A novel hybrid plant for a mixture of methane and hydrogen (enriched methane) production from a steam reforming reactor whose heat duty is supplied by a molten salt stream heated up by a concentrating solar power (CSP) plant developed by ENEA is here presented. By this way, a hydrogen stream, mixed with natural gas, is produced from solar energy by a consolidated production method as the steam reforming process and by a pre-commercial technology as molten salts parabolic mirrors solar plant. After the hydrogen production plant, the residual heat stored in molten salt stream is used to produce electricity and the plant is co-generative (hydrogen + electricity). The heat-exchanger-shaped reactor is dimensioned by a design tool developed in MatLab environment. A reactor 3.5 m long and with a diameter of 2″ is the most efficient in terms of methane conversion (14.8%) and catalyst efficiency (4.7 Nm 3/h of hydrogen produced per kgcat). © 2011, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights.

Solar enriched methane production by steam reforming process: Reactor design / DE FALCO, Marcello; Piemonte, Vincenzo. - In: INTERNATIONAL JOURNAL OF HYDROGEN ENERGY. - ISSN 0360-3199. - 36:13(2011), pp. 7759-7762. [10.1016/j.ijhydene.2011.01.044]

Solar enriched methane production by steam reforming process: Reactor design

Marcello De Falco;PIEMONTE, Vincenzo
2011

Abstract

A novel hybrid plant for a mixture of methane and hydrogen (enriched methane) production from a steam reforming reactor whose heat duty is supplied by a molten salt stream heated up by a concentrating solar power (CSP) plant developed by ENEA is here presented. By this way, a hydrogen stream, mixed with natural gas, is produced from solar energy by a consolidated production method as the steam reforming process and by a pre-commercial technology as molten salts parabolic mirrors solar plant. After the hydrogen production plant, the residual heat stored in molten salt stream is used to produce electricity and the plant is co-generative (hydrogen + electricity). The heat-exchanger-shaped reactor is dimensioned by a design tool developed in MatLab environment. A reactor 3.5 m long and with a diameter of 2″ is the most efficient in terms of methane conversion (14.8%) and catalyst efficiency (4.7 Nm 3/h of hydrogen produced per kgcat). © 2011, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights.
2011
csp plant; enriched methane; hydrogen production; molten salt; solar energy
01 Pubblicazione su rivista::01a Articolo in rivista
Solar enriched methane production by steam reforming process: Reactor design / DE FALCO, Marcello; Piemonte, Vincenzo. - In: INTERNATIONAL JOURNAL OF HYDROGEN ENERGY. - ISSN 0360-3199. - 36:13(2011), pp. 7759-7762. [10.1016/j.ijhydene.2011.01.044]
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Utilizza questo identificativo per citare o creare un link a questo documento: https://hdl.handle.net/11573/337524
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