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Carbon-based membrane reactors conversion

A mathematical model was used in literature (Abashar, 2004) based on the combination of SRM and dry reforming in a fluidized bed membrane reactor showing complete conversion of methane at low temperature. The produced carbon dioxide in the SR was used in dry reforming to produce syngas. A comparison between the traditional reactor and MR was discussed the higher performance was obtained for the fluidized bed MR. [Pg.63]

This system includes several mixing and heat exchange units. A concept for an integrated, microtechnology-based fuel processor was proposed by PNNF [8]. As examples for unit operations which may be included in future integrated systems the same publication mentions reactors for steam reforming and/or partial oxidation, water-gas shift reactors and preferential oxidation reactors for carbon monoxide conversions, heat exchangers, membranes or other separation components. [Pg.245]


See other pages where Carbon-based membrane reactors conversion is mentioned: [Pg.397]    [Pg.322]    [Pg.57]    [Pg.216]    [Pg.221]    [Pg.156]    [Pg.547]    [Pg.39]    [Pg.60]    [Pg.48]    [Pg.147]    [Pg.250]    [Pg.187]    [Pg.511]    [Pg.154]    [Pg.388]    [Pg.666]    [Pg.270]    [Pg.210]    [Pg.661]    [Pg.356]    [Pg.389]    [Pg.392]    [Pg.532]    [Pg.528]    [Pg.515]    [Pg.129]    [Pg.145]    [Pg.1128]    [Pg.969]    [Pg.763]    [Pg.419]   
See also in sourсe #XX -- [ Pg.385 ]




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