Full Length ArticleEnhancing TFC membrane permeability by incorporating single-layer MSN into polyamide rejection layer
Graphical abstract
Introduction
Reverse osmosis (RO) process, which just needs about one-tenth energy consumption than distillation and evaporation processes in purifying equivalent amount of wastewater, is gradually becoming a currently mainstream technique for both brackish and sea water desalination [1], [2], [3]. However, the development of RO technique has encountered bottleneck, due to the contradictory between membrane selectivity and permeability [4]. Therefore, how to significantly enhance the membrane permeability without decreasing its separating property has become the key point to break the bottleneck.
Recent years, lots of efforts have been payed to improve RO membrane permeability and avoid damage to the membrane selectivity. There are some studies tried to improve the membrane permeability through enhancing the membrane hydrophilicity by incorporating large amounts of hydrophilic additives into polyamide rejection layer. Yi Li et al. successfully improved the permeability of TFC RO membrane by adding hydrophilic carbon dots into polyamide rejection layer [5]. Lin Zhao et al. incorporated o-aminobenzoic acid–triethylamine, a hydrophilic additive, into the rejection layer of TFC RO membrane and successfully increased the membrane water flux [6]. However, these types of improvement approaches were too limited to significantly enhance the membrane permeability. Meanwhile, several researchers mimicked the structure of biological membrane to incorporate varied “water channels” into polyamide rejection layer to improve membrane permeability. Aquaporins as a kind of water channel proteins have been widely used to fabricate high-flux RO membranes. Yang Zhao et al. successfully introduced Aquaporin Z-containing proteoliposomes into polyamide rejection layer improving the membrane permeability by about 40% [7]. Whereas, the protein activity is difficult to remain for long, due to the high salinity and high pressure in practical applications. Carbon nanotubes as a kind of 1 D inorganic water channel material have also been extensively applied in the fabrication of high permeability RO membrane. Xiao-Hua Ma et al. successfully manufactured a TFC membrane containing carbon nanotubes in rejection layer by a special interfacial polymerization technology with the assistance of a high voltage electric field [8]. Nonetheless, the arrangement of carbon nanotubes in rejection layer is out-of-order. As a result, it was unable to make full use of the 1 D water channels inside the nanotubes. Therefore, developing inorganic 3 D water channel materials which sprawling in all directions is still very promising to enhance the RO membrane permeability in practical applications.
Mesoporous silica nanoparticles (MSN), as a kind of porosity material inside which the mesopore size is easy to adjusted as required, have plentifully molecular-based 3 D nanochannels [9]. Given the special characters of abundant 3 D nanochannels sprawling in all directions, tunable mesopore size, and high porosity, MSN have been widely applied in many fields, such as nanomaterial carrier [10], desalination [11] and medical delivery [12], [13]. Especially in desalination process, MSN have been introduced into polyamide rejection layer to fabricate high-flux membranes. Hui-Qing Wu et al. incorporated mesoporous silica nanoparticles, which had been modified by amino groups, into polyamide rejection layer and successfully improved the membrane permeability and anti-fouling ability [14]. Masoumeh Zargar et al. fabricated a kind of hollow mesoporous silica nanoparticles (HMSN) and successfully introduced the HMSN into polyamide rejection layer improving water flux by about 40% [15]. However, the agglomeration of MSN seriously restricted the exertion of water channels within MSN and then limited the further increase of membrane permeability.
To solve the problem of MSN agglomeration, we developed a simple layer-by-layer assembly method based on free radical graft polymerization to manufacture MSN-TFC RO membranes. Vinyltrimethoxysilane (VTMS), as a kind of silane coupling agent, contains organic radical which can react with organic materials and silane radical which can react with inorganic materials [16], [17], [18], [19]. Considering the high reaction activity and low price, VTMS was chosen as the linking agent to immobilize MSN on PVDF membrane surface uniformly. Then, the MSN were embedded within polyamide rejection layer within the interfacial polymerization process. Therefore, 3D water channels within MSN would be able to significantly enhance the permeability of TFC membrane.
Section snippets
Main materials
Mesoporous silica nanoparticles (MSN) was procured from Shanghai So-Fe Biochemical Co., Ltd. Polyvinylidene fluoride (PVDF) was obtained from Shanghai Dongfu Chemical Technology Co., Ltd. Polyvinylpyrrolidone (PVP) was obtained from Nanjing Ruize Fine Chemical Co., Ltd. M-phenylenediamine (MPD, 99%), azodiisobutyronitrile (AIBN, 0.2 M in toluene), vinyltrimethoxysilane (VTMS, 98%) and trimesoyl chloride (TMC, 98%) were obtained from Sigma-Aldrich. N, N-Dimethylacetamide (DMAc, 99%) was obtained
Membrane characterization
As shown in Fig. 1, Fig. 2, VTMS was firstly grafted on the membrane surface and then MSN were grafted on the VTMS/PVDF substrate surface. To illustrate the success of the grafting process, the membranes were characterized by FTIR, XPS and TGA, respectively. Fig. 4(a) shows the FTIR spectra of PVDF, VTMS/PVDF and MSN/VTMS/PVDF membranes. Compared to the PVDF membrane, the VTMS/PVDF membrane owns two new peaks at 1737 cm−1 and 1240 cm−1, which are the characteristic absorption peaks of Si-OCH3
Conclusions
In this paper, the MSN with abundant nanochannels were successfully grafted on surface of PVDF membrane with VTMS as silane coupling agent through the free radical polymerization method firstly and then were embedded into polyamide rejection layer by the interfacial polymerization method. Under the optimized grafting conditions, the MSN grafted density reaches up to 8.73 mg/dm2. The prepared MSN-TFC membrane has excellent permeability and desalination properties. It can be attributed to the
CRediT authorship contribution statement
Hao Sun: Conceptualization, Methodology, Investigation, Formal analysis, Visualization, Data curation, Writing - original draft, Writing - review & editing. Bing Liu: Methodology, Software, Writing - review & editing. Dan Li: Validation, Software, Writing - review & editing. Jie Yao: Resources, Supervision, Project administration, Funding acquisition, Writing - review & editing.
Declaration of Competing Interest
The authors declare that they have no known competing financial interests or personal relationships that could have appeared to influence the work reported in this paper.
Acknowledgments
This research was funded by the “Central Guidance for Local Science and Technology Development Program (No. ZY17C10)” from China.
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