利用 MOF-801/Pebax 混合基质膜同时去除二氧化碳和水蒸气:分子模拟和实验研究

Mahdi Ahmadi , Saravanan Janakiram , Sadiye Velioğlu , Arne Lindbråthen , Brian Arthur Grimes , Magne Hillestad , Liyuan Deng
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摘要

脱水和去除二氧化碳是两个重要的气体分离过程。一种能同时降低天然气和发电厂烟道气等潮湿气流中水蒸气和二氧化碳含量的高效膜可推动这些工艺的发展。在本研究中,合成了一种平均粒径为 120 nm 的水收集金属有机框架 MOF-801,然后将其分散在 Pebax 基质中以制造混合基质膜 (MMM)。研究人员评估了 MOF-801 作为 MMM 中填料的潜力,用于从 CO2/N2 和 CO2/CH4 混合气体流中分离水和二氧化碳。与纯净的 Pebax 膜相比,在 10 巴 CO2/CH4 潮湿进料成分条件下,添加 20 wt.% MOF 的 MMM 的透水性提高了 70%。此外,还获得了相当高的 CO2/N2 分离系数(108)和二氧化碳渗透率(270 巴),在干燥和潮湿状态下均超过了罗伯逊上限。分子模拟研究揭示了 MOF 晶格中的吸附位点以及与气体的有利相互作用。有趣的是,在靠近 Zr 原子的地方观察到了气体成分之间的竞争,而这正是二氧化碳和水的有利吸附位点。研究发现,竞争吸附是 MOF-801 中 CO2 和 H2O 选择性传输的主要传输机制,这揭示了 MOF-801 在 MMM 中用于在潮湿和干燥条件下分离 CO2 和水蒸气的作用。
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Enabling simultaneous CO2 and water vapor removal by MOF-801/Pebax mixed matrix membranes: Molecular simulation and experimental study
Dehydration and CO2 removal are two important gas separation processes. An efficient membrane enabling simultaneous reduction of water vapor and CO2 levels from humid gas streams, such as natural gas and power plant flue gas, may advance these processes. In this study, a water-harvesting metal-organic framework, MOF-801, was synthesized with an average particle size of 120 nm, which was then dispersed in a Pebax matrix to fabricate mixed matrix membranes (MMMs). The potential of the MOF-801 as a filler in MMMs was evaluated for water and CO2 separation from CO2/N2 and CO2/CH4 mixed gas streams. Compared with the neat Pebax membrane, 70% enhancement in the water permeability was achieved for an MMM of 20 wt.% MOF loading at 10 bar with a humid feed composition of CO2/CH4. A considerable CO2/N2 separation factor (108) and CO2 permeability (270 Barrer) were also obtained, exceeding the Robeson upper bound at both dry and humid states. A molecular simulation study was performed to reveal the adsorption sites in the MOF lattice and favorable interactions with gases. Interestingly, competition between gas components close to the Zr atom was observed, which is the favorable site for both CO2 and water. Competitive adsorption was found to be the dominating transport mechanism for the selective transport of CO2 and H2O in MOF-801, revealing the role of MOF-801 in MMMs for CO2 and water vapor separation under both humid and dry conditions.
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