Sources 2005, 27, 931–940. [Google Scholar] [CrossRef]
  5. Michigan Biomass Energy Program Clean Energy from Wood Residues in Michigan. Available online: http://www.michigan.gov/documents/wood_energy_in_michigan--final1_169999_7.pdf (accessed on 20 June 2018).
  6. Ong, Y.K.; Bhatia, S. The current status and perspectives of biofuel production via catalytic cracking of edible and non-edible oils. Energy 2010, 35, 111–119. [Google Scholar] [CrossRef]
  7. Chen, W.H.; Chen, J.C.; Tsai, C.D.; Jiang, T.L. Transient gasification and syngas formation for coal particles in a fixed-bed reactor. Int. J. Energy Res. 2007, 31, 895–911. [Google Scholar] [CrossRef]
  8. Chen, W.H.; Kuo, P.C. A study on torrefaction of various biomass materials and its impact on lignocellulosic structure simulated by thermogravimetry. Energy 2010, 35, 2580–2586. [Google Scholar] [CrossRef]
  9. Rodrigues, T.O. Efeitos da Torrefação no Condicionamento de Biomassa Para Fins Energéticos. Master’s Thesis, University of Brasília, Brasília, Brazil, 2009. [Google Scholar]
  10. Knapic, S.; Pirralho, M.; Louzada, J.L.; Pereira, H. Early assessment of density features for 19 Eucalyptus species using X-ray microdensitometry in a perspective of potential biomass production. Wood Sci. Technol. 2014, 48, 37–49. [Google Scholar] [CrossRef]
  11. Neiva, D.M.; Araújo, S.; Lourenço, A.; Gominho, J.; Fernandes, L.; Simões, R.; Pereira, H. Chemical composition and kraft pulping potential of 12 eucalypt species. Ind. Crop. Prod. 2015, 66, 89–95. [Google Scholar] [CrossRef]
  12. STM International. ASTM D5373-08 Standard Test Method for Instrumental Determination of Carbon, Hydrogen and Nitrogen in Laboratory Samples of Coal; ASTM International: West Conshohocken, PA, USA, 2008. [Google Scholar]
  13. De Normas Técnicas, A.B. NBR 8633: Carvão vegetal-Determinação do Poder Calorífico-Método de Ensaio; ABNT: Rio do Janeiro, Brazil, 1984. [Google Scholar]
  14. Kitani, O.; Hall, C.W. Biomass Handbook; Gordon and Breach Science Publishers: New York, NY, USA, 1989; pp. 56–65. [Google Scholar]
  15. Quirino, F.W.; Vale, A.T.; Andrade, A.P.A.; Abreu, V.L.S.; Azevedo, A.C.S. Poder calorífico da madeira e de materiais lignocelulósicos. Revista da Madeira 2005, 89, 100–106. [Google Scholar]
  16. Ciolkosz, D.; Wallace, R. A review of torrefaction for bioenergy feedstock production. Biofuels Bioprod. Biorefin. 2011, 5, 317–329. [Google Scholar] [CrossRef]
  17. Brito, J.O.; Silva, F.G.; Leao, M.M.; Almeida, G. Chemical composition changes in Eucalyptus and Pinus woods submitted to heat treatment. Bioresour. Technol. 2008, 18, 8545–8548. [Google Scholar] [CrossRef] [PubMed]
  18. Felfli, F.F.; Luengo, C.A.; Suarez, J.A.; Beaton, P.A. Wood briquette torrefaction. Energy Sustain. Dev. 2005, 9, 19–22. [Google Scholar] [CrossRef]
  19. Bridgeman, T.G.; Jones, J.M.; Shield, I.; Williams, P.T. Torrefaction of reed canary grass, wheat straw and willow to enhance solid fuel qualities and combustion properties. Fuel 2008, 87, 844–856. [Google Scholar] [CrossRef]
  20. Nhuchhen, D.R.; Basu, P.; Acharya, B. A Comprehensive review on biomass torrefaction. Int. J. Renew. Energy Biofuels 2014, 2014, 1–56. [Google Scholar] [CrossRef]
