Next Article in Journal
Technologies Used to Purify the Air of Suspended Dust in Local Particulate Elimination Devices
Previous Article in Journal
The 5th EWaS International Conference: “Water Security and Safety Management: Emerging Threats or New Challenges? Moving from Therapy and Restoration to Prognosis and Prevention”
 
 
Font Type:
Arial Georgia Verdana
Font Size:
Aa Aa Aa
Line Spacing:
Column Width:
Background:
Proceeding Paper

Understanding the Impacts of Pyrolysis Temperature on the Energy Performance of Eucalyptus spp. Charcoal †

by
Allana Katiussya Silva Pereira
1,*,
Dalton Longue Júnior
2,
Álison Moreira da Silva
1,
Elias Costa de Souza
1,
Fabíola Martins Delatorre
3,
Brunela Pollastrelli Rodrigues
4 and
Ananias Francisco Dias Júnior
3
1
Agriculture College “Luiz de Queiroz”, University of São Paulo (ESALQ/USP), Piracicaba, São Paulo 13418-900, Brazil
2
Forest Science Graduate Program, Southwestern Bahia State University (UESB), Vitória da Conquista 45031-900, Brazil
3
Department of Forest and Wood Sciences, Federal University of Espírito Santo (UFES), Jerônimo Monteiro 29550-000, Brazil
4
Department of Sustainable Bioproducts/Forest and Wildlife Research Center (FWRC), College of Forest Resources (CFR), Mississippi State University, Starkville, MS 39762, USA
*
Author to whom correspondence should be addressed.
Presented at the 2nd International Electronic Conference on Forests—Sustainable Forests: Ecology, Management, Products and Trade, 1–15 September 2021. Available Online: https://iecf2021.sciforum.net/.
Environ. Sci. Proc. 2022, 13(1), 25; https://doi.org/10.3390/IECF2021-10794
Published: 31 August 2021

Abstract

:
This study aimed to investigate the influence of two pyrolysis temperatures (300 °C and 450 °C) on the energy quality of charcoal using a mix of commercial eucalypt woods. In this study, pyrolysis was carried out at a heating rate of 3.33 °C.min−1 for a duration of 3 h. The apparent density, bulk density, immediate analysis, high heating value, energy density, and combustibility index of the charcoal were measured. Under the conditions analyzed, pyrolysis performed at a final temperature of 450 °C resulted in charcoal with better energy performance than that produced at 300 °C.

1. Introduction

Primary energy resources, such as wood energy, are sources of energy and supplies obtained from nature [1,2]. Humanity has been using energy derived from biomass since the dawn of history. This fuel type has been widely used for heat production, converting wood energy for cooking and/or heating [1,2,3]. Currently, biomass is the only source of fuel for domestic use in many households in developing countries. It is the most important renewable energy source, accounting for about 6% of the total primary energy supply [1]. The search for energy efficiency has led to charcoal becoming an important wood product used in several applications over time.
There are several commercial processes available for pyrolyzing biomass and turning it into charcoal. Historically, kilns have been used with intensive labor and require a high degree of control to produce good quality and high charcoal yields [4]. These charcoal production methods are considered rudimentary, even though they have been practiced for centuries [5,6]. Charcoal’s specific properties are dictated by the control over the process variables and the homogenization of the raw material, constituting significant challenges for obtaining a high-quality product. Thus, understanding the influence of different pyrolysis temperatures becomes important since the temperature is an essential variable in determining the energy quality of charcoal [7,8].
Although much research has been carried out with a focus on the wood quality of Eucalyptus species and the pyrolysis variables [8,9,10], it is necessary that research continues to be developed to directly assist in decision making on the charcoal production process and contribute important technical information for the global charcoal sector. This study investigated the effect of two pyrolysis temperatures of a eucalypt wood mix on the energetic properties of charcoal.

2. Materials and Methods

2.1. Wood Preparation

To perform this study, a commercial Eucalyptus plantation area was selected in the southwest region of Bahia State, Brazil. The location is characterized by flat to slightly undulating relief, and the climate is classified as Cwb (tropical altitude), according to the Köppen classification, with an average temperature of 21 °C and annual precipitation of 700 mm [11]. Discs were obtained at different trunk positions from the collected trees (at 0%, 50%, and 100% of the commercial height; minimum diameter = 8 cm), homogenized, and transformed into smaller samples for the charcoal process.
Previous analyzes showed that the wood used had an average basic density of 500 kg.m−3, 29% of lignin, and 5% of extractives.

