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Kinetic triplet of Colombian sawmill wastes using thermogravimetric analysis
The potential of sawmill wastes as a raw material in pyrolysis process is presented in this study. Non-isothermal thermogravimetric analysis (TGA and DTG) and isoconversional methods were employed to determine triplet kinetic (activation energy, reaction model and pre-exponential factor). Through TG...
Autores principales: | , , |
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Formato: | Online Artículo Texto |
Lenguaje: | English |
Publicado: |
Elsevier
2019
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Materias: | |
Acceso en línea: | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC6838918/ https://www.ncbi.nlm.nih.gov/pubmed/31720467 http://dx.doi.org/10.1016/j.heliyon.2019.e02723 |
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author | Bonilla, Javier Salazar, Robert Paul Mayorga, Manuel |
author_facet | Bonilla, Javier Salazar, Robert Paul Mayorga, Manuel |
author_sort | Bonilla, Javier |
collection | PubMed |
description | The potential of sawmill wastes as a raw material in pyrolysis process is presented in this study. Non-isothermal thermogravimetric analysis (TGA and DTG) and isoconversional methods were employed to determine triplet kinetic (activation energy, reaction model and pre-exponential factor). Through TGA and DTG, the conversion degree is described as a function of temperature for five heating rates (10, 20, 30, 40 and [Formula: see text] C/min) and four model-free methods (Flynn-Wall-Ozawa (FWO), Kissinger-Akahira-Sunose (KAS), Friedman, and Vyazovkin) with temperatures ranging from 25 to 1000(°)C were employed. Isoconversional lines were built for every method at different isoconversional degrees [Formula: see text]. The activation energy E was found as a function of α in the interval [Formula: see text] where each isoconversional methods were in agreement and the estimated error was sufficiently small. Findings show the same activation energy profile independently of the isoconversional method. In particular the total variation of E in [Formula: see text] was as follows: 209.909–228.238 kJ/mol (FWO); 211.235–229.277 kJ/mol (KAS); 223.050–188.512 kJ/mol (Friedman), and 211.449 kJ/mol-229.512 kJ/mol (Vyazovkin). The reaction model of the process in [Formula: see text] matched with a two-dimensional diffusion ([Formula: see text]) by using a master-plot analysis. The calculated and reported parameters are fundamental information for the pyrolysis reactor design using Sawmill wastes as feedstock. |
format | Online Article Text |
id | pubmed-6838918 |
institution | National Center for Biotechnology Information |
language | English |
publishDate | 2019 |
publisher | Elsevier |
record_format | MEDLINE/PubMed |
spelling | pubmed-68389182019-11-12 Kinetic triplet of Colombian sawmill wastes using thermogravimetric analysis Bonilla, Javier Salazar, Robert Paul Mayorga, Manuel Heliyon Article The potential of sawmill wastes as a raw material in pyrolysis process is presented in this study. Non-isothermal thermogravimetric analysis (TGA and DTG) and isoconversional methods were employed to determine triplet kinetic (activation energy, reaction model and pre-exponential factor). Through TGA and DTG, the conversion degree is described as a function of temperature for five heating rates (10, 20, 30, 40 and [Formula: see text] C/min) and four model-free methods (Flynn-Wall-Ozawa (FWO), Kissinger-Akahira-Sunose (KAS), Friedman, and Vyazovkin) with temperatures ranging from 25 to 1000(°)C were employed. Isoconversional lines were built for every method at different isoconversional degrees [Formula: see text]. The activation energy E was found as a function of α in the interval [Formula: see text] where each isoconversional methods were in agreement and the estimated error was sufficiently small. Findings show the same activation energy profile independently of the isoconversional method. In particular the total variation of E in [Formula: see text] was as follows: 209.909–228.238 kJ/mol (FWO); 211.235–229.277 kJ/mol (KAS); 223.050–188.512 kJ/mol (Friedman), and 211.449 kJ/mol-229.512 kJ/mol (Vyazovkin). The reaction model of the process in [Formula: see text] matched with a two-dimensional diffusion ([Formula: see text]) by using a master-plot analysis. The calculated and reported parameters are fundamental information for the pyrolysis reactor design using Sawmill wastes as feedstock. Elsevier 2019-11-01 /pmc/articles/PMC6838918/ /pubmed/31720467 http://dx.doi.org/10.1016/j.heliyon.2019.e02723 Text en © 2019 Published by Elsevier Ltd. http://creativecommons.org/licenses/by-nc-nd/4.0/ This is an open access article under the CC BY-NC-ND license (http://creativecommons.org/licenses/by-nc-nd/4.0/). |
spellingShingle | Article Bonilla, Javier Salazar, Robert Paul Mayorga, Manuel Kinetic triplet of Colombian sawmill wastes using thermogravimetric analysis |
title | Kinetic triplet of Colombian sawmill wastes using thermogravimetric analysis |
title_full | Kinetic triplet of Colombian sawmill wastes using thermogravimetric analysis |
title_fullStr | Kinetic triplet of Colombian sawmill wastes using thermogravimetric analysis |
title_full_unstemmed | Kinetic triplet of Colombian sawmill wastes using thermogravimetric analysis |
title_short | Kinetic triplet of Colombian sawmill wastes using thermogravimetric analysis |
title_sort | kinetic triplet of colombian sawmill wastes using thermogravimetric analysis |
topic | Article |
url | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC6838918/ https://www.ncbi.nlm.nih.gov/pubmed/31720467 http://dx.doi.org/10.1016/j.heliyon.2019.e02723 |
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