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2D-enabled membranes: materials and beyond

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Abstract

Membranes could reform the field of molecular separations by enabling new low energy manufacturing technologies. This review article discusses the current state of the art and the potential in the 2D-enabled membrane separation processes by highlighting emerging and existing areas in which robust 2D materials significantly impact the energy-efficient separation process. Analysis of 2D-enabled membrane classes and prospective materials for 2D-enabled membranes are also discussed with emphasis on the surface chemistry of basal plane engineered 2D materials.

Background

Molecular separation processes are a critical compartment of the world’s manufacturing infrastructure. In a current carbon-constrained world, separation processes present both challenges and opportunities for the development of low-energy, low-carbon manufacturing platform. Traditional thermal separation processes involving energetically less-favorable phase change but efficiently purify hydrocarbon streams still comprise up to 80% of current industrial separation platforms [1]. However, in seawater desalination, a non-thermal technique of membrane-based reverse osmosis (RO) has been a practical solution since the 1970s and currently dominates the worldwide market [2]. The drive behind this paradigm shift was simple—the operating energy cost for the pressure-driven RO process was roughly 5–10 times lower than thermal separation processes such as multi-stage flash (MSF) [3], and this revolutionary path represents the potential of membrane-based processes in diverse industrial areas. Industrial-scale membrane-based separation processes heavily rely on the development of more rigid polymeric barriers that can discriminate molecules with very small size differences at high permeability [4]. Among newly emerging membrane materials with refined selectivities and permeabilities, materials fabricated in low-dimensional (preferentially in two-dimensional structures) architectures have the potential to combine excellent molecular specificity and flux when integrated into the membrane structure. Performance of the separation membranes, which exploit the effect of mass transport across a selective diffusion barrier to separate molecules, can be improved by reducing the thickness of the membrane. Ultimately achievable refinement in the thickness of materials is a one-atom-thick layer that can solely be achieved by 2D materials. Recently, ultrathin membranes have been fabricated using various techniques such as interfacial polymerization [5] (polyamide membrane < 10 nm), atomic-layer deposition (ZnO layer thickness ~ 200 nm, effective ZIF-8 membrane would also be < 200 nm) [6], and 3D printing (polyamide membrane < 20–80 nm) [7]. In this review, we discuss 2D materials as building blocks for membrane structure, highlight recent development of 2D-enabled membranes, and outline future directions of 2D-enabled membranes.

Indeed, similar to inorganic membranes, membranes fabricated using 2D materials with refined micropores can be used to differentiate even very similarly sized compounds. Several key industrial sectors—pharmaceutical manufacturing, biofuel production, semiconductor manufacturing, and petrochemical separation—have the potential to be positively impacted by the use of advanced membranes to complement and supplement existing separation needs [8]. The critical need for membrane scientists and engineers facing more challenging molecular mixtures is the development of more robust, thin, and selective membrane materials. Specifically, 2D materials with few-atom-thick layers with engineered intrinsic (in-plane) micropores can be used to separate similarly sized molecules at high flux. These intrinsic pores or basal planes have the possibility to be functionalized with various chemical moieties, further refining the molecular specificity of the membranes. This review illustrates the challenges in permeability and molecular selectivity of the 2D-enabled membranes with variations on themes. A very distinct pattern in the development of the 2D-enabled membranes will be discussed followed by emerging 2D-enabled membrane materials that can be used in membrane architecture. The “molecular separations” can further be tuned via the engineered basal plane of various 2D materials, including nanocomposites, and these are discussed in respective sections. Finally, critiques and perspectives will be given on scalable development of 2D-enabled membranes with emphasis on future directions in the emerging areas.

A transformative path for 2D-enabled membrane development

The recent development of the 2D-enabled membrane architecture shows a distinctive pattern that differs from the development of the conventional polymeric membrane designs. Up to this point, three well-defined classes of the membrane systems have emerged with the development of 2D materials. Each class of the 2D-enabled membranes can be specified by the presence of the microporosity of the 2D building blocks and stacking structure (Fig. 1a-c). Representative molecular separation performance (for H2/CO2 gas pair) of the 2D-enabled membranes is shown in Fig. 1d. The class 1 membranes are lamellar-type membranes that are composed of compactly interlocked 2D nanosheets. Nanosheets used in this class have no intrinsic (in-plane) microporosity. Representative materials used in class 1 membranes are graphene (G) and graphene oxide (GO) nanosheets. Tortuous transport pathways are formed between nonporous nanosheets that allow size-specific permeation of molecules (Fig. 1a). Since these nanoscopic pathways are produced in between the sheets, we define these as an external microporosity of the class 1 membranes. Class 1 membranes have shown the ability to effectively remove solvated solutes from an aqueous feed at exceptionally high fluxes, as well as molecular size differentiation up to a 0.1 nm difference in kinetic diameter of the gas molecules. This suggests that the external microporosity spans the range from ultramicropore (< 0.7 nm) to supermicropore (0.7–2.0 nm) [9] based on different nanosheets and stacking modes.

Fig. 1
figure1

Three classes of 2D-enabled membranes: a Class 1 membrane with highly interlocked 2D nanosheets. b Class 2 membrane with interlocked 2D nanosheets that have intrinsic microporosity. Red arrow represents transport pathways through the external nanopores and yellow arrow represents transport pathways through the intrinsic nanopores. c Class 3 membrane with one- or layered membrane. d H2/CO2 separation performance (permeability and selectivity) of class 1 (graphene oxide [11, 157, 158], MXene [42], MoS2 [159]), Class 2 (2D ZIFs [80], 2D MOFs [84]), Class 3 [160], and 2D nanosheet based MMM [149, 161]. Straight red line refers to 2008 upper bound [162]

