Oxy-Steam Reforming of Liquefied Natural Gas (LNG) on Mono- and Bimetallic (Ag, Pt, Pd or Ru)/Ni Catalysts
This work presents, for the first time, the comparative physicochemical and reactivity studies of a range of bimetallic Pt-Ni, Pd-Ni, Ru-Ni, and Ag-Ni catalysts in the oxy-steam reforming (OSR) of liquefied natural gas (LNG) reaction towards hydrogen generation. In order to achieve the intended purp...
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oai:doaj.org-article:8a7475fdce4f412cb325d37c5871b8582021-11-25T17:06:48ZOxy-Steam Reforming of Liquefied Natural Gas (LNG) on Mono- and Bimetallic (Ag, Pt, Pd or Ru)/Ni Catalysts10.3390/catal111114012073-4344https://doaj.org/article/8a7475fdce4f412cb325d37c5871b8582021-11-01T00:00:00Zhttps://www.mdpi.com/2073-4344/11/11/1401https://doaj.org/toc/2073-4344This work presents, for the first time, the comparative physicochemical and reactivity studies of a range of bimetallic Pt-Ni, Pd-Ni, Ru-Ni, and Ag-Ni catalysts in the oxy-steam reforming (OSR) of liquefied natural gas (LNG) reaction towards hydrogen generation. In order to achieve the intended purpose of this work, a binary oxide CeO<sub>2</sub>·ZrO<sub>2</sub> (1:2) support was prepared via a co-precipitation method. The catalysts’ physicochemical properties were studied using X-ray diffraction (XRD), BET, TPR-H<sub>2</sub>, TPD-NH<sub>3</sub>, SEM-EDS and XPS methods. The highest activity in the studied process was exhibited by the 1%Pt-5%Ni catalyst supported on CeO<sub>2</sub>·ZrO<sub>2</sub> (1:2) system. The highest activity of this system is explained by the specific interactions occurring between the components of the active phase and between the components of the active phase and the carrier itself. The activity results showed that this catalytic system exhibited above 71% of the methane conversion at 600 °C and 60% yield of hydrogen formation. The results of this work demonstrate that the Pt-Ni and Ru-Ni catalytic systems hold promise to be applied in the production of hydrogen to power solid oxide fuel cells.Pawel MierczynskiMagdalena MosinskaWaldemar ManiukiewiczKrasimir VasilevMalgorzata Iwona Szynkowska-JozwikMDPI AGarticlenoble metalbimetallic catalystnickel catalysthydrogen productionoxy-steam reformingLNGChemical technologyTP1-1185ChemistryQD1-999ENCatalysts, Vol 11, Iss 1401, p 1401 (2021) |
institution |
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collection |
DOAJ |
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EN |
topic |
noble metal bimetallic catalyst nickel catalyst hydrogen production oxy-steam reforming LNG Chemical technology TP1-1185 Chemistry QD1-999 |
spellingShingle |
noble metal bimetallic catalyst nickel catalyst hydrogen production oxy-steam reforming LNG Chemical technology TP1-1185 Chemistry QD1-999 Pawel Mierczynski Magdalena Mosinska Waldemar Maniukiewicz Krasimir Vasilev Malgorzata Iwona Szynkowska-Jozwik Oxy-Steam Reforming of Liquefied Natural Gas (LNG) on Mono- and Bimetallic (Ag, Pt, Pd or Ru)/Ni Catalysts |
description |
This work presents, for the first time, the comparative physicochemical and reactivity studies of a range of bimetallic Pt-Ni, Pd-Ni, Ru-Ni, and Ag-Ni catalysts in the oxy-steam reforming (OSR) of liquefied natural gas (LNG) reaction towards hydrogen generation. In order to achieve the intended purpose of this work, a binary oxide CeO<sub>2</sub>·ZrO<sub>2</sub> (1:2) support was prepared via a co-precipitation method. The catalysts’ physicochemical properties were studied using X-ray diffraction (XRD), BET, TPR-H<sub>2</sub>, TPD-NH<sub>3</sub>, SEM-EDS and XPS methods. The highest activity in the studied process was exhibited by the 1%Pt-5%Ni catalyst supported on CeO<sub>2</sub>·ZrO<sub>2</sub> (1:2) system. The highest activity of this system is explained by the specific interactions occurring between the components of the active phase and between the components of the active phase and the carrier itself. The activity results showed that this catalytic system exhibited above 71% of the methane conversion at 600 °C and 60% yield of hydrogen formation. The results of this work demonstrate that the Pt-Ni and Ru-Ni catalytic systems hold promise to be applied in the production of hydrogen to power solid oxide fuel cells. |
format |
article |
author |
Pawel Mierczynski Magdalena Mosinska Waldemar Maniukiewicz Krasimir Vasilev Malgorzata Iwona Szynkowska-Jozwik |
author_facet |
Pawel Mierczynski Magdalena Mosinska Waldemar Maniukiewicz Krasimir Vasilev Malgorzata Iwona Szynkowska-Jozwik |
author_sort |
Pawel Mierczynski |
title |
Oxy-Steam Reforming of Liquefied Natural Gas (LNG) on Mono- and Bimetallic (Ag, Pt, Pd or Ru)/Ni Catalysts |
title_short |
Oxy-Steam Reforming of Liquefied Natural Gas (LNG) on Mono- and Bimetallic (Ag, Pt, Pd or Ru)/Ni Catalysts |
title_full |
Oxy-Steam Reforming of Liquefied Natural Gas (LNG) on Mono- and Bimetallic (Ag, Pt, Pd or Ru)/Ni Catalysts |
title_fullStr |
Oxy-Steam Reforming of Liquefied Natural Gas (LNG) on Mono- and Bimetallic (Ag, Pt, Pd or Ru)/Ni Catalysts |
title_full_unstemmed |
Oxy-Steam Reforming of Liquefied Natural Gas (LNG) on Mono- and Bimetallic (Ag, Pt, Pd or Ru)/Ni Catalysts |
title_sort |
oxy-steam reforming of liquefied natural gas (lng) on mono- and bimetallic (ag, pt, pd or ru)/ni catalysts |
publisher |
MDPI AG |
publishDate |
2021 |
url |
https://doaj.org/article/8a7475fdce4f412cb325d37c5871b858 |
work_keys_str_mv |
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