Effects of Briquetting and High Pyrolysis Temperature on Hydrolysis Lignin Char Properties and Reactivity in CO-CO<sub>2</sub>-N<sub>2</sub> Conditions

Carbonaceous reductants for pyrometallurgical applications are usually obtained from fossil-based sources. The most important properties of the reductants greatly depend on the application and the feeding of the reductant into the process. However, the mechanical strength, calorific value, fixed car...

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Main Authors: Aki Koskela, Anne Heikkilä, Davide Bergna, Justin Salminen, Timo Fabritius
Format: Article
Language:English
Published: MDPI AG 2021-02-01
Series:Minerals
Subjects:
Online Access:https://www.mdpi.com/2075-163X/11/2/187
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spelling doaj-57b7e3183fa249d1a7b45b0010a0e1c82021-02-12T00:03:46ZengMDPI AGMinerals2075-163X2021-02-011118718710.3390/min11020187Effects of Briquetting and High Pyrolysis Temperature on Hydrolysis Lignin Char Properties and Reactivity in CO-CO<sub>2</sub>-N<sub>2</sub> ConditionsAki Koskela0Anne Heikkilä1Davide Bergna2Justin Salminen3Timo Fabritius4Process Metallurgy, University of Oulu, P.O. Box 4300, FI-90014 Oulu, FinlandProcess Metallurgy, University of Oulu, P.O. Box 4300, FI-90014 Oulu, FinlandSustainable Chemistry, University of Oulu, P.O. Box 3000, FI-90014 Oulu, FinlandBoliden Kokkola Oy, P.O. Box 26, 67101 Kokkola, FinlandProcess Metallurgy, University of Oulu, P.O. Box 4300, FI-90014 Oulu, FinlandCarbonaceous reductants for pyrometallurgical applications are usually obtained from fossil-based sources. The most important properties of the reductants greatly depend on the application and the feeding of the reductant into the process. However, the mechanical strength, calorific value, fixed carbon content, and reactivity of the reductant are the properties that usually define the applicability of the reductant for different processes. The reactivity of the biochars is usually high in comparison to metallurgical coke, which may restrict the applicability of the biochar in reduction processes. One cause of the higher reactivity is the higher surface area of the biochars, which can be suppressed with agglomeration treatment, e.g., briquetting. In this work, hydrolysis lignin was used for slow pyrolysis experiments to produce biochars. The biochars were pyrolyzed in briquetted form and in as-received form at various temperatures. The reactivity values of the biochars were tested in dynamic reactivity tests in a CO-CO<sub>2</sub>-N<sub>2</sub> gas atmosphere at temperatures of up to 1350 °C. It was found that the yield of the hydrolysis lignin char only decreased by 3.36 wt% when the pyrolysis temperature was elevated from 600 to 1200 °C, while a decrease in yield of 4.88 wt% occurred when the pyrolysis temperature was elevated from 450 to 600 °C. The mass loss of hydrolysis lignin biochar in the reactivity experiment in CO-CO<sub>2</sub>-N<sub>2</sub> atmosphere was significantly decreased from 79.41 wt% to 56.80 wt% when the hydrolysis lignin was briquetted before the slow pyrolysis process and the temperature of the pyrolysis process was elevated from 600 to 1200 °C. This means that the mass loss of the material was suppressed by 22.61 wt% due to the higher pyrolysis temperature and briquetting process.https://www.mdpi.com/2075-163X/11/2/187biocharhigh-temperature pyrolysisbiomasshydrolysis ligninbiochar reactivity
collection DOAJ
language English
format Article
sources DOAJ
author Aki Koskela
Anne Heikkilä
Davide Bergna
Justin Salminen
Timo Fabritius
spellingShingle Aki Koskela
Anne Heikkilä
Davide Bergna
Justin Salminen
Timo Fabritius
Effects of Briquetting and High Pyrolysis Temperature on Hydrolysis Lignin Char Properties and Reactivity in CO-CO<sub>2</sub>-N<sub>2</sub> Conditions
Minerals
biochar
high-temperature pyrolysis
biomass
hydrolysis lignin
biochar reactivity
author_facet Aki Koskela
Anne Heikkilä
Davide Bergna
Justin Salminen
Timo Fabritius
author_sort Aki Koskela
title Effects of Briquetting and High Pyrolysis Temperature on Hydrolysis Lignin Char Properties and Reactivity in CO-CO<sub>2</sub>-N<sub>2</sub> Conditions
title_short Effects of Briquetting and High Pyrolysis Temperature on Hydrolysis Lignin Char Properties and Reactivity in CO-CO<sub>2</sub>-N<sub>2</sub> Conditions
title_full Effects of Briquetting and High Pyrolysis Temperature on Hydrolysis Lignin Char Properties and Reactivity in CO-CO<sub>2</sub>-N<sub>2</sub> Conditions
title_fullStr Effects of Briquetting and High Pyrolysis Temperature on Hydrolysis Lignin Char Properties and Reactivity in CO-CO<sub>2</sub>-N<sub>2</sub> Conditions
title_full_unstemmed Effects of Briquetting and High Pyrolysis Temperature on Hydrolysis Lignin Char Properties and Reactivity in CO-CO<sub>2</sub>-N<sub>2</sub> Conditions
title_sort effects of briquetting and high pyrolysis temperature on hydrolysis lignin char properties and reactivity in co-co<sub>2</sub>-n<sub>2</sub> conditions
publisher MDPI AG
series Minerals
issn 2075-163X
publishDate 2021-02-01
description Carbonaceous reductants for pyrometallurgical applications are usually obtained from fossil-based sources. The most important properties of the reductants greatly depend on the application and the feeding of the reductant into the process. However, the mechanical strength, calorific value, fixed carbon content, and reactivity of the reductant are the properties that usually define the applicability of the reductant for different processes. The reactivity of the biochars is usually high in comparison to metallurgical coke, which may restrict the applicability of the biochar in reduction processes. One cause of the higher reactivity is the higher surface area of the biochars, which can be suppressed with agglomeration treatment, e.g., briquetting. In this work, hydrolysis lignin was used for slow pyrolysis experiments to produce biochars. The biochars were pyrolyzed in briquetted form and in as-received form at various temperatures. The reactivity values of the biochars were tested in dynamic reactivity tests in a CO-CO<sub>2</sub>-N<sub>2</sub> gas atmosphere at temperatures of up to 1350 °C. It was found that the yield of the hydrolysis lignin char only decreased by 3.36 wt% when the pyrolysis temperature was elevated from 600 to 1200 °C, while a decrease in yield of 4.88 wt% occurred when the pyrolysis temperature was elevated from 450 to 600 °C. The mass loss of hydrolysis lignin biochar in the reactivity experiment in CO-CO<sub>2</sub>-N<sub>2</sub> atmosphere was significantly decreased from 79.41 wt% to 56.80 wt% when the hydrolysis lignin was briquetted before the slow pyrolysis process and the temperature of the pyrolysis process was elevated from 600 to 1200 °C. This means that the mass loss of the material was suppressed by 22.61 wt% due to the higher pyrolysis temperature and briquetting process.
topic biochar
high-temperature pyrolysis
biomass
hydrolysis lignin
biochar reactivity
url https://www.mdpi.com/2075-163X/11/2/187
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