2.2. Charcoal Production

Wood samples measuring approximately 3 cm × 3 cm × 6 cm were dried in an oven at 103 ± 2 °C and placed in a metallic reactor whose volume was 1.34 dm3. Approximately 420 g of wood was used in each pyrolysis test. Five pyrolysis tests were carried out at a heating rate of 3.33 °C.min−1, with a duration of 3 h and two final temperatures (300 °C and 450 °C) to make a total of 10 tests. The tests were performed in an electric muffle furnace with a water-cooled condenser and condensable gases collector (Figure 1).

2.3. Characterization of Charcoal

To evaluate the charcoal samples, the following analyzes were performed:
  • Immediate analysis (volatile materials, ash, fixed carbon, %)—D-1762-84 [12];
  • Apparent density (kg.m−3)—NBR 11,941 [13];
  • Bulk density (kg.m−3)—NBR 6922 [14];
  • High heating value, Useful calorific value (MJ.kg−1) [15];
  • Combustion test—ICOM [16].
The energy density (GJ.m−3) of the charcoal was defined as the maximum amount of energy per unit volume of charcoal, determined by the product of the bulk density and the useful calorific value. To determine the combustibility index, 149 ± 1.22 g of dry charcoal with a homogeneous particle size of 16 mm was used [17]. Ignition was carried out using 4.5 g of anhydrous alcohol 96° INPM. The temperature reached, and the mass consumed throughout the test were recorded every 3 min. The beginning of the test was marked by when the alcohol volatilization occurred in the system, and the end was determined as when the combustion of the material was complete, i.e., after the system does not show mass variation for five consecutive readings.

2.4. Data Analysis

The data obtained were subjected to Student’s t test after checking the normality and homoscedasticity of the residuals at 5% significance, using the Shapiro–Wilk and Bartlett tests, respectively.

3. Results

The apparent density and ash were the same for both pyrolysis temperatures. The charcoal pyrolyzed at 450 °C provided the higher value of fixed carbon content (82.98%), lower volatile matter content (15.92%), and higher heating value (32 MJ/kg) (Table 1).
In contrast, the charcoal produced at 300 °C showed a higher energy density (3.58 GJ.m−3) and higher bulk density (133.86 kg.m−3). The charcoal produced at a temperature of 450 °C had a combustion index of 0.135 and the charcoal produced at 300 °C had combustion index of 0.058.
Figure 2 illustrates the variation in temperature (A) and mass consumption (B) during the pyrolysis process.

4. Discussion

Increasing the temperature causes the degradation of cellulose, hemicellulose, and lignin, concentrating the carbon and increasing the calorific value of charcoal [18,19]. However, degradation of the wood components leads to a marked loss of mass with a low loss of volume, making the material less dense [20]. As the peaks of wood degradation during the pyrolysis process occur at different temperatures, depending on its chemical and elemental composition, this loss of mass and reduction in the charcoal density occurred differently for the charcoal produced at 300 and 400 °C. While the degradation of hemicellulose and cellulose occurs at lower temperature ranges (220–315 °C and 315–400 °C, respectively), lignin has greater thermal stability, and despite initiating degradation at lower temperatures, its mass loss is slow and occurs even at higher temperatures (160–900 °C) [21]. Despite losing some of the components due to thermal degradation, the samples carbonized at 300 °C still had a higher concentration of lignin and cellulose in their composition compared with the samples carbonized at 450 °C. This higher concentration directly reflects the high content of volatile matter, and consequently, the lower fixed carbon content of charcoal, resulting in products with different physical and chemical characteristics [20,22,23].
Charcoal that has a high fixed carbon content (>73%) accompanied by a low content of volatile matter (<25%) and a low ash content (<1.5%) is suitable for application both in the steel industry and as charcoal for barbecues [9,20,24]. According to the data collected in this work, only charcoal produced at 450 °C reached the levels required for these two uses. In addition to these properties, another considered essential to defining the energy quality of charcoal is its calorific value. Although the calorific value is intrinsic to the material being used, the pyrolysis parameters can influence the content of other properties such as fixed carbon. High fixed carbon contents are related to high calorific values of charcoal. Confirming this trend, charcoal with a higher fixed carbon content (produced at 450 °C) also had a higher heating value (32 MJ.kg−1) compared with the other analyzed charcoal (28.25 MJ.kg−1).
Regarding the inorganic portion of charcoal, the ash content must be considered when evaluating the energy efficiency of solid fuel. However, the ash content of the material is not changed by the pyrolysis process as the mineral composition is intrinsic to the wood. High contents of ash, which are related to the mineral fraction of charcoal, can compromise the use of solid fuel in some types of boilers [20]. Therefore, it is interesting that strategies are devised to reduce the ash content in waste reused for energy generation. As Eucalyptus has a low ash content, eucalypt wood blends can be the solution to reduce ash and improve the energy properties of other biomasses used as fuel [25].
In addition, the energy properties determined in this study depend on the combustion efficiency of the material. The Combustion Index (ICOM) evaluates the amount of energy released in relation to the amount of mass consumed during the combustion process [25]. That is, the larger the ICOM, the greater the heat generation for the same amount of mass [25]. The final carbonization temperature influenced the ICOM of the studied materials, providing an increase of about 42.3% in the ICOM for the charcoal produced at a temperature of 450 °C. Investigating the influence of carbonization temperature on the energy quality of charcoal is essential to increasing knowledge about the thermal behavior of biomass when exposed to heat. However, other pyrolysis parameters can influence the physical, mechanical, chemical, and energetic properties of charcoal, and they must be studied in a complementary way.

