Thermochemical Conversion of Biomass in the Presence of Molten Alkali-Metal Carbonates under Reducing Environments of N<sub>2</sub> and CO<sub>2</sub>
The impact of N<sub>2</sub> and CO<sub>2</sub> atmospheres on the interaction between Eucalyptus pilularis biomass and a ternary molten carbonate eutectic (Li<sub>2</sub>CO<sub>3</sub>: Na<sub>2</sub>CO<sub>3</sub>: K<sub>...
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doaj-3e94a80b367d4f7689c59b222c45b3cc2020-11-25T02:26:16ZengMDPI AGEnergies1996-10732020-10-01135395539510.3390/en13205395Thermochemical Conversion of Biomass in the Presence of Molten Alkali-Metal Carbonates under Reducing Environments of N<sub>2</sub> and CO<sub>2</sub>Tahereh Jalalabadi0Behdad Moghtaderi1Jessica Allen2School of Chemical Engineering, University of Newcastle, University Drive, Callaghan, NSW 2308, AustraliaSchool of Chemical Engineering, University of Newcastle, University Drive, Callaghan, NSW 2308, AustraliaSchool of Chemical Engineering, University of Newcastle, University Drive, Callaghan, NSW 2308, AustraliaThe impact of N<sub>2</sub> and CO<sub>2</sub> atmospheres on the interaction between Eucalyptus pilularis biomass and a ternary molten carbonate eutectic (Li<sub>2</sub>CO<sub>3</sub>: Na<sub>2</sub>CO<sub>3</sub>: K<sub>2</sub>CO<sub>3</sub>) has been investigated at 600 °C and 900 °C. For lower temperature conversion under CO<sub>2</sub>, prevention of volatile release in the eutectic treated biomass is slightly higher than under N<sub>2</sub> injection; however, similar bubble-shaped morphology of the remnant char is observed under both carrier gases. By increasing the temperature to 900 °C under CO<sub>2</sub>, the reverse Boudouard reaction begins to consume carbon fuel, while molten carbonate gasification also accelerates the reaction to a lower temperature set point (shifted from ~735 °C to ~640 °C). The mass loss of carbonate under CO<sub>2</sub> and N<sub>2</sub> at 900 °C is 0 (negligible) and 18 wt.%, respectively. In the absence of carbon particles, the decomposition of carbonate to M<sub>2</sub>O (l) and CO<sub>2</sub> (g), as well as molten salt vaporization, are the sole potential routes of weight loss in an inert gas. Previous observations of biomass and eutectic mixture thermochemical conversion under N<sub>2</sub> have suggested carbon/carbonate gasification is dominant at elevated temperatures, with production of CO expected. However, analysis of gas chromatography (GC) suggests that carbon/carbonate gasification is the weaker pathway by producing only 7 vol.% of CO, compared with molten carbonate decomposition with 27 vol.% CO<sub>2 </sub>emission for this system.https://www.mdpi.com/1996-1073/13/20/5395slow pyrolysisBoudouard reactioncarbonate gasificationternary eutecticbiomass |
collection |
DOAJ |
language |
English |
format |
Article |
sources |
DOAJ |
author |
Tahereh Jalalabadi Behdad Moghtaderi Jessica Allen |
spellingShingle |
Tahereh Jalalabadi Behdad Moghtaderi Jessica Allen Thermochemical Conversion of Biomass in the Presence of Molten Alkali-Metal Carbonates under Reducing Environments of N<sub>2</sub> and CO<sub>2</sub> Energies slow pyrolysis Boudouard reaction carbonate gasification ternary eutectic biomass |
author_facet |
Tahereh Jalalabadi Behdad Moghtaderi Jessica Allen |
author_sort |
Tahereh Jalalabadi |
title |
Thermochemical Conversion of Biomass in the Presence of Molten Alkali-Metal Carbonates under Reducing Environments of N<sub>2</sub> and CO<sub>2</sub> |
title_short |
Thermochemical Conversion of Biomass in the Presence of Molten Alkali-Metal Carbonates under Reducing Environments of N<sub>2</sub> and CO<sub>2</sub> |
title_full |
Thermochemical Conversion of Biomass in the Presence of Molten Alkali-Metal Carbonates under Reducing Environments of N<sub>2</sub> and CO<sub>2</sub> |
title_fullStr |
Thermochemical Conversion of Biomass in the Presence of Molten Alkali-Metal Carbonates under Reducing Environments of N<sub>2</sub> and CO<sub>2</sub> |
title_full_unstemmed |
Thermochemical Conversion of Biomass in the Presence of Molten Alkali-Metal Carbonates under Reducing Environments of N<sub>2</sub> and CO<sub>2</sub> |
title_sort |
thermochemical conversion of biomass in the presence of molten alkali-metal carbonates under reducing environments of n<sub>2</sub> and co<sub>2</sub> |
publisher |
MDPI AG |
series |
Energies |
issn |
1996-1073 |
publishDate |
2020-10-01 |
description |
The impact of N<sub>2</sub> and CO<sub>2</sub> atmospheres on the interaction between Eucalyptus pilularis biomass and a ternary molten carbonate eutectic (Li<sub>2</sub>CO<sub>3</sub>: Na<sub>2</sub>CO<sub>3</sub>: K<sub>2</sub>CO<sub>3</sub>) has been investigated at 600 °C and 900 °C. For lower temperature conversion under CO<sub>2</sub>, prevention of volatile release in the eutectic treated biomass is slightly higher than under N<sub>2</sub> injection; however, similar bubble-shaped morphology of the remnant char is observed under both carrier gases. By increasing the temperature to 900 °C under CO<sub>2</sub>, the reverse Boudouard reaction begins to consume carbon fuel, while molten carbonate gasification also accelerates the reaction to a lower temperature set point (shifted from ~735 °C to ~640 °C). The mass loss of carbonate under CO<sub>2</sub> and N<sub>2</sub> at 900 °C is 0 (negligible) and 18 wt.%, respectively. In the absence of carbon particles, the decomposition of carbonate to M<sub>2</sub>O (l) and CO<sub>2</sub> (g), as well as molten salt vaporization, are the sole potential routes of weight loss in an inert gas. Previous observations of biomass and eutectic mixture thermochemical conversion under N<sub>2</sub> have suggested carbon/carbonate gasification is dominant at elevated temperatures, with production of CO expected. However, analysis of gas chromatography (GC) suggests that carbon/carbonate gasification is the weaker pathway by producing only 7 vol.% of CO, compared with molten carbonate decomposition with 27 vol.% CO<sub>2 </sub>emission for this system. |
topic |
slow pyrolysis Boudouard reaction carbonate gasification ternary eutectic biomass |
url |
https://www.mdpi.com/1996-1073/13/20/5395 |
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