Analysis of new strategies integrating bipolar membrane electrodialysis and absorption systems in DAC applications

IF 10.2
Carbon Capture Science & Technology Pub Date : 2026-03-01 Epub Date: 2026-01-28 DOI:10.1016/j.ccst.2026.100579
Grazia Leonzio , Lei Xing , Nilay Shah
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引用次数: 0

Abstract

Solvent-based carbon dioxide capture technologies remain among the most promising capture strategies but conventional thermal regeneration methods are hindered by significant drawbacks. In this context, electrochemical regeneration, particularly through the bipolar membrane electrodialysis, offers potential advantages. However, its application is challenged by carbon dioxide bubble formation in the acid compartment, which increases energy requirements. To address this issue, a novel process is proposed in which carbonates in the rich solvent react with weak organic acids to release carbon dioxide while forming acid salts treated in the electrodialysis unit, enabling simultaneous the regeneration of both acid and solvent. To date, comprehensive economic and environmental assessments of such approaches are lacking in the state-of-the-art. This study aims to fill that gap by simulating both the conventional process and alternative pathways based on formic acid and a formic/acetic acid mixtures. Comprehensive material and energy balances are established, alongside detailed evaluations of capital and operating expenditures, and the environmental impact are conducted through life cycle assessment implemented in OpenLCA. Although the alternative processes exhibit higher energy consumption (2314 kWh/tonCO₂ vs 1907 kWh/tonCO₂ with formic acid, and 1943 kWh/tonCO₂ with the acid mixture), the conventional route remains more favorable in terms of both overall cost and environmental impact. Specifically, the total cost and climate change impact of the conventional capture process are estimated to be 480 $/tonCO₂ and –0.9593 kgCO₂eq/kgCO₂, respectively. On the other hand, the alternative process using formic acid and the mixture acid incur higher costs of 510 $/tonCO2 and 519 $/tonCO2 with corresponding environmental impacts of -0.9378 kgCO2eq/kgCO2 and 0.9238 kgCO2eq/kgCO2, respectively. Further optimization of the conventional process, particularly in mitigating carbon dioxide bubble formation, appears essential to fully exploit its economic and environmental potential.
双极膜电渗析和吸收系统在DAC应用中的新策略分析
溶剂型二氧化碳捕集技术仍然是最有前途的捕集策略之一,但传统的热再生方法受到显著缺陷的阻碍。在这种情况下,电化学再生,特别是通过双极膜电渗析,提供了潜在的优势。然而,它的应用受到了酸室中二氧化碳气泡形成的挑战,这增加了能量需求。为了解决这个问题,提出了一种新的工艺,在这种工艺中,富溶剂中的碳酸盐与弱有机酸反应释放二氧化碳,同时在电渗析装置中形成酸盐,使酸和溶剂同时再生。迄今为止,最先进的技术还没有对这种方法进行全面的经济和环境评价。本研究旨在通过模拟传统工艺和基于甲酸和甲酸/乙酸混合物的替代途径来填补这一空白。建立全面的材料和能源平衡,以及对资本和运营支出的详细评估,并通过OpenLCA实施的生命周期评估来进行环境影响。虽然替代工艺表现出更高的能耗(2314 kWh/tonCO₂,甲酸为1907 kWh/tonCO₂,酸混合物为1943 kWh/tonCO₂),但传统路线在总体成本和环境影响方面仍然更有利。具体来说,传统捕集过程的总成本和气候变化影响估计分别为480美元/吨二氧化碳和-0.9593千克二氧化碳当量/千克二氧化碳。另一方面,使用甲酸和混合酸的替代工艺成本较高,分别为510美元/吨co2和519美元/吨co2,相应的环境影响分别为-0.9378 kgCO2eq/kgCO2和0.9238 kgCO2eq/kgCO2。进一步优化常规工艺,特别是在减少二氧化碳气泡形成方面,似乎对充分利用其经济和环境潜力至关重要。
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