Experimental validation of kinetics and VLE of carbon di-oxide absorption in aqueous MEA at deep removal conditions

• Kinetics and solubility for CO 2 absorption in 5 M MEA is investigated for CO 2 deep removal. • The absorption rate is reported as absorption flux per unit driving force. • Using this specific absorption flux avoids errors due to solubility and diffusivity correlations. • Usefulness of this absorption flux approach is illustrated using Aspen Plus implementation. The increasing attention for deep removal (99 %+) of carbon di-oxide (CO 2 ) from flue gases, requires confirmation of absorption kinetics and VLE under the relevant operating conditions. In this work, the CO 2 absorption rate and the equilibrium capacity in aqueous solution of 5 M Mono-ethanolamine (MEA) is investigated for the deep-removal regime (2000 ppm to 100 ppm CO 2 ) using a stirred-cell contactor. The absorption flux is measured over a temperature range of 20–45 °C with solvent loadings from 0 to 0.36 mol CO 2 /mol MEA, while the equilibrium capacity is evaluated between 30–60 °C, at solvent loadings ranging from 0.05 to 0.35 mol CO 2 /mol MEA. For the accurate measurement of absorption kinetics under these conditions, the gas-phase mass transfer coefficient (k g ) was characterized using various solvent systems. The kinetic and VLE data presented in this work covers the experimental conditions not studied before, still very relevant to the deep CO 2 removal operating conditions. The absorption kinetics are reported as the absorption flux per unit driving force (referred to as specific absorption flux). The specific absorption flux allows an independent assessment of absorption kinetics (as a function of solvent loading and temperature), unaffected by possible errors introduced by the solubility and diffusivity data. The specific absorption flux is described using an Arrhenius type equation. The application of specific absorption flux for calculating the absorber column height in Aspen Plus is illustrated with a typical Natural gas combined cycle (NGCC) case.

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Publication Details

Journal
Chemical Engineering Science
Published
2025-08-25
DOI
https://doi.org/10.1016/j.ces.2025.122487
Citations
1
Primary Topic
Carbon Dioxide Capture Technologies
Type
article
Field-Weighted Citation Impact
0.71

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article

Experimental validation of kinetics and VLE of carbon di-oxide absorption in aqueous MEA at deep removal conditions

Derk W.F. Brilman, J. Ganesan, A.G.J. van der Ham
1 citations
Chemical Engineering Science
Carbon Dioxide Capture Technologies
0.71
article

Experimental validation of kinetics and VLE of carbon di-oxide absorption in aqueous MEA at deep removal conditions

Derk W.F. Brilman, J. Ganesan, A.G.J. van der Ham
article en
1 citations

Abstract

• Kinetics and solubility for CO 2 absorption in 5 M MEA is investigated for CO 2 deep removal. • The absorption rate is reported as absorption flux per unit driving force. • Using this specific absorption flux avoids errors due to solubility and diffusivity correlations. • Usefulness of this absorption flux approach is illustrated using Aspen Plus implementation. The increasing attention for deep removal (99 %+) of carbon di-oxide (CO 2 ) from flue gases, requires confirmation of absorption kinetics and VLE under the relevant operating conditions. In this work, the CO 2 absorption rate and the equilibrium capacity in aqueous solution of 5 M Mono-ethanolamine (MEA) is investigated for the deep-removal regime (2000 ppm to 100 ppm CO 2 ) using a stirred-cell contactor. The absorption flux is measured over a temperature range of 20–45 °C with solvent loadings from 0 to 0.36 mol CO 2 /mol MEA, while the equilibrium capacity is evaluated between 30–60 °C, at solvent loadings ranging from 0.05 to 0.35 mol CO 2 /mol MEA. For the accurate measurement of absorption kinetics under these conditions, the gas-phase mass transfer coefficient (k g ) was characterized using various solvent systems. The kinetic and VLE data presented in this work covers the experimental conditions not studied before, still very relevant to the deep CO 2 removal operating conditions. The absorption kinetics are reported as the absorption flux per unit driving force (referred to as specific absorption flux). The specific absorption flux allows an independent assessment of absorption kinetics (as a function of solvent loading and temperature), unaffected by possible errors introduced by the solubility and diffusivity data. The specific absorption flux is described using an Arrhenius type equation. The application of specific absorption flux for calculating the absorber column height in Aspen Plus is illustrated with a typical Natural gas combined cycle (NGCC) case.

Chemical Engineering ScienceVol. 320
University of Twente, Ministerie van Economische Zaken en Klimaat
Clean water and sanitation
Openalex Percentile: Top 28%
Carbon Dioxide Capture Technologies
0.71
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