Počet záznamů: 1  

Pyrolysis of methane via thermal steam plasma for the production of hydrogen and carbon black

  1. 1.
    SYSNO ASEP0540039
    Druh ASEPJ - Článek v odborném periodiku
    Zařazení RIVJ - Článek v odborném periodiku
    Poddruh JČlánek ve WOS
    NázevPyrolysis of methane via thermal steam plasma for the production of hydrogen and carbon black
    Tvůrce(i) Mašláni, Alan (UFP-V) RID
    Hrabovský, Milan (UFP-V) RID
    Křenek, Petr (UFP-V) RID
    Hlína, Michal (UFP-V) RID
    Raman, R. (US)
    Sikarwar, Vineet Singh (UFP-V) ORCID
    Jeremiáš, Michal (UFP-V) ORCID
    Celkový počet autorů7
    Zdroj.dok.International Journal of Hydrogen Energy. - : Elsevier - ISSN 0360-3199
    Roč. 46, č. 2 (2021), s. 1605-1614
    Poč.str.10 s.
    Jazyk dok.eng - angličtina
    Země vyd.US - Spojené státy americké
    Klíč. slovaCarbon ; Equilibrium calculation ; Hydrogen ; Methane pyrolysis ; Thermal plasma
    Vědní obor RIVJE - Nejaderná energetika, spotřeba a využití energie
    Obor OECDEnergy and fuels
    CEPGC17-10246J GA ČR - Grantová agentura ČR
    Způsob publikováníOmezený přístup
    Institucionální podporaUFP-V - RVO:61389021
    UT WOS000605147300015
    EID SCOPUS85095852170
    DOI10.1016/j.ijhydene.2020.10.105
    AnotaceMethane pyrolysis for the production of hydrogen and solid carbon was studied in plasma reactor PlasGas equipped with a DC plasma torch with the arc stabilized by a water vortex. Steam plasma is produced by direct contact of electric arc discharge with water surrounding the arc column in a cylindrical torch chamber. The composition of the gas produced was compared with the results of the equilibrium calculations for different flow rates of input methane. We have found that for the net plasma power 52 kW the optimal flow rate of the input methane was between 200 slm and 300 slm, for which high methane conversions of 75% and 80% are achieved. For the flow rate of 500 slm, the methane conversion is only 60%, however, the output still consists of a mixture of hydrogen, methane and solid carbon, without other unwanted components. For the flow rate of 100 slm, the methane conversion is 88%. For 100 and 200 slm of input methane the energy excess for the reaction with respect to the calculated value is 16 kW and 4 kW. On the other hand, for 300 and 500 slm of input methane we have the energy lack of 10 kW and 38 kW. The solid carbon produced was composed of well-defined spherical particles of the size about 1 μm. Comparison with the steam and dry reforming of methane in the same system shows that the presence of oxygen increases the methane conversion, despite lower available energy produced.
    PracovištěÚstav fyziky plazmatu
    KontaktVladimíra Kebza, kebza@ipp.cas.cz, Tel.: 266 052 975
    Rok sběru2021
    Elektronická adresahttps://www.sciencedirect.com/science/article/abs/pii/S0360319920339227?via%3Dihub
Počet záznamů: 1  

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