Economic Feasibility of Power/Heat Cogeneration by Biogas–Solid Oxide Fuel Cell (SOFC) Integrated Systems

Based upon the thermodynamic simulation of a biogas-SOFC integrated process and the costing of its elements, the present work examines the economic feasibility of biogas-SOFCs for combined heat and power (CHP) generation, by the comparison of their economic performance against the conventional bioga...

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Main Authors: Costas Athanasiou, Christos Drosakis, Gaylord Kabongo Booto, Costas Elmasides
Format: Article
Language:English
Published: MDPI AG 2022-12-01
Series:Energies
Subjects:
Online Access:https://www.mdpi.com/1996-1073/16/1/404
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author Costas Athanasiou
Christos Drosakis
Gaylord Kabongo Booto
Costas Elmasides
author_facet Costas Athanasiou
Christos Drosakis
Gaylord Kabongo Booto
Costas Elmasides
author_sort Costas Athanasiou
collection DOAJ
description Based upon the thermodynamic simulation of a biogas-SOFC integrated process and the costing of its elements, the present work examines the economic feasibility of biogas-SOFCs for combined heat and power (CHP) generation, by the comparison of their economic performance against the conventional biogas-CHP with internal combustion engines (ICEs), under the same assumptions. As well as the issues of process scale and an SOFC’s cost, examined in the literature, the study brings up the determinative effects of: (i) the employed SOFC size, with respect to its operational point, as well as (ii) the feasibility criterion, on the feasibility assessment. Two plant capacities were examined (250 m<sup>3</sup>·h<sup>−1</sup> and 750 m<sup>3</sup>·h<sup>−1</sup> biogas production), and their feasibilities were assessed by the Internal Rate of Return (IRR), the Net Present Value (NPV) and the Pay Back Time (PBT) criteria. For SOFC costs at 1100 and 2000 EUR·kW<sub>el</sub><sup>−1</sup>, foreseen in 2035 and 2030, respectively, SOFCs were found to increase investment (by 2.5–4.5 times, depending upon a plant’s capacity and the SOFC’s size) and power generation (by 13–57%, depending upon the SOFC’s size), the latter increasing revenues. SOFC-CHP exhibits considerably lower IRRs (5.3–13.4% for the small and 16.8–25.3% for the larger plant), compared to ICE-CHP (34.4%). Nonetheless, according to NPV that does not evaluate profitability as a return on investment, small scale biogas-SOFCs (NPV<sub>max</sub>: EUR 3.07 M) can compete with biogas-ICE (NPV: EUR 3.42 M), for SOFCs sized to operate at 70% of the maximum power density (MPD) and with a SOFC cost of 1100 EUR·kW<sub>el</sub><sup>−1</sup>, whereas for larger plants, SOFC-CHP can lead to considerably higher NPVs (EUR 12.5–21.0 M) compared to biogas-ICE (EUR 9.3 M). Nonetheless, PBTs are higher for SOFC-CHP (7.7–11.1 yr and 4.2–5.7 yr for the small and the large plant, respectively, compared to 2.3 yr and 3.1 yr for biogas-ICE) because the criterion suppresses the effect of SOFC-CHP-increased revenues to a time period shorter than the plant’s lifetime. Finally, the economics of SOFC-CHP are optimized for SOFCs sized to operate at 70–82.5% of their MPD, depending upon the SOFC cost and the feasibility criterion. Overall, the choice of the feasibility criterion and the size of the employed SOFC can drastically affect the economic evaluation of SOFC-CHP, whereas the feasibility criterion also determines the economically optimum size of the employed SOFC.
