Hydrogen production by thermo-catalytic conversion of methane over lanthanum strontium cobalt ferrite (LSCF) and αAl2O3 supported Ni catalysts

This study investigates hydrogen production by thermo-catalytic steam methane reforming over lanthanum strontium cobalt ferrite supported Nickel (Ni/LSCF) and commercial Ni/αAl2O3 catalysts. The Ni/LSCF catalyst was synthesized using wet impregnation method and characterized by XRD, TEM, SEM, EDX, N...

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Main Authors: Ayodele, Bamidele V., Mohamed Yazrul, Mohd Yassin, Rosmawati, Naim, Sureena, Abdullah
Format: Article
Language:English
Published: Elsevier Ltd. 2019
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Online Access:http://umpir.ump.edu.my/id/eprint/25380/1/Hydrogen%20production%20by%20thermo-catalytic%20conversion%20of%20methane%20.pdf
http://umpir.ump.edu.my/id/eprint/25380/
https://doi.org/10.1016/j.joei.2018.07.014
https://doi.org/10.1016/j.joei.2018.07.014
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spelling my.ump.umpir.253802019-10-25T03:46:49Z http://umpir.ump.edu.my/id/eprint/25380/ Hydrogen production by thermo-catalytic conversion of methane over lanthanum strontium cobalt ferrite (LSCF) and αAl2O3 supported Ni catalysts Ayodele, Bamidele V. Mohamed Yazrul, Mohd Yassin Rosmawati, Naim Sureena, Abdullah QD Chemistry TP Chemical technology This study investigates hydrogen production by thermo-catalytic steam methane reforming over lanthanum strontium cobalt ferrite supported Nickel (Ni/LSCF) and commercial Ni/αAl2O3 catalysts. The Ni/LSCF catalyst was synthesized using wet impregnation method and characterized by XRD, TEM, SEM, EDX, N2-physisorption analysis, and H2-TPR. The characterization analyses show that Ni/LSCF and Ni/αAl2O3 possess the required physicochemical properties to catalyze the steam methane reforming reaction. The activity of the Ni/LSCF catalyst in steam methane reforming at 750 °C, 800 °C, and 850 °C resulted in CH4 conversions of 73.46%, 78.67%, and 87.56%, respectively. In addition, hydrogen (H2) yields of 64.34%, 72.57%, and 82.56% were obtained from the steam methane reforming at 750 °C, 800 °C, and 850 °C, respectively over the Ni/LSCF catalyst. The Ni/LSCF catalyst was found to have higher activities in term of CH4conversion and H2 yield compare to the commercial Ni/αAl2O3. However, the stability test conducted at 480 min time on stream (TOS) revealed that the commercial Ni-αAl2O3 was more stable in the steam methane reforming than the Ni/LSCF catalyst. The characterization of the used catalysts by TEM, XRD and TGA shows evidence of carbon deposition mostly on the used Ni/LSCF catalyst. Elsevier Ltd. 2019-08 Article PeerReviewed pdf en http://umpir.ump.edu.my/id/eprint/25380/1/Hydrogen%20production%20by%20thermo-catalytic%20conversion%20of%20methane%20.pdf Ayodele, Bamidele V. and Mohamed Yazrul, Mohd Yassin and Rosmawati, Naim and Sureena, Abdullah (2019) Hydrogen production by thermo-catalytic conversion of methane over lanthanum strontium cobalt ferrite (LSCF) and αAl2O3 supported Ni catalysts. Journal of the Energy Institute, 92 (4). pp. 892-903. ISSN 1743-9671 https://doi.org/10.1016/j.joei.2018.07.014 https://doi.org/10.1016/j.joei.2018.07.014
institution Universiti Malaysia Pahang
building UMP Library
collection Institutional Repository
continent Asia
country Malaysia
content_provider Universiti Malaysia Pahang
content_source UMP Institutional Repository
url_provider http://umpir.ump.edu.my/
language English
topic QD Chemistry
TP Chemical technology
spellingShingle QD Chemistry
TP Chemical technology
Ayodele, Bamidele V.
Mohamed Yazrul, Mohd Yassin
Rosmawati, Naim
Sureena, Abdullah
Hydrogen production by thermo-catalytic conversion of methane over lanthanum strontium cobalt ferrite (LSCF) and αAl2O3 supported Ni catalysts
description This study investigates hydrogen production by thermo-catalytic steam methane reforming over lanthanum strontium cobalt ferrite supported Nickel (Ni/LSCF) and commercial Ni/αAl2O3 catalysts. The Ni/LSCF catalyst was synthesized using wet impregnation method and characterized by XRD, TEM, SEM, EDX, N2-physisorption analysis, and H2-TPR. The characterization analyses show that Ni/LSCF and Ni/αAl2O3 possess the required physicochemical properties to catalyze the steam methane reforming reaction. The activity of the Ni/LSCF catalyst in steam methane reforming at 750 °C, 800 °C, and 850 °C resulted in CH4 conversions of 73.46%, 78.67%, and 87.56%, respectively. In addition, hydrogen (H2) yields of 64.34%, 72.57%, and 82.56% were obtained from the steam methane reforming at 750 °C, 800 °C, and 850 °C, respectively over the Ni/LSCF catalyst. The Ni/LSCF catalyst was found to have higher activities in term of CH4conversion and H2 yield compare to the commercial Ni/αAl2O3. However, the stability test conducted at 480 min time on stream (TOS) revealed that the commercial Ni-αAl2O3 was more stable in the steam methane reforming than the Ni/LSCF catalyst. The characterization of the used catalysts by TEM, XRD and TGA shows evidence of carbon deposition mostly on the used Ni/LSCF catalyst.
format Article
author Ayodele, Bamidele V.
Mohamed Yazrul, Mohd Yassin
Rosmawati, Naim
Sureena, Abdullah
author_facet Ayodele, Bamidele V.
Mohamed Yazrul, Mohd Yassin
Rosmawati, Naim
Sureena, Abdullah
author_sort Ayodele, Bamidele V.
title Hydrogen production by thermo-catalytic conversion of methane over lanthanum strontium cobalt ferrite (LSCF) and αAl2O3 supported Ni catalysts
title_short Hydrogen production by thermo-catalytic conversion of methane over lanthanum strontium cobalt ferrite (LSCF) and αAl2O3 supported Ni catalysts
title_full Hydrogen production by thermo-catalytic conversion of methane over lanthanum strontium cobalt ferrite (LSCF) and αAl2O3 supported Ni catalysts
title_fullStr Hydrogen production by thermo-catalytic conversion of methane over lanthanum strontium cobalt ferrite (LSCF) and αAl2O3 supported Ni catalysts
title_full_unstemmed Hydrogen production by thermo-catalytic conversion of methane over lanthanum strontium cobalt ferrite (LSCF) and αAl2O3 supported Ni catalysts
title_sort hydrogen production by thermo-catalytic conversion of methane over lanthanum strontium cobalt ferrite (lscf) and αal2o3 supported ni catalysts
publisher Elsevier Ltd.
publishDate 2019
url http://umpir.ump.edu.my/id/eprint/25380/1/Hydrogen%20production%20by%20thermo-catalytic%20conversion%20of%20methane%20.pdf
http://umpir.ump.edu.my/id/eprint/25380/
https://doi.org/10.1016/j.joei.2018.07.014
https://doi.org/10.1016/j.joei.2018.07.014
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