2022
DOI: 10.1016/j.cej.2021.132044
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CO2 absorption mechanism in aqueous ternary solutions of alkanolamines: Experimental and thermodynamic modeling approaches

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Cited by 14 publications
(6 citation statements)
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“…The baseline solvent for CO 2 capture, MEA, was proposed by R. R. Bottoms back in 1930 126 . Carbamate salt formed when CO 2 reacts with MEA is stable and requires a large amount of energy to break down the carbamate bond to release the captured CO 2 127‐131 . The total thermal energy requirement for regeneration of CO 2 from MEA solvent in a PCC plant is huge, in the range 3.5–4 GJ t −1 CO 2 .…”
Section: Process Intensification Options For Pccmentioning
confidence: 99%
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“…The baseline solvent for CO 2 capture, MEA, was proposed by R. R. Bottoms back in 1930 126 . Carbamate salt formed when CO 2 reacts with MEA is stable and requires a large amount of energy to break down the carbamate bond to release the captured CO 2 127‐131 . The total thermal energy requirement for regeneration of CO 2 from MEA solvent in a PCC plant is huge, in the range 3.5–4 GJ t −1 CO 2 .…”
Section: Process Intensification Options For Pccmentioning
confidence: 99%
“…The blended solvent approach has attracted a lot of interest in recent times to see the possibilities of addressing the challenges associated with the use of most of the amine-based solvents. Kim et al 129 studied the CO 2 absorption mechanism in aqueous ternary solutions of MEA, diisopropanolamine (DIPA) and 2-amino-2-methyl-propanol (AMP) over a wide temperature range and several blending ratios (MEA:DIPA:AMP) on carbomate, bicarbomate and carbomate molar fractions in the liquid phase, CO 2 cyclic capacity, CO 2 loading and heat of absorption. Therefore, for effective blending of amine solvent both absorption equilibrium and solvent kinetics must be considered simultaneously.…”
Section: Modified Packing For Enhanced Co 2 Capturementioning
confidence: 99%
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“…The potential shift exhibited a saturated behavior on the 1-CO 2 concentration and was controlled by the associated constants for the binding of H1 and its reduced form based on the Nernst equation. 28 Control experiments using diethanolamine 2, 2-(methylamino) ethanol 3, triethanolamine 4, and 2-diisopropylaminoethanol 5 to replace 1 led to reduction potential shifts of the reduction CO 2 adducts 29,30 (Figure 2e). The obvious spectral variation and isosbestic points in the absorption spectral titration of H1 upon the addition of these CO 2 adducts demonstrated the formation of a host−guest complex (Figures S5, S6, and S13−S16).…”
Section: ■ Introductionmentioning
confidence: 99%
“…Designing liquid solvents with varying affinities for gases is a common strategy in gas separation, exploiting differences in gas solubilities to enhance process efficiency. However, traditional liquid solvents such as aqueous inorganic acids, 17 ammonia water, 18 and aqueous alkanolamines 19,20 used for gas separation are highly volatile and lack structural designability, thereby highlighting the need for investigating new liquid solvents that possess low volatility and high structural designability for gas separation.…”
Section: Introductionmentioning
confidence: 99%