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Activity of La(0.75)Sr(0.25)Cr(0.5)Mn(0.5)O(3−δ), Ni(3)Sn(2) and Gd-doped CeO(2) towards the reverse water-gas shift reaction and carburisation for a high-temperature H(2)O/CO(2) co-electrolysis

The syngas mixture of CO and H(2), e.g. from natural gas reforming, is currently an important feedstock supplier for the synthesis of numerous chemicals. In order to minimize fossil source dependency and reduce global warming, alternative processes to produce syngas, such as high-temperature co-elec...

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Autores principales: Bogolowski, Nicky, Sánchez Batalla, Beatriz, Shin, Baekkyoung, Drillet, Jean-Francois
Formato: Online Artículo Texto
Lenguaje:English
Publicado: The Royal Society of Chemistry 2020
Materias:
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC9050351/
https://www.ncbi.nlm.nih.gov/pubmed/35498580
http://dx.doi.org/10.1039/d0ra00362j
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author Bogolowski, Nicky
Sánchez Batalla, Beatriz
Shin, Baekkyoung
Drillet, Jean-Francois
author_facet Bogolowski, Nicky
Sánchez Batalla, Beatriz
Shin, Baekkyoung
Drillet, Jean-Francois
author_sort Bogolowski, Nicky
collection PubMed
description The syngas mixture of CO and H(2), e.g. from natural gas reforming, is currently an important feedstock supplier for the synthesis of numerous chemicals. In order to minimize fossil source dependency and reduce global warming, alternative processes to produce syngas, such as high-temperature co-electrolysis of H(2)O and CO(2)via the internal reverse water-gas shift (RWGS) reaction, may be meaningful. In this study, the influence of the H(2) : CO(2) ratio on the activity, selectivity and stability of the as-prepared La(0.75)Sr(0.25)Cr(0.5)Mn(0.5)O(3−δ) (LSCrM) and Ni(3)Sn(2) as well as commercial Ni and Gd-doped CeO(2) (GDC(20)) powder materials for the reverse RWGS reaction was investigated in a tubular quartz glass reactor at 700 °C and 800 °C and ambient pressure. The highest conversion factor close to the maximum value of 50% for CO was yielded for the LSCrM, Ni and GDC(20) samples by applying a 0.5 : 0.5 H(2) : CO(2) feed ratio at 800 °C. Similar activity was calculated for the Ni(3)Sn(2) alloy after normalization to the Ni mass content. Moreover, all the investigated catalysts exhibited higher selectivity for CO and H(2)O products than Ni, with which CH(4) molar concentrations up to 0.9% and 2.4% were collected at 800 °C and 700 °C, respectively. The influence of feed pressure on the carburisation process was inspected in a tubular Ni–Cr reactor. Under a carbon-rich gas mixture at 3 bar and 700 °C, large amounts of graphitic carbon were deposited solely on the Ni sample after 100 h of exposure time. After the exposure of the powder materials to 0.5 : 0.5 and 0.9 : 0.1 H(2) : CO(2) atmospheres for 300 h at 700 °C and 10 bar, traces of amorphous carbon were surprisingly detected only on Ni(3)Sn(2) powder via Raman microscopy. Thus, because GDC(20) ist not active for electrochemical H(2) production, LSCrM or a mixture of both LSCrM and GDC(20) materials appears to be the most promising candidate for Ni substitution in high-temperature H(2)O/CO(2) co-electrolysis.
