Techno-economic analysis of promoter-enhanced CO2 capture with electrochemical regeneration: A comparative study with CESAR1 on a CHP plant

This study presents a techno-economic analysis (TEA) comparing an alkaline solvent-based carbon capture technology utilizing electrochemical regeneration (ConsenCUS) with a conventional amine-based thermal regeneration approach (CESAR1) when retrofitted to a combined heat and power (CHP) plant to capture 0.45 Mtonne CO 2 annually. The study also investigates the integration of immobilized carbonic anhydrase (CA) as a promoter to enhance CO 2 absorption kinetics in the ConsenCUS system (ConsenCUS-CA). The results demonstrate that CESAR1 has a regeneration energy requirement of 3.23 GJ th /tonne CO 2 , compared with 3.74 GJ el /tonne CO 2 for ConsenCUS. Meanwhile, ConsenCUS-CA demonstrates significant improvements, including an 18.6% reduction in solvent requirement, a two-thirds decrease in absorber height, and an 18.4% reduction in electrical regeneration energy requirement, resulting in a 14.1% decrease in total capital requirement, a 12.2% decrease in operating cost, and a 22.3% decrease in the cost of CO 2 avoided when using renewable energy. Despite requiring 30% lower capital investment than CESAR1, ConsenCUS-CA incurs up to 23% higher annual operating costs, primarily due to the electricity required for electrochemical regeneration. The impact of regeneration energy sources is also examined. The economic comparison shows that CESAR1, using a natural gas boiler for steam generation, has an €11.38/tonne CO 2 higher cost of CO 2 avoided but a €2.60/tonne steam lower additional steam production cost than ConsenCUS-CA using renewable electricity. The study further examines the impacts of technological learning, electricity price, CA cost and lifetime, CO 2 emission price, discount rate, plant lifetime, and potential performance improvements on the economic viability of the technologies. The findings indicate that, with continued technological development, ConsenCUS-CA could achieve operating cost parity with CESAR1 if its electrical energy consumption is reduced by at least 25%.

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Publication Details

Journal
International journal of greenhouse gas control
Published
2026-09-30
DOI
https://doi.org/10.1016/j.ijggc.2026.104802
Primary Topic
Carbon Dioxide Capture Technologies
Type
article
Field-Weighted Citation Impact
0.00

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article

Techno-economic analysis of promoter-enhanced CO2 capture with electrochemical regeneration: A comparative study with CESAR1 on a CHP plant

Ashween Kaur Virdee, Susana García, Friday O. Ochedi, Mijndert W. van der Spek et al.
International journal of greenhouse gas control
Carbon Dioxide Capture Technologies
article

Techno-economic analysis of promoter-enhanced CO2 capture with electrochemical regeneration: A comparative study with CESAR1 on a CHP plant

Ashween Kaur Virdee, Susana García, Friday O. Ochedi, Mijndert W. van der Spek, Fariborz Shaahmadi, Grigorios Itskos, Sotirios Efstathios Antonoudis, John Andresen, Ilias Kakanis
article en

Abstract

This study presents a techno-economic analysis (TEA) comparing an alkaline solvent-based carbon capture technology utilizing electrochemical regeneration (ConsenCUS) with a conventional amine-based thermal regeneration approach (CESAR1) when retrofitted to a combined heat and power (CHP) plant to capture 0.45 Mtonne CO 2 annually. The study also investigates the integration of immobilized carbonic anhydrase (CA) as a promoter to enhance CO 2 absorption kinetics in the ConsenCUS system (ConsenCUS-CA). The results demonstrate that CESAR1 has a regeneration energy requirement of 3.23 GJ th /tonne CO 2 , compared with 3.74 GJ el /tonne CO 2 for ConsenCUS. Meanwhile, ConsenCUS-CA demonstrates significant improvements, including an 18.6% reduction in solvent requirement, a two-thirds decrease in absorber height, and an 18.4% reduction in electrical regeneration energy requirement, resulting in a 14.1% decrease in total capital requirement, a 12.2% decrease in operating cost, and a 22.3% decrease in the cost of CO 2 avoided when using renewable energy. Despite requiring 30% lower capital investment than CESAR1, ConsenCUS-CA incurs up to 23% higher annual operating costs, primarily due to the electricity required for electrochemical regeneration. The impact of regeneration energy sources is also examined. The economic comparison shows that CESAR1, using a natural gas boiler for steam generation, has an €11.38/tonne CO 2 higher cost of CO 2 avoided but a €2.60/tonne steam lower additional steam production cost than ConsenCUS-CA using renewable electricity. The study further examines the impacts of technological learning, electricity price, CA cost and lifetime, CO 2 emission price, discount rate, plant lifetime, and potential performance improvements on the economic viability of the technologies. The findings indicate that, with continued technological development, ConsenCUS-CA could achieve operating cost parity with CESAR1 if its electrical energy consumption is reduced by at least 25%.

International journal of greenhouse gas controlVol. 156
Heriot-Watt University (GB), Centre for Research and Technology Hellas (GR)
HORIZON EUROPE Framework Programme
Openalex Percentile: Top 22%
Carbon Dioxide Capture Technologies
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