Oxidative Dehydrogenation of Ethane over NiO-loaded High Surface Area ZrO2 Catalysts

The oxidative dehydrogenation of ethane (ODHE) over POn/NiO/ZrO2 (High Surface area Zirconia: HSZ) catalyst was carried out with a fix-bed flow reactor at 450°C under atmospheric pressure. The ODHE without dilution of reactants with inert gas resulted in ethane conversion of 32.1%, with a high ethen...

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Published inJournal of the Japan Petroleum Institute Vol. 53; no. 6; pp. 327 - 335
Main Authors Miyake, Takanori, Suzuki, Toshimitsu, Nakamura, Ken-ichi, Ikenaga, Na-oki, Sakitani, Kazuki
Format Journal Article
LanguageEnglish
Published Tokyo The Japan Petroleum Institute 01.11.2010
Japan Science and Technology Agency
Subjects
Online AccessGet full text
ISSN1346-8804
1349-273X
DOI10.1627/jpi.53.327

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Abstract The oxidative dehydrogenation of ethane (ODHE) over POn/NiO/ZrO2 (High Surface area Zirconia: HSZ) catalyst was carried out with a fix-bed flow reactor at 450°C under atmospheric pressure. The ODHE without dilution of reactants with inert gas resulted in ethane conversion of 32.1%, with a high ethene selectivity of 64.2% and an ethene yield of 20.6%. In addition, the catalytic activity did not decrease for at least 12 h. In XPS analysis, Ni species of NiO/HSZ catalyst after the reaction exhibited partly reduced metallic Ni. In contrast, in POn/NiO/HSZ, Ni species exhibited mostly the NiO form after the reaction. It was found to be important for high ethane conversion and ethene selectivity, the Ni species not to be reduced to metallic Ni during the ODHE reaction. The addition of a small amount of POn to NiO/HSZ catalyst significantly contributed to the resistance to the facile reduction of NiO.
AbstractList The oxidative dehydrogenation of ethane (ODHE) over POn/NiO/ZrO2 (High Surface area Zirconia: HSZ) catalyst was carried out with a fix-bed flow reactor at 450°C under atmospheric pressure. The ODHE without dilution of reactants with inert gas resulted in ethane conversion of 32.1%, with a high ethene selectivity of 64.2% and an ethene yield of 20.6%. In addition, the catalytic activity did not decrease for at least 12 h. In XPS analysis, Ni species of NiO/HSZ catalyst after the reaction exhibited partly reduced metallic Ni. In contrast, in POn/NiO/HSZ, Ni species exhibited mostly the NiO form after the reaction. It was found to be important for high ethane conversion and ethene selectivity, the Ni species not to be reduced to metallic Ni during the ODHE reaction. The addition of a small amount of POn to NiO/HSZ catalyst significantly contributed to the resistance to the facile reduction of NiO.
Author Ikenaga, Na-oki
Nakamura, Ken-ichi
Sakitani, Kazuki
Suzuki, Toshimitsu
Miyake, Takanori
Author_xml – sequence: 1
  fullname: Miyake, Takanori
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  fullname: Suzuki, Toshimitsu
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  fullname: Nakamura, Ken-ichi
  organization: Dept. of Chemical Engineering and High Technology Research Center, Kansai University
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  fullname: Ikenaga, Na-oki
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  fullname: Sakitani, Kazuki
  organization: Dept. of Chemical Engineering and High Technology Research Center, Kansai University
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Snippet The oxidative dehydrogenation of ethane (ODHE) over POn/NiO/ZrO2 (High Surface area Zirconia: HSZ) catalyst was carried out with a fix-bed flow reactor at...
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SubjectTerms Ethane
Nickel oxide
Oxidative dehydrogenation
Phosphoric oxide
Surface area
Zirconium oxide
Title Oxidative Dehydrogenation of Ethane over NiO-loaded High Surface Area ZrO2 Catalysts
URI https://www.jstage.jst.go.jp/article/jpi/53/6/53_6_327/_article/-char/en
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Volume 53
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