醇胺溶液CO2吸收过程反应机制OA
Reaction mechanisms during CO2 absorption in ethanolamine solutions
[目的]当前醇胺法CO2捕集存在能耗与成本较高的缺点,解决这一问题的主要方法是协同不同类型醇胺的吸收、解吸优势构建复合胺溶液.羟乙基乙二胺(AEEA)和N-甲基二乙醇胺(MDEA)是2种常用主吸收剂,其调配需要准确掌握CO2吸收规律,包括CO2负载量、产物离子浓度分布规律、反应级数等.目前对其吸收规律认识尚不足,相关反应参数缺乏,限制了工艺模型预测准确性.[方法]研究AEEA和MDEA溶液CO2吸收过程,厘清其反应机理,并基于pH值法构建产物离子浓度分布模型,回归2种胺液的反应级数,确定反应速率模型.[结果和结论]同一浓度AEEA溶液吸收容量和吸收速率均高于MDEA溶液.AEEA溶液CO2吸收过程呈现出两阶段特征,接近于二级反应.AEEA与CO2反应生成两性中间离子(R1R2NH+COO-)是吸收过程的初始控制步骤,而其吸收后期为传质-反应共同控制阶段.MDEA溶液CO2吸收过程是碱催化水合过程,反应速率与MDEA浓度线性相关,为一级反应.基于所得新认识和模型,为碳捕集工艺中溶剂浓度、溶剂停留时间,溶剂循环量、塔器设计优化等提供理论指导.
[Objective]Presently,CO2 capture technology based on the ethanolamine solutions suffers from drawbacks such as high energy consumption and elevated costs.A primary method to address these challenges is to construct blen-ded amine solutions by synergistically integrating the absorption and desorption advantages of different types of ethano-lamines.Hydroxyethyl ethylenediamine(AEEA)and N-methyldiethanolamine(MDEA)represent two major commonly used absorbents,and their blending necessitates an accurate understanding of their CO2 absorption patterns,including CO2 loading capacity,the ion-concentration distribution patterns of reaction products,and reaction orders.Currently,their absorption mechanisms remain poorly understood,and there is a lack of relevant reaction parameters,jointly under-mining the prediction accuracy of process models.[Methods]By investigating the CO2 absorption processes of AEEA and MDEA solutions,this study clarified the reaction mechanisms of both solutions.Furthermore,it established ion con-centration distribution models of the reaction products based on pH values,determined the reaction orders through re-gression analysis,and developed the reaction rate models of both solutions.[Results and Conclusions]The results in-dicate that,under the same concentration,the AEEA solution exhibited higher CO2 absorption capacity and rates com-pared to the MDEA solution.The AEEA solution presented a two-stage CO2 absorption process,with reaction orders ap-proaching 2.Initially,the CO2 absorption process in the AEEA solution was controlled by the formation of zwitterionic intermediates(R1R2NH+COO-)from AEEA-CO2 reactions.In the late stage,this process was jointly governed by mass transfer and reactions.In contrast,the CO2 absorption in the MDEA solution was identified as a base-catalyzed hydra-tion process,with the reaction rate showing a linear correlation with the MDEA concentration and the reaction order de-termined at 1.The novel insights and models of this study provide theoretical guidance for the optimization of the con-centration,retention time,and circulation rate of solvents,along with column design,in carbon capture technique.
滕卫卫;吴燕;樊玉新;廖涛;王梓丞;于徽;李梦;许孝玲
新疆油田公司,新疆克拉玛依 834000新疆油田公司采油工艺研究院,新疆克拉玛依 834000新疆油田公司采油工艺研究院,新疆克拉玛依 834000新疆油田公司采油工艺研究院,新疆克拉玛依 834000新疆油田公司采油工艺研究院,新疆克拉玛依 834000新疆油田公司采油工艺研究院,新疆克拉玛依 834000中国石油大学(北京)克拉玛依校区工学院,新疆克拉玛依34000中国石油大学(北京)克拉玛依校区工学院,新疆克拉玛依34000
能源科技
CO2捕集AEEAMDEA离子浓度反应级数
CO2 capturehydroxyethyl ethylenediamine(AEEA)N-methyldiethanolamine(MDEA)ion concentrationreaction order
《煤田地质与勘探》 2026 (1)
71-79,9
新疆维吾尔自治区"一事一议"战略人才引进项目(XQZX20240054)
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