Techno-economic analysis of integrating an on-board CCS system and a PtG technology in a heavy vehicle fleet

Decarbonising the heavy-duty transport sector requires switching internal combustion engine (ICE) fuel from fossil to synthetic fuels. In this context, on-board carbon capture and storage (OCCS) in ICEs could provide the CO 2 needed by Power-to-gas (PtG) technologies to produce synthetic natural gas (SNG), which is then consumed again by the vehicle fleet, closing in this way the carbon loop. This study presents a techno-economic analysis of a heavy-duty vehicle fleet integrating an OCCS system with a PtG plant. The OCCS system operates by temperature swing adsorption where two sorbents, PPN-6-CH 2 -DETA and zeolite 13X, are evaluated at carbon capture rates (CCR) of 70 % and 100 %. A fifth scenario examined the effect of varying the H 2 :CO 2 ratio in the methanation plant at 100 % CCR using PPN-6-CH 2 -DETA. Both systems were simulated using Aspen Plus and AVL Boost softwares. Moreover, a sensitivity analysis was conducted considering three key performance indicators: the CO 2 tax, natural gas (NG), and electricity prices. The results indicate that the carbon abatement cost reaches a break-even point at 150 €/tCO₂ for a fleet size of 400 vehicles. However, the capital expenditures do not achieve payback within 20 years due to the high operational expenditures and low incomes in the evaluated scenarios. The sensitivity analyses show that the CO 2 tax and the NG price must be higher than 400 €/tCO₂ and 160 €/MWh, respectively, to compensate for the current electricity price and allow the proposed systems to be techno-economic feasible. • Novel integration between an OCCS system and PtG. • PPN sorbent performs better but has manufacturing and availability limitations. • Lowering the H₂:CO₂ ratio reduces costs but worsens SNG quality. • A CO₂ tax above 400 €/tCO₂ improves economic feasibility. • CAC break-even is reached at around 150 €/tCO₂ for a vehicle fleet of 400 units.

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Publication Details

Journal
Journal of CO2 Utilization
Published
2025-02-28
DOI
https://doi.org/10.1016/j.jcou.2025.103046
Primary Topic
Catalytic Processes in Materials Science
Type
article
Field-Weighted Citation Impact
0.00

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article

Techno-economic analysis of integrating an on-board CCS system and a PtG technology in a heavy vehicle fleet

Alexander García‐Mariaca, Jorge Perpiñán, Uriel Fernando Carreño Sayago
Journal of CO2 Utilization
Catalytic Processes in Materials Science
article

Techno-economic analysis of integrating an on-board CCS system and a PtG technology in a heavy vehicle fleet

Alexander García‐Mariaca, Jorge Perpiñán, Uriel Fernando Carreño Sayago
article en

Abstract

Decarbonising the heavy-duty transport sector requires switching internal combustion engine (ICE) fuel from fossil to synthetic fuels. In this context, on-board carbon capture and storage (OCCS) in ICEs could provide the CO 2 needed by Power-to-gas (PtG) technologies to produce synthetic natural gas (SNG), which is then consumed again by the vehicle fleet, closing in this way the carbon loop. This study presents a techno-economic analysis of a heavy-duty vehicle fleet integrating an OCCS system with a PtG plant. The OCCS system operates by temperature swing adsorption where two sorbents, PPN-6-CH 2 -DETA and zeolite 13X, are evaluated at carbon capture rates (CCR) of 70 % and 100 %. A fifth scenario examined the effect of varying the H 2 :CO 2 ratio in the methanation plant at 100 % CCR using PPN-6-CH 2 -DETA. Both systems were simulated using Aspen Plus and AVL Boost softwares. Moreover, a sensitivity analysis was conducted considering three key performance indicators: the CO 2 tax, natural gas (NG), and electricity prices. The results indicate that the carbon abatement cost reaches a break-even point at 150 €/tCO₂ for a fleet size of 400 vehicles. However, the capital expenditures do not achieve payback within 20 years due to the high operational expenditures and low incomes in the evaluated scenarios. The sensitivity analyses show that the CO 2 tax and the NG price must be higher than 400 €/tCO₂ and 160 €/MWh, respectively, to compensate for the current electricity price and allow the proposed systems to be techno-economic feasible. • Novel integration between an OCCS system and PtG. • PPN sorbent performs better but has manufacturing and availability limitations. • Lowering the H₂:CO₂ ratio reduces costs but worsens SNG quality. • A CO₂ tax above 400 €/tCO₂ improves economic feasibility. • CAC break-even is reached at around 150 €/tCO₂ for a vehicle fleet of 400 units.

Journal of CO2 UtilizationVol. 93
Universidad de Zaragoza (ES), Fundación Universitaria Los Libertadores (CO)
European Regional Development Fund
Decent work and economic growth
Openalex Percentile: Top 97%
Catalytic Processes in Materials Science
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