K. Tomishige et al., Development of a new generation reforming catalyst: Catalytic performance and carbon deposition behavior on nickel-magnesia catalysts, KINET CATAL, 40(3), 1999, pp. 388-394
Catalytic performance and carbon deposition behavior in CO2 reforming and C
O2-steam reforming of methane over nickel-magnesia solid solution with or w
ithout Ca ions added, supported Ni/MgO, and commercial steam reforming cata
lysts are discussed. No carbon deposition in CO2 reforming of methane was o
bserved on Ni0.03Mg0.97O at 0.1 MPa, but at 2.0 MPa, carbon deposited on th
e catalyst. The addition of Ca ion to nickel-magnesia solid solution cataly
st inhibited carbon deposition through the enhancement of surface basicity.
It is strongly suggested that carbon is formed via methane decomposition o
n supported Ni/MgO and commercial catalyst, while the disproportionation of
CO is the main source of carbon on Ni0.03Mg0.97O solid solution catalyst.