02813nas a2200253   4500008004100000022001400041245008900055210006900144260000800213300001600221490000700237520198700244653000802231653003302239653002302272653001602295653002602311653002802337100002002365700001802385700001802403700001902421856011902440       2023                        eng d  a0360-319900aHydrogen from catalytic non-thermal plasma-assisted steam methane reforming reaction0 aHydrogen from catalytic nonthermal plasmaassisted steam methane   cJUL  a24328-243410 v483 a<p>
	Steam methane reforming reaction was carried out in a dielectric barrier plasma reactor. A systematic study is conducted to understand the influence of input power, flow rate, and water for the conversion, yield, and selectivity of the reaction over strategically designed catalysts. In particular, the production rate and selectivity of the products (H2, CO and C2 hydrocarbons) are monitored. CeO2 was used as packing material, mixed with oxides of manganese or copper and their combination. The optimum Cu/CeO2 catalyst illustrated the production rate of 248.7 mmolg-1h-1 and 11.25 mmolg-1h-1 for H2, and CO, respectively at specific energy input of 19.8 JL-1. DFT calculations exhibit apparent change in electronic structure of the CeO2 after inclusion of oxides of manganese and copper that enhance interaction with methane. Based on these findings, a plausible mechanism is elucidatedSteam methane reforming reaction was carried out in a dielectric barrier plasma reactor. A systematic study is conducted to understand the influence of input power, flow rate, and water for the conversion, yield, and selectivity of the reaction over strategically designed catalysts. In particular, the production rate and selectivity of the products (H2, CO and C2 hydrocarbons) are monitored. CeO2 was used as packing material, mixed with oxides of manganese or copper and their combination. The optimum Cu/CeO2 catalyst illustrated the production rate of 248.7 mmolg-1h-1 and 11.25 mmolg-1h-1 for H2, and CO, respectively at specific energy input of 19.8 JL-1. DFT calculations exhibit apparent change in electronic structure of the CeO2 after inclusion of oxides of manganese and copper that enhance interaction with methane. Based on these findings, a plausible mechanism is elucidated which can help to design catalyst for other applications in non-thermal plasma atmosphere. &amp; COPY; 2023 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.</p>
10aDFT10aDielectric barrier discharge10aNon-thermal plasma10aselectivity10aSpecific energy input10aSteam methane reforming1 aBajpai, Abhinav1 aMehta, Shweta1 aJoshi, Kavita1 aKumar, Sushant  uhttps://library.ncl.res.in/content/hydrogen-catalytic-non-thermal-plasma-assisted-steam-methane-reforming-reaction