Preliminary Equipment Design for On-Board Hydrogen Production by Steam Reforming in Palladium Membrane Reactors

Hydrogen, as an energy carrier, can take the main role in the transition to a new energy model based on renewable sources. However, its application in the transport sector is limited by its difficult storage and the lack of infrastructure for its distribution. On-board H2 production is proposed as a...

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Main Authors: Marina Holgado, David Alique
Format: Article
Language:English
Published: MDPI AG 2019-01-01
Series:ChemEngineering
Subjects:
Online Access:http://www.mdpi.com/2305-7084/3/1/6
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spelling doaj-cbeb9fe0bc584504a26a262ab53628142020-11-25T00:50:50ZengMDPI AGChemEngineering2305-70842019-01-0131610.3390/chemengineering3010006chemengineering3010006Preliminary Equipment Design for On-Board Hydrogen Production by Steam Reforming in Palladium Membrane ReactorsMarina Holgado0David Alique1Department of Chemical, Energy and Mechanical Technology, Rey Juan Carlos University, C/Tulipán s/n, 28933 Móstoles, SpainDepartment of Chemical, Energy and Mechanical Technology, Rey Juan Carlos University, C/Tulipán s/n, 28933 Móstoles, SpainHydrogen, as an energy carrier, can take the main role in the transition to a new energy model based on renewable sources. However, its application in the transport sector is limited by its difficult storage and the lack of infrastructure for its distribution. On-board H2 production is proposed as a possible solution to these problems, especially in the case of considering renewable feedstocks such as bio-ethanol or bio-methane. This work addresses a first approach for analyzing the viability of these alternatives by using Pd-membrane reactors in polymer electrolyte membrane fuel cell (PEM-FC) vehicles. It has been demonstrated that the use of Pd-based membrane reactors enhances hydrogen productivity and provides enough pure hydrogen to feed the PEM-FC requirements in one single step. Both alternatives seem to be feasible, although the methane-based on-board hydrogen production offers some additional advantages. For this case, it is possible to generate 1.82 kmol h−1 of pure H2 to feed the PEM-FC while minimizing the CO2 emissions to 71 g CO2/100 km. This value would be under the future emissions limits proposed by the European Union (EU) for year 2020. In this case, the operating conditions of the on-board reformer are T = 650 °C, Pret = 10 bar and H2O/CH4 = 2.25, requiring 1 kg of catalyst load and a membrane area of 1.76 m2.http://www.mdpi.com/2305-7084/3/1/6hydrogenon-boardsteam reformingethanolmethanemembrane reactorpalladiummodeling
collection DOAJ
language English
format Article
sources DOAJ
author Marina Holgado
David Alique
spellingShingle Marina Holgado
David Alique
Preliminary Equipment Design for On-Board Hydrogen Production by Steam Reforming in Palladium Membrane Reactors
ChemEngineering
hydrogen
on-board
steam reforming
ethanol
methane
membrane reactor
palladium
modeling
author_facet Marina Holgado
David Alique
author_sort Marina Holgado
title Preliminary Equipment Design for On-Board Hydrogen Production by Steam Reforming in Palladium Membrane Reactors
title_short Preliminary Equipment Design for On-Board Hydrogen Production by Steam Reforming in Palladium Membrane Reactors
title_full Preliminary Equipment Design for On-Board Hydrogen Production by Steam Reforming in Palladium Membrane Reactors
title_fullStr Preliminary Equipment Design for On-Board Hydrogen Production by Steam Reforming in Palladium Membrane Reactors
title_full_unstemmed Preliminary Equipment Design for On-Board Hydrogen Production by Steam Reforming in Palladium Membrane Reactors
title_sort preliminary equipment design for on-board hydrogen production by steam reforming in palladium membrane reactors
publisher MDPI AG
series ChemEngineering
issn 2305-7084
publishDate 2019-01-01
description Hydrogen, as an energy carrier, can take the main role in the transition to a new energy model based on renewable sources. However, its application in the transport sector is limited by its difficult storage and the lack of infrastructure for its distribution. On-board H2 production is proposed as a possible solution to these problems, especially in the case of considering renewable feedstocks such as bio-ethanol or bio-methane. This work addresses a first approach for analyzing the viability of these alternatives by using Pd-membrane reactors in polymer electrolyte membrane fuel cell (PEM-FC) vehicles. It has been demonstrated that the use of Pd-based membrane reactors enhances hydrogen productivity and provides enough pure hydrogen to feed the PEM-FC requirements in one single step. Both alternatives seem to be feasible, although the methane-based on-board hydrogen production offers some additional advantages. For this case, it is possible to generate 1.82 kmol h−1 of pure H2 to feed the PEM-FC while minimizing the CO2 emissions to 71 g CO2/100 km. This value would be under the future emissions limits proposed by the European Union (EU) for year 2020. In this case, the operating conditions of the on-board reformer are T = 650 °C, Pret = 10 bar and H2O/CH4 = 2.25, requiring 1 kg of catalyst load and a membrane area of 1.76 m2.
topic hydrogen
on-board
steam reforming
ethanol
methane
membrane reactor
palladium
modeling
url http://www.mdpi.com/2305-7084/3/1/6
work_keys_str_mv AT marinaholgado preliminaryequipmentdesignforonboardhydrogenproductionbysteamreforminginpalladiummembranereactors
AT davidalique preliminaryequipmentdesignforonboardhydrogenproductionbysteamreforminginpalladiummembranereactors
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