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Novel Approach to Tar Removal from Biomass Producer Gas by Means of a Nickel-based Catalyst

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    SYSNO ASEP0330704
    Document TypeC - Proceedings Paper (int. conf.)
    R&D Document TypeConference Paper
    TitleNovel Approach to Tar Removal from Biomass Producer Gas by Means of a Nickel-based Catalyst
    TitleOdstraňování dehtu na niklovém katalyzátoru z plynu ze zplyňování biomasy
    Author(s) Vosecký, Martin (UCHP-M)
    Kameníková, Petra (UCHP-M) RID, SAI
    Pohořelý, Michael (UCHP-M) RID, ORCID, SAI
    Skoblia, Sergej (UCHP-M)
    Punčochář, Miroslav (UCHP-M) RID, ORCID, SAI
    Source TitleProceedings. - Beijing : Tsingua University Press, 2009 / Yue G. ; Zhang H. ; Zhao C. ; Luo Z. - ISBN 978-7-302-20146-5
    Pagess. 740-746
    Number of pages7 s.
    ActionInternational Conference on Fluidized Bed Combustion /20./
    Event date18.05.2009-21.05.2009
    VEvent locationXi’an
    CountryCN - China
    Event typeWRD
    Languageeng - English
    CountryCN - China
    Keywordscatalytic tar removal ; nickel catalyst ; biomass gasification
    Subject RIVCI - Industrial Chemistry, Chemical Engineering
    R&D ProjectsGA104/07/0977 GA ČR - Czech Science Foundation (CSF)
    2B08048 GA MŠMT - Ministry of Education, Youth and Sports (MEYS)
    CEZAV0Z40720504 - UCHP-M (2005-2011)
    AnnotationThe nickel-based catalyst was exposed to the raw gas from gasification of woody biomass with air in a fluidized-bed. Steam reforming reactions led to decomposition of tar and all hydrocarbons higher than CH4 into mainly H2 and CO which further underwent reaction with steam via the water gas shift reaction to CO2. The reforming reactions caused approximately 10-20 % decrease in the lower heating values of the producer gas from the inlet values 5.0–6.5 MJ m-3. The gas yield increased from values 2.4–2.6 m3 kg-1 to values 2.8–3.0 m3 kg-1 on dry biomass basis. The chosen tar removal concept based on combination of dolomite in the fluidized-bed with the secondary catalytic reactor was proved by 20 hours long experiment in which the final tar content below 30 mg m-3 was attained corresponding to more than 97 % tar conversion.
    WorkplaceInstitute of Chemical Process Fundamentals
    ContactEva Jirsová, jirsova@icpf.cas.cz, Tel.: 220 390 227
    Year of Publishing2010
Number of the records: 1  

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