Experimental and Speciation Analysis of Biphasic TETA/TMEDA Blend for CO<sub>2</sub> Capture

Abstract Biphasic solvents show promise for CO 2 capture due to lower energy consumption but face challenges like high regeneration energy and phase separation instability. This study introduces a biphasic aqueous solvent system with triethylenetetramine (TETA) and tetramethylethylenediamine (TMEDA). The effects of TETA:TMEDA ratios on CO 2 absorption, viscosity, density, and phase separation were tested at various temperatures and compared to 5 M mono‐ethanolamine (MEA). The optimal 1.5 M TETA:2.5 M TMEDA at 40 °C captured 0.72 mol CO 2 mol −1 amine, with 84 % CO 2 in the lower phase. Desorption at 90 °C achieved 0.43 mol CO 2 L −1 , improving cyclic capacity by 62 % over MEA. The solvent required 2.77 GJ t CO 2 −1 for regeneration, 22 % less than MEA. Nuclear magnetic resonance (NMR) analyses elucidated reaction mechanisms and phase behavior. Stability was confirmed by over 10 absorption–desorption cycles.

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Publication Details

Journal
Chemical Engineering & Technology
Published
2025-06-09
DOI
https://doi.org/10.1002/ceat.70048
Citations
1
Primary Topic
Carbon Dioxide Capture Technologies
Type
article
Field-Weighted Citation Impact
0.71
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Experimental and Speciation Analysis of Biphasic TETA/TMEDA Blend for CO2 Capture

Monoj Kumar Mondal, Sujit Yuvraj Pimple
1 citations
Chemical Engineering & Technology
Carbon Dioxide Capture Technologies
0.71
article

Experimental and Speciation Analysis of Biphasic TETA/TMEDA Blend for CO2 Capture

Monoj Kumar Mondal, Sujit Yuvraj Pimple
article en
1 citations

Abstract

Abstract Biphasic solvents show promise for CO 2 capture due to lower energy consumption but face challenges like high regeneration energy and phase separation instability. This study introduces a biphasic aqueous solvent system with triethylenetetramine (TETA) and tetramethylethylenediamine (TMEDA). The effects of TETA:TMEDA ratios on CO 2 absorption, viscosity, density, and phase separation were tested at various temperatures and compared to 5 M mono‐ethanolamine (MEA). The optimal 1.5 M TETA:2.5 M TMEDA at 40 °C captured 0.72 mol CO 2 mol −1 amine, with 84 % CO 2 in the lower phase. Desorption at 90 °C achieved 0.43 mol CO 2 L −1 , improving cyclic capacity by 62 % over MEA. The solvent required 2.77 GJ t CO 2 −1 for regeneration, 22 % less than MEA. Nuclear magnetic resonance (NMR) analyses elucidated reaction mechanisms and phase behavior. Stability was confirmed by over 10 absorption–desorption cycles.

Chemical Engineering & TechnologyVol. 48(7)
Banaras Hindu University (IN)
Affordable and clean energy
Openalex Percentile: Top 32%
Carbon Dioxide Capture Technologies
0.71
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