Nair et al. [10] reported the permeation of water molecules through GO stacked membranes (class 1) with submicron thickness (Fig. 2a). The non-oxidized region of the GO laminate can form a nanoscopic capillary network for enhanced water transport in between GO sheets, while the oxide region provides mechanical support to maintain the laminate structure with specific interlayer spacing (Fig. 2b, c). Kim et al. [11] reported both few-layered graphene and graphene oxide membranes prepared in an interlocked structure. In the case of GO membranes, due to the affinitive interaction between a carboxylic acid group of GO and the effect of humidity, superior CO2 permeability and selectivity were observed. This class of the 2D membrane was further explored on a hollow fiber architecture by Huang et al. [12]. 2D membranes fabricated onto ceramic hollow fiber support showed excellent water permeation for various aqueous organic mixtures via a pervaporation process. Formation of the 2D-enabled membranes in a more scalable hollow fiber platform could open up the possibility of mass production of these newly emerging membrane architectures. For scalable manufacturing of these 2D-enabled membranes, roll-to-roll production of large area GO membranes also have been demonstrated [13]. Furthermore, various class 1 membranes based on reduced graphene oxide (rGO) membranes have recently been reported. Hung et al. [14] fabricated rGO membranes with a thickness of 50 nm with solvated rGO (S-rGO). Nanoscopic channels produced in this way fell into the right size range for capably discriminating salt ions and dye molecules. Their membrane showed high water permeance of 80 Lm−2h− 1bar− 1 with a high rejection rate of Red 80 dye over 99.0%. However, the exact separation mechanism (e.g., transport mechanism) of the graphene oxide membranes have not been clearly defined [15]. Since 2D-enabled membranes are in the early stage of development compared to other conventional membrane systems, several different analyses of the transport mechanism through the external micropores have been reported. Recently, Ibrahim and Lin proposed two separate transport mechanisms for GO-based membranes that can be categorized as an inter-sheet pathway (external micropore) and inner-sheet pathway (defective pathway) (Fig. 3). The authors suggested the inconsistency in reported permeabilities of GO-based membranes were due to the presence of the inner-sheet pathway, which is highly correlated with the defective sites of GO sheets. With their transport model, gas permeation through GO-based membranes can be categorized as Knudsen-like transport (inter-sheet pathway with a longer path length) and viscous transport (inner-sheet pathway with a shorter path length). Large gas molecules such as CH4, N2, and CO2 are primarily transported through the inter-sheet pathway and smaller molecules like H2 and He permeates through either the inner- or inter-sheet pathway, which have a higher permeability for smaller gas molecules. For further development of class 1 (2D) membranes, the exact mechanism of gas permeations characterized by sorptivity, diffusivity, porosity and tortuosity of the nanosheets should be considered.

Fig. 2
figure2

a Permeation through the GO membranes. Water is freely evaporated through GO membrane similar to open aperture (blue line). b Structure of the single graphene capillary in the GO films. Pristine graphene capillaries form monolayer water channel. The dashed lines indicate the capillary state with low humidity. c Possible permeation routes for permeation through laminates. Adapted with permission from ref [10]. Copyright 2012 American Association for the Advancement of Science

Fig. 3
figure3

Predicted transport model through GO membranes [A] path denotes the pathway through external nanopores and interlayer channel. [B] path denotes the pathway through the intrinsic pores of each layer [15]. Adapted with permission from ref [15]. Copyright 2018 for the Elsevier

Conventionally, these class 1 membranes are fabricated using several different techniques such as vacuum filtration, vacuum suction, spray coating, spin coating, and dip coating. The most common method is dynamic vacuum filtration of the composite suspensions on a porous support to construct layer-by-layer deposited membrane. In this method, a solution containing well-dispersed 2D nanosheets are slowly filtered onto a desired porous support. Closely packed nanosheets are obtained after filtration that can be readily used in molecular separation testing. Even though the well-defined layered structure is achievable through filtration, it generally requires sufficient filtration time (up to several days) and constant driving force (vacuum level) that hinders rapid scale-up of this method. GO membrane prepared on a ceramic hollow fiber [12] is a good example showing the feasibility of this method. In this case, the vacuum filtration was performed on a ceramic hollow fiber with a sealed end. It was shown that uniform 2D membrane can be prepared on support with high curvature and elongated surface. In addition, various coating techniques are also applied to form 2D-enabled membranes. In “spray coating” method [16], dilute composites suspension with volatile solvents are sprayed onto the support. During the evaporation of solvents, 2D nanosheets are self-assembled into the lamellar-like structure. One advantageous feature of the spray coating method is that it can achieve ultrathin membranes by controlling the viscosity of the solution and spray pressure. In the case of "spin coating" method, the composite suspension is poured onto the center of the support and the suspension spread out via centrifugal force. Through this “spin coating” method [11], very thin, highly uniform and highly interlocked membranes based on 2D nanosheets can be formed. In “dip coating” method [17], the support is directly dipped into the composite suspension and the drawing out process forms a thin layer on the outer surface of the support. Similar to other coating methods, the 2D structure can be formed via evaporation and self-assembly.

Class 2 membranes are classified as 2D membranes that utilize nanosheets with intrinsic (in-plane) microporosity on the basal plane. Nanosheets with intrinsic microporosity capable of differentiating molecular size differences up to 0.01–0.05 nm are exploited in this class of membranes [18,19,20]. This intrinsic microporosity is different from external microporosity of the class 1 membranes and also differentiates itself from the intrinsic defects formed in 2D materials. Nanosheets derived (or delaminated) from 3D microporous crystalline materials such as zeolite [18], metal-organic framework (MOF) [19] and, covalent-organic framework (COF) [20] are a representative building block in class 2 membranes as well as “nanoporous” graphene or graphene oxide. When these ultra-microporous building blocks are efficiently packed into the lamellar structure, forming external microporosity via sheet stacking, class 2 membranes gain the potential to combine high molecular selectivity and flux stems from intrinsic micropores and external micropores. Since the discovery of exfoliated zeolite nanosheets, there have been many attempts to fabricate membranes with zeolite nanosheets. Zhang et al. [21] fabricated class 2 membranes with MFI zeolite nanosheets by a simple vacuum filtration method on a polymeric support. 2D Zeolite membranes produced in this way showed excellent n-butane permeance (up to 1000 GPU) with n-butane/iso-butane selectivity of ~ 5. Interlayers between zeolite nanosheets act both as a gallery for enhanced molecular transport and as size-selective transport pathways. Zeolite nanosheets have been used as seeds for further zeolite membrane growth—the hydrothermal secondary membrane growth efficiently closes the interlayer gaps and significantly enhances the membrane performances [22,23,24]. However, these secondarily grown membranes (inter-grown) are not in the scope of this review article. Nanoporous graphene or graphene oxide can be produced via etching of carbon atoms on a basal plane, which can form a pore with an area of 2.6 Å2 per single carbon atom etched [25]. Weiwei et al. [26] used an oxygen plasma etching method to enhance the water permeation through a reduced graphene oxide (r-GO) membrane by modifying the hydrophilicity of the surface of r-GO layers. Triple-layered graphene oxide membranes were formed by thermal reduction with exposure to oxygen plasma for 8–30 s. After the plasma treatment, water permeance through the r-GO membrane has significantly increased up to 4–40 Lm−2h− 1bar− 1 from less than 2 Lm−2h− 1bar−1 of the non-treated r-GO membrane. Formation of nanoporous layers can dramatically improve the membrane performance by forming a shortened transport pathway (Fig. 1b, Class 2) using in-plane nanoscopic pores—which is the main difference between class 2 membranes and class 1 membranes. Peng et al. [27] fabricated a 1-nm thick MOF nanosheet by a soft-physical exfoliation method using Zn2(benzimidazole)4 as a parent 3D framework (Fig. 4a). Nanosheet suspension was drop coated on heated support (hot drop coating) that lead to disordered stacking due to the variation on the rate of evaporation across the film. In contrast, conventional filtration method applies constant force across the film, ordered restacking of the nanosheets are obtained, which have been identified from x-ray diffraction. However, the ordered stacking of MOF nanosheets showed partially or blocked micropores, therefore hot drop coating method was preferred to efficiently fabricate class 2 membranes for these materials. Their membranes showed impressive selectivity for the H2/CO2 pair (~ 260) at 120 °C with linearly increased H2 permeance through the membranes at high temperature (Fig. 4b).

