首页|Modeling of phase separation solvent for CO2 capture using COSMO-SAC model

Modeling of phase separation solvent for CO2 capture using COSMO-SAC model

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Background: Phase separation solvents are proposed to replace conventional solvents for CO2 capture due to a significant reduction of absorbent regeneration heat. A predictive approach based on COSMO-SAC is developed to model the CO2 capture process using the phase separation solvent of 2-(ethylamino)ethanol (EAE) + water + diethylene glycol diethyl ether (DEGDEE). Methods: In this approach, liquid phase compositions, including CO2 solubility, are determined from vapor liquid-liquid equilibrium calculation with a chemisorption reaction in both liquid phases. The behavior of phase separation after CO2 capture and CO2 solubility in both CO2-lean and CO2-rich phases at 313 and 353 K can be well described by the proposed approach. Significant findings: The overall root-mean-square-deviation (RMSD) in predicting compositions (128 data points) of all components in both liquid phases is 0.064, which is slightly better than a previous study on the accuracy of COSMO-SAC in LLE prediction (RMSD = 0.105). The phase separation behavior of solvent can be realized with the hydrophilic product upon CO2 absorption from the s-profile analysis. The proposed framework is expected to be a useful tool for the development of a new phase separation solvent. (C) 2022 Taiwan Institute of Chemical Engineers. Published by Elsevier B.V. All rights reserved.

COSMO-SACVapor-liquid-liquid equilibriumPhase separation solventCO2 captureCARBON-DIOXIDE ABSORPTIONLIQUID-LIQUID EQUILIBRIUMMONOETHANOLAMINE MEABIPHASIC SOLVENTSVAPOR-PRESSUREIONIC LIQUIDSPREDICTIONRSTEMPERATUREPERFORMANCE

Hung, Ying-Chieh、Hsieh, Chieh-Ming、Machida, Hiroshi、Lin, Shiang-Tai、Shimoyama, Yusuke

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Tokyo Inst Technol

Natl Cent Univ

Nagoya Univ

Natl Taiwan Univ

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2022

Journal of the Taiwan Institute of Chemical Engineers

Journal of the Taiwan Institute of Chemical Engineers

EISCI
ISSN:1876-1070
年,卷(期):2022.135
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