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Article

Hydrogen Production via the Oxy-Steam Reforming of LNG or Methane on Ni Catalysts

by
Pawel Mierczynski
*,
Natalia Stępińska
,
Magdalena Mosinska
,
Karolina Chalupka
,
Jadwiga Albinska
,
Waldemar Maniukiewicz
,
Jacek Rogowski
,
Magdalena Nowosielska
and
Malgorzata I. Szynkowska
*
Institute of General and Ecological Chemistry, Lodz University of Technology, Zeromskiego 116, 90-924 Lodz, Poland
*
Authors to whom correspondence should be addressed.
Catalysts 2020, 10(3), 346; https://doi.org/10.3390/catal10030346
Submission received: 25 February 2020 / Revised: 11 March 2020 / Accepted: 17 March 2020 / Published: 20 March 2020
(This article belongs to the Special Issue Catalysts for Production and Conversion of Syngas)

Abstract

Ni catalysts supported on ZrO2, 5%CeO2-ZrO2, and 5%La2O3-ZrO2 were prepared via the impregnation method and tested in the oxy-steam reforming of methane and liquified natural gas (LNG). All tested catalysts exhibited high catalytic activity in the studied process at 700 and 900 °C. The improvement of the stability of Ni catalysts after the addition of CeO2 oxide in the studied oxy-steam reforming of LNG process was confirmed. In addition, high activity and selectivity towards hydrogen was proven in the oxy-steam reforming process at 900 °C over a 20%Ni/5%CeO2-ZrO2 catalyst. It was also proved that the addition of CeO2 onto a ZrO2 carrier leads to a decrease in the NiO and metallic Ni crystallite sizes that were detected by the X-Ray diffraction (XRD) technique. The solid solution formation between NiO and ZrO2 and/or NiO and CeO2 was proved. Superior reactivity in the oxy-steam reforming of CH4 and the LNG process exhibited a 20%Ni/ZrO2 catalyst, which showed the highest methane conversions at 500 and 600 °C, equal to 63% and 89%, respectively. In addition, also in the case of the LNG reforming reaction, the most active catalyst was the 20%Ni/ZrO2 system, which demonstrated 46.3% and 76.9% of the methane conversion value at 500 and 600 °C and the total conversion of others hydrocarbons (ethane, propane and butane). In addition, this catalytic system exhibited the highest selectivity towards hydrogen formation in the oxy-steam reforming of the LNG reaction equal to 71.2% and 71.3% at 500 and 600 °C, respectively. The highest activity of this system can be explained by the uniform distributions of Ni species and their highest concentration compared to the rest of the monometallic Ni catalysts. Time-of-flight secondary ion mass spectrometry (ToF-SIMS) results also confirmed a strong interaction of NiO with ZrO2 in the case of the 20%Ni/ZrO2 catalysts. The presence of selected NiZrO+ ions emitted from the investigated surface of the 20%Ni/ZrO2 system was detected.
Keywords: reforming of methane; LNG; nickel catalysts; syngas; ZrO2; reforming of liquid natural gas reforming of methane; LNG; nickel catalysts; syngas; ZrO2; reforming of liquid natural gas

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MDPI and ACS Style

Mierczynski, P.; Stępińska, N.; Mosinska, M.; Chalupka, K.; Albinska, J.; Maniukiewicz, W.; Rogowski, J.; Nowosielska, M.; Szynkowska, M.I. Hydrogen Production via the Oxy-Steam Reforming of LNG or Methane on Ni Catalysts. Catalysts 2020, 10, 346. https://doi.org/10.3390/catal10030346

AMA Style

Mierczynski P, Stępińska N, Mosinska M, Chalupka K, Albinska J, Maniukiewicz W, Rogowski J, Nowosielska M, Szynkowska MI. Hydrogen Production via the Oxy-Steam Reforming of LNG or Methane on Ni Catalysts. Catalysts. 2020; 10(3):346. https://doi.org/10.3390/catal10030346

Chicago/Turabian Style

Mierczynski, Pawel, Natalia Stępińska, Magdalena Mosinska, Karolina Chalupka, Jadwiga Albinska, Waldemar Maniukiewicz, Jacek Rogowski, Magdalena Nowosielska, and Malgorzata I. Szynkowska. 2020. "Hydrogen Production via the Oxy-Steam Reforming of LNG or Methane on Ni Catalysts" Catalysts 10, no. 3: 346. https://doi.org/10.3390/catal10030346

APA Style

Mierczynski, P., Stępińska, N., Mosinska, M., Chalupka, K., Albinska, J., Maniukiewicz, W., Rogowski, J., Nowosielska, M., & Szynkowska, M. I. (2020). Hydrogen Production via the Oxy-Steam Reforming of LNG or Methane on Ni Catalysts. Catalysts, 10(3), 346. https://doi.org/10.3390/catal10030346

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