Fig. 4
figure4

a A cartoon illustrating the gas separation through porous Zn2(Bim)3 nanosheets. Only Zn atoms are shown for clarity, and the light blue planes represent the nanosheets regardless of their amphiprotic natures. The blue line indicates the pathway of H2 and the red line represents the pathway of CO2 [27]. b The change of permeance of H2/CO2 and mixture separation factor of Zn2(Bim)3 nanosheet membrane for different temperature condition [27]. Adapted with permission from ref [27]. Copyright 2017 for the John Wiley and Sons

The ultimate class of the 2D-enabled membranes is the class 3 membranes that are one- or a few atoms thick layers with intrinsic microporosity. Class 3 membranes represent the lower limits for any membrane fabrication (one atom thick) combined with ultra-permeability via an atomically-thick membrane layer. Membranes in this class are a version extended from class 2 membranes by the formation of large-area atomically thin membranes. Generally, class 2 membranes have a wide range of thicknesses (a few tens of nanometers to a few micrometers) due to the stacking of nanosheets; however, class 3 membranes are classified as few nanometer thick membranes fabricated from 2D nanosheets. Single or few-atomic-layer membranes with tuned intrinsic micropores, such as graphene nanosheets with engineered nanoscopic pores are representative membranes in this class. The advantage of atomically thin membranes is their maximized molecular flux (minimized transport resistance) [28]. Although the graphene itself can form perfectly two-dimensional single atomic layers, a perfect single layer still cannot permeate a small gas such as helium. The molecular sieving potential of nanoporous graphene is gained from the fact that by selectively (and regularly) removing carbon atoms from the lattice, it should be possible to develop membranes that offer exquisite molecular sieving properties and ultra-high molecular fluxes. The membrane reported in Surwade et al. [25, 29] is one of the representative class 3 membranes. Surwade et al. created a one-atom-thick nanoporous graphene membrane using plasma etching. Single layer graphene was deposited on a copper surface and transferred to a silicon nitride wafer with 5-μm holes. A short burst of oxygen plasma created nanoscopic pores on the graphene layer with sufficient areal density to allow ultra-high water flux combined with a nearly perfect salt rejection. Huang et al. [30] reported a relatively large area (1 mm2) single-layer graphene film as a class 3 gas separation membrane. To minimize the formation of cracks during transfer process from chemical-vapor deposition (CVD) derived graphene on porous supported graphene (Fig. 5a), researchers used nanoporous carbon as a sacrificial layer to protect the graphene membrane layer during the transfer process. Intrinsic defects of graphene that originated from the CVD process produced reasonably high hydrogen permeance (up to 4 × 10–7 mol m− 2 s− 1 Pa− 1) (Fig. 5b) with H2/CH4 selectivity up to 25 (Fig. 5c), which was comparable to state-of-the-art polymeric membranes with 1 μm thickness. Researchers further demonstrated ozone functionalization that enhanced the areal density of the nanoscopic pores on the basal plane of the graphene membrane, which is directly related to the productivity (flux) of the graphene-based membrane. One important question about class 3 membranes is the durability of the single layer membranes at various pressure and temperature conditions. Kumar et al. [31] tested the stability of single-layer graphene membranes (5 μm diameter) by a temperature swing cycle (25–200 °C) with transmembrane pressure up to 0.5 bar. In various conditions, non-porous (as synthesized) single-layer graphene membranes showed impressive stability for several days. Then, researchers introduced an oxygen etching technique to create nanoscopic pores on the graphene layer to allow the transport of gas molecules. Although the pressure testing was not entirely investigated on the nanoporous graphene membrane, this result provided a guide for standardization of membrane testing procedures for 2D-enabled membranes. Nevertheless, a fundamental understanding of the permselectivity of the class 3 membrane is still under development. A few mechanisms for gas permeation through the sub-nanometer graphene pores was proposed by Yuan et al. [32]. In their model, gas permeation through the graphene pores was described in a two-step process of adsorption and translocation. First, the gas molecules are adsorbed on the entrance of the generated pores and these are translocated along the graphene membrane via a chemical potential gradient. Then the rate coefficient of translocation obeys Arrhenius-type behavior, indicating that the ‘solution-diffusion model’ defined in conventional membrane systems with a continuum-level assumption might be applied to the single-layer 2D membranes. The transport models of 2D-enabled membranes are suggested by several reports. Graphene based class 3 membranes are often treated as a test bed for modeling work on atomically thin membranes. For class 3 membranes, the relative size of pores and the penetrating molecule is a dominant factor that can ultimately modify the permeability through the membrane [33, 34]. For relatively large pores (pore size larger than the penetrants), steric regime model can be applied to describe the transport of gas molecules [35]. In this model, gas molecules are treated as a rigid sphere with specific kinetic diameters. Steric regime model suggests no interaction between the pore edge sites and penetrants, therefore energetic barrier for gas transport in the pore is low. On the other hand, activated regime model assumes that certain energy barrier exists when the penetrants attempt to pass through the pores. In this case, Lennard-Jones potential is used to describe penetrant-pore interaction [36]. For relatively small pores (pore size smaller than the penetrants), activated regime model is used to predict molecular transport across the membrane. Limitations of these models include lack of consideration of the adsorptive flux near the nanosheet surface and the detailed chemical structure of nanopores. Du et al. [37] and Sun et al. [38] reported the significance of adsorptive flux near the surface of graphene through molecular simulations. The affinity difference between gas molecules with a carbon atom of the graphene layer will alter the permeability across the class 3 graphene membrane and eventually affect the selectivity of different gas pairs. For example, N2 can form the adsorptive flux near the graphene layer through van der Waals interaction that leads to high N2/H2 selectivity. In summary, to consider the transport model in 2D-enabled membranes, in addition to the pore size, the interaction between the penetrants and 2D materials should be fully considered. Although research into the nanoporous graphene membrane (class 3) is still in its early stages, these membranes will open up the new possibilities in molecularly-selective separation processes for future generations.

