亲核取代NH2-MIL-125 (Ti)/聚偏氟乙烯中空纤维混合基质膜用于CO2/CH4分离和CO2渗透的理论模型预测

IF 8.4 1区 工程技术 Q1 ENGINEERING, CHEMICAL
Sie Hao Ding , Pei Ching Oh , Hilmi Mukhtar , Asif Jamil
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引用次数: 3

摘要

聚偏氟乙烯上亲核取代程度不当会降低膜的结晶度,削弱膜的力学性能。随后,膜结晶度的下降可能会导致膜性能的下降,特别是在气体分离方面,这是不吉利的。此外,由于预测MMMs中CO2渗透的模型不合适,导致理论结果与实验CO2渗透数据不一致,从而影响膜分离系统的设计。在目前的工作中,使用3种不同浓度的氨溶液(25、30和35% v/v)来修饰含有2 wt% NH2-MIL-125 (Ti)的PVDF。通过SEM、XPS、XRD、接触角和力学分析分别考察了其结构变化、在PVDF上取代度、结晶度、亲水性和机械强度的变化。在单一气体和CO2/CH4(50:50)混合气体试验中,PVDF-4表现出最高的理想选择性和实际选择性,与纯PVDF和2 wt% NH2-MIL-125 (Ti)/PVDF HFMMM相比,其CO2渗透率也有较好的提高。因此,需要适当的氨溶液改性条件来提高膜的性能,同时又不严重影响膜的稳定性,保证更好的CO2气体分离。老化后,PVDF-4的CO2透过率降低了23%,同时CO2/CH4的理想选择性也提高了9%。然后将优化后的膜涂覆PDMS,以提高其CO2/CH4(50:50)的混合气体分离性能。采用Maxwell、Bruggeman、Pal、Lewis-Nielson和Bottcher模型以及改进的Pal模型对所研制的PVDF HFMMMS的CO2渗透率进行了估算。修正Pal模型对PVDF-2的AARE值为−3.68 %,与本研究其他模型相比,PVDF-2对CO2渗透的预测精度更高。
本文章由计算机程序翻译,如有差异,请以英文原文为准。

Nucleophilic substituted NH2-MIL-125 (Ti)/polyvinylidene fluoride hollow fiber mixed matrix membranes for CO2/CH4 separation and CO2 permeation prediction via theoretical models

Nucleophilic substituted NH2-MIL-125 (Ti)/polyvinylidene fluoride hollow fiber mixed matrix membranes for CO2/CH4 separation and CO2 permeation prediction via theoretical models

Improper degree of nucleophilic substitution on PVDF may reduce the crystallinity of the membrane and weaken mechanical properties. Subsequently, the drop in membrane crystallinity might cause a decline in membrane performance, particularly in gas separation, which was unpropitious. Also, inappropriate models for predicting CO2 permeation of MMMs would lead to incompatibility between theoretical results and experimental CO2 permeation data, subsequently affecting the design of the membrane separation system. In the current work, ammonia solutions with 3 different concentrations (25, 30, and 35% v/v) were used to modify PVDF incorporated with 2 wt% NH2-MIL-125 (Ti). The SEM, XPS, XRD, contact angle, and mechanical analyses were performed to investigate the structural changes, degree of substitution on PVDF, crystallinity, hydrophilicity, and changes in mechanical strength, respectively. In single and CO2/CH4 (50:50) mixed gas test, PVDF-4 showed the highest ideal and real selectivity, which also showed a good increment in CO2 permeance compared to pure PVDF and 2 wt% NH2-MIL-125 (Ti)/PVDF HFMMM. Therefore, appropriate ammonia solution modification conditions are required to enhance the membrane properties without severely compromising the stability of the membrane and ensuring better CO2 gas separation. After aging, PVDF-4 demonstrated a 23% reduction in CO2 permeance, while also showing a 9% improvement in CO2/CH4 ideal selectivity. The optimized membranes were then coated with PDMS to enhance its CO2/CH4 (50:50) mixed gas separation performance. The basic Maxwell, Bruggeman, Pal, Lewis–Nielson, and Bottcher model, along with modified Pal model, were used to estimate the CO2 permeation of PVDF HFMMMS developed. Modified Pal model demonstrated −3.68 AARE% towards PVDF-2 which has higher accuracy in the prediction of CO2 permeation compared to other models in this study.

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来源期刊
Journal of Membrane Science
Journal of Membrane Science 工程技术-高分子科学
CiteScore
17.10
自引率
17.90%
发文量
1031
审稿时长
2.5 months
期刊介绍: The Journal of Membrane Science is a publication that focuses on membrane systems and is aimed at academic and industrial chemists, chemical engineers, materials scientists, and membranologists. It publishes original research and reviews on various aspects of membrane transport, membrane formation/structure, fouling, module/process design, and processes/applications. The journal primarily focuses on the structure, function, and performance of non-biological membranes but also includes papers that relate to biological membranes. The Journal of Membrane Science publishes Full Text Papers, State-of-the-Art Reviews, Letters to the Editor, and Perspectives.
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