Tailoring permeation channels of graphene oxide membranes for precise ion separation
Introduction
Materials with nanopores and nanochannels such as carbon nanotubes [1], [2], nanoporous graphene [3], graphene oxide (GO) [4], [5], have attracted significant research interest in recent years due to their potential applications in separation [6]. GO, one of the most important derivatives of graphene, contains hydroxyl and epoxy functional groups on the basal planes, along with carbonyl and carboxyl groups at the flake edges [7]. GO can be exfoliated into aqueous colloidal suspensions of flakes and then assembled into free-standing membranes, thin films or paper-like materials by means of drop-casting, spin-coating [8], vacuum or pressure driven filtration [9], gas–liquid interfacial self-assembly [10], L–B [11], etc. Water permeation is expected to proceed through the whole interlayer space including oxidized areas which occupy a major part of the graphene oxide surface [12] and the nonoxidized regions [13], [14]. This endows the GO membranes excellent performance in water purification [15], [16], liquid pervaporation [17], [18] and fuel cells [19].
Although single layered GO flake exhibits outstanding mechanical strength, the weak interaction between GO flakes results in unsatisfactory mechanical performance of GO membranes [20]. The hydrophilic functional groups also lead to unstability and easily damage of GO membranes especially in aqueous solutions [21]. The integral mechanical strength of GO membranes is considered as the critical challenge for the practical separation. To solve these problems, chemical crosslinking of GO membranes with metal ions [22], borate [23], dopamine [24], amino acids, acyl chloride, isocyanates, dicarboxylic acids, diols, polyols [25], silsesquioxane [26], polyallylamine [27], polyetheramine [28], etc., has been reported to produce membranes with improved mechanical properties and stability [29]. Apparently, the molecular structure of the crosslinkers determines the reaction locations (basal planes and/or edges of GO flakes), structure and properties (hydrophilicity, charges, coordination capability, etc.) of GO membranes. Nevertheless, to our best knowledge, there are few reports related to the design and tailoring of micro-structure of GO membranes. Crosslinking both of the basal planes and edges of GO flakes is also seldom addressed. Moreover, the GO membranes are usually applied in the dialysis of single salt solution [30] while the application in the separation of mixed salts solutions is very limited.
Herein, we employed dicarboxylic acids and diamines successively to bond both of the basal planes and edges of GO flakes. By adjusting the molecular structure of diamines and dicarboxylic acids, the size, structure and properties of permeation channels are tuned, giving rise to the adjustable permeation, hydrophilicity, mechanical strength and stability of GO membranes. This is critical for precise separation of ions or molecules in practice [31], [32]. The permeation performance of GO membranes were conducted in the single salt solution and mixed salts solution (KCl, NaCl, MgCl2 and NiCl2), and distinct orders of permeation fluxes in the two cases were observed for the first time.
Section snippets
Materials
H2SO4 (>98.0%), H2O2 (30%), hydrochloric acid, KMnO4, NaNO3, propandioic acid (PA), hexanedioic acid (HA), ethylene diamine (EDA), propylene diamine (PDA), butanediamine (BDA), hexamethylene diamine (HMDA), p-phenylenediamine (PPD), or o-phenylenediamine (OPD), KCl, NaCl, MgCl2 and NiCl2. The above chemicals were analytical grade and provided by Beijing Chemical Factory.
Preparation of GO
GO was prepared by the modified Hummers' method [34], [35]. 5 g of graphite was added gradually into 115 mL of H2SO4
Characterization of GO membranes
Fig. 1a and b shows the scanning electron microscope (SEM) images of the as-obtained GO membranes, which displays a wrinkled surface and stacked lamellar structure. In the FTIR spectra (Fig. S1), the broad band at 3214 cm−1 is attributed to O–H stretching vibrations. The peak at 1630 cm−1 is related to CC vibration and 1720 cm−1 is assigned to carboxyl absorption [36]. The peak at 1380 cm−1 is the C–O vibration, and 1049 cm−1 is from the epoxy vibration [37]. After crosslinking by diamines, a
Conclusions
In summary, we successfully demonstrate the tailoring of permeation channels of GO membranes. For the permeation of single salt solution, the flux of metal cation is related to the swelling degree of GO membranes. For the permeation of mixed salt solutions, the fluxes are determined by the radii of hydrated cations, and the crosslinked GO membranes display excellent size-selectivity to metal ions due to the enhanced stability of permeation channels in aqueous solutions. The fluxes of metal ions
Acknowledgments
The authors gratefully acknowledge the support from the National Natural Science Foundation of China (No. 21076024), China Scholarship Council (No. 201308110020), and State Key Laboratory Breeding Base of Green Chemistry-Synthesis Technology (GCTKF2014008). The authors thank Bill Allman, Mark Anson and Kai Chen (Columbus, Ohio, US) for their help in editing of the paper.
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