Fig. 5
figure5

a Fabrication process of large-area graphene membrane through the nanoporous carbon film-assisted transfer method. b The permeance of H2 for 8 different graphene membranes with different temperature condition. c H2/CH4 selectivity for 8 different graphene membranes with different temperature condition [30]. Adapted with permission from ref [30] under a Creative Commons Attribution 4.0 License (http://creativecommons.org/licenses/by/4.0/)

Newly emerging materials as “contenders” in 2D-enabled membranes

The development of the 2D-enabled membranes to date have been largely led by the use of graphene and graphene oxide. Particularly, graphene oxide (GO) is prepared inexpensively on a large scale by oxidation and exfoliation of graphite. These GO nanosheets can be easily dispersed in water and provide an easy means for membrane fabrication via conventional filtration technique. On the laboratory scale, a 1–10 cm2 membrane sample is sufficient to generate transport data. However, the large-scale application requires membranes scaled up in a few orders of magnitudes in a defect-free manner [39]. Fabrication of defect-free, large-scale graphene or graphene oxide membranes for gas and liquid separation has not yet been fully exploited and is sometimes extremely challenging due to their poor mechanical properties. Moreover, forming uniform intrinsic micropores on the graphene layer (class 3 membranes) or tuning the uniform tortuous path (external micropores in class 1 or 2 membranes) in laminate graphene oxide membranes are still questionable [40]. In this section, we discuss the applicability of the recently emerging 2D nanosheets other than graphene-derived materials in a membrane structure that may help to advance the development of 2D-enabled membranes. More detailed surface chemistry and functionalization of the 2D materials will be discussed in the following separate section.

MXenes

MXenes are the inorganic compound that has a chemical formula of Mn+1XnTx (M: Transition metal, X: Carbon or nitrogen, T: Functional group on the basal plane). MXenes are derived from the parent MAX phases, where A consists of 3A metals or 4A elements. In the MAX phases, M-A bonds have weaker interaction than M-X bonds, so A element can be selectively removed at high temperature or etching by HF treatment. Removal of the A induces the formation of MXene nanosheets with a form of M2X, M2X2, and M4X3 [41]. Representative MXene family members include Ti3C2, Ti2C, Nb2C, V2C, (Ti0.5Nb0.5)2C, (V0.5Cr0.5)3C2, Ti3CN and Ta4C3. In MXene nanosheets, the functional groups (T) play a critical role in creating the nanochannels between two MXene nanosheets. Functional groups contribute to the stability of MXene membranes by adjusting the interaction between the individual MXene nanosheets. Using these MXene nanosheets, various class 1 membranes have been demonstrated in gas and liquid separations. Ding et al. [42] fabricated membranes with titanium-based MXenes (Ti3C2Tx) by vacuum filtration on an anodic aluminum oxide support. The interlayer spacing between MXene layers was ~ 0.35 nm and allowed the high permeability of the gas molecules such as hydrogen (2100 Barrer) and He (2400 Barrer) (Fig. 6). Due to the much smaller interlayer spacing provided in MXene based membranes compared to GO based membranes, MXene based membranes show promising molecular sieving properties for the H2/CO2 pair with selectivity over 100. Chemical functionalization on the MXene surfaces can further refine the selectivity of specific gaseous species. Jie et al. [43] used borates to selectively transport CO2 through MXene channels by crosslinking the borates (B4O72−) with hydroxyl groups on the surface of MXene nanosheets (Fig. 7a). It reduced the interlayer distance between MXene nanosheets, thus confirming the reversible desorption of trapped CO2 in the nanosheets. At 75 °C, the borate modified MXene membrane showed 13% enhancement of CO2 adsorption capacity compared to a pristine MXene membrane (Fig. 7b). Further interlocking between MXene nanosheets was achieved by cross-linking the borate and polyethyleneimine (PEI). Positively charged PEI molecules help to reduce the interlayer spacing when mixed with borate and MXene flakes, tuning the interlayer spacing down to 0.34 nm at 75 °C—which fall into the range of kinetic diameters of CH4 (0.36 nm) and CO2 (0.32 nm). MXene with borate and PEI achieved 5.2 times enhancement of CO2 permeance compared to the pristine MXene membrane (350 GPU for MXene with borate and PEI and 67 GPU for pristine MXene membrane).

Fig. 6
figure6

Single-gas permeability of various gases with different kinetic diameters across the 2-μm-thick MXene membrane at 25 °C and 1 bar. The inner graph showed the selectivity of 3 equimolar mixed gases [42]. Adapted with permission from ref [42]. Copyright 2018 for the John Wiley and Sons

Fig. 7
figure7

a Structure and gas transport pathway of gas-selective MXene nanosheets. b Gas adsorption data for pristine and functionalized MXene at 25 °C [43]. Adapted with permission from ref [43] under a Creative Commons Attribution 4.0 License (http://creativecommons.org/licenses/by/4.0/)

MXene based membranes also show promising liquid separation performances. Chang et al. [44] reported MXene membranes that had ultrafast water flux and high ion selectivity. One interesting feature is that even with a relatively thick membrane (0.9–1.5 μm), their membrane achieved very high water permeance (~ 38 Lm−2h− 1bar− 1), which was much higher than that of the 1.5 μm thick GO membranes (~ 6.5 Lm−2h− 1bar− 1). Researchers suggested that the thin layer of water molecules formed between the MXene nanosheets, which provided a fast transport pathway for water molecules, was responsible for this high water permeance. In addition, their membrane showed size and charge-selective permeation of ions. Na+ had the highest permeation rate among differently charged cations, achieving a 25 times higher permeation rate compared to Al3+ and 7 times higher than Ca2+. The ionic selectivity of the MXene based membranes reflects that the MXene nanosheets are also promising building blocks for 2D-enabled membranes. Wang et al. [45] fabricated 4.5 nm thick lamellar MXene nanosheets that attained surprisingly high water permeances (~ 2300 Lm−2h− 1bar− 1) and organic solvent permeances (up to 5000 Lm−2h−1bar−1 for both acetone and acetonitrile). These permeances are at least 20 times higher than those of the 18 nm thick reduced GO membranes for acetone. The regular and ordered flow channels created between MXene nanosheets were the vehicle for the high water and solvent permeances, opening up the possibility of the use of MXene membranes in the field of organic solvent nanofiltration (OSN). Li et al. [46] used a molecular dynamics simulation in a quest to find the optimal design of the MXene lamellar structure for selective molecular separations. Two factors, interlayer distance (d) and intercalated molecules were identified as critical factors in designing MXene based membranes for optimal separation performances. The interlayer distance (d), of course, provides tortuous pathways for molecular transport and plays a critical role for molecular sieving of similarly sized molecules. By simulating the variation in the interlayer distance from 5 to 13 Å, the authors showed that anhydrous MXene nanosheets with ~ 5 Å interlayer distance can effectively separate H2/CO2 (kinetic diameter H2 is 2.89 Å and CO2 is 3.3 Å) mixture. In addition, the intercalated molecules between MXene sheets can modify the transport characteristics of the permeating molecules by partially tuning the “effective interlayer distance”. Through the simulations, the diffusivity of several gas molecules in the hydrous (water-filled) MXene channel was calculated smaller than that of anhydrous MXene channels. When MXene sheets are hydrated, these water molecules can scatter the gas molecules or even block the pores, therefore decreasing the diffusion coefficient of gas molecules. For very small interlayer distance, water molecules even can block the gas transport channel of MXene nanosheets. The suggestions from their molecular simulation can be broadly used in most of the class 1 type membranes.

