01447nas a2200229   4500008004100000022001400041245013100055210006900186260007500255300001000330490000800340520053700348653002200885653003000907653003100937653002500968653002000993100002401013700002601037700002301063856013101086       2007                        eng d  a0936-521400aCO2 reforming of methane to syngas over highly active and stable supported CoOx (accompanied with MgO, ZrO2 or CeO2) catalysts0 aCO2 reforming of methane to syngas over highly active and stable  aRUDIGERSTR 14, D-70469 STUTTGART, GERMANYbGEORG THIEME VERLAG KGcJAN  a47-520 v3163 a<p>{Catalytically inactive CoOx-MgO (calcined at 900 degrees C) becomes highly active and selective in the CO2 reforming of methane to syngas when it is deposited on a commercial low surface-area macro-porous silica-alumina support (SA-5205) or when CoOx is deposited on the support precoated with MgO. Both the supported CoOx and MgO containing catalysts (CoOx -MgO/SA-5205 and CoOx/MgO/SA-5205) show high methane conversion (&gt; 98%) activity and H-2 selectivity (&gt; 94%) and also high stability against carbon deposition [</p>10aarylboronic acids10adiarylmethylidenefluorene10adibromomethylidenefluorene10aPd-mediated coupling10aSuzuki reaction1 aMondal, Kartick, C.1 aChoudhary, Vasant, R.1 aJoshi, Upendra, A.  uhttps://library.ncl.res.in/content/co2-reforming-methane-syngas-over-highly-active-and-stable-supported-coox-accompanied-mgo-0