5. Conclusions

Under the conditions analyzed, pyrolysis performed at a final temperature of 450 °C resulted in better charcoal energy performance than charcoal produced at 300 °C. This study can serve as a basis for new research assessing the influence of other pyrolysis parameters on the energy quality of different charcoal produced from diverse eucalypt wood mixes. Future studies should assess the practical production of charcoal from eucalypt wood mixes and improve its applications and operational efficiency for the steel industry or for barbecues.

Author Contributions

A.K.S.P. conducted and performed lab experiments, collected and analyzed data, and prepared the manuscript; Á.M.d.S., E.C.d.S., F.M.D. provided a strong contribution to the writing and review; A.K.S.P. and D.L.J. designed the study; A.F.D.J. supervised the analyses at all stages and provided a review of the manuscript; B.P.R. provided critical feedback, review, and editing of the manuscript. All authors have read and agreed to the published version of the manuscript.

Funding

This research received no external funding.

Institutional Review Board Statement

Not applicable.

Informed Consent Statement

Not applicable.

Data Availability Statement

Not applicable.

Acknowledgments

The authors acknowledge the financial support from the Coordination for the Improvement of Higher Education Personnel (CAPES), in association with the Technology of Forest Products Laboratory of the Southwestern Bahia State University (UESB), and to the Biomass Energy Laboratory of the Federal University of Espírito Santo (UFES) for technical support.

Conflicts of Interest

The authors declare no conflict of interest.

