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    Investigation of the catalytic performance of Ni/MgO catalysts in partial oxidation, dry reforming and combined reforming of methane
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    Keywords:
    Carbon dioxide reforming
    Partial oxidation
    Methane reformer
    Nanocrystalline material
    The main technologies for reforming natural gas to syngas at present are summarized including methane steam reforming,methane partial oxidation,carbon dioxide reforming of methane,coupling reaction of methane steam reforming and partial oxidation,coupling reaction of methane partial oxidation and carbon dioxide reforming,coupling reaction of methane steam reforming and carbon dioxide reforming,and tri-reforming of methane. The catalysts used in the first three typical reactions are focused on. It is pointed out that coupling the three typical reactions,and accompanied with lattice oxygen technology,plasma technology and microwave irradiation technology are development tendency of natural gas reforming to syngas.
    Carbon dioxide reforming
    Methane reformer
    Partial oxidation
    Citations (0)
    One of the most attractive routes for the production of hydrogen or syngas for use in fuel cell applications is the reforming and partial oxidation of hydrocarbons. The use of hydrocarbons in high temperature fuel cells is achieved through either external or internal reforming. Reforming and partial oxidation catalysis to convert hydrocarbons to hydrogen rich syngas plays an important role in fuel processing technology. The current research in the area of reforming and partial oxidation of methane, methanol and ethanol includes catalysts for reforming and oxidation, methods of catalyst synthesis, and the effective utilization of fuel for both external and internal reforming processes. In this paper the recent progress in these areas of research is reviewed along with the reforming of liquid hydrocarbons, from this an overview of the current best performing catalysts for the reforming and partial oxidizing of hydrocarbons for hydrogen production is summarized.
    Partial oxidation
    Methane reformer
    Catalytic reforming
    Oxidizing agent
    Carbon dioxide reforming
    Citations (379)
    The methane reforming with and steam for manufacture of synthesis gas over catalyst was investigated. Mixed reforming carried out dry reforming with and steam for development of DME process in pilot plant. To improve a catalyst deactivation by coke formation, the mixed reforming added carbon dioxide and steam as a oxidizer of the methane reforming was suggested. The result of experiments over commercial catalyst in dry reforming has shown that the catalyst activity decrease rapidly after 20 hours. In case of catalyst, the deactivation of 20 percent after 30 hours was occurred. The activity of Ni/C catalyst still was not decreased dramatically after 100 hours. The effect of reforming with steam over catalyst obtained the optimal conversion of methane and carbon dioxide, and could be produced synthesis gas at ratio of under 1.5.
    Carbon dioxide reforming
    Methane reformer
    Catalytic reforming
    Citations (2)
    Methane reformer
    Carbon dioxide reforming
    Partial oxidation
    Carbon fibers
    Catalytic reforming