Sustainable hydrogen production and CO2 mitigation from acetic acid dry reforming over Ni/Al2O3 catalyst

Dry reforming of acetic acid (DRA) was first-time investigated on 10%Ni/Al2O3 at varied temperatures within 923–973 K employing several CO2:CH3COOH ratios of 1.5:2; 1:1; and 2:1. Depending on NiO particle size and location on support surface or inside the porous support structure, the H2 reduction o...

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Main Authors: Nguyen, Anh-Tam, Ng, Kim Hoong, Kumar, Ponnusamy Senthil, Pham, Thuy-Phuong T., Herma Dina, Setiabudi, Mohammad Yusuf, ., Pham, Le Kim Hoang, Show, Pau Loke, Hussain, Ijaz, Vo, Dai-Viet N.
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Language:English
English
Published: Elsevier Ltd 2024
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Online Access:http://umpir.ump.edu.my/id/eprint/43114/1/Sustainable%20hydrogen%20production%20and%20CO2%20mitigation_ABST.pdf
http://umpir.ump.edu.my/id/eprint/43114/2/Sustainable%20hydrogen%20production%20and%20CO2%20mitigation.pdf
http://umpir.ump.edu.my/id/eprint/43114/
https://doi.org/10.1016/j.ijhydene.2024.02.179
https://doi.org/10.1016/j.ijhydene.2024.02.179
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spelling my.ump.umpir.431142024-12-10T07:18:09Z http://umpir.ump.edu.my/id/eprint/43114/ Sustainable hydrogen production and CO2 mitigation from acetic acid dry reforming over Ni/Al2O3 catalyst Nguyen, Anh-Tam Ng, Kim Hoong Kumar, Ponnusamy Senthil Pham, Thuy-Phuong T. Herma Dina, Setiabudi Mohammad Yusuf, . Pham, Le Kim Hoang Show, Pau Loke Hussain, Ijaz Vo, Dai-Viet N. TP Chemical technology Dry reforming of acetic acid (DRA) was first-time investigated on 10%Ni/Al2O3 at varied temperatures within 923–973 K employing several CO2:CH3COOH ratios of 1.5:2; 1:1; and 2:1. Depending on NiO particle size and location on support surface or inside the porous support structure, the H2 reduction of NiO phase to active metallic Ni0 form was evidenced at different reduction temperatures within 550–950 K and the estimated degree of reduction was about 73.68%. Weak, medium, and strong basic centres were evidenced on 10%Ni/Al2O3 via CO2 desorption measurement. Increasing DRA temperature improved both CH3COOH and CO2 conversions with the corresponding apparent activation energy of 100.71 and 58.50 kJ mol−1. As CO2 partial pressure was increased from 0 to 40 kPa, the initial CH3COOH conversion was noticeably enhanced from 30.5% to 97.8% whilst H2/CO ratio always remained less than unity (0.73–0.77). Notably, DRA was a two-step process and barely negligible CH4 intermediate product was evidenced since it was promptly reformed by CO2 into syngas. The Ni0 active form was not susceptible to oxidation during DRA and carbon deposited on spent catalyst surface was heterogeneous in nature with the evident co-existence of amorphous and graphitic carbons. Elsevier Ltd 2024-05-20 Article PeerReviewed pdf en http://umpir.ump.edu.my/id/eprint/43114/1/Sustainable%20hydrogen%20production%20and%20CO2%20mitigation_ABST.pdf pdf en http://umpir.ump.edu.my/id/eprint/43114/2/Sustainable%20hydrogen%20production%20and%20CO2%20mitigation.pdf Nguyen, Anh-Tam and Ng, Kim Hoong and Kumar, Ponnusamy Senthil and Pham, Thuy-Phuong T. and Herma Dina, Setiabudi and Mohammad Yusuf, . and Pham, Le Kim Hoang and Show, Pau Loke and Hussain, Ijaz and Vo, Dai-Viet N. (2024) Sustainable hydrogen production and CO2 mitigation from acetic acid dry reforming over Ni/Al2O3 catalyst. International Journal of Hydrogen Energy, 67. 1044 -1055. ISSN 0360-3199. (Published) https://doi.org/10.1016/j.ijhydene.2024.02.179 https://doi.org/10.1016/j.ijhydene.2024.02.179
institution Universiti Malaysia Pahang Al-Sultan Abdullah
building UMPSA Library
collection Institutional Repository
continent Asia
country Malaysia
content_provider Universiti Malaysia Pahang Al-Sultan Abdullah
content_source UMPSA Institutional Repository
url_provider http://umpir.ump.edu.my/
language English
English
topic TP Chemical technology
spellingShingle TP Chemical technology
Nguyen, Anh-Tam
Ng, Kim Hoong
Kumar, Ponnusamy Senthil
Pham, Thuy-Phuong T.
