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Computational study of MEA adsorption on hydroxylated Cr_2O_3 surfaces

机译:MEA在羟基化Cr_2O_3表面上吸附的计算研究

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Aqueous alkanolamine solvents are mostly frequently used for the removal of CO_2 from flue gas and natural gas. However, corrosion represents one of the major operational issue of this process. It is therefore essential to evaluate the stability of the protective Cr_2O_3 layer on stainless steels, when it is in contact with different species found in CO_2 capture processes, e.g. water, monoethanolamine (MEA), a well-known CO_2 capture amine, and the reaction products with CO_2 (carbamate, bicarbonate). The adsorption of MEA on the hydroxylated (0001)-Cr_2O_3 surface was investigated by periodic density functional theory (DFT). using both static and dynamics calculations [1]. Two different adsorption modes were investigated: by direct adsorption of MEA onto the surface and by substitution of a surface water molecule by MEA. Several MEA coverages were studied (from 0.25 to 1 monolayer), as well as temperature and solvation effects. The calculations show that MEA adsorption onto the surface with a density up to 2.37 MEA per nm~2 (0.5 ML) is exergonic at 298 K in an aqueous environment, while the substitution process was found to be endergonic at all coverages at temperatures of 298 K and above. We are currently using these DFT-data to develop parameters for a ReaxFF reactive force field [2], allowing us to model larger systems, including the most abundant species in the aqueous phase and to explore larger time scales.
机译:链烷醇胺水溶液最常用于从烟道气和天然气中去除CO_2。但是,腐蚀是该过程的主要操作问题之一。因此,当不锈钢中的Cr_2O_3保护层与CO_2捕集过程中发现的不同物种接触时,评估其保护性至关重要。水,单乙醇胺(MEA),一种著名的CO_2捕获胺以及与CO_2(氨基甲酸酯,碳酸氢盐)的反应产物。利用周期密度泛函理论(DFT)研究了MEA在羟基化(0001)-Cr_2O_3表面的吸附。同时使用静态和动态计算[1]。研究了两种不同的吸附模式:通过将MEA直接吸附到表面上以及通过用MEA代替表面水分子。研究了几种MEA覆盖率(从0.25到1单层),以及温度和溶剂化效果。计算表明,在水性环境中,在298 K上,MEA吸附到表面的MEA密度高达2.37 MEA / nm〜2(0.5 ML)是能带电的,而在298°C的温度下,覆盖范围内的吸附过程都是带负电的。 K及以上。我们目前正在使用这些DFT数据来开发ReaxFF反作用力场的参数[2],从而使我们能够为更大的系统建模,包括水相中最丰富的物种,并探索更大的时间尺度。

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