Catalytic Methanation of Methanol

Masahiko Matsukata, Tatsuya Hayashi, Masashi Nishiyama, Eiichi Kikuchi, Yoshiro Morita

    研究成果: Article

    抄録

    To produce town gas catalytic methanation of methanol was investigated in the temperature range of 300—350°C. Nickel and alumina were excellent components of the catalyst. The catalysts containing 80wt% of nickel prepared by coprecipitation methods showed especially high activities at 300°C. The methanol conversion over the coprecipitated catalysts was dependent upon the size of the nickel crystallite, while the methane selectivities were not. The activity and selectivity of coprecipitated catalysts were steady during a 20hr-run and on addition of water to methanol.

    元の言語English
    ページ(範囲)265-272
    ページ数8
    ジャーナルSekiyu Gakkaishi (Journal of the Japan Petroleum Institute)
    30
    発行部数4
    DOI
    出版物ステータスPublished - 1987

    Fingerprint

    Methanation
    Methanol
    Catalysts
    Catalyst selectivity
    Nickel
    Coprecipitation
    Catalyst activity
    Methane
    Alumina
    Gases
    Water
    Temperature

    ASJC Scopus subject areas

    • Fuel Technology

    これを引用

    Catalytic Methanation of Methanol. / Matsukata, Masahiko; Hayashi, Tatsuya; Nishiyama, Masashi; Kikuchi, Eiichi; Morita, Yoshiro.

    :: Sekiyu Gakkaishi (Journal of the Japan Petroleum Institute), 巻 30, 番号 4, 1987, p. 265-272.

    研究成果: Article

    Matsukata, M, Hayashi, T, Nishiyama, M, Kikuchi, E & Morita, Y 1987, 'Catalytic Methanation of Methanol', Sekiyu Gakkaishi (Journal of the Japan Petroleum Institute), 巻. 30, 番号 4, pp. 265-272. https://doi.org/10.1627/jpi1958.30.265
    Matsukata, Masahiko ; Hayashi, Tatsuya ; Nishiyama, Masashi ; Kikuchi, Eiichi ; Morita, Yoshiro. / Catalytic Methanation of Methanol. :: Sekiyu Gakkaishi (Journal of the Japan Petroleum Institute). 1987 ; 巻 30, 番号 4. pp. 265-272.
    @article{66068780d48843289249ec911efb94af,
    title = "Catalytic Methanation of Methanol",
    abstract = "To produce town gas catalytic methanation of methanol was investigated in the temperature range of 300—350°C. Nickel and alumina were excellent components of the catalyst. The catalysts containing 80wt{\%} of nickel prepared by coprecipitation methods showed especially high activities at 300°C. The methanol conversion over the coprecipitated catalysts was dependent upon the size of the nickel crystallite, while the methane selectivities were not. The activity and selectivity of coprecipitated catalysts were steady during a 20hr-run and on addition of water to methanol.",
    keywords = "Catalyst preparation, Coprecipitation method, Metal catalyst, Methane, Methanol, Reaction mechanism",
    author = "Masahiko Matsukata and Tatsuya Hayashi and Masashi Nishiyama and Eiichi Kikuchi and Yoshiro Morita",
    year = "1987",
    doi = "10.1627/jpi1958.30.265",
    language = "English",
    volume = "30",
    pages = "265--272",
    journal = "Journal of the Japan Petroleum Institute",
    issn = "1346-8804",
    publisher = "Japan Petroleum Institute",
    number = "4",

    }

    TY - JOUR

    T1 - Catalytic Methanation of Methanol

    AU - Matsukata, Masahiko

    AU - Hayashi, Tatsuya

    AU - Nishiyama, Masashi

    AU - Kikuchi, Eiichi

    AU - Morita, Yoshiro

    PY - 1987

    Y1 - 1987

    N2 - To produce town gas catalytic methanation of methanol was investigated in the temperature range of 300—350°C. Nickel and alumina were excellent components of the catalyst. The catalysts containing 80wt% of nickel prepared by coprecipitation methods showed especially high activities at 300°C. The methanol conversion over the coprecipitated catalysts was dependent upon the size of the nickel crystallite, while the methane selectivities were not. The activity and selectivity of coprecipitated catalysts were steady during a 20hr-run and on addition of water to methanol.

    AB - To produce town gas catalytic methanation of methanol was investigated in the temperature range of 300—350°C. Nickel and alumina were excellent components of the catalyst. The catalysts containing 80wt% of nickel prepared by coprecipitation methods showed especially high activities at 300°C. The methanol conversion over the coprecipitated catalysts was dependent upon the size of the nickel crystallite, while the methane selectivities were not. The activity and selectivity of coprecipitated catalysts were steady during a 20hr-run and on addition of water to methanol.

    KW - Catalyst preparation

    KW - Coprecipitation method

    KW - Metal catalyst

    KW - Methane

    KW - Methanol

    KW - Reaction mechanism

    UR - http://www.scopus.com/inward/record.url?scp=84996314592&partnerID=8YFLogxK

    UR - http://www.scopus.com/inward/citedby.url?scp=84996314592&partnerID=8YFLogxK

    U2 - 10.1627/jpi1958.30.265

    DO - 10.1627/jpi1958.30.265

    M3 - Article

    VL - 30

    SP - 265

    EP - 272

    JO - Journal of the Japan Petroleum Institute

    JF - Journal of the Japan Petroleum Institute

    SN - 1346-8804

    IS - 4

    ER -