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对燃烧后碳捕集中一乙醇胺和 N-甲基-4-吗啉混合溶剂的物理性质、动力学、吸收能力和再生热负荷进行深入分析。

Insightful analysis of physical properties, kinetics, absorption capacity, and regeneration heat duty of monoethanolamine and N-methyl-4-piperidinol blended solvent in post-combustion carbon capture.

机构信息

Petrochemistry and Polymer Science Program, Faculty of Science, Chulalongkorn University, Pathumwan, Bangkok, 10330, Thailand.

Department of Chemical Engineering, Faculty of Engineering, Mahidol University, Nakhon Pathom, 73170, Thailand.

出版信息

Environ Sci Pollut Res Int. 2024 Aug;31(40):52868-52885. doi: 10.1007/s11356-024-34606-x. Epub 2024 Aug 21.

DOI:10.1007/s11356-024-34606-x
PMID:39164560
Abstract

In this study, the high potential tertiary N-methyl-4-piperidinol or MPDL (0.25-1.00 M) was blended with 5 M monoethanolamine (MEA) to formulate 5.25-6.00 M MEA-MPDL solvent and compare with the benchmark 5 M MEA. It was found that the density and the Henry's constant slightly decreased, while the viscosity increased as the MPDL concentration in the blend increased. Even though the equilibrium CO-loaded viscosity considerably increased (by 34.3-40.2%) as the MPDL content increased, it was still in a great operating region of less than 10 mPa.s. Experimental overall reaction kinetics constant ( ) was well corresponding with the zwitterion mechanism of MEA and the base-catalyze hydration mechanism of MPDL based absorption kinetics model, with %AAD of 0.56%. Interestingly, an addition of MPDL into 5 M MEA slightly enhanced (1.2-3.3% increment) and considerably favored absorption capacity (13-31% elevation), and regeneration heat duty (28-47% reduction), respecting 5 M MEA. The proposed strategic blending can maintain the overall solvent reactivity at the same level of the benchmark, while obviously increase the absorption capacity and largely reduce the regeneration heat duty. This highly favors a solvent upgrading for the existing 5 M MEA based CO capture plant. According to the recent data, 5 M MEA + 1.00 M MPDL was suggested. Since the blend was formulated at high concentration, its corrosiveness should also be considered.

摘要

在这项研究中,高浓度的叔胺 N-甲基-4-哌啶醇(MPDL,0.25-1.00 M)与 5 M 单乙醇胺(MEA)混合,制成 5.25-6.00 M 的 MEA-MPDL 溶剂,并与基准 5 M MEA 进行比较。结果发现,随着混合物中 MPDL 浓度的增加,密度和亨利常数略有降低,而粘度增加。尽管平衡 CO 负载粘度随着 MPDL 含量的增加而显著增加(增加 34.3-40.2%),但其仍处于小于 10 mPa.s 的良好操作区域内。实验总反应动力学常数( )与 MEA 的两性离子机制和 MPDL 的基催化水合机制的吸收动力学模型很好地对应,平均绝对偏差(AAD)为 0.56%。有趣的是,向 5 M MEA 中添加 MPDL 会略微提高(增加 1.2-3.3%),并显著有利于吸收能力(提高 13-31%)和再生热负荷(降低 28-47%),优于 5 M MEA。所提出的战略混合可以在保持基准溶剂整体反应性相同的水平下,明显提高吸收能力,并大大降低再生热负荷。这非常有利于现有 5 M MEA 基 CO 捕集装置的溶剂升级。根据最近的数据,建议使用 5 M MEA+1.00 M MPDL。由于混合液是在高浓度下配制的,因此还应考虑其腐蚀性。

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