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Corrosion Behavior of Carbon Steel in CO_2 Saturated Amine and Room Temperature Ionic Liquid Solutions

机译:碳钢在CO_2饱和胺和室温离子液体溶液中的腐蚀行为

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The aggressive corrosive behaviour of conventional amines is one of main barriers against large-scale commercial amine based CO_2 capture processes. This work shows a recent investigation on the corrosion behaviour of carbon steel CS1018 in three CO_2 absorbents classes. The first class focused on the classical amine solutions; monoethnaolamine (MEA), diethanolamine (DEA) and methyl diethanolamine (MDEA). The second-class included the use of piperazine (PZ) promoter mixed with the same amines used in the first class making them advanced amine CO_2 absorbents. The third class includes the novel mixtures of classical amines and room temperature ionic liquids (RTIL). Imidazolium-based ILs with different anions namely; 1-butyl-3-methyl imidazolium tetrafluoroborate ([C_4MIM][BF_4]), 1-butyl-3methyl imidazolium trifluoromethanesulfonate ([C_4MIM][Otf]), tributyl(methyl)phosphonium acetate ([P4441][Ac]) and choline acetate ([Ch][Ac]) were used in the experiments. Electrochemical polarization techniques were used to determine the absorbent corrosiveness via corrosion rate and polarization behaviour experiments. The process parameters of interest were CO_2 loading and test temperature. In single amine systems, the corrosivity order of CO_2 saturated amines was governed mainly by their characteristic CO2 absorption capacity. Corrosivity order ranking of classical amines at 40 °C was obtained as MDEA > MEA > DEA and the ranking changed to MEA > DEA > MDEA at 80 °C. Piperazine activated amines resulted in lower corrosion rates and higher CO_2 absorption capacity compared to single classical amines. At CO_2 saturation and 80 °C corrosivity ranking was MEA > MEA/MDEA > MEA/PZ > MEA/MDEA/PZ > MDEA > MDEA/PZ. The results of MEA/RTIL mixtures showed that the partial replacement of aqueous phase in MEA solution by hydrophilic RTIL reduced corrosion rates by 40 to 70% compared to aqueous MEA solution. MEA/[P4441][Ac] and MEA/[Ch][Ac] showed promising corrosion inhibition performance compared to imidazolium-based RTILs with corrosivity ranking of MEA/[P4441][Ac] > MEA/[Ch][Ac] > MEA/[C_4MIM][BF_4] at 25 °C and CO_2 saturation condition.
机译:常规胺的腐蚀性行为是阻止大规模基于胺的商业CO_2捕集工艺的主要障碍之一。这项工作显示了对碳钢CS1018在三种CO_2吸收剂类别中的腐蚀行为的最新研究。第一类集中在经典的胺溶液上。单乙醇胺(MEA),二乙醇胺(DEA)和甲基二乙醇胺(MDEA)。第二类包括将哌嗪(PZ)促进剂与第一类中使用的相同胺混合使用,从而使它们成为高级胺CO_2吸收剂。第三类包括经典胺和室温离子液体(RTIL)的新型混合物。具有不同阴离子的咪唑基ILs; 1-丁基-3-甲基咪唑四氟硼酸盐([C_4MIM] [BF_4]),1-丁基-3甲基咪唑三氟甲烷磺酸盐([C_4MIM] [Otf]),三丁基(甲基)乙酸acetate([P4441] [Ac])和胆碱在实验中使用了乙酸盐([Ch] [Ac])。电化学极化技术用于通过腐蚀速率和极化行为实验确定吸收剂的腐蚀性。感兴趣的工艺参数是CO_2负载和测试温度。在单胺体系中,CO_2饱和胺的腐蚀阶数主要由其特征性的CO2吸收能力决定。当MDEA> MEA> DEA时,获得了传统胺在40°C时的腐蚀性顺序排名,在80°C时该排名更改为MEA> DEA> MDEA。与单一的传统胺相比,哌嗪活化的胺导致较低的腐蚀速率和较高的CO_2吸收能力。在CO_2饱和和80°C时,腐蚀等级为MEA> MEA / MDEA> MEA / PZ> MEA / MDEA / PZ> MDEA> MDEA / PZ。 MEA / RTIL混合物的结果表明,与MEA水溶液相比,亲水性RTIL部分替代MEA溶液中的水相可将腐蚀率降低40%至70%。与基于咪唑鎓的RTIL相比,MEA / [P4441] [Ac]和MEA / [Ch] [Ac]表现出良好的缓蚀性能,其腐蚀等级为MEA / [P4441] [Ac]> MEA / [Ch] [Ac]> MEA / [C_4MIM] [BF_4]在25°C和CO_2饱和条件下。

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