Steam Reforming of High-Concentration Toluene as a Model Biomass Tar Using a Nickel Catalyst Supported on Carbon Black

Biomass tar, an inevitable byproduct of biomass pyrolysis and gasification, poses a significant challenge due to its tendency to condense in pipelines, causing clogging and operational issues. Catalytic steam reforming can convert tar into syngas, addressing the tar issue while simultaneously produc...

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Main Authors: Soohyun Kim, Sangjun Yoon, Zulqarnain, Jiho Yoo, Hyuk Im, Sangdo Kim, Donghyuk Chun, Hokyung Choi, Jeonghwan Lim
Format: Article
Language:English
Published: MDPI AG 2025-01-01
Series:Energies
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Online Access:https://www.mdpi.com/1996-1073/18/2/327
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author Soohyun Kim
Sangjun Yoon
Zulqarnain
Jiho Yoo
Hyuk Im
Sangdo Kim
Donghyuk Chun
Hokyung Choi
Jeonghwan Lim
author_facet Soohyun Kim
Sangjun Yoon
Zulqarnain
Jiho Yoo
Hyuk Im
Sangdo Kim
Donghyuk Chun
Hokyung Choi
Jeonghwan Lim
author_sort Soohyun Kim
collection DOAJ
description Biomass tar, an inevitable byproduct of biomass pyrolysis and gasification, poses a significant challenge due to its tendency to condense in pipelines, causing clogging and operational issues. Catalytic steam reforming can convert tar into syngas, addressing the tar issue while simultaneously producing hydrogen. However, the reforming catalyst is highly susceptible to deactivation by coking, especially when dealing with highly concentrated polymeric hydrocarbons such as tar. This study focused on enhancing the durability of tar-reforming catalysts. Nickel-based catalysts were prepared using carbon supports known for their high coking resistance, such as carbon black (CB), activated carbon (AC), and low-rank coal (LRC). Their performance was then tested for the steam reforming of high-concentration toluene, a representative tar. All three carbon supports (CB, AC, LRC) showed high catalytic performance with NiMg catalysts at 500 °C. Among them, the mesoporous CB support exhibited the highest stability when exposed to steam, with NiMg on CB (NiMg/CB) remaining stable for long-term continuous operation without any deactivation due to coking or thermal degradation.
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institution Kabale University
issn 1996-1073
language English
publishDate 2025-01-01
publisher MDPI AG
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series Energies
spelling doaj-art-5eeebde6e2c843b7ae01dbb040f9928a2025-01-24T13:31:04ZengMDPI AGEnergies1996-10732025-01-0118232710.3390/en18020327Steam Reforming of High-Concentration Toluene as a Model Biomass Tar Using a Nickel Catalyst Supported on Carbon BlackSoohyun Kim0Sangjun Yoon1Zulqarnain2Jiho Yoo3Hyuk Im4Sangdo Kim5Donghyuk Chun6Hokyung Choi7Jeonghwan Lim8Clean Air Research Laboratory, Korea Institute of Energy Research, Daejeon 34129, Republic of KoreaClean Fuel Research Laboratory, Korea Institute of Energy Research, Daejeon 34129, Republic of KoreaClean Air Research Laboratory, Korea Institute of Energy Research, Daejeon 34129, Republic of KoreaClean Air Research Laboratory, Korea Institute of Energy Research, Daejeon 34129, Republic of KoreaClean Air Research Laboratory, Korea Institute of Energy Research, Daejeon 34129, Republic of KoreaClean Air Research Laboratory, Korea Institute of Energy Research, Daejeon 34129, Republic of KoreaClean Air Research Laboratory, Korea Institute of Energy Research, Daejeon 34129, Republic of KoreaClean Air Research Laboratory, Korea Institute of Energy Research, Daejeon 34129, Republic of KoreaClean Air Research Laboratory, Korea Institute of Energy Research, Daejeon 34129, Republic of KoreaBiomass tar, an inevitable byproduct of biomass pyrolysis and gasification, poses a significant challenge due to its tendency to condense in pipelines, causing clogging and operational issues. Catalytic steam reforming can convert tar into syngas, addressing the tar issue while simultaneously producing hydrogen. However, the reforming catalyst is highly susceptible to deactivation by coking, especially when dealing with highly concentrated polymeric hydrocarbons such as tar. This study focused on enhancing the durability of tar-reforming catalysts. Nickel-based catalysts were prepared using carbon supports known for their high coking resistance, such as carbon black (CB), activated carbon (AC), and low-rank coal (LRC). Their performance was then tested for the steam reforming of high-concentration toluene, a representative tar. All three carbon supports (CB, AC, LRC) showed high catalytic performance with NiMg catalysts at 500 °C. Among them, the mesoporous CB support exhibited the highest stability when exposed to steam, with NiMg on CB (NiMg/CB) remaining stable for long-term continuous operation without any deactivation due to coking or thermal degradation.https://www.mdpi.com/1996-1073/18/2/327biomass tarsteam reformingcarbon blackcokinghydrogen
spellingShingle Soohyun Kim
Sangjun Yoon
Zulqarnain
Jiho Yoo
Hyuk Im
Sangdo Kim
Donghyuk Chun
Hokyung Choi
Jeonghwan Lim
Steam Reforming of High-Concentration Toluene as a Model Biomass Tar Using a Nickel Catalyst Supported on Carbon Black
Energies
biomass tar
steam reforming
carbon black
coking
hydrogen
title Steam Reforming of High-Concentration Toluene as a Model Biomass Tar Using a Nickel Catalyst Supported on Carbon Black
title_full Steam Reforming of High-Concentration Toluene as a Model Biomass Tar Using a Nickel Catalyst Supported on Carbon Black
title_fullStr Steam Reforming of High-Concentration Toluene as a Model Biomass Tar Using a Nickel Catalyst Supported on Carbon Black
title_full_unstemmed Steam Reforming of High-Concentration Toluene as a Model Biomass Tar Using a Nickel Catalyst Supported on Carbon Black
title_short Steam Reforming of High-Concentration Toluene as a Model Biomass Tar Using a Nickel Catalyst Supported on Carbon Black
title_sort steam reforming of high concentration toluene as a model biomass tar using a nickel catalyst supported on carbon black
topic biomass tar
steam reforming
carbon black
coking
hydrogen
url https://www.mdpi.com/1996-1073/18/2/327
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