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• W3037125526 endingPage "1509" @default.
• W3037125526 startingPage "1491" @default.
• W3037125526 abstract "The existing rate-based modeling of monoethanolamine (MEA) solvent for CO2 capturing has been improved using different kinetic models. Different models obtained from a combination of 15 kinetic models and 4 mass transfer correlations have been applied. The results show that the mass transfer correlation is instrumental for a reliable rate-based model. The resulting framework predicts the temperature and composition profiles at both liquid and gas phases with good accuracy. Overall, this allowed for improved prediction of (i) the CO2 capture performance, (ii) the CO2 partial pressure in output gas, and (iii) the temperature and CO2 composition profiles in the liquid." @default.
• W3037125526 created "2020-07-02" @default.
• W3037125526 creator A5031380913 @default.
• W3037125526 creator A5038211904 @default.
• W3037125526 creator A5040380606 @default.
• W3037125526 creator A5057421130 @default.
• W3037125526 creator A5076505547 @default.
• W3037125526 date "2020-06-29" @default.
• W3037125526 modified "2023-10-15" @default.
• W3037125526 title "Rigorous rate-based model for CO₂ capture via monoethanolamine-based solutions: effect of kinetic models, mass transfer, and holdup correlations on prediction accuracy" @default.
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• W3037125526 doi "https://doi.org/10.1080/01496395.2020.1784943" @default.

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