首页> 外文期刊>Chemical Engineering Science >CO2 absorption into aqueous amine blended solutions containing monoethanolamine (MEA), N,N-dimethylethanolamine (DMEA), N,N-diethylethanolamine (DEEA) and 2-amino-2-methyl-1-propanol (AMP) for post-combustion capture processes
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CO2 absorption into aqueous amine blended solutions containing monoethanolamine (MEA), N,N-dimethylethanolamine (DMEA), N,N-diethylethanolamine (DEEA) and 2-amino-2-methyl-1-propanol (AMP) for post-combustion capture processes

机译:CO2吸收到胺混合溶液中,该溶液包含一乙醇胺(MEA),N,N-二甲基乙醇胺(DMEA),N,N-二乙基乙醇胺(DEEA)和2-氨基-2-甲基-1-丙醇(AMP),用于燃烧后捕集流程

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Presently monoethanolamine (MEA) remains the industrial standard solvent for CO2 capture processes. Operating issues relating to corrosion and degradation of MEA at high temperatures and concentrations, and in the presence of oxygen, in a traditional PCC process, have introduced the requisite for higher quality and costly stainless steels in the construction of capture equipment and the use of oxygen scavengers and corrosion inhibitors. While capture processes employing MEA have improved significantly in recent Limes there is a continued attraction towards alternative solvents systems which offer even more improvements. This movement includes aqueous amine blends which are gaining momentum as new generation solvents for CO2 capture processes. Given the exhaustive array of amines available to date endless opportunities exist to tune and tailor a solvent to deliver specific performance and physical properties in line with a desired capture process. The current work is focussed on the rationalisation of CO2 absorption behaviour in a series of aqueous amine blends incorporating monoethanolamine, N,N-dimethylethanolamine (DMEA), N,N-diethylethanolamine (DEEA) and 2-amino-2-methyl-l-propanol (AMP) as solvent components. Mass transfer/kinetic measurements have been performed using a wetted wall column (WWC) contactor at 40 degrees C for a series of blends in which the blend properties including amine concentration, blend ratio, and CO2 loadings from 0.0-0.4 (moles CO2/total moles amine) were systematically varied and assessed. Equilibrium CO2 solubility in each of the blends has been estimated using a software tool developed in Matlab for the prediction of vapour liquid equilibrium using a combination of the known chemical equilibrium reactions and constants for the individual amine components which have been combined into a blend.
机译:目前,单乙醇胺(MEA)仍然是用于CO2捕集工艺的工业标准溶剂。在传统的PCC工艺中,在高温和高浓度下以及在有氧气的情况下,与MEA的腐蚀和降解有关的操作问题为捕获设备的构造和氧气的使用引入了更高质量和成本的不锈钢的要求清除剂和腐蚀抑制剂。尽管在最近的Limes中采用MEA的捕集工艺已有显着改善,但对提供更多改进的替代溶剂系统的吸引力仍在继续。这一趋势包括胺水溶液混合物,这种混合物作为用于CO2捕集工艺的新一代溶剂正得到发展。鉴于迄今为止可用的胺种类繁多,存在无限的机会来调整和定制溶剂,以根据所需的捕获过程提供特定的性能和物理性质。当前的工作集中在合理化一系列含水胺共混物中的二氧化碳吸收行为,这些共混物包含单乙醇胺,N,N-二甲基乙醇胺(DMEA),N,N-二乙基乙醇胺(DEEA)和2-氨基-2-甲基-1-丙醇(AMP)作为溶剂成分。已经使用湿式壁柱(WWC)接触器在40°C下进行了一系列物质的传质/动力学测量,其中一系列的共混物特性包括胺浓度,共混比和CO2负载量为0.0-0.4(摩尔CO2 /总摩尔胺)进行系统地更改和评估。已使用Matlab开发的软件工具估算了每种混合物中的平衡CO2溶解度,该软件工具使用已知化学平衡反应和已合并到混合物中的单个胺成分的常数的组合来预测汽液平衡。

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