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spelling doaj.art-8347c0d7baef4345940991db27f9096c2023-11-16T15:18:47ZengMDPI AGEnergies1996-10732022-12-0116140410.3390/en16010404Economic Feasibility of Power/Heat Cogeneration by Biogas–Solid Oxide Fuel Cell (SOFC) Integrated SystemsCostas Athanasiou0Christos Drosakis1Gaylord Kabongo Booto2Costas Elmasides3Department of Environmental Engineering, Democritus University of Thrace, 67100 Xanthi, GreeceDepartment of Mechanical Engineering, University of Western Macedonia, 50100 Kila Kozanis, GreeceEnvironmental Impacts & Sustainability, NILU—Norwegian Institute for Air Research, Instituttveien 18, 2007 Kjeller, NorwayDepartment of Environmental Engineering, Democritus University of Thrace, 67100 Xanthi, GreeceBased upon the thermodynamic simulation of a biogas-SOFC integrated process and the costing of its elements, the present work examines the economic feasibility of biogas-SOFCs for combined heat and power (CHP) generation, by the comparison of their economic performance against the conventional biogas-CHP with internal combustion engines (ICEs), under the same assumptions. As well as the issues of process scale and an SOFC’s cost, examined in the literature, the study brings up the determinative effects of: (i) the employed SOFC size, with respect to its operational point, as well as (ii) the feasibility criterion, on the feasibility assessment. Two plant capacities were examined (250 m<sup>3</sup>·h<sup>−1</sup> and 750 m<sup>3</sup>·h<sup>−1</sup> biogas production), and their feasibilities were assessed by the Internal Rate of Return (IRR), the Net Present Value (NPV) and the Pay Back Time (PBT) criteria. For SOFC costs at 1100 and 2000 EUR·kW<sub>el</sub><sup>−1</sup>, foreseen in 2035 and 2030, respectively, SOFCs were found to increase investment (by 2.5–4.5 times, depending upon a plant’s capacity and the SOFC’s size) and power generation (by 13–57%, depending upon the SOFC’s size), the latter increasing revenues. SOFC-CHP exhibits considerably lower IRRs (5.3–13.4% for the small and 16.8–25.3% for the larger plant), compared to ICE-CHP (34.4%). Nonetheless, according to NPV that does not evaluate profitability as a return on investment, small scale biogas-SOFCs (NPV<sub>max</sub>: EUR 3.07 M) can compete with biogas-ICE (NPV: EUR 3.42 M), for SOFCs sized to operate at 70% of the maximum power density (MPD) and with a SOFC cost of 1100 EUR·kW<sub>el</sub><sup>−1</sup>, whereas for larger plants, SOFC-CHP can lead to considerably higher NPVs (EUR 12.5–21.0 M) compared to biogas-ICE (EUR 9.3 M). Nonetheless, PBTs are higher for SOFC-CHP (7.7–11.1 yr and 4.2–5.7 yr for the small and the large plant, respectively, compared to 2.3 yr and 3.1 yr for biogas-ICE) because the criterion suppresses the effect of SOFC-CHP-increased revenues to a time period shorter than the plant’s lifetime. Finally, the economics of SOFC-CHP are optimized for SOFCs sized to operate at 70–82.5% of their MPD, depending upon the SOFC cost and the feasibility criterion. Overall, the choice of the feasibility criterion and the size of the employed SOFC can drastically affect the economic evaluation of SOFC-CHP, whereas the feasibility criterion also determines the economically optimum size of the employed SOFC.https://www.mdpi.com/1996-1073/16/1/404biogasSOFCsimulationeconomic feasibility
spellingShingle Costas Athanasiou
Christos Drosakis
Gaylord Kabongo Booto
Costas Elmasides
Economic Feasibility of Power/Heat Cogeneration by Biogas–Solid Oxide Fuel Cell (SOFC) Integrated Systems
Energies
biogas
SOFC
simulation
economic feasibility
title Economic Feasibility of Power/Heat Cogeneration by Biogas–Solid Oxide Fuel Cell (SOFC) Integrated Systems
title_full Economic Feasibility of Power/Heat Cogeneration by Biogas–Solid Oxide Fuel Cell (SOFC) Integrated Systems
title_fullStr Economic Feasibility of Power/Heat Cogeneration by Biogas–Solid Oxide Fuel Cell (SOFC) Integrated Systems
title_full_unstemmed Economic Feasibility of Power/Heat Cogeneration by Biogas–Solid Oxide Fuel Cell (SOFC) Integrated Systems
title_short Economic Feasibility of Power/Heat Cogeneration by Biogas–Solid Oxide Fuel Cell (SOFC) Integrated Systems
title_sort economic feasibility of power heat cogeneration by biogas solid oxide fuel cell sofc integrated systems
topic biogas
SOFC
simulation
economic feasibility
url https://www.mdpi.com/1996-1073/16/1/404
work_keys_str_mv AT costasathanasiou economicfeasibilityofpowerheatcogenerationbybiogassolidoxidefuelcellsofcintegratedsystems
AT christosdrosakis economicfeasibilityofpowerheatcogenerationbybiogassolidoxidefuelcellsofcintegratedsystems
AT gaylordkabongobooto economicfeasibilityofpowerheatcogenerationbybiogassolidoxidefuelcellsofcintegratedsystems
AT costaselmasides economicfeasibilityofpowerheatcogenerationbybiogassolidoxidefuelcellsofcintegratedsystems