@article { ISI:000228226800025,
	title = {Carbon-free dry reforming of methane to syngas over NdCoO3 perovskite-type mixed metal oxide catalyst},
	journal = {Catalysis Letters},
	volume = {100},
	number = {3-4},
	year = {2005},
	month = {APR},
	pages = {271-276},
	publisher = {SPRINGER},
	type = {Article},
	address = {233 SPRING ST, NEW YORK, NY 10013 USA},
	abstract = {<p>CoNdOx (Co/Nd = 1) is a highly promising catalyst for the carbon-free CO2 reforming of methane. Influence of the Co/Nd ratio on the catalyst performance in the CO2 reforming and also on the crystalline phases and reduction by temperature programmed reduction (TPR) of the CoNdOx catalyst has also been investigated. The CoNdOx (CoNd = 1.0) catalyst consisted of mainly NdCoO3 perovskite- type mixed metal oxide and it showed not only a high resistance to carbon formation at different process conditions ( viz. temperature = 750 - 900 degrees C and gas hourly space velocity (GHSV) = 10000 - 50000 cm(3) g(-1) h(-1)) but also high activity and selectivity in the CO2 reforming process. The high resistance to carbon formation for this catalyst is attributed mostly to strong metal (Co degrees) - support (Nd2O3) interactions.</p>},
	keywords = {CO2 reforming of methane to syngas, CoNdOx catalyst, NdCoO3 perovskite, resistance to carbon formation in CO2 reforming},
	issn = {1011-372X},
	doi = {10.1007/s10562-004-3467-0},
	author = {Choudhary, Vasant R. and Mondal, Kartick C. and Mamman, Ajit Singh and Joshi, Upendra A.}
}
@article {sanjayan,
	title = {CO2 reforming of methane to syngas over highly active and stable supported CoOx (accompanied with MgO, ZrO2 or CeO2) catalysts},
	journal = {Applied Catalysis A-General},
	volume = {316},
	number = {1},
	year = {2007},
	month = {JAN},
	pages = {47-52},
	publisher = {GEORG THIEME VERLAG KG},
	type = {Article},
	address = {RUDIGERSTR 14, D-70469 STUTTGART, GERMANY},
	abstract = {<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>},
	keywords = {arylboronic acids, diarylmethylidenefluorene, dibromomethylidenefluorene, Pd-mediated coupling, Suzuki reaction},
	issn = {0936-5214},
	doi = { 10.1016/j.apcata.2006.09.016},
	author = {Mondal, Kartick C. and Choudhary, Vasant R. and Joshi, Upendra A.}
}