References

  1. Food and Agriculture Organization of the United Nations, FAO. Wood Energy. Available online: http://www.fao.org/forestry/energy/en/ (accessed on 20 April 2021).
  2. Tvaronavičienė, M.; Baublys, J.; Raudeliūnienė, J.; Jatautaitė, D. Global Energy Consumption Peculiarities and Energy Sources: Role of Renewables. Energy Transformation Towards Sustainability; Elsevier: Amsterdam, The Netherlands, 2020; ISBN 9780128176887. [Google Scholar]
  3. Bassam, N. Energy Resources, Global Contribution, and Applications; Elsevier Inc.: Amsterdam, The Netherlands, 2021; Volume 2, ISBN 9780128216057. [Google Scholar]
  4. Norgate, T.; Haque, N.; Somerville, M.; Jahanshahi, S. Biomass as a Source of Renewable Carbon for Iron and Steelmaking. ISIJ Int. 2012, 52, 1472–1481. [Google Scholar] [CrossRef]
  5. Food and Agriculture Organization of the United Nations, FAO. The Charcoal Transition; FAO: Rome, Italy, 2017; ISBN 9789251096802. [Google Scholar]
  6. Iiyama, M.; Chenevoy, A.; Otieno, E.; Kinyanjui, T.; Ndegwa, G.; Vandenabeele, J.; Njenga, M.; Johnson, O. Achieving Sustainable Charcoal in Kenya: Harnessing the Opportunities for Cross-Sectoral Integration; World Agroforestry (ICRAF), Stockholm Environment Institute (SEI): Nairobi, Kenya, 2014; pp. 2–5. [Google Scholar]
  7. Jahirul, M.I.; Rasul, M.G.; Chowdhury, A.A.; Ashwath, N. Biofuels Production through Biomass Pyrolysis- A Technological Review. Energies 2012, 5, 4952–5001. [Google Scholar] [CrossRef]
  8. Solar, J.; de Marco, I.; Caballero, B.M.; Lopez-Urionabarrenechea, A.; Rodriguez, N.; Agirre, I.; Adrados, A. Influence of Temperature and Residence Time in the Pyrolysis of Woody Biomass Waste in a Continuous Screw Reactor. Biomass Bioenergy 2016, 95, 416–423. [Google Scholar] [CrossRef]
  9. Assis, M.R.; Brancheriau, L.; Napoli, A.; Trugilho, P.F. Factors Affecting the Mechanics of Carbonized Wood: Literature Review. Wood Sci. Technol. 2016, 50, 519–536. [Google Scholar] [CrossRef]
  10. Kan, T.; Strezov, V.; Evans, T.J. Lignocellulosic Biomass Pyrolysis: A Review of Product Properties and Effects of Pyrolysis Parameters. Renew. Sustain. Energy Rev. 2016, 57, 1126–1140. [Google Scholar] [CrossRef]
  11. de Oliveira, A.M.; Barreto-Garcia, P.A.B.; Alves, B.J.R.; Conceição Júnior, V.; Gama-Rodrigues, E.F. Efeito de Rotações Sucessivas de Eucalipto Na Mineralização de Nitrogênio e Carbono Do Solo e Suprimento de Nitrogênio, No Sudoeste Da Bahia, Brasil. Sci. For. 2020, 48, 1–12. [Google Scholar] [CrossRef]
  12. D1762-84; Standard Test Method for Chemical Analysis of Wood Charcoal. American Society for Testing and Material. ASTM International: West Conshohocken, PA, USA, 2007.
  13. NBR 11941; Madeira—Determinação Da Densidade Básica. Associação Brasileira de Normas Técnicas. ABNT: Rio de Janeiro, Brazil, 2003.
  14. NBR 6922; Carvão Vegetal—Ensaios Fisícos—Determinação Da Massa Específica Do Carvão Vegetal. Associação Brasileira de Normas Técnicas. ABNT: Rio de Janeiro, Brazil, 1981; p. 2.
  15. EN 14918; Determination of Calorific Value: Belim. Deutsches Institut für Normung. DIN: Berlim, Germany, 2010.
  16. Quirino, W.F.; Brito, J.O. Características e Índice de Combustão de Briguetes de Carvão Vegetal; Laboratório de Produtos Florestais—LPF: Brasília, Brazil, 1991; p. 19. [Google Scholar]
  17. Dias Júnior, A.F.; Brito, J.O.; Andrade, C.R. Granulometric Influence on the Combustion of Charcoal for Barbecue. Rev. Árvore 2015, 39, 1127–1133. [Google Scholar] [CrossRef]
  18. de Paula Protásio, T.; Roque Lima, M.D.; Scatolino, M.V.; Silva, A.B.; Rodrigues de Figueiredo, I.C.; Gherardi Hein, P.R.; Trugilho, P.F. Charcoal Productivity and Quality Parameters for Reliable Classification of Eucalyptus Clones from Brazilian Energy Forests. Renew. Energy 2021, 164, 34–45. [Google Scholar] [CrossRef]
  19. Trugilho, P.F.; Lima, J.T.; Mori, F.A.; Lino, A.L. Avaliação de Clones de Eucalyptus Para Produção de Carvão Vegetal. Cerne 2001, 7, 104–114. [Google Scholar]
  20. Dias Junior, A.F.; Esteves, R.P.; da Silva, Á.M.; Sousa Júnior, A.D.; Oliveira, M.P.; Brito, J.O.; Napoli, A.; Braga, B.M. Investigating the Pyrolysis Temperature to Define the Use of Charcoal. Eur. J. Wood Wood Prod. 2020, 78, 193–204. [Google Scholar] [CrossRef]
  21. Yang, H.; Yan, R.; Chen, H.; Lee, D.H.; Zheng, C. Characteristics of Hemicellulose, Cellulose and Lignin Pyrolysis. Fuel 2007, 86, 1781–1788. [Google Scholar] [CrossRef]
  22. Dias Júnior, A.F.; Pirola, L.P.; Takeshita, S.; Lana, A.Q.; Brito, J.O.; Andrade, A.M. Higroscopicity of Charcoal Produced in Differen Temperatures. Cerne 2016, 22, 423–430. [Google Scholar] [CrossRef]
  23. Oliveira, A.C.; de Carneiro, A.C.O.; Vital, B.R.; Almeida, W.; Pereira, B.L.C.; Cardoso, M.T. Parâmetros de Qualidade Da Madeira e Do Carvão Vegetal de Eucalyptus Pellita F. Muell. Sci. For. 2010, 38, 431–439. [Google Scholar]
  24. São Paulo. Resolução SAA—40, de 14 de Dezembro Da Secretaria de Agricultura e Abastecimento. Dispõe de Padrões Mínimos de Qualidade de Carvão Vegetal; São Paulo, Brazil, 2015; pp. 1–11. Available online: http://www.codeagro.agricultura.sp.gov.br/arquivos/selo/SAA%2040%20Carvao%20Vegetal%202015.pdf (accessed on 20 April 2021).
  25. Dias Júnior, A.F.; Anuto, R.B.; Andrade, C.R.; de Souza, N.D.; Takeshita, S.; Brito, J.O.; Nolasco, A.M. Influence of eucalyptus wood addition to urban wood waste during combustion. Cerne 2017, 23, 455–464. [Google Scholar] [CrossRef]
Figure 1. Schematic procedure of pyrolysis carried out in a muffle furnace. A: muffle furnace; B: condenser; C: collector of pyroligneous acid; and D: burning of non-condensable gases. Source: the authors (2021).
Figure 1. Schematic procedure of pyrolysis carried out in a muffle furnace. A: muffle furnace; B: condenser; C: collector of pyroligneous acid; and D: burning of non-condensable gases. Source: the authors (2021).
Environsciproc 13 00025 g001
Figure 2. Variation in temperature (A) and mass consumption (B) during the combustion tests.
Figure 2. Variation in temperature (A) and mass consumption (B) during the combustion tests.
Environsciproc 13 00025 g002
Table 1. Results obtained from the charcoal characterization.
Table 1. Results obtained from the charcoal characterization.
TPRVMASFC ADBD ED HHV
(°C)(%)(%)(%)(kg·m−3)(kg·m−3)(GJ·m−3)(MJ·kg−1)
30033.23 * (1.26)1.07 (0.01)65.70 (1.25)299.74 (21.48)133.86 * (2.33)3.58 * (0.01)28.25 (0.06)
45015.92 (1.65)1.11 (0.03)82.98 * (1.68)320.90 (15.27)105.36 (0.02)3.22 (0.02)32.00 * (0.21)
Results are mean values followed by standard error. TPR = temperature; VM = volatile matter; AS = ash; FC = fixed carbon; AD = apparent density; BD = bulk density; ED = energy density; HHV = high heating value. * Significant at the 5% using the t test.
Disclaimer/Publisher’s Note: The statements, opinions and data contained in all publications are solely those of the individual author(s) and contributor(s) and not of MDPI and/or the editor(s). MDPI and/or the editor(s) disclaim responsibility for any injury to people or property resulting from any ideas, methods, instructions or products referred to in the content.

