... Catalyst for Hydrogen Production From Glycerol ,” Int. J. Hydrogen Energy , 41 ( 4 ), pp. 1 – 13 . 10.1016/j.ijhydene.2015.12.075 [3] Ketir , W. , Bouguelia , A. , and Trari , M. , 2009 , “ NO 3 − Removal With a New Delafossite CuCrO 2 Photocatalyst ,” Desalination , 244 ( 1–3...

..., 2012; published online March 21, 2013. Assoc. Editor: Ken Reifsnider. 26 07 2012 02 11 2012 In this work, catalytic steam reforming of glycerol for hydrogen production was performed over Ce/Al 2 O 3 and Pd/Al 2 O 3 catalysts prepared via the impregnation method. The catalysts...

...Joonguen Park; Joongmyeon Bae This paper studies the heat and mass transfer characteristics in a steam reforming reactor using numerical simulation and investigates the operating parameters for effective hydrogen production. Simultaneous analysis of governing equations and chemical reaction...

... is feasible. 18 01 2011 04 04 2011 05 07 2011 05 07 2011 electrochemical electrodes electrolysis hydrogen production scandium compounds zirconium compounds solid oxide electrolysis cell steam electrolysis gas concentration performance electrode polarization...

.... 23 07 2009 22 03 2010 17 08 2010 17 08 2010 combustion equipment flames fuel cells heat transfer steam reforming reactor combustion burner hydrogen production The fuel conversion and mean temperature of Type B: ( a ) fuel ratio of 5.00 and ( b ) fuel ratio...

... slightly with higher GHSVs. However, the large pressure drop caused by a high GHSV can reduce the system efficiency. 22 09 2009 25 09 2009 20 07 2010 20 07 2010 catalysts combustion heat transfer hydrogen production mass transfer numerical analysis thermal analysis...

... but an increase in limiting current density from a higher hydrogen production. The numerical results show that the flow rates and reformer length are critical design parameters because if not properly designed they can lead to incomplete conversion of the methane fuel to hydrogen in the reformer, which has...

...S. Cordiner; G. de Simone A comprehensive computational model for the design of methane catalytic partial oxidation monolith reactors for hydrogen production has been developed and tested with respect to available experimental data. Allowing a simplified description of the heat release mechanism...

... of the catalyst on methanol conversion, selectivity, and product yields was evaluated. The addition of zinc enhanced the methanol conversion and hydrogen production. The excess steam promoted the methanol conversion and suppressed the carbon monoxide formation. Different strategies have been mentioned to minimize...

...Antonio Carlos Caetano de Souza; José Luz-Silveira; Maria Isabel Sosa Steam reforming is the most usual method of hydrogen production due to its high production efficiency and technological maturity. The use of ethanol for this purpose is an interesting option because it is a renewable...

... on detailed thermodynamic and electrochemical analyses of the systems. A comparison is made between six specific cycle configurations, which use fuel cell heat to drive hydrogen production in a reformer using both external and internal reforming options. SOFC plant performance has been evaluated on the basis...