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    Catalytic conversion of rape oil into alkane-aromatic fraction in the presence of Pd-Zn/MFI

    New search for: Tsodikov, M. V.
    New search for: Chistyakov, A. V.
    New search for: Gubanov, M. A.
    New search for: Murzin, V. Yu.
    New search for: Bukina, Z. M.
    New search for: Kolesnichenko, N. V.
    New search for: Khadzhiev, S. N.

    Abstract Results on the conversion of rape oil into the alkane-aromatic fraction in the presence of a prototype of a MFI-based industrial catalyst (Si/Al = 30) promoted with 0.6 wt % Pd and 1 wt % Zn are presented. It has been shown that an increase in the process temperature from 360 to 420°C leads to a significant increase in the yield of aromatic compounds, and an increase in the substrate space velocity leads to a three-fold increase in the yield of C4–C6 alkanes of primarily the iso-branched structure. The genesis of active Pd and Zn clusters is discussed on the basis of X-ray data.

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    Catalytic conversion of rape oil into alkane-aromatic fraction in the presence of Pd-Zn/MFI

    New search for: Tsodikov, M. V.
    New search for: Chistyakov, A. V.
    New search for: Gubanov, M. A.
    New search for: Murzin, V. Yu.
    New search for: Bukina, Z. M.
    New search for: Kolesnichenko, N. V.
    New search for: Khadzhiev, S. N.

    Abstract Results on the conversion of rape oil into the alkane-aromatic fraction in the presence of a prototype of a MFI-based industrial catalyst (Si/Al = 30) promoted with 0.6 wt % Pd and 1 wt % Zn are presented. It has been shown that an increase in the process temperature from 360 to 420°C leads to a significant increase in the yield of aromatic compounds, and an increase in the substrate space velocity leads to a three-fold increase in the yield of C4–C6 alkanes of primarily the iso-branched structure. The genesis of active Pd and Zn clusters is discussed on the basis of X-ray data.

    Access

    Check access
    Check availability in my library
    Order at Subito €

    Catalytic conversion of rape oil into alkane-aromatic fraction in the presence of Pd-Zn/MFI

    New search for: Tsodikov, M. V.
    New search for: Chistyakov, A. V.
    New search for: Gubanov, M. A.
    New search for: Murzin, V. Yu.
    New search for: Bukina, Z. M.
    New search for: Kolesnichenko, N. V.
    New search for: Khadzhiev, S. N.

    Abstract Results on the conversion of rape oil into the alkane-aromatic fraction in the presence of a prototype of a MFI-based industrial catalyst (Si/Al = 30) promoted with 0.6 wt % Pd and 1 wt % Zn are presented. It has been shown that an increase in the process temperature from 360 to 420°C leads to a significant increase in the yield of aromatic compounds, and an increase in the substrate space velocity leads to a three-fold increase in the yield of C4–C6 alkanes of primarily the iso-branched structure. The genesis of active Pd and Zn clusters is discussed on the basis of X-ray data.

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    Title:

    Catalytic conversion of rape oil into alkane-aromatic fraction in the presence of Pd-Zn/MFI

    Contributors:

    Tsodikov, M. V. (author) / Chistyakov, A. V. (author) / Gubanov, M. A. (author) / Murzin, V. Yu. (author) / Bukina, Z. M. (author) / Kolesnichenko, N. V. (author) / Khadzhiev, S. N. (author)

    Published in:

    Petroleum Chemistry ; 53 ; 46-53

    Publication date:

    2013-01-01

    Size:

    8 pages

    ISSN:

    1555-6239 , 0965-5441

    DOI:

    https://doi.org/10.1134/S0965544113010106

    Type of media:

    Article (Journal)

    Type of material:

    Electronic Resource

    Language:

    English

    Keywords:

    heterogeneous catalysis , zeolites , rape oil , triglycerides of fatty acids , alkanes , aromatics , biodiesel , production of fuel components Chemistry , Industrial Chemistry/Chemical Engineering

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