沸石
化学
膜
催化作用
ZSM-5型
分离(统计)
化学工程
有机化学
计算机科学
生物化学
机器学习
工程类
作者
Yifei Wang,Yingdong Yang,Yuxing Liu,Xinkang Zhang,Fangfang Mo,Tao Huang,Yongjiang Shan,Ting Wu,Fei Zhang,Xiangshu Chen,Hidetoshi Kita
标识
DOI:10.1021/acs.iecr.5c00003
摘要
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.
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