  21. Arias, B.; Pevida, C.; Fermoso, J.; Plaza, M.G.; Rubiera, F.; Pis, J.J. Influence of torrefaction on the grindability and reactivity of woody biomass. Fuel Process. Technol. 2008, 89, 169–175. [Google Scholar] [CrossRef] [Green Version]
  22. Demirbas, F.; Balat, M.; Balat, H. Potential contribution of biomass to the sustainable energy development. Energy Convers. Manag. 2009, 50, 1746–1760. [Google Scholar] [CrossRef]
  23. Hossain, M.K.; Strezov, V.; Nelson, P.F. Thermal characterisation of products of wastewater sludge pyrolysis. J. Anal. Appl. Pyrolysis 2009, 85, 442–446. [Google Scholar] [CrossRef]
  24. Saddawi, A.; Jones, J.M.; Williams, A.; Le Coeur, C. Commodity fuels from biomass through pretreatment and torrefaction: Effects of mineral content on torrefied fuel characteristics and quality. Energy Fuel 2012, 26, 6466–6674. [Google Scholar] [CrossRef]
  25. Sen, A.; Marques, A.V.; Gominho, J.; Pereira, H. Study of thermochemical treatments of cork in the 150–400 °C range using colour analysis and FTIR spectroscopy. Ind. Crop. Prod. 2012, 38, 132–138. [Google Scholar] [CrossRef]
  26. Esteves, B.; Velez Marques, A.; Domingos, I.; Pereira, H. Influence of steam heating on the properties of pine (Pinus pinaster) and eucalypt (Eucalyptus globulus) wood. Wood Sci. Technol. 2007, 41, 193–207. [Google Scholar] [CrossRef]
  27. Benavente, V.; Fullana, A. Torrefaction of olive mill waste. Biomass Bioenergy 2015, 73, 186–194. [Google Scholar] [CrossRef] [Green Version]
  28. Wilk, M.; Magdziarz, A.; Kalemba, I. Characterisation of renewable fuels’ torrefaction process with different instrumental techniques. Energy 2015, 87, 259–269. [Google Scholar] [CrossRef]
  29. European Committee for Standardization. EN15289 Solid Biofuels-Determination of Total Content of Sulfur and Chlorine; European Committee for Standardization (CEN): Wien, Austria, 2015. [Google Scholar]
  30. International Organization for Standardization. ISO17225-1 Solid biofuels-Fuel Specifications and Classes-Part 1: General Requirements; International Organization for Standardization: Geneva, Switzerland, 2014. [Google Scholar]
Figure 1. Thermogravimetric analysis (TGA) (left y-axis) and derivative thermogravimetry (DTG) (right y-axis) curves of untreated (U) and heat-treated (T) wood samples of E. botryoides Sm. (a), E. globulus Labill. (b), E. grandis W.Hill ex Maiden (c), E. maculata (Hook.) K.D. Hill & L.A.S.Johnson (d), E. propinqua Maiden Deane (e), E rudis Endl. (f), E. saligna Sm. (g) and E. viminalis Labill. (h) under a nitrogen atmosphere and 10 °C/min heating rate.
Figure 1. Thermogravimetric analysis (TGA) (left y-axis) and derivative thermogravimetry (DTG) (right y-axis) curves of untreated (U) and heat-treated (T) wood samples of E. botryoides Sm. (a), E. globulus Labill. (b), E. grandis W.Hill ex Maiden (c), E. maculata (Hook.) K.D. Hill & L.A.S.Johnson (d), E. propinqua Maiden Deane (e), E rudis Endl. (f), E. saligna Sm. (g) and E. viminalis Labill. (h) under a nitrogen atmosphere and 10 °C/min heating rate.
Forests 09 00535 g001