Herma Dina, Setiabudi
Mohammad Yusuf, .
Pham, Le Kim Hoang
Show, Pau Loke
Hussain, Ijaz
Vo, Dai-Viet N.
Sustainable hydrogen production and CO2 mitigation from acetic acid dry reforming over Ni/Al2O3 catalyst
description Dry reforming of acetic acid (DRA) was first-time investigated on 10%Ni/Al2O3 at varied temperatures within 923–973 K employing several CO2:CH3COOH ratios of 1.5:2; 1:1; and 2:1. Depending on NiO particle size and location on support surface or inside the porous support structure, the H2 reduction of NiO phase to active metallic Ni0 form was evidenced at different reduction temperatures within 550–950 K and the estimated degree of reduction was about 73.68%. Weak, medium, and strong basic centres were evidenced on 10%Ni/Al2O3 via CO2 desorption measurement. Increasing DRA temperature improved both CH3COOH and CO2 conversions with the corresponding apparent activation energy of 100.71 and 58.50 kJ mol−1. As CO2 partial pressure was increased from 0 to 40 kPa, the initial CH3COOH conversion was noticeably enhanced from 30.5% to 97.8% whilst H2/CO ratio always remained less than unity (0.73–0.77). Notably, DRA was a two-step process and barely negligible CH4 intermediate product was evidenced since it was promptly reformed by CO2 into syngas. The Ni0 active form was not susceptible to oxidation during DRA and carbon deposited on spent catalyst surface was heterogeneous in nature with the evident co-existence of amorphous and graphitic carbons.
format Article
author Nguyen, Anh-Tam
Ng, Kim Hoong
Kumar, Ponnusamy Senthil
Pham, Thuy-Phuong T.
Herma Dina, Setiabudi
Mohammad Yusuf, .
Pham, Le Kim Hoang
Show, Pau Loke
Hussain, Ijaz
Vo, Dai-Viet N.
author_facet Nguyen, Anh-Tam
Ng, Kim Hoong
Kumar, Ponnusamy Senthil
Pham, Thuy-Phuong T.
Herma Dina, Setiabudi
Mohammad Yusuf, .
Pham, Le Kim Hoang
Show, Pau Loke
Hussain, Ijaz
Vo, Dai-Viet N.
author_sort Nguyen, Anh-Tam
title Sustainable hydrogen production and CO2 mitigation from acetic acid dry reforming over Ni/Al2O3 catalyst
title_short Sustainable hydrogen production and CO2 mitigation from acetic acid dry reforming over Ni/Al2O3 catalyst
title_full Sustainable hydrogen production and CO2 mitigation from acetic acid dry reforming over Ni/Al2O3 catalyst
title_fullStr Sustainable hydrogen production and CO2 mitigation from acetic acid dry reforming over Ni/Al2O3 catalyst
title_full_unstemmed Sustainable hydrogen production and CO2 mitigation from acetic acid dry reforming over Ni/Al2O3 catalyst
title_sort sustainable hydrogen production and co2 mitigation from acetic acid dry reforming over ni/al2o3 catalyst
publisher Elsevier Ltd
publishDate 2024
url http://umpir.ump.edu.my/id/eprint/43114/1/Sustainable%20hydrogen%20production%20and%20CO2%20mitigation_ABST.pdf
http://umpir.ump.edu.my/id/eprint/43114/2/Sustainable%20hydrogen%20production%20and%20CO2%20mitigation.pdf
http://umpir.ump.edu.my/id/eprint/43114/
https://doi.org/10.1016/j.ijhydene.2024.02.179
https://doi.org/10.1016/j.ijhydene.2024.02.179
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