膜
渗透
分离过程
体积流量
阶段(地层学)
分离(统计)
膜技术
色谱法
过程(计算)
工作(物理)
单级
分数(化学)
材料科学
化学
分析化学(期刊)
计算机科学
机械
工程类
机械工程
物理
古生物学
生物化学
机器学习
操作系统
航空航天工程
生物
作者
Bingcheng Liu,Xuan Yang,Ting Wang,Mengmeng Zhang,Pen‐Chi Chiang
标识
DOI:10.4209/aaqr.2019.10.0519
摘要
In this work, a three-stage membrane process for CO2 separation was proposed and optimized. The results of this study revealed that the proposed technology is a suitable process for the CO2 separation at higher concentrations. In addition, MATLAB was used to simulate and obtain the optimal operational parameters for a three-stage membrane process. A partial cycle was established, and the CO2 was recovered from the permeation side of the second-stage membrane, which enhanced the purity of the CO2 gas stream. The results of this study indicated that when the CO2 concentration was higher than 50% at a flow rate of 100000 Nm3 d–1, CO2 separation could be achieved under optimal operating conditions. Under conditions where the membrane areas were 2400, 3800, and 1800 m2 for the first-, second-, and third-stage membranes, respectively, and where the operational pressure at the first- and third stage membranes were 3.0 and 2.5 MPa, respectively, the CO2 separation fraction was higher than 90%, and the CH4 loss rate was less than 5%. The results of this study indicate a high potential for practical application.
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