Techno-economic analysis on temperature vacuum swing adsorption system integrated with pre-dehumidification for direct air capture

被引:7
作者
Ji, Y. [1 ]
Liu, W. [1 ]
Yong, J. Y. [1 ]
Zhang, X. J. [1 ]
Jiang, L. [1 ]
机构
[1] Zhejiang Univ, Inst Refrigerat & Cryogen, Key Lab Refrigerat & Cryogen Technol Zhejiang Prov, Hangzhou 310027, Peoples R China
来源
CARBON CAPTURE SCIENCE & TECHNOLOGY | 2024年 / 12卷
基金
中国国家自然科学基金;
关键词
Direct air capture; Adsorption; Dehumidification; LCOD; CARBON CAPTURE; FLUE-GAS; CO2; PERFORMANCE; SORBENT;
D O I
10.1016/j.ccst.2024.100199
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
In addressing the practical application of direct air capture (DAC) technology to achieve net -zero greenhouse gas emissions by 2050, the intricate climatic environment presents a significant challenge in selecting capture adsorbents with excellent adsorption performance, high moisture tolerance and stability. This study seeks to assess the efficacy of a temperature vacuum swing adsorption (TVSA) system for DAC, integrated with two distinct pre-dehumidification methods: condensation dehumidification and solid desiccant dehumidification. Initially, to balance enhanced adsorption capacity with the energy required for regeneration in the presence of water vapor, the optimal techno-economic performance is achieved at a 40 % relative humidity (RH). This corresponds to 15.49 GJ/t of heat consumption and 194.08 $/tonCO2 of CO2 the levelized cost of DAC (LCOD). Following dynamic simulation, the dehumidification system effectively controlled the outlet RH. Furthermore, economic analysis indicates that reducing environmental air to 40 % RH is more suitable and cost-efficient for both integrated systems. The optimal LCODs are 200.29 $/tonCO2 for the solid desiccant dehumidification system and 197.16 $/tonCO2 for the condensation dehumidification system, which could effectively save 7.09 % and 5.61 % of LCOD, respectively, compared to systems without a dehumidification process.
引用
收藏
页数:13
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