Bicarbonate-Carbonate Selectivity through Nanofiltration for Direct Air Capture of Carbon Dioxide

IF 7.4 Q1 ENGINEERING, ENVIRONMENTAL ACS ES&T engineering Pub Date : 2024-06-06 DOI:10.1021/acsestengg.4c0015010.1021/acsestengg.4c00150
Anatoly Rinberg*,  and , Michael J. Aziz, 
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Abstract

Direct air capture (DAC) of carbon dioxide is one approach among many proposed that is capable of offsetting hard-to-avoid emissions. In previous work, we developed the alkalinity concentration swing (ACS) method, which is driven through concentrating an alkaline solution that has been loaded with atmospheric CO2 by desalination technologies, such as reverse osmosis or capacitive deionization. Though the ACS is promising in terms of energy usage and implementation, its absorption rate and water requirements are infeasible for a large-scale DAC process. Here, we propose an improvement on the ACS, the bicarbonate-enriched alkalinity concentration swing (BE-ACS), which selects bicarbonate ions from a stream of aqueous alkaline solution that has absorbed atmospheric CO2. The bicarbonate-rich stream is then concentrated, which greatly increases its CO2 partial pressure, and then CO2 is extracted from solution. We experimentally investigate the use of pressure-driven nanofiltration (NF) membrane-based separation to select bicarbonate ions over carbonate ions. We screen commercial membranes and select one high-performance membrane for detailed studies, quantifying its bicarbonate-carbonate selectivity factor and bicarbonate-passage factor. Feed pH, the combined concentration of aqueous CO2, bicarbonate, and carbonate species (or dissolved inorganic carbon), alkalinity, and permeation flux are systematically varied to study NF separation properties. We find that the selectivity factor, which exceeds 30 times in certain regimes, increases with higher feed pH and higher alkalinity. The performance metrics of the selected NF membrane are input into a theoretical BE-ACS cycle analysis, and the required energy input and cycle capacity output are evaluated. Ideal cycle energy is found to be as low as around 250 kJ/mol, with opportunities identified for further decreases through process engineering and forward osmosis energy recovery.

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通过纳米过滤实现碳酸氢盐-碳酸氢盐选择性,直接在空气中捕获二氧化碳
二氧化碳的直接空气捕集(DAC)是众多已提出的能够抵消难以避免的排放的方法之一。在之前的工作中,我们开发了碱度浓缩摆动(ACS)方法,该方法通过反渗透或电容去离子等脱盐技术,浓缩含有大气二氧化碳的碱性溶液。虽然 ACS 在能源使用和实施方面很有前景,但其吸收率和对水的要求对于大规模 DAC 工艺来说并不可行。在这里,我们提出了一种 ACS 的改进方案,即富含碳酸氢盐的碱度浓度摆动(BE-ACS),它可以从吸收了大气中二氧化碳的碱性水溶液流中选择碳酸氢盐离子。然后浓缩富含碳酸氢盐的水流,大大提高其二氧化碳分压,然后从溶液中提取二氧化碳。我们通过实验研究了如何利用压力驱动的纳滤(NF)膜分离来选择碳酸氢根离子而不是碳酸根离子。我们筛选了商用膜,并选择了一种高性能膜进行详细研究,量化了其碳酸氢盐-碳酸氢盐选择因子和碳酸氢盐通过因子。进料 pH 值、二氧化碳、碳酸氢盐和碳酸盐物种(或溶解的无机碳)的综合浓度、碱度和渗透通量被系统地改变,以研究 NF 的分离特性。我们发现,进料 pH 值和碱度越高,选择性系数越大,在某些情况下超过 30 倍。将所选 NF 膜的性能指标输入 BE-ACS 循环理论分析,并评估所需的能量输入和循环能力输出。理想的循环能量可低至约 250 kJ/mol,并有机会通过工艺工程和正渗透能量回收进一步降低。
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ACS ES&T engineering
ACS ES&T engineering ENGINEERING, ENVIRONMENTAL-
CiteScore
8.50
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0.00%
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0
期刊介绍: ACS ES&T Engineering publishes impactful research and review articles across all realms of environmental technology and engineering, employing a rigorous peer-review process. As a specialized journal, it aims to provide an international platform for research and innovation, inviting contributions on materials technologies, processes, data analytics, and engineering systems that can effectively manage, protect, and remediate air, water, and soil quality, as well as treat wastes and recover resources. The journal encourages research that supports informed decision-making within complex engineered systems and is grounded in mechanistic science and analytics, describing intricate environmental engineering systems. It considers papers presenting novel advancements, spanning from laboratory discovery to field-based application. However, case or demonstration studies lacking significant scientific advancements and technological innovations are not within its scope. Contributions containing experimental and/or theoretical methods, rooted in engineering principles and integrated with knowledge from other disciplines, are welcomed.
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