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• W2750555588 abstract "Abstract The studies on the characteristics of absorbents are important to develop process and evaluate performance. Among the absorbent studies, the overall mass transfer coefficient was used as a key data for design packing type and absorber height to achieve cost effective process. In this study, the overall mass transfer rates of the K 2 CO 3 based absorbents were measured by a wetted-wall column (WWC) apparatus. Experimental conditions of temperature and pressure were maintained at 313.15 K ∼ 333.15 K and 1.15 bar, respectively. The injected CO 2 concentrations were 3 vol.% ∼ 12 vol.% (N 2 balanced). As a result of experiment, the mass transfer rates increased following the order: MEA > K 2 CO 3 +CL-4 > K 2 CO 3 +CL-2 > K 2 CO 3 +CL-3 > K 2 CO 3 +CL-1 > K 2 CO 3 +FG-1 > K 2 CO 3 +FG-2 > K 2 CO 3 +FG-3 at 333.15 K. In case of promoters containing hydroxyl functional groups, the equilibrium partial pressure of CO 2 increased and the slope of the flux decreased. The effect was greater than those of promoters containing increased chain length. The mass transport rate of K 2 CO 3 +CL-4 solution was similar to that of the commercial MEA solution." @default.
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• W2750555588 date "2017-07-01" @default.
• W2750555588 modified "2023-09-26" @default.
• W2750555588 title "Promoter Characteristic Study on the K2CO3 Absorbents for CO2 Capture: Mass Transfer According to Functional Group and Chain Length of Promoter" @default.
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• W2750555588 doi "https://doi.org/10.1016/j.egypro.2017.03.1910" @default.
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