Number of the records: 1  

Activity and Selectivity of Co(Ni)Mo Sulfides Supported on MgO, Al2O3, ZrO2, TiO2, MCM-41 and Activated Carbon in Parallel Hydrodeoxygenation of Octanoic Acid and Hydrodesulfurization of 1-Benzothiophene.

  1. 1.
    SYSNO ASEP0506359
    Document TypeJ - Journal Article
    R&D Document TypeJournal Article
    Subsidiary JČlánek ve WOS
    TitleActivity and Selectivity of Co(Ni)Mo Sulfides Supported on MgO, Al2O3, ZrO2, TiO2, MCM-41 and Activated Carbon in Parallel Hydrodeoxygenation of Octanoic Acid and Hydrodesulfurization of 1-Benzothiophene.
    Author(s) Kaluža, Luděk (UCHP-M) RID, ORCID, SAI
    Karban, Jindřich (UCHP-M) RID, ORCID, SAI
    Gulková, Daniela (UCHP-M) RID, ORCID, SAI
    Source TitleReaction Kinetics Mechanism and Catalysis. - : Springer - ISSN 1878-5190
    Roč. 127, č. 2 (2019), s. 887-902
    Number of pages6 s.
    Languageeng - English
    CountryHU - Hungary
    KeywordsHDO/HDS ; octanoic acid ; benzothiophene
    Subject RIVCF - Physical ; Theoretical Chemistry
    OECD categoryPhysical chemistry
    R&D ProjectsGA17-22490S GA ČR - Czech Science Foundation (CSF)
    Method of publishingLimited access
    Institutional supportUCHP-M - RVO:67985858
    UT WOS000475580200022
    EID SCOPUS85067883872
    DOI10.1007/s11144-019-01620-x
    AnnotationMo, CoMo and NiMo sulfide catalysts were prepared using MgO, Al2O3, ZrO2, TiO2, MCM-41 and activated carbon supports. The catalysts were tested in parallel hydrodeoxygenation (HDO) of octanoic acid and hydrodesulfurization (HDS) of 1-benzothiophene. For all supports, NiMo catalysts were more active in both HDO and HDS than Mo and CoMo catalysts. HDO activity of NiMo catalysts decreased with type of support in the following order TiO2 > C > ZrO2 > Al2O3 > MCM-41 > MgO. The products of HDO were linear C7 and C8 hydrocarbons. Some isomerization and cracking activity was observed only with MCM-41 support. HDS activity of NiMo catalysts decreased in the following order C > ZrO2 > TiO2 > Al2O3 > MgO > MCM-41. HDO/HDS selectivity was influenced by the active phase and the support type and it was the highest over the NiMo/TiO2 catalyst.
    WorkplaceInstitute of Chemical Process Fundamentals
    ContactEva Jirsová, jirsova@icpf.cas.cz, Tel.: 220 390 227
    Year of Publishing2020
    Electronic addresshttp://hdl.handle.net/11104/0297627
Number of the records: 1  

  This site uses cookies to make them easier to browse. Learn more about how we use cookies.