Selective aromatic production from fast pyrolysis of sugarcane bagasse lignin over ZSM-5 catalyst
Organosolv lignin extracted from sugarcane bagasse (BG-lignin) and commercial grade lignin (Comm-OS) were use as starting materials in this study. From our previous work, aromatic furan (2,3-dihydrobenzofurn) was mainly produced from fast pyrolysis of BG-lignin and Comm-OS at 400–600 °C while alkyl...
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oai:doaj.org-article:3bfa42a425c142c0848839ba2f1a4fa62021-11-18T04:49:25ZSelective aromatic production from fast pyrolysis of sugarcane bagasse lignin over ZSM-5 catalyst2352-484710.1016/j.egyr.2021.07.057https://doaj.org/article/3bfa42a425c142c0848839ba2f1a4fa62021-11-01T00:00:00Zhttp://www.sciencedirect.com/science/article/pii/S2352484721005230https://doaj.org/toc/2352-4847Organosolv lignin extracted from sugarcane bagasse (BG-lignin) and commercial grade lignin (Comm-OS) were use as starting materials in this study. From our previous work, aromatic furan (2,3-dihydrobenzofurn) was mainly produced from fast pyrolysis of BG-lignin and Comm-OS at 400–600 °C while alkyl phenol and phenol are more favorable at 700 °C. However, more thermal fragmentation was simultaneously redundant which results in low aromatic selectivity. In this work, aromatic production from lignin with molecular sieve ZSM-5 catalysts was studied using Py-GCMS instrument with biomass to catalyst ratio (B:C) of 1:1, 1:5, and 1:10. Aromatic furan and monolignol (H-unit, G-unit, and S-unit) were transform to hydrocarbon species with addition of ZSM-5 catalyst according to elimination of side chain by demethoxylation, dehydroxylation, and dealkylation reactions. Maximum aromatic production was found at B:C of 1:10 for both Comm-OS and BG-lignin of 87.31% and 88.22%, respectively, while aliphatic hydrocarbon was more abundant for BG-lignin of 43.21% (1:5). Moreover, ZSM-5 exhibit instinctive performance on MAHs and PAHs production especially at B:C of 1:5 and 1:10. Nevertheless, polymerization between MAHs results in PAHs also observed for both Comm-OS and BG-lignin. From the result, transformation of aromatic furan could be limited by introduction of molecular sieve ZSM-5 which enhance the oxygen elimination from phenol derivative and favorable for aromatic and BTX production.Kanit SoongprasitViboon SricharoenchaikulDuangduen AtongElsevierarticleLigninSugarcane bagasseOrganosolv processFast pyrolysisZSM-5AromaticElectrical engineering. Electronics. Nuclear engineeringTK1-9971ENEnergy Reports, Vol 7, Iss , Pp 830-843 (2021) |
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Lignin Sugarcane bagasse Organosolv process Fast pyrolysis ZSM-5 Aromatic Electrical engineering. Electronics. Nuclear engineering TK1-9971 |
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Lignin Sugarcane bagasse Organosolv process Fast pyrolysis ZSM-5 Aromatic Electrical engineering. Electronics. Nuclear engineering TK1-9971 Kanit Soongprasit Viboon Sricharoenchaikul Duangduen Atong Selective aromatic production from fast pyrolysis of sugarcane bagasse lignin over ZSM-5 catalyst |
description |
Organosolv lignin extracted from sugarcane bagasse (BG-lignin) and commercial grade lignin (Comm-OS) were use as starting materials in this study. From our previous work, aromatic furan (2,3-dihydrobenzofurn) was mainly produced from fast pyrolysis of BG-lignin and Comm-OS at 400–600 °C while alkyl phenol and phenol are more favorable at 700 °C. However, more thermal fragmentation was simultaneously redundant which results in low aromatic selectivity. In this work, aromatic production from lignin with molecular sieve ZSM-5 catalysts was studied using Py-GCMS instrument with biomass to catalyst ratio (B:C) of 1:1, 1:5, and 1:10. Aromatic furan and monolignol (H-unit, G-unit, and S-unit) were transform to hydrocarbon species with addition of ZSM-5 catalyst according to elimination of side chain by demethoxylation, dehydroxylation, and dealkylation reactions. Maximum aromatic production was found at B:C of 1:10 for both Comm-OS and BG-lignin of 87.31% and 88.22%, respectively, while aliphatic hydrocarbon was more abundant for BG-lignin of 43.21% (1:5). Moreover, ZSM-5 exhibit instinctive performance on MAHs and PAHs production especially at B:C of 1:5 and 1:10. Nevertheless, polymerization between MAHs results in PAHs also observed for both Comm-OS and BG-lignin. From the result, transformation of aromatic furan could be limited by introduction of molecular sieve ZSM-5 which enhance the oxygen elimination from phenol derivative and favorable for aromatic and BTX production. |
format |
article |
author |
Kanit Soongprasit Viboon Sricharoenchaikul Duangduen Atong |
author_facet |
Kanit Soongprasit Viboon Sricharoenchaikul Duangduen Atong |
author_sort |
Kanit Soongprasit |
title |
Selective aromatic production from fast pyrolysis of sugarcane bagasse lignin over ZSM-5 catalyst |
title_short |
Selective aromatic production from fast pyrolysis of sugarcane bagasse lignin over ZSM-5 catalyst |
title_full |
Selective aromatic production from fast pyrolysis of sugarcane bagasse lignin over ZSM-5 catalyst |
title_fullStr |
Selective aromatic production from fast pyrolysis of sugarcane bagasse lignin over ZSM-5 catalyst |
title_full_unstemmed |
Selective aromatic production from fast pyrolysis of sugarcane bagasse lignin over ZSM-5 catalyst |
title_sort |
selective aromatic production from fast pyrolysis of sugarcane bagasse lignin over zsm-5 catalyst |
publisher |
Elsevier |
publishDate |
2021 |
url |
https://doaj.org/article/3bfa42a425c142c0848839ba2f1a4fa6 |
work_keys_str_mv |
AT kanitsoongprasit selectivearomaticproductionfromfastpyrolysisofsugarcanebagasseligninoverzsm5catalyst AT viboonsricharoenchaikul selectivearomaticproductionfromfastpyrolysisofsugarcanebagasseligninoverzsm5catalyst AT duangduenatong selectivearomaticproductionfromfastpyrolysisofsugarcanebagasseligninoverzsm5catalyst |
_version_ |
1718425033600139264 |