The role of post-pyrolysis carbon dioxide capture in hydrogen recovery from waste-derived pyrolysis gas

The study elucidated the role of post-pyrolysis CO2 removal using a CaO sorbent on upgrading pyrolysis gas into H2-rich gas. The pyrolysis gas was obtained from various waste-derived feedstocks (municipal sewage sludge, refused derived fuel (RDF), pine sawdust (biomass), and marine litter) by pyroly...

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Main Authors: Wang, Yuxin, Veksha, Andrei, Ong, Joel, Ueki, Yasuaki, Yoshiie, Ryo, Naruse, Ichiro, Lisak, Grzegorz
Other Authors: School of Civil and Environmental Engineering
Format: Article
Language:English
Published: 2024
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Online Access:https://hdl.handle.net/10356/180711
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Institution: Nanyang Technological University
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spelling sg-ntu-dr.10356-1807112024-10-21T08:11:49Z The role of post-pyrolysis carbon dioxide capture in hydrogen recovery from waste-derived pyrolysis gas Wang, Yuxin Veksha, Andrei Ong, Joel Ueki, Yasuaki Yoshiie, Ryo Naruse, Ichiro Lisak, Grzegorz School of Civil and Environmental Engineering Nanyang Environment and Water Research Institute Residues and Resource Reclamation Centre Engineering Pyrolysis-thermolysis Kinetic parameters The study elucidated the role of post-pyrolysis CO2 removal using a CaO sorbent on upgrading pyrolysis gas into H2-rich gas. The pyrolysis gas was obtained from various waste-derived feedstocks (municipal sewage sludge, refused derived fuel (RDF), pine sawdust (biomass), and marine litter) by pyrolysis (600 °C), and underwent the treatment with CaO (600 °C) followed by the thermolytic decomposition at 1300 °C. The results show that CaO utilization does not change significantly H2 yield and higher heating value of gas on a feedstock mass basis but increases H2 purity from 49.6–83.3 to 63.7–94.4 vol% and H2/CO ratio from 1.1–5.7 to 1.9–19.8 of the product gas across all feedstocks. Normalized rate constants K for CO2 capture by CaO, determined by the grain model, varied between 0.0001 and 0.0006 min−1, revealing the feedstock-specific effectiveness of CaO. The higher CaO consumption rates were observed in case of RDF and biomass compared to sludge and marine litter. This could be attributed to the coking and faster carbonation of CaO caused by the composition of pyrolytic products. The obtained results emphasize the potential of integrating CaO sorbent into pyrolysis-based processes for the production of decarbonized H2-rich gas with higher purity. Moreover, the use of normalized kinetic parameters provides a straightforward method for the selection of feedstocks suitable for decarbonization of pyrolysis gas using CaO sorbent. The predominant factor affecting the carbonation kinetics of the CaO sorbent was found to be the CO2 flow rates in their respective pyrolysis gases. National Research Foundation (NRF) Public Utilities Board (PUB) The authors extend their gratitude to the World Wide Fund for Nature (Singapore) Limited for supplying a feedstock essential for this study. We also thank the DII Collaborative Graduate Program and the THERS Interdisciplinary Frontier Next Generation Researcher, Nagoya University for their financial support. This work was supported by the National Research Foundation, Singapore, and PUB, Singapore’s National Water Agency, under the RIE2025 Urban Solutions and Sustainability (USS) (Water) Center of Excellence (CoE) Program awarded to the Nanyang Environment & Water Research Institute (NEWRI), Nanyang Technological University, Singapore. The views expressed herein are those of the authors and do not necessarily reflect the views of the National Research Foundation, Singapore, or PUB, Singapore’s National Water Agency. 2024-10-21T08:11:49Z 2024-10-21T08:11:49Z 2025 Journal Article Wang, Y., Veksha, A., Ong, J., Ueki, Y., Yoshiie, R., Naruse, I. & Lisak, G. (2025). The role of post-pyrolysis carbon dioxide capture in hydrogen recovery from waste-derived pyrolysis gas. Fuel, 381, 133293-. https://dx.doi.org/10.1016/j.fuel.2024.133293 0016-2361 https://hdl.handle.net/10356/180711 10.1016/j.fuel.2024.133293 2-s2.0-85205136868 381 133293 en Fuel © 2024 Elsevier Ltd. All rights are reserved, including those for text and data mining, AI training, and similar technologies.