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spelling pubmed-90503512022-04-29 Activity of La(0.75)Sr(0.25)Cr(0.5)Mn(0.5)O(3−δ), Ni(3)Sn(2) and Gd-doped CeO(2) towards the reverse water-gas shift reaction and carburisation for a high-temperature H(2)O/CO(2) co-electrolysis Bogolowski, Nicky Sánchez Batalla, Beatriz Shin, Baekkyoung Drillet, Jean-Francois RSC Adv Chemistry The syngas mixture of CO and H(2), e.g. from natural gas reforming, is currently an important feedstock supplier for the synthesis of numerous chemicals. In order to minimize fossil source dependency and reduce global warming, alternative processes to produce syngas, such as high-temperature co-electrolysis of H(2)O and CO(2)via the internal reverse water-gas shift (RWGS) reaction, may be meaningful. In this study, the influence of the H(2) : CO(2) ratio on the activity, selectivity and stability of the as-prepared La(0.75)Sr(0.25)Cr(0.5)Mn(0.5)O(3−δ) (LSCrM) and Ni(3)Sn(2) as well as commercial Ni and Gd-doped CeO(2) (GDC(20)) powder materials for the reverse RWGS reaction was investigated in a tubular quartz glass reactor at 700 °C and 800 °C and ambient pressure. The highest conversion factor close to the maximum value of 50% for CO was yielded for the LSCrM, Ni and GDC(20) samples by applying a 0.5 : 0.5 H(2) : CO(2) feed ratio at 800 °C. Similar activity was calculated for the Ni(3)Sn(2) alloy after normalization to the Ni mass content. Moreover, all the investigated catalysts exhibited higher selectivity for CO and H(2)O products than Ni, with which CH(4) molar concentrations up to 0.9% and 2.4% were collected at 800 °C and 700 °C, respectively. The influence of feed pressure on the carburisation process was inspected in a tubular Ni–Cr reactor. Under a carbon-rich gas mixture at 3 bar and 700 °C, large amounts of graphitic carbon were deposited solely on the Ni sample after 100 h of exposure time. After the exposure of the powder materials to 0.5 : 0.5 and 0.9 : 0.1 H(2) : CO(2) atmospheres for 300 h at 700 °C and 10 bar, traces of amorphous carbon were surprisingly detected only on Ni(3)Sn(2) powder via Raman microscopy. Thus, because GDC(20) ist not active for electrochemical H(2) production, LSCrM or a mixture of both LSCrM and GDC(20) materials appears to be the most promising candidate for Ni substitution in high-temperature H(2)O/CO(2) co-electrolysis. The Royal Society of Chemistry 2020-03-10 /pmc/articles/PMC9050351/ /pubmed/35498580 http://dx.doi.org/10.1039/d0ra00362j Text en This journal is © The Royal Society of Chemistry https://creativecommons.org/licenses/by-nc/3.0/
spellingShingle Chemistry
Bogolowski, Nicky
Sánchez Batalla, Beatriz
Shin, Baekkyoung
Drillet, Jean-Francois
Activity of La(0.75)Sr(0.25)Cr(0.5)Mn(0.5)O(3−δ), Ni(3)Sn(2) and Gd-doped CeO(2) towards the reverse water-gas shift reaction and carburisation for a high-temperature H(2)O/CO(2) co-electrolysis
title Activity of La(0.75)Sr(0.25)Cr(0.5)Mn(0.5)O(3−δ), Ni(3)Sn(2) and Gd-doped CeO(2) towards the reverse water-gas shift reaction and carburisation for a high-temperature H(2)O/CO(2) co-electrolysis
title_full Activity of La(0.75)Sr(0.25)Cr(0.5)Mn(0.5)O(3−δ), Ni(3)Sn(2) and Gd-doped CeO(2) towards the reverse water-gas shift reaction and carburisation for a high-temperature H(2)O/CO(2) co-electrolysis
title_fullStr Activity of La(0.75)Sr(0.25)Cr(0.5)Mn(0.5)O(3−δ), Ni(3)Sn(2) and Gd-doped CeO(2) towards the reverse water-gas shift reaction and carburisation for a high-temperature H(2)O/CO(2) co-electrolysis
title_full_unstemmed Activity of La(0.75)Sr(0.25)Cr(0.5)Mn(0.5)O(3−δ), Ni(3)Sn(2) and Gd-doped CeO(2) towards the reverse water-gas shift reaction and carburisation for a high-temperature H(2)O/CO(2) co-electrolysis
title_short Activity of La(0.75)Sr(0.25)Cr(0.5)Mn(0.5)O(3−δ), Ni(3)Sn(2) and Gd-doped CeO(2) towards the reverse water-gas shift reaction and carburisation for a high-temperature H(2)O/CO(2) co-electrolysis
title_sort activity of la(0.75)sr(0.25)cr(0.5)mn(0.5)o(3−δ), ni(3)sn(2) and gd-doped ceo(2) towards the reverse water-gas shift reaction and carburisation for a high-temperature h(2)o/co(2) co-electrolysis
topic Chemistry
url https://www.ncbi.nlm.nih.gov/pmc/articles/PMC9050351/
https://www.ncbi.nlm.nih.gov/pubmed/35498580
http://dx.doi.org/10.1039/d0ra00362j
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