Share and Cite

MDPI and ACS Style

Pereira, A.K.S.; Júnior, D.L.; da Silva, Á.M.; de Souza, E.C.; Delatorre, F.M.; Rodrigues, B.P.; Júnior, A.F.D. Understanding the Impacts of Pyrolysis Temperature on the Energy Performance of Eucalyptus spp. Charcoal. Environ. Sci. Proc. 2022, 13, 25. https://doi.org/10.3390/IECF2021-10794

AMA Style

Pereira AKS, Júnior DL, da Silva ÁM, de Souza EC, Delatorre FM, Rodrigues BP, Júnior AFD. Understanding the Impacts of Pyrolysis Temperature on the Energy Performance of Eucalyptus spp. Charcoal. Environmental Sciences Proceedings. 2022; 13(1):25. https://doi.org/10.3390/IECF2021-10794

Chicago/Turabian Style

Pereira, Allana Katiussya Silva, Dalton Longue Júnior, Álison Moreira da Silva, Elias Costa de Souza, Fabíola Martins Delatorre, Brunela Pollastrelli Rodrigues, and Ananias Francisco Dias Júnior. 2022. "Understanding the Impacts of Pyrolysis Temperature on the Energy Performance of Eucalyptus spp. Charcoal" Environmental Sciences Proceedings 13, no. 1: 25. https://doi.org/10.3390/IECF2021-10794

APA Style

Pereira, A. K. S., Júnior, D. L., da Silva, Á. M., de Souza, E. C., Delatorre, F. M., Rodrigues, B. P., & Júnior, A. F. D. (2022). Understanding the Impacts of Pyrolysis Temperature on the Energy Performance of Eucalyptus spp. Charcoal. Environmental Sciences Proceedings, 13(1), 25. https://doi.org/10.3390/IECF2021-10794

Article Metrics

Back to TopTop