Techno-economic evaluation of emission control configurations for AMP/PZ-based post-combustion CO₂ capture

Minimizing the environmental impacts of amine-based post-combustion carbon capture technologies is essential for regulatory compliance and public acceptance. Experimental campaigns at RWE's CO 2 capture pilot plant in Niederaussem using CESAR1 demonstrated that combining existing emission abatement technologies can substantially reduce the concentration of amines and degradation products in the CO 2 -depleted flue gas to below the detection limit of an infrared spectrometer. The campaign confirmed that a proprietary dry bed technology (OEASE aerozone™) or a second water wash can reduce AMP and PZ emissions to below 1 mg/Nm 3 . However, an acid or chemically active wash downstream of the water wash is necessary to reduce NH 3 emissions to very low levels (<2 mg/Nm 3 ). Combining a dry bed with an acid wash significantly reduces both the required acid solution and the resulting acid waste. The techno-economic analysis indicates that implementing emission mitigation technologies provides substantial environmental benefits for the CESAR1 process, with only a marginal increase (<1 €/tCO₂) in both the carbon capture cost (CCC) and CO₂ avoidance cost (CAC). The additional capital cost associated with extra column packing is offset by operational cost savings from reduced solvent losses. For stringent emission permits targeting NH₃, a configuration combining a dry bed upstream of the water wash followed by an acid wash achieves the best balance between emission control and cost efficiency. This configuration results in a Levelized Cost of Electricity (LCOE) of 143 €/MWh, a CCC of 45.4 €/tCO₂, and a CAC of 88.4 €/tCO₂. • Integrated techno-economic assessment of six CESAR1 emission mitigation configurations. • Combines experimental data from RWE's Niederaussem pilot with validated process modelling. • Single water wash insufficient; dry bed and acid wash essential for NH₃ control (<2 mg/Nm 3 ). • Combined dry bed + acid wash minimizes solvent losses, acid use, and waste generation. • Optimal configuration achieves CCC = 45.4 €/tCO₂ and CAC = 88.4 €/tCO₂ with full emission compliance.

Authors

Institutions

Publication Details

Journal
Chemical Engineering Journal
Published
2025-12-03
DOI
https://doi.org/10.1016/j.cej.2025.171446
Citations
1
Primary Topic
Carbon Dioxide Capture Technologies
Type
article
Field-Weighted Citation Impact
0.71
Controls
|||
ALL TIME
JAN
FEB
MAR
APR
MAY
JUN
JUL
AUG
SEP
OCT
article

Techno-economic evaluation of emission control configurations for AMP/PZ-based post-combustion CO₂ capture

Michael Matuszewski, Susana García, Laura Herraiz, Peter Moser et al.
1 citations
Chemical Engineering Journal
Carbon Dioxide Capture Technologies
0.71
article

Techno-economic evaluation of emission control configurations for AMP/PZ-based post-combustion CO₂ capture

Michael Matuszewski, Susana García, Laura Herraiz, Peter Moser, Mijndert W. van der Spek, Torsten Stoffregen, Koteswara Rao Putta, Georg Wiechers, Joshua C. Morgan
article en
1 citations

Abstract

Minimizing the environmental impacts of amine-based post-combustion carbon capture technologies is essential for regulatory compliance and public acceptance. Experimental campaigns at RWE's CO 2 capture pilot plant in Niederaussem using CESAR1 demonstrated that combining existing emission abatement technologies can substantially reduce the concentration of amines and degradation products in the CO 2 -depleted flue gas to below the detection limit of an infrared spectrometer. The campaign confirmed that a proprietary dry bed technology (OEASE aerozone™) or a second water wash can reduce AMP and PZ emissions to below 1 mg/Nm 3 . However, an acid or chemically active wash downstream of the water wash is necessary to reduce NH 3 emissions to very low levels (<2 mg/Nm 3 ). Combining a dry bed with an acid wash significantly reduces both the required acid solution and the resulting acid waste. The techno-economic analysis indicates that implementing emission mitigation technologies provides substantial environmental benefits for the CESAR1 process, with only a marginal increase (<1 €/tCO₂) in both the carbon capture cost (CCC) and CO₂ avoidance cost (CAC). The additional capital cost associated with extra column packing is offset by operational cost savings from reduced solvent losses. For stringent emission permits targeting NH₃, a configuration combining a dry bed upstream of the water wash followed by an acid wash achieves the best balance between emission control and cost efficiency. This configuration results in a Levelized Cost of Electricity (LCOE) of 143 €/MWh, a CCC of 45.4 €/tCO₂, and a CAC of 88.4 €/tCO₂. • Integrated techno-economic assessment of six CESAR1 emission mitigation configurations. • Combines experimental data from RWE's Niederaussem pilot with validated process modelling. • Single water wash insufficient; dry bed and acid wash essential for NH₃ control (<2 mg/Nm 3 ). • Combined dry bed + acid wash minimizes solvent losses, acid use, and waste generation. • Optimal configuration achieves CCC = 45.4 €/tCO₂ and CAC = 88.4 €/tCO₂ with full emission compliance.

Chemical Engineering JournalVol. 527
Heriot-Watt University (GB), National Energy Technology Laboratory (US), Linde (Germany) (DE), RWE (Germany) (DE)
Openalex Percentile: Top 24%
Carbon Dioxide Capture Technologies
0.71
AI Navigator

Ask Laika to Summarize, Analyze, and Connect papers live on the map.

Summarize Papers & Methodologies

Extract key findings, datasets, and comparative methods across publications.

Benchmark Rankings & Visual Analytics

Rank top research institutions, authors, funders, topics, and journals by Field-Weighted Citation Impact (FWCI) and paper volume with instant charts.

Connect Distant Disciplines

Bridge topological clusters on the map to find hidden collaborative intersections.