Modelling of tubular-designed solid oxide fuel cell with indirect internal reforming operation fed by different primary fuels

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Author listDokmaingam P., Assabumrungrat S., Soottitantawat A., Laosiripojana N.

PublisherElsevier

Publication year2010

JournalJournal of Power Sources (0378-7753)

Volume number195

Issue number1

Start page69

End page78

Number of pages10

ISSN0378-7753

eISSN1873-2755

URLhttps://www.scopus.com/inward/record.uri?eid=2-s2.0-69549114305&doi=10.1016%2fj.jpowsour.2009.06.102&partnerID=40&md5=894edcc1749c83d0a8927fa7457d0aa0

LanguagesEnglish-Great Britain (EN-GB)


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Abstract

Mathematical models of an indirect internal reforming solid oxide fuel cell (IIR-SOFC) fed by four different primary fuels, i.e., methane, biogas, methanol and ethanol, are developed based on steady-state, heterogeneous, two-dimensional and tubular-design SOFC models. The effect of fuel type on the thermal coupling between internal endothermic reforming with exothermic electrochemical reactions and system performance are determined. The simulation reveals that an IIR-SOFC fuelled by methanol provides the smoothest temperature gradient with high electrochemical efficiency. Furthermore, the content of CO2 in biogas plays an important role on system performance since electrical efficiency is improved by the removal of some CO2 from biogas but a larger temperature gradient is expected. Sensitivity analysis of three parameters, namely, a operating pressure, inlet steam to carbon (S:C) ratio and flow direction is then performed. By increasing the operating pressure up to 10 bar, the system efficiency increases and the temperature gradient can be minimized. The use of a high inlet S:C ratio reduces the cooling spot at the entrance of reformer channel but the electrical efficiency is considerably decreased. An IIR-SOFC with a counter-flow pattern (as based case) is compared with that with co-flow pattern (co-flow of air and fuel streams through fuel cell). The IIR-SOFC with co-flow pattern provides higher voltage and a smoother temperature gradient along the system due to superior matching between heat supplied from electrochemical reaction and heat required for steam reforming reaction; thus it is expected to be a better option for practical applications. ฉ 2009 Elsevier B.V. All rights reserved.


Keywords

Indirect internal reformingmethaneMethanol


Last updated on 2023-03-10 at 07:35