2019
DOI: 10.1016/j.energy.2019.04.174
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Experimental and kinetic study of the catalytic desorption of CO2 from CO2-loaded monoethanolamine (MEA) and blended monoethanolamine – Methyl-diethanolamine (MEA-MDEA) solutions

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Cited by 56 publications
(37 citation statements)
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“…The CO 2 absorption capacities measured for the ChCl:LvAc DESs are clearly lower than the CO 2 absorption capacity reported in the literature for aqueous solutions of MEA at 30 wt% [ 34 ], as shown in Figure 3 . This might be due to the fact that the CO 2 absorption mechanism is different in both cases: CO 2 absorption in MEA solutions is a combination of chemisorption and physisorption [ 35 , 36 ], whereas the CO 2 absorption in the DESs studied in this work is limited to physisorption only [ 37 ].…”
Section: Resultsmentioning
confidence: 99%
“…The CO 2 absorption capacities measured for the ChCl:LvAc DESs are clearly lower than the CO 2 absorption capacity reported in the literature for aqueous solutions of MEA at 30 wt% [ 34 ], as shown in Figure 3 . This might be due to the fact that the CO 2 absorption mechanism is different in both cases: CO 2 absorption in MEA solutions is a combination of chemisorption and physisorption [ 35 , 36 ], whereas the CO 2 absorption in the DESs studied in this work is limited to physisorption only [ 37 ].…”
Section: Resultsmentioning
confidence: 99%
“…The NAC bond stretches and, eventually, breaks, which causes the zwitterion to become MEA and CO 2 . At high regeneration temperatures, the CO 2 solubility in the aqueous solution is low and the CO 2 will then transfer to the gas phase [81,[84][85][86]. Therefore, this also explains why when more HZSM-5 catalysts are present, the concentrations of available protons would increase and, therefore, allow MEACOO-to react with the protons at an increased rate.…”
Section: Limited Number Of Protons Availablementioning
confidence: 99%
“…Nonetheless, there remain some challenges to such absorbents like low vapor pressure, amine solvent degradation and equipment corrosion. However, the high cost of energy consumption in the solvent regeneration section is known as the main problem in the industrial usage of amine solvents because of strong chemical reactions (Akachuku et al 2019). Therefore, widespread studies have been performed to introduce new approaches for the reduction of energy consumption in amine stripping. )…”
Section: Introductionmentioning
confidence: 99%