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H2 production with low carbon content via MSR in packed bed membrane reactors for high-temperature polymeric electrolyte membrane fuel cell

Title
H2 production with low carbon content via MSR in packed bed membrane reactors for high-temperature polymeric electrolyte membrane fuel cell
Type
Article in International Scientific Journal
Year
2017
Authors
P. Ribeirinha
(Author)
FEUP
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M. Abdollahzadeh
(Author)
FEUP
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M. Boaventura
(Author)
FEUP
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A. Mendes
(Author)
FEUP
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Journal
Title: Applied EnergyImported from Authenticus Search for Journal Publications
Vol. 188
Pages: 409-419
ISSN: 0306-2619
Publisher: Elsevier
Indexing
Other information
Authenticus ID: P-00M-G4K
Resumo (PT):
Abstract (EN): This work compares the hydrogen purity and recovery produced by a methanol steam reforming (MSR) packed bed membrane reactor (PBMR) equipped with a membrane selective to hydrogen (Pd-Ag) and with a membrane selective to carbon dioxide (porous membrane filled with ionic liquids-ILs). A 3- dimensional non-isothermal PBMR model was developed in Fluent (AnsysTM) for simulating a PBMR equipped with these two types of membranes and simulating a conventional packed bed reactor (PBR). For the development PBMR models a MSR mechanistic kinetic model was fitted to experimental reaction rates of a commercial catalyst (BASF RP60). The results indicated that selective hydrogen removal from the reaction medium originates a significant increase in the methanol conversion, while the carbon dioxide removal has a smaller effect. CO2-PBMR showed to be more efficient in terms of energy consumption than H2-PMBR. The simulation results showed also that ILs membranes must have a minimum permeance of P1 x 106 mol s1 m2 Pa1 and CO2/H2 selectivity of P200 at 473 K to be attractive for this type of applications. The advantages and limitations of each reactor configuration are discussed based on experimental and simulated data.
Language: English
Type (Professor's evaluation): Scientific
No. of pages: 11
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