Nucleophilic substituted NH2-MIL-125 (Ti)/polyvinylidene fluoride hollow fiber mixed matrix membranes for CO2/CH4 separation and CO2 permeation prediction via theoretical models
{"title":"Nucleophilic substituted NH2-MIL-125 (Ti)/polyvinylidene fluoride hollow fiber mixed matrix membranes for CO2/CH4 separation and CO2 permeation prediction via theoretical models","authors":"Sie Hao Ding , Pei Ching Oh , Hilmi Mukhtar , Asif Jamil","doi":"10.1016/j.memsci.2023.121746","DOIUrl":null,"url":null,"abstract":"<div><p><span><span>Improper degree of nucleophilic substitution on PVDF may reduce the crystallinity of the membrane and weaken </span>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 CO</span><sub>2</sub> permeation of MMMs would lead to incompatibility between theoretical results and experimental CO<sub>2</sub><span> 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% NH</span><sub>2</sub><span><span>-MIL-125 (Ti). The SEM, XPS, </span>XRD<span>, 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 CO</span></span><sub>2</sub>/CH<sub>4</sub> (50:50) mixed gas test, PVDF-4 showed the highest ideal and real selectivity, which also showed a good increment in CO<sub>2</sub> permeance compared to pure PVDF and 2 wt% NH<sub>2</sub>-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 CO<sub>2</sub> gas separation. After aging, PVDF-4 demonstrated a 23% reduction in CO<sub>2</sub> permeance, while also showing a 9% improvement in CO<sub>2</sub>/CH<sub>4</sub><span> ideal selectivity. The optimized membranes were then coated with PDMS to enhance its CO</span><sub>2</sub>/CH<sub>4</sub> (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 CO<sub>2</sub> permeation of PVDF HFMMMS developed. Modified Pal model demonstrated −3.68 AARE<em>%</em> towards PVDF-2 which has higher accuracy in the prediction of CO<sub>2</sub> permeation compared to other models in this study.</p></div>","PeriodicalId":368,"journal":{"name":"Journal of Membrane Science","volume":"681 ","pages":"Article 121746"},"PeriodicalIF":8.4000,"publicationDate":"2023-09-05","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"3","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Journal of Membrane Science","FirstCategoryId":"5","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S0376738823004027","RegionNum":1,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q1","JCRName":"ENGINEERING, CHEMICAL","Score":null,"Total":0}
引用次数: 3
Abstract
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.
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.