Experimental investigation on CO2 absorption capacity and viscosity for high concentrated 1-dimethylamino-2-propanol–monoethanolamine aqueous blends. (December 2019)

• Record Type: Journal Article
• Authors: Wang, Lemeng; Tian, Xiangfeng; Fu, Dong; Du, Xiaoqian; Ye, Junhong
• Is Part Of: Journal of chemical thermodynamics. Volume 139(2019)
• Publication Date: 2019-12
• Subjects: Absorption capacity -- Viscosity -- MEA -- DMA2P; Thermodynamics -- Periodicals; Thermochemistry -- Periodicals; Thermodynamique -- Périodiques; Thermochimie -- Périodiques; Thermochemistry; Thermodynamics; Periodicals; 541.369
• DOI: 10.1016/j.jct.2019.07.007
• Languages: English
• ISSNs: 0021-9614

Abstract

Highlights: Absorption of CO2 in DMA2P aqueous solution can be accelerated by addition of MEA. Viscosities of the carbonated MEA-DMA2P solutions were measured and calculated. Activation energy of MEA-DMA2P solutions was calculated base on the viscosities. Temperature, mass fraction and CO2 loading dependences of viscosity were illustrated. Good absorption performance and appropriate viscosity were simultaneously achieved. Abstract: Experimental data of CO2 absorption capacity for high concentrated 1-dimethylamino-2-propanol (DMA2P)–monoethanolamine (MEA) aqueous blends are presented under atmospheric pressure in a temperature range of 303.2–323.2 K, at different mass fractions of DMA2P (30 wt%–50 wt%) and MEA (5 wt%–15 wt%). The mass fraction and temperature dependences of the absorption capacity are illustrated. The addition of small amount of MEA into DMA2P aqueous solution leads to an obvious increase in the absorption rate of CO2 . However, the absorption rate increases not so significantly when w MEA is of high value. Moreover, the temperature affects the absorption rate not so significantly as compared to solution concentration. The CO2 absorption heat of DMA2P-MEA based on the Gibbs-Helmholtz equation was found to be −55.0 kJ/mol. Besides, the viscosities of both CO2 -unloaded and CO2 -loaded aqueous solutions were measured and modeled in a temperature range of 303.2–323.2 K, and in atmospheric pressure. The effects of temperature, composition and CO2 loading on viscosities were demonstrated. The Weiland equation gave a good prediction with an average relative deviation of 2.42%. Moreover, the activation energy ( E a) was estimated based on the viscosity.