Hydroxyl Free-Radical-Assisted Synthesis of the ZSM-58 Zeolite Membrane for CO2/CO Separation

IF 3.9 3区 工程技术 Q2 ENGINEERING, CHEMICAL
Yifei Wang, Yingdong Yang, Yuxing Liu, Xinkang Zhang, Fengming Mo, Tao Huang, Yongjiang Shan, Ting Wu, Fei Zhang, Xiangshu Chen, Hidetoshi Kita
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引用次数: 0

Abstract

Capturing and recovering CO2 from steel industry gases is essential for environmental preservation since it lowers greenhouse gas emissions and raises CO concentrations. Because of its high selectivity, energy efficiency, and continuous operation, membrane separation technology has a lot of potential for CO2 separation. In the present work, a hydroxyl free radical (OH), generated by the addition of a small amount of sodium persulfate to the precursor solution, was introduced for the first time to induce the synthesis of the ZSM-58 crystals and membranes. Hydroxyl free radicals can promote the depolymerization and condensation of silica sources during the synthesis process, thereby accelerating nucleation and crystallization. Compared with the precursor solution without sodium persulfate, the synthesis time of the membrane can be reduced by 30%, the resulting zeolite membrane exhibits a CO2/CO separation factor of 16 and a high CO2 permeance of 1.5 × 10–7 mol m–2 s–1 Pa–1. In addition, CO2/N2 and CO2/CH4 separation performances were also tested to evaluate the membrane quality. The separation factor of the equimolar CO2/N2 and equimolar CO2/CH4 mixtures reached 28.6 and 248.3 at 298 K at 0.1 MPa, accompanying the corresponding CO2 permeance of 1.3 × 10–7 mol m–2 s–1 Pa–1 and 1.5 × 10–7 mol m–2 s–1 Pa–1, respectively. This research presents an innovative and effective method for fabricating zeolite membranes.

Abstract Image

羟基自由基辅助合成用于CO2/CO分离的ZSM-58沸石膜
从钢铁工业气体中捕获和回收二氧化碳对环境保护至关重要,因为它可以降低温室气体排放并提高CO浓度。膜分离技术具有高选择性、高能效、连续操作等优点,在CO2分离中具有很大的应用潜力。本文首次在前驱体溶液中加入少量过硫酸钠生成羟基自由基(•OH),诱导ZSM-58晶体和膜的合成。羟基自由基在合成过程中可以促进二氧化硅源的解聚缩聚,从而加速成核结晶。与不含过硫酸钠的前驱体溶液相比,膜的合成时间可缩短30%,所制得的沸石膜CO2/CO分离系数为16,CO2透过率为1.5 × 10-7 mol m-2 s-1 Pa-1。此外,还测试了CO2/N2和CO2/CH4的分离性能,以评价膜的质量。在298 K和0.1 MPa条件下,等摩尔CO2/N2和等摩尔CO2/CH4混合物的分离系数分别为28.6和248.3,对应的CO2渗透率分别为1.3 × 10-7 mol m-2 s-1 Pa-1和1.5 × 10-7 mol m-2 s-1 Pa-1。本研究提出了一种创新而有效的沸石膜制备方法。
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来源期刊
Industrial & Engineering Chemistry Research
Industrial & Engineering Chemistry Research 工程技术-工程:化工
CiteScore
7.40
自引率
7.10%
发文量
1467
审稿时长
2.8 months
期刊介绍: ndustrial & Engineering Chemistry, with variations in title and format, has been published since 1909 by the American Chemical Society. Industrial & Engineering Chemistry Research is a weekly publication that reports industrial and academic research in the broad fields of applied chemistry and chemical engineering with special focus on fundamentals, processes, and products.
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