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Investigation of CO2 desorption kinetics in MDEA and MDEA+DEA rich amine solutions with thermo-gravimetric analysis method
International Journal of Greenhouse Gas Control ( IF 3.9 ) Pub Date : 2020-01-11 , DOI: 10.1016/j.ijggc.2019.102947
Kang Shunji , Shen Xizhou , Yang Wenze

In this paper, by means of thermo-gravimetric analysis(TGA), the desorption kinetics of CO2 absorbed in two kinds of rich amine solutions, MDEA (3.25mol/L) and MDEA+DEA(3.25mol/L-0.3mol/L), were investigated under different heating rates(2.5℃/min, 5℃/min, 10℃/min and 20℃/min). The thermal analysis kinetics was applied to analyze the TG-DTG curves of two rich amine solutions so as to research CO2 desorption kinetics. In addition, the CO2 desorption kinetics parameters have been calculated with model-free method Flynn-Wall-Ozawa (FWO) and model-fitting method Coats-Redfern (CR). The results indicated that CO2 desorption process could be divided into two stages. The CO2 and H2O were released with non-uniform speed in the first stage and MDEA or DEA with higher boiling points were evaporated in the second stage. For MDEA solution the average activation energy E was 50.36kJ/mol, the pre-exponential factor A was 1.68×107, and the most probable integral mechanism function was Gα=α3/2. For MDEA+DEA solution the average activation energy E was 59.68kJ/mol, the pre-exponential factor A was 2.22×107, and the most probable integral mechanism function was Gα=[(1+α)1/31]2. The technical feasibility of CO2 desorption performance in rich amine solutions with thermo-gravimetric analysis method was demonstrated.



中文翻译:

热重分析法研究MDEA和MDEA + DEA富胺溶液中CO 2的解吸动力学

本文通过热重分析(TGA),研究了MDEA(3.25mol / L)和MDEA + DEA(3.25mol / L-0.3mol / m)两种富胺溶液中CO 2的解吸动力学。L),在不同的加热速率(2.5℃/ min,5℃/ min,10℃/ min和20℃/ min)下进行研究。利用热分析动力学分析了两种富胺溶液的TG-DTG曲线,以研究CO 2的解吸动力学。另外,已经用无模型方法Flynn-Wall-Ozawa(FWO)和模型拟合方法Coats-Redfern(CR)计算了CO 2解吸动力学参数。结果表明,CO 2解吸过程可分为两个阶段。CO 2和H 2O在第一阶段以不均匀的速度释放,第二阶段蒸发具有较高沸点的MDEA或DEA。对于MDEA溶液,平均活化能E为50.36kJ / mol,指数前因子A为1.68×10 7,最可能的积分机制为Gα=α3/2。对于MDEA + DEA溶液,平均活化能E为59.68kJ / mol,指数前因子A为2.22×10 7,最可能的积分机制为Gα=[1个+α1个/3-1个]2。通过热重分析法证明了在富胺溶液中CO 2解吸性能的技术可行性。

更新日期:2020-01-13
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