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基于功能化膜从高CO进料浓度中分离CO的响应曲面法建模与优化

RSM Modeling and Optimization of CO Separation from High CO Feed Concentration over Functionalized Membrane.

作者信息

Suhaimi Nadia Hartini, Yeong Yin Fong, Jusoh Norwahyu, Chew Thiam Leng, Bustam Mohammad Azmi, Mubashir Muhammad

机构信息

Department of Chemical Engineering, Universiti Teknologi PETRONAS, Bandar Seri Iskandar 32610, Malaysia.

CO2 Research Centre (CO2RES), R&D Building, Universiti Teknologi PETRONAS, Bandar Seri Iskandar 32610, Malaysia.

出版信息

Polymers (Basel). 2022 Mar 28;14(7):1371. doi: 10.3390/polym14071371.

Abstract

The challenges in developing high CO gas fields are governed by several factors such as reservoir condition, feed gas composition, operational pressure and temperature, and selection of appropriate technologies for bulk CO separation. Thus, in this work, we report an optimization study on the separation of CO from CH at high CO feed concentration over a functionalized mixed matrix membrane using a statistical tool, response surface methodology (RSM) statistical coupled with central composite design (CCD). The functionalized mixed matrix membrane containing NH-MIL-125 (Ti) and 6FDA-durene, fabricated in our previous study, was used to perform the separation performance under three operational parameters, namely, feed pressure, temperature, and CO feed concentration, ranging from 3.5-12.5 bar, 30.0-50.0 °C and 15-70 mol%, respectively. The CO permeability and CO/CH separation factor obtained from the experimental work were varied from 293.2-794.4 Barrer and 5.3-13.0, respectively. In addition, the optimum operational parameters were found at a feed pressure of 12.5 bar, a temperature of 34.7 °C, and a CO feed concentration of 70 mol%, which yielded the highest CO permeability of 609.3 Barrer and a CO/CH separation factor of 11.6. The average errors between the experimental data and data predicted by the model for CO permeability and CO/CH separation factor were 5.1% and 3.3%, respectively, confirming the validity of the proposed model. Overall, the findings of this work provide insights into the future utilization of NH-MIL-125 (Ti)/6FDA-based mixed matrix membranes in real natural gas purification applications.

摘要

开发高CO气田面临的挑战受多种因素制约,如储层条件、原料气组成、操作压力和温度,以及选择合适的大规模CO分离技术。因此,在本工作中,我们报告了一项使用统计工具响应面法(RSM)结合中心复合设计(CCD),在高CO进料浓度下从CH中分离CO的功能化混合基质膜的优化研究。使用我们先前研究中制备的含有NH-MIL-125(Ti)和6FDA-均四甲苯的功能化混合基质膜,在三个操作参数下进行分离性能测试,即进料压力、温度和CO进料浓度,范围分别为3.5 - 12.5 bar、30.0 - 50.0 °C和15 - 70 mol%。实验工作得到的CO渗透率和CO/CH分离因子分别在293.2 - 794.4 Barrer和5.3 - 13.0之间变化。此外,在进料压力为12.5 bar、温度为34.7 °C和CO进料浓度为70 mol%时发现了最佳操作参数,此时CO渗透率最高为609.3 Barrer,CO/CH分离因子为11.6。CO渗透率和CO/CH分离因子的实验数据与模型预测数据之间的平均误差分别为5.1%和3.3%,证实了所提出模型的有效性。总体而言,本工作的研究结果为NH-MIL-125(Ti)/6FDA基混合基质膜在实际天然气净化应用中的未来利用提供了见解。

https://cdn.ncbi.nlm.nih.gov/pmc/blobs/203a/9003211/705f1513e00e/polymers-14-01371-g001a.jpg

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