2021
DOI: 10.1016/j.cep.2021.108582
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Enhancement of CO2 desorption from MEA-based nanofluids in membrane contactor: Simulation study

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Cited by 12 publications
(5 citation statements)
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“…In addition, Mohammaddoost et al 32 claimed that the CO 2 desorption rate of the rich water-based nanofluids exceeded 97%. Mohammed et al 14 simulated the CO 2 desorption process in SiO 2 −MEA nanofluids for the first time in the HFMC. It was noted that the gas-phase flow rate had a negligible effect on the desorption effect compared to the liquid-phase flow rate.…”
Section: Co 2 Desorption By Nanofluidsmentioning
confidence: 99%
See 1 more Smart Citation
“…In addition, Mohammaddoost et al 32 claimed that the CO 2 desorption rate of the rich water-based nanofluids exceeded 97%. Mohammed et al 14 simulated the CO 2 desorption process in SiO 2 −MEA nanofluids for the first time in the HFMC. It was noted that the gas-phase flow rate had a negligible effect on the desorption effect compared to the liquid-phase flow rate.…”
Section: Co 2 Desorption By Nanofluidsmentioning
confidence: 99%
“…The number of publications has been increasing year by year, indicating growing interest in this field. Various types of nanofluids have been used in these studies, including water- and amine-based nanofluids containing multiple categories of nanoparticles, such as metals, metal oxides, non-metals, and non-metal oxides. …”
Section: Introductionmentioning
confidence: 99%
“…Using a solvent with higher surface tension could lower the possibility of membrane wetting. 18,19 Conventional solvents such as monoethanolamine (MEA) and diethanolamine (DEA) have been used in membrane contactors due to their high reactivity toward CO 2 , low price and good biodegradability, 20,21 but they do not prevent wetting. [22][23][24] Thus, recent research has focused on the use of other solvents such as amino acids (AAs), [25][26][27] ionic liquids [28][29][30] or ammonia [31][32][33] in order to replace alkanolamines.…”
Section: Introductionmentioning
confidence: 99%
“…Nanoparticles such as SiO 2 and Al 2 O 3 , along with MEA aqueous solution, help reduce the energy consumption of CO 2 stripping. The highest mass transfer resistance is in the liquid phase, and increased liquid velocity increases the desorption flux [27].…”
Section: Introductionmentioning
confidence: 99%