institution Nanyang Technological University
building NTU Library
continent Asia
country Singapore
Singapore
content_provider NTU Library
collection DR-NTU
language English
topic Engineering
Pyrolysis-thermolysis
Kinetic parameters
spellingShingle Engineering
Pyrolysis-thermolysis
Kinetic parameters
Wang, Yuxin
Veksha, Andrei
Ong, Joel
Ueki, Yasuaki
Yoshiie, Ryo
Naruse, Ichiro
Lisak, Grzegorz
The role of post-pyrolysis carbon dioxide capture in hydrogen recovery from waste-derived pyrolysis gas
description The study elucidated the role of post-pyrolysis CO2 removal using a CaO sorbent on upgrading pyrolysis gas into H2-rich gas. The pyrolysis gas was obtained from various waste-derived feedstocks (municipal sewage sludge, refused derived fuel (RDF), pine sawdust (biomass), and marine litter) by pyrolysis (600 °C), and underwent the treatment with CaO (600 °C) followed by the thermolytic decomposition at 1300 °C. The results show that CaO utilization does not change significantly H2 yield and higher heating value of gas on a feedstock mass basis but increases H2 purity from 49.6–83.3 to 63.7–94.4 vol% and H2/CO ratio from 1.1–5.7 to 1.9–19.8 of the product gas across all feedstocks. Normalized rate constants K for CO2 capture by CaO, determined by the grain model, varied between 0.0001 and 0.0006 min−1, revealing the feedstock-specific effectiveness of CaO. The higher CaO consumption rates were observed in case of RDF and biomass compared to sludge and marine litter. This could be attributed to the coking and faster carbonation of CaO caused by the composition of pyrolytic products. The obtained results emphasize the potential of integrating CaO sorbent into pyrolysis-based processes for the production of decarbonized H2-rich gas with higher purity. Moreover, the use of normalized kinetic parameters provides a straightforward method for the selection of feedstocks suitable for decarbonization of pyrolysis gas using CaO sorbent. The predominant factor affecting the carbonation kinetics of the CaO sorbent was found to be the CO2 flow rates in their respective pyrolysis gases.
author2 School of Civil and Environmental Engineering
author_facet School of Civil and Environmental Engineering
Wang, Yuxin
Veksha, Andrei
Ong, Joel
Ueki, Yasuaki
Yoshiie, Ryo
Naruse, Ichiro
Lisak, Grzegorz
format Article
author Wang, Yuxin
Veksha, Andrei
Ong, Joel
Ueki, Yasuaki
Yoshiie, Ryo
Naruse, Ichiro
Lisak, Grzegorz
author_sort Wang, Yuxin
title The role of post-pyrolysis carbon dioxide capture in hydrogen recovery from waste-derived pyrolysis gas
title_short The role of post-pyrolysis carbon dioxide capture in hydrogen recovery from waste-derived pyrolysis gas
title_full The role of post-pyrolysis carbon dioxide capture in hydrogen recovery from waste-derived pyrolysis gas
title_fullStr The role of post-pyrolysis carbon dioxide capture in hydrogen recovery from waste-derived pyrolysis gas
title_full_unstemmed The role of post-pyrolysis carbon dioxide capture in hydrogen recovery from waste-derived pyrolysis gas
title_sort role of post-pyrolysis carbon dioxide capture in hydrogen recovery from waste-derived pyrolysis gas
publishDate 2024
url https://hdl.handle.net/10356/180711
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