Boron nitride (BN)

Two dimensional boron nitride nanosheets are sometimes referred to as “white graphene” since they are the isomorphs of the graphene structure. 2D hexagonal boron nitride (h-BN) can be formed in a graphene-like structure by the mechanical cleavage from bulk BN crystal or the chemical vapor decomposition reactions of precursor molecules [47]. Its high mechanical and chemical stability is reported by multiple studies [48,49,50,51]. Both graphene and BN shows hexagonal atomic structure formed with strong covalent sp2 bonds. However, BN exhibits intrinsically inorganic nature whereas graphene shows partially organic nature, therefore BN is generally treated as a chemically more inert compared to graphene. However, for fabricating a large area of h-BN nanosheets, thermal catalytic chemical vapor deposition is highly favored over the mechanical cleavage techniques, partially overcoming the scalability problems related to 2D materials [47]. Each h-BN nanosheet has a honeycomb structure consisting of a borazine ring (B3N3H6) with a B-N bond length of 1.45 Å. The center-to-center distance of the adjacent borazine rings is 2.50 Å, which is slightly longer than 2.46 Å in the graphene basal plane [52]. In addition, the stack order of h-BN is different from that of graphene. In the graphene layers, each carbon atom is located right above the center or the carbon ring (AB stacking); however, in h-BN, each B atom eclipses an N atom on the adjacent h-BN layer (AA’ stacking). Sutter et al. [53] reported the chemical vapor deposition (CVD) method to fabricate large-area hexagonal boron nitride (h-BN) monolayers. With the low partial pressure of borazine, h-BN sparsely nucleated the domain and merged into a single layer. They also reported that the amount of hydrogen gas in the precursor gas controlled the expansion and morphology of growing h-BN domains. In addition, hydrogen gas inhibited the formation of surface oxides on metal substrates. The additional H2 with the borazine precursor provides evidence that the B and N incorporation at the h-BN edge can be modulated to control the growth and to achieve different types of h-BN domain morphology. Especially, unlike graphene derivatives, h-BN has high chemical stability under both acidic and basic conditions. Although boron nitride has high stability in harsh conditions, it is difficult to fabricate class 1 membranes with h-BN nanosheets due to its hydrophobicity, which highlights the importance of functionalization of h-BN to enhance the stacking properties of BN based membranes. Chen et al. [54] reported the use of amino-functionalized h-BN membranes in organic solvent nanofiltration (OSN). Class 1 membranes were fabricated using water-dispersible (functionalized) BN nanosheets. Membranes formed using functionalized boron nitride nanosheets have a superior solvent flux while also having moderate-to-high solute rejections in both organic and aqueous solvents. Their 400 nm-thick membranes showed a water flux of 1500 Lm− 2 h− 1 and 99% rejection rate for Congo Red dye (696.7 g/mol). However the rejection rates for methylene blue (MB, 320 g/mol), Rhodamine B (RhB, 479 g/mol), and Rhodamine 6G (R6G, 479 g/mol) were 50.3, 58.3, 83.8%, respectively. For ethanol, it showed an ethanol flux of 1480 Lm− 2 h− 1 with 54% rejection rate for Congo Red dye and 620 Lm− 2 h− 1 with 99% rejection rate for Au nanoparticles. And for methanol it showed the flux of 600, 740, 640 and 560 Lm− 2 h− 1 with 99, 60, 88.7 and 99% rejection rate for Congo Red dye, methylene blue (MB), Acid fuchsin (ACF, 586 g/mol), Evans blue (EB, 961 g/mol), respectively. In addition, compared to graphene derivatives, the functionalized inorganic boron nitride membrane demonstrated high stability for acid, alkali, and oxidative media conditions. Lei et al. [40] reported the adsorptive separation performance of BN laminates for oils, organic solvents, and water. The layered structure of the BN was synthesized via a dynamic templating approach, and BN laminate attained a notable BET surface area (~ 1400 m2 g− 1) and pore volume (~ 1 cm3 g− 1) indicating the possible application of the BN lamellar structure in membrane-based separations. Liu et al. [55] fabricated a mixed-matrix membrane (MMM) of poly (vinylidene fluoride) and boron nitride nanosheets. Mixed-matrix membranes (MMMs) formed with 2D materials is further discussed in the following section, so it would be appropriate to briefly introduce the MMM formed with BN nanosheets here. Their membrane had a thickness of around 300 μ m and the BN nanosheets had many holes with a diameter range from 20 to 100 nm. A 300 mm thick MMM fabricated with BN nanosheets achieved largely enhanced water permeability (~ 8.2 × 104 L-μm-m−2h− 1bar− 1) that was three orders of magnitude higher than that of the pristine polyvinylidene fluoride (PVDF) membranes. Moreover, their membrane showed excellent filtration efficiency for several pharmaceuticals, such as carbamazepine, indicating the applications in organic solvent nanofiltrations.

