2013
DOI: 10.1016/j.enconman.2013.02.008
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Modeling and parametric simulations of solid oxide fuel cells with methane carbon dioxide reforming

Abstract: Abstract:A two-dimensional model is developed to simulate the performance of solid oxide fuel cells

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Cited by 119 publications
(54 citation statements)
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“…This probably implies that reaction (R22) dominates cell performance. Promotion of reaction (R23) is expected to enhance cell performance, as shown by theoretical studies (Ni, 2013). This can be achieved by developing selective electrocatalysts for reaction (R23).…”
Section: Advanced Biogas Utilizationmentioning
confidence: 99%
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“…This probably implies that reaction (R22) dominates cell performance. Promotion of reaction (R23) is expected to enhance cell performance, as shown by theoretical studies (Ni, 2013). This can be achieved by developing selective electrocatalysts for reaction (R23).…”
Section: Advanced Biogas Utilizationmentioning
confidence: 99%
“…This concept, also called direct-biogas solid oxide fuel cell (DB-SOFC), offers several advantages in comparison to the previously discussed method of external reforming (Figure 5), has currently received much attention in both experimental (Goula et al, 2006;Yentekakis, 2006 FIGURE 5 | Schematic of the differences between external (A) and internal (B) reforming concepts for SOFC-added electrical power generation from biogas. Papadam et al, 2012;Takahashi et al, 2012;Lanzini et al, 2013;Ma et al, 2015; and references therein) and modeling studies (Lanzini et al, 2011;Ni, 2013;Janardhanan, 2015a,b). Most of these studies made use of Ni-based cermet anodes, doped with additives in some cases in order to prevent carbon deposition (e.g., Yentekakis, 2006;Ma et al, 2015;Niakolas et al, 2015).…”
Section: Advanced Biogas Utilizationmentioning
confidence: 99%
“…Furthermore, the costs of auxiliary components (e.g., transformers, exhaust-flow controllers, etc.) were estimated at 5% of the main equipment cost, i.e., $101,000, as the maintenance cost in China is relatively lower than that in some developed countries [19]. Therefore, the estimated total cost of SOFC-based subsystem was $2.121 million, and of the integrated system, $2.436 million.…”
Section: Capex and Opex Analysismentioning
confidence: 97%
“…Note that the transfer coefficient applied in Eqs. (7)-(9) is set to be 0.5, which is a very typical value for SOFCs electrode [21,22]. The porosity is set as 0.3 according to experimental testing of an SOFC using similar fabrication techniques [23].…”
Section: Electrochemical Modelmentioning
confidence: 99%