Table 1. Higher Heating Value (HHV, MJ kg−1) of Untreated and Torrefied Wood Samples from Eight Eucalyptus Species.
Table 1. Higher Heating Value (HHV, MJ kg−1) of Untreated and Torrefied Wood Samples from Eight Eucalyptus Species.
Wood SpeciesHigher Heating Value (MJ kg−1)
UntreatedTorrefied
E. botryoides Sm.19.221.0
E. globulus Labill.19.020.1
E. grandis W.Hill ex Maiden19.020.9
E. maculata (Hook.) K.D. Hill & L.A.S.Johnson19.119.5
E. propinqua Maiden Deane19.921.3
E. rudis Endl.19.221.3
E. saligna Sm.19.621.0
E. viminalis Labill.19.420.8
Table 2. Elemental Analysis of Untreated (U) and Torrefied (T) Wood Samples of Eight Eucalyptus Species.
Table 2. Elemental Analysis of Untreated (U) and Torrefied (T) Wood Samples of Eight Eucalyptus Species.
WoodAsh (%)C (%)H (%)N (%)Ca (%)S (%)K (%)Mg (%)O (%)Cl (%)
E. botryoidesU0.748.276.060.40.020.040.10.0244.100.4
T1.055.335.880.40.050.030.20.0437.110.3
E. globulusU0.648.746.120.20.070.010.10.0643.720.3
T0.751.505.770.30.100.010.20.0441.400.2
E. grandisU0.648.086.120.20.040.010.10.0244.400.1
T0.653.725.830.20.060.010.10.0239.060.3
E. maculataU1.147.556.150.20.280.030.10.0244.780.2
T1.452.675.560.20.300.010.10.0340.310.1
E. propinquaU0.549.176.070.20.020.010.10.0443.380.3
T0.853.755.810.20.030.010.10.0439.080.2
E. rudisU0.846.045.700.20.040.040.20.0946.830.4
T1.053.515.740.40.090.050.20.0939.020.2
E. salignaU0.449.576.150.20.050.010.10.0242.800.3
T0.653.565.800.20.070.010.10.0239.260.3
E. viminalisU0.747.956.010.20.060.010.20.0344.590.3
T0.752.605.760.20.070.010.10.0240.320.2
Table 3. Mass Loss (%) of Untreated (U) and Torrefied (T) Wood of Eight Eucalyptus Species during Thermal Degradation (along Successive Temperature Ranges).
Table 3. Mass Loss (%) of Untreated (U) and Torrefied (T) Wood of Eight Eucalyptus Species during Thermal Degradation (along Successive Temperature Ranges).
WoodTemperature range (°C)
50 to 100100 to 150150 to 200200 to 250250 to 300300 to 350350 to 400400 to 450Residual Mass (450)
E. botryoidesU1213212613430
T2002182413537
E. globulusU0212202915428
T1101132715734
E. grandisU011115408629
T100120269735
E. maculataU0113172719429
T01116389737
E. propinquaU1213212613431
T11018379636
E. rudisU011217347433
T1001123210737
E. salignaU0211192716630
T100111368735
E. viminalisU0112222714329
T1101172217435

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MDPI and ACS Style

Araújo, S.D.O.; Neiva, D.M.; Carneiro, A.D.C.; Esteves, B.; Pereira, H. Potential of Mild Torrefaction for Upgrading the Wood Energy Value of Different Eucalyptus Species. Forests 2018, 9, 535. https://doi.org/10.3390/f9090535

AMA Style

Araújo SDO, Neiva DM, Carneiro ADC, Esteves B, Pereira H. Potential of Mild Torrefaction for Upgrading the Wood Energy Value of Different Eucalyptus Species. Forests. 2018; 9(9):535. https://doi.org/10.3390/f9090535

Chicago/Turabian Style

Araújo, Solange De Oliveira, Duarte M. Neiva, Angélica De Cássia Carneiro, Bruno Esteves, and Helena Pereira. 2018. "Potential of Mild Torrefaction for Upgrading the Wood Energy Value of Different Eucalyptus Species" Forests 9, no. 9: 535. https://doi.org/10.3390/f9090535

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