Molybdenum disulfide (MoS2)

More than 60 types of transition metal dichalcogenide (TMD) have been discovered since 1960, and molybdenum disulfide (MoS2) is one of the popular materials in this class and also a strong contender as building blocks for 2D-enabled membranes. Among various TMDs, 2D MoS2 is characterized by the well-defined, uniform two-dimensional transport channels with limited undesirable chemical defects [56]. The uniform nanoscopic channel structure of MoS2 is very advantageous for studying fundamental transport mechanisms in tortuous pathways in class 1 or class 2 membranes. In general, TMDs consist of a transition metal layer sandwiched between two chalcogen layers. Compared to other two-dimensional membrane materials, the TMD monolayer is unique for this “sandwiched structure” [57] (Fig. 8a). Due to this sandwiched structure, TMDs can have different crystal polytypes. For example, MoS2 can have four different crystal structures, 2H, 1 T, 1 T’ and 3R [58], with different coordination models. The 2H type has trigonal prismatic coordination consisting of hexagonally packed atoms with ABA staking mode (S-Mo-S′). The 1 T type has an octahedral phase. It has a stacking mode of ABC (S-Mo-S′). 1 T’ type is called ‘distorted 1T type’. It also has an octahedral phase, however, superlattice structures can exist in each layer. The 3R type also has trigonal prismatic coordination. The multilayers of 3R type showed a rhombohedral symmetry. Although MoS2 can have diverse crystal structures, due to the thermodynamical stability, the 2H type is dominantly formed during synthesis [57] (Fig. 8a, b). Mainly, exfoliation and filtration induced stacking of MoS2 nanosheets is similar to those of the graphene-based membranes. Recently, vapor and liquid permeation through the MoS2 lamellar structure that is comparable to graphene oxide derived membranes were reported. Lamellar (class 1) MoS2 membranes [56] showed better stability in a harsh aqueous environment (stability under a low wide range of pH) than GO membranes while allowing permeation of light organic vapors (e.g., MeOH, EtOH, cyclohexane, and acetone) as well as water vapor. The 2D nanoscopic channel produced in the stacked MoS2-platelet membrane also suggests the molecular sieving of various ions and dye molecules. Hirunpinyopas et al. [59] reported a functionalized MoS2 lamellar membrane that effectively prevents MoS2 membranes from swelling from water exposure. Various dye molecules (crystal violet, sunset yellow, and neutral red) are used to functionalize the MoS2 surface and the effect of dye functionalization was confirmed by forward-osmosis type experiments. Notably, the MoS2 membrane functionalized by sunset yellow dye with a 5 μm thickness showed a nearly 99% NaCl rejection and 5 times higher water flux (0.033 L m− 2 h− 1 bar− 1) through the membrane than that of a similar thickness GO membrane (0.007 L m− 2h− 1bar− 1). Heiranian et al. [60] calculated the performance of class 3 type membranes formed by a single layer MoS2 membrane via MD simulations. Due to the sandwiched triple layer structure of the MoS2, edge site chemistry played a significant role in water permeation via the difference in hydrophobicity of different sites. By tuning the pore area of a single layer MoS2 membrane, salt rejection of the membrane reached up to 88% with water permeability comparable to that of the GO membranes. Wang et al. [61] reported the effect of hydration states on the size of the nano-channels between MoS2 layers. When the MoS2 membrane was fully hydrated, the free spacing between the layers was 0.9 nm, while a perfectly dehydrated MoS2 membrane had a 0.3 nm free spacing. Fully hydrated MoS2 membranes maintained the interlayer distance by the van der Waals interaction and hydration force which created aqueous stability of the MoS2 membranes. Water molecules were transported through the fully hydrated MoS2 membranes and their membrane showed a high water flux of 30–250 L m− 2 h− 1 bar− 1. However, other organic molecules (rhodamine-WT and methylene blue) are moderately cut off by their size which is larger than the free spacing between MoS2 layers. Chen et al. [62] impregnated ionic liquid (1-butyl-3-methylimidazolium tetrafluoroborate [BMIM][BF4]) into the interlayer of the MoS2 membranes. Due to the high solubility of CO2 toward [BMIM][BF4], their ionic liquid confined MoS2 membranes showed noticeable selectivity for various mixtures such as CO2/N2 (~ 131), CO2/CH4 (~ 43) and CO2/H2 (~ 14). MoS2 nanosheets have also been used in desalination via forward osmosis (FO) operation. Li et al. [63] stacked MoS2 nanosheets on the surface of polyethersulfone (PES) FO membrane by layer-by-layer (LBL) deposition method. The presence of MoS2 increase the hydrophilicity of the FO membrane and furthermore tuned the average pore radius that potentially affected the water permeability of the FO membrane. MoS2 coated FO membrane showed ~ 35% enhanced water flux compared to that of the pristine FO membrane. Hydrophilic and smooth MoS2 nanochannels contribute to the higher water flux of coated FO membrane. Moreover, the reverse NaCl flux of MoS2 coated membrane is decreased to 16.42 gm-2h-1, 35.91% enhanced compared to reverse NaCl flux of pristine PES FO membrane. Through the dynamic cross-fouling test with Bovine serum albumin (BSA) molecule, MoS2 coated FO membrane showed stronger fouling resistance than pristine PES FO membrane. MoS2 is definitely an attractive candidate for 2D-enabled membranes due to its planar characteristics of limiting defects with a uniform and well-established structure of a two dimensional transport channel.

Fig. 8
figure8

a The structure difference between 1 T, 2H and 3R [163]. Adapted with permission from ref [163]. Copyright 2016 for John Wiley and Sons. b Top and side views for 2H (left) and 1 T (Right) phase of MoS2 single layer [106]. Adapted with permission from ref [106], under a Creative Commons Attribution 4.0 License (http://creativecommons.org/licenses/by/4.0/)

Metal organic frameworks (MOF)

The metal organic framework (MOF) is a class of microporous material similar to the zeolite family. MOF crystals are synthesized by connecting the metal clusters by various multitopic organic linkers (or ligands). To date, more than 70,000 different MOFs have been experimentally confirmed in about 138,000 hypothetical frameworks [64, 65]. Unlike zeolites, which are characterized by their rigid, regular microporosity, MOFs show a higher degree of flexibility due to the rotational or translational freedom of organic linkers, such as imidazolate, carboxylate, and azolate. MOFs are frequently used as a filler for fabrication of a mixed matrix membrane due to the partial organic nature of its framework—affinity toward a polymeric matrix is higher than other purely inorganic materials. Two dimensional (MOF nanosheets) MOFs have been also reported to show favorable applications in catalysis [66, 67], gas storage and separations [68, 69], and chemical sensors [70, 71]. MOF nanosheets are prepared in two different ways: 1) Bottom-up synthesis (c.f., arresting crystallization) [72], 2) Top-down synthesis (c.f., exfoliation of layered MOF crystals) [73, 74] (Fig. 9). In bottom-up synthesis, a dominant growth of the 2D plane is achieved by using the appropriate ligands or surfactants. For instance, specific surfactants direct the growth of a preferential plane by their selective attachment on the specific facets of nanocrystals. Surfactant attachment on the surface of the crystal reduces the surface energy via dipole-dipole interaction, enabling the controlled growth of crystal facets [75]. Zhao et al. [76] reported the fabrication of ultrathin 2D M-TCPP nanosheets (M = Zn or Cu, TCPP = Tetrakis(4-carboxyphenyl)porphyrin) using a surfactant such as poly (vinyl pyrrolidone). Conventional solvothermal synthesis without the use of a surfactant naturally creates bulk crystals of M-TCPP, but with PVP, anisotropic growth of nanocrystals is observed, and ultrathin 2D nanosheets with a thickness of 8.7 ± 2 .7nm are formed. Similarly, other small modifier molecules can bind preferentially to a particular facet of growing crystals. For example, the use of pyridine in synthesizing copper based 2D MOF nanosheets [77] and the use of PVP in synthesizing cobalt based 2D MOF nanosheets have been reported [78]. 2D nanosheets of MOF can also be produced using phase-interface directed crystal growth. In the top-down synthesis of MOF nanosheets, a number of different exfoliation methods have been reported. Abherve et al. [73] mimicked the famous “scotch tape method” [79] to produce MOF nanosheets. Their MOF nanosheets had few micron lateral sizes with 2 nm thickness. Ball mill, grinder, stirrer, or ultrasonication have been used to mechanically exfoliate bulk layered MOFs [80,81,82,83]. Alternatively, the interlayer space in layered MOF materials can be enlarged by the intercalation of ionic/molecular species between MOF layers to enhance the delamination of the nanosheets.

Fig. 9
figure9

a A cartoon showing the mass transport through COF membranes [86] Adapted with permission from ref [86]. Copyright 2013 for Royal Society of Chemistry. b Various example of 2D COF building blocks [164]. Adapted with permission from ref [164]. Copyright 2016 for John Wiley and Sons

These MOF nanosheets are frequently used to form class 2 or class 3 (2D) membranes. Peng et al. [80] reported 1 nm thick MOF nanosheets with a large lateral area and their application in fabricating molecular sieving membranes. Parent poly (Zn2(benzimidazole)4) MOF has two-dimensional layers oriented normal to the c axis connected by weak van der Waals interactions between layers. Wet ball milling and ultrasonication can break these weak interactions to exfoliate nanosheets and the suspension of nanosheets was further deposited onto the surface of α-Al2O2 via a hot-drop coating method. The class 2 type membrane produced by this method had sharp molecular sieving properties with high H2 permeance (up to 3700 GPU) and decent H2/CO2 selectivity (up to 290). Similarly, Peng et al. [27] reported sub-10 nm thick MOF nanosheets of Zn2(benzimidazole)3(OH)(H2O). Exfoliated MOF nanosheets were deposited using the hot-drop coating method and tested for separation of an H2/CO2 mixture (H2 permeance up to 2300 GPU and H2/CO2 selectivity up to 166). Wang et al. [84] also used the hot-drop coating method to prepare 2D MOF membranes. 2D Mesh Adjustable Molecular Sieve (MAMS-1) nanosheets were prepared by a freeze-thaw process of the parent 3D framework. During the freeze-thaw process, the parent MAMS-1 crystals were frozen in a liquid nitrogen bath and thawed in hot water bath, repeatedly. Due to the shear force derived from the volumetric change of solvent, the 2D MAMS-1 nanosheets were exfoliated. And then a nanoscale MAMS-1 membrane was fabricated on hot anodic aluminum oxide. This membrane also selectively permeated H2 over CO2 with H2 permeance up to 800 GPU with H2/CO2 selectivity up to 268. Overall, atomically thin MOF nanosheets have been re-assembled and interlocked on porous supports to produce class 2 type membranes that combine the intrinsic micropores of MOF nanosheets and external nanopores between MOF nanosheets.

Covalent organic frameworks (COF)

Covalent organic frameworks are a novel class of microporous crystalline materials based on the integration of organic building blocks into highly ordered networks. These organic ligands are coordinated into a periodic two-dimensional networks structures to construct highly uniform micro- or mesoporous pores (Fig. 10a, b). Compared to its parent 3D structures, 2D COFs form lamellar nanosheets that can be widely exploited in class 2 or class 3 membranes. In general, Schiff base-type COFs form pore sizes in 0.8–5.0 nm that are useful in nanofiltration (NF) type separations, however, the pore size can further be tuned by the introduction of functional groups at the pore edge sites. Since organic linkers are covalently linked in the microporous framework, COFs show high stability under various organic conditions and further be used in organic solvent separations. A self-standing COF membrane (M-TpTD, Tp: 1,3,5-triformylphloroglucinol, TD: 4,4′-p-Phenylenedianiline) with a pore size of 2.6 nm showed impressive permeance for several different aprotic solvents [85]. Especially, methanol recorded the highest permeance of 138 Lm− 2 h− 1 bar− 1 with high rejection rate for Rose Bengal (MW: 1017.6, 99% rejection), Congo Red (MW: 696.6, 96% rejection) and Methylene Blue (MW: 319.8, 94% rejection). Zhang et al. [86] used a facile bottom-up interfacial crystallization approach to obtain a 2D COF (EB-COF:Br, EB = ethidium bromide) membrane with average pore size of 1.68 nm and an interlayer distance of 1.65 nm. Their membrane showed high permeance for protic solvents such as methanol (1272 L m− 2 h− 1 bar− 1), ethanol (564 L m− 2 h− 1 bar− 1) and n-propanol (477 L m− 2 h− 1 bar− 1), and for aprotic solvents such as acetone (2640 L m− 2 h− 1 bar− 1), acetonitrile (2095 L m− 2 h− 1 bar− 1). Interestingly, near perfect (~ 100%) rejection for anionic dyes (Methyl Orange, Fluorescein Sodium salt, Potassium Permanganate) due to the strong electrostatic interaction with the positively charged pore walls of COF. Shinde et al. [87] used the Langmuir-Blodgett (LB) method to fabricate 2D COF membrane with crystalline TFP-DHF and performed organic solvent nanofiltration. β-ketoenamine linkages between TFP and DHF are formed and inclined AA stacked hexagonal lattice COF with the pore size of 1.41 nm are synthesized. Through the LB method, membrane thickness can be controlled precisely. Their membrane showed large high contact angle (84.5) and thermal stability up to 200 °C. Previously, imine bonded two-dimensional COF membranes (thickness of 1.7, 2.3, and 4 .7nm) by using LB method were reported [88]. Compared to the previously reported membrane, their newly fabricated membrane showed 100 times higher solvent permeability. The molecular weight cutoff (MWCO) of TFP-DHF 2D COF membrane showed around 900 Da and the molecular weight retention onset (MWRO) of the membrane is around 600 Da. Zhang et al. [89] reported MD simulation of 2D COF membrane for desalination. The triformylphloroglucinol (Tp) and p-phenylenediamine (Pa) with several functional groups (X) are used to fabricate 2D COF membrane (TpPa-X) by tuning the aperture sizes in the range of 5.1–7.6 Å. Hydrophilic functional groups with larger aperture size were advantageous in high water permeance of the 2D COF membranes. Through MD simulation, their 2D COF based membranes showed 1–2 orders of magnitude higher water permeance compared to that of 3D ZIF membranes, which have totally opposite structure to 2D COF membrane, with relatively long channels.

Fig. 10
figure10

Scheme of various bottom-up and top-down synthesis [74]. Adapted with permission from ref [74] under a Creative Commons Attribution 4.0 License (http://creativecommons.org/licenses/by/4.0/)

In addition to organic solvent separations, various gas separation membranes are also demonstrated using 2D COF nanosheets. Li et al. [90] exfoliated microporous COF-1 nanosheets (average pore size ~ 0.39 nm) to fabricate ultrathin COF-1 membrane (COF nanosheets layer of ~ 100 nm). The COF-1 membrane was fabricated through solvothermal condensation of 1,4-benzenediboronic acid (BDBA) in a 1,4-dioxane-mesitylene mixture. Their membrane showed the H2 permeance of 10− 6 mol m− 2 Pa− 1 s− 1 (3000 GPU), which surpass the performance of ZIF-8 membrane with 100 nm thickness (5.46 × 10− 8 mol m− 2 Pa− 1 s− 1, 163 GPU). Tong et al. [91] reported molecular dynamics simulation of triazine-based 2D COF membranes (CTF-1) with an average pore size of 12 Å. With different stacking mode, gate closing effect was studied by varying the interlayer distance of COF nanosheets. They simulated the transport behavior of CO2/N2 mixture through their membrane. By tuning the structure of four-layered 2D COF membrane, high CO2/N2 selectivity up to 36 was obtained while maintaining the CO2 flux of 23 molecules/ns. Through their work, tuning the stacking mode of nanosheets can be one of the most effective strategies to fabricate the ultrathin membrane with high permeance and selectivity. Due to its inherently large pore sizes (Schiff based COFs), 2D COF based membranes show preferential applications in organic solvent separations. Pharmaceutical industries or biorefinery where there is a need for solvent-resistant membranes with high permeance of organic solvents are expected to be positively impacted by 2D COF membranes.

Basal plane engineering and surface chemistry of 2D nanocomposite materials

Surface functionalization of GO

The surface characteristics of graphene oxide (GO) has been extensively investigated owing to its unique properties: a tunable chemical structure, pore generation, high permeability and single-atomic thickness with lateral dimensions [92]. It is well-known that GO presents various oxygen-containing functional groups, such as hydroxyl, epoxy, carbonyl, and carboxylic acid groups, on its surfaces, which can be reacted with their corresponding chemical reactions to fabricate high-performance membranes. Those functional groups can be chemically modified with other functional groups using various chemical reactions: amide coupling [93], nucleophilic substitution [94], diazotization [95], silylation [96], etc. (Fig. 11a). Since there are several focused reviews on the surface chemistry of GO sheets, we focus on the surface modifications of GO for membrane applications. The amide coupling reaction has been frequently used to functionalize GO sheets with primary amine groups to introduce positive charges on their surface in a colloidal state, and the negatively charged GO and positively charged GO-NH2 was utilized as a building block to construct multi-layered structures of GO sheets through a layer-by-layer (LbL) assembly process to fabricate a membrane for durable reverse-osmosis application [97]. The resulting LbL multi-layers on a polyamide membrane resulted in significantly improved antifouling properties against proteins and the resistance of membrane degradation by chlorine during a salt rejection process. This amide coupling strategy can be also used to cross-link the assembled GO sheets with lamella-like structures by inter-connection of carboxylic acid groups of GO sheets to improve their mechanical stability. For example, the laminated GO sheets on a polycarbonate membrane were spontaneously delaminated in aqueous media by brief sonication or incubation in basic conditions. However, the cross-linked GO laminates with branched polyethyleneimine (BPEI) were stable in a wide range of pH values with prolonged sonication up to 1 h, and the BPEI cross-linking process did not affect the filtration performance of laminated GO sheets, such as the rejection rate against both negatively and positively charged organic dye molecules [98]. The nucleophile substitution reaction was harnessed for carboxylation of GO and the carboxylated GO (GO-COOH) presented higher water dispersibility and chemical tailorability than pristine GO owing to the increased density of carboxylic acid groups. When the GO-COOH prepared by reaction with glycine was laminated on a polyethersulfone (PES) membrane, its laminated structures provided many wrinkles and hydrophilic surface properties, which was different from pristine GO, which acts as an active water transport channel [99]. As a result, the laminated GO-COOH provided a prominent water flux with improved desalting properties by enhancement of electrostatic repulsion (Fig. 11b). The silylation is also an important chemical reaction in modifying GO with desirable functional groups [96]. As GO presents many hydroxyl groups on its basal plane, it can be easily reacted with diverse silane compounds presenting different functional groups [100]. For the membrane application, the surface of GO was modified with N-(trimethoxysilylpropyl) ethylenediamine triacetic acid (EDTA-silane) to increase the density of carboxylic acid groups [101]. The EDTA-silane functionalized GO (EDTA-GO) exhibited much higher aqueous dispersibility than pristine GO, and furthermore, it can be stably dispersed in water even after chemical reduction (EDTA-RGO). The laminated EDTA-RGO showed high applicability for ion separation with a significantly reduced permeation rate of small cations such as K+ and Na+ (Fig. 11c). The non-covalent approach is another effective strategy for surface functionalization of GO through various secondary interactions, such as electrostatic, hydrogen bonding and hydrophobic interaction (Fig. 11a). GO has a highly negative-charged surface and can be utilized to construct laminated structures by an LbL assembly process with poly (allylamine hydrochloride) (PAAH) [102] and gelatin [103]. The resulting laminated structures exhibited considerably improved performance for water purification and mixed solvent separation. The surface functionalization of GO with a cationic surfactant through electrostatic and hydrophobic interactions improved the forward osmosis process [104].

Fig. 11
figure11

a Surface functionalization of the GO sheet by covalent and non-covalent interactions. b Membrane performance of laminated GO and GO-COOH under the equal condition [99]. Adapted with permission from ref [99]. Copyright 2017 for Elsevier. c Na+ ion permeation through 0.9 μm-thick EDTA-GO and EDTA-rGO membranes (insert: 1 μm-thick EDTA-GO membrane) [101]. Adapted with permission from ref [101]. Copyright 2016 for Nature Publishing Group

Surface functionalization of MoS2

MoS2 is one of the most representative TMDs owing to its physicochemical properties such as single-atomic thickness, tailorable surface, thermal and chemical stability [105]. Despite the high potential, the membrane application of MoS2 has been relatively restricted owing to the difficulty for large-scale preparation of single-layered sheets with a large lateral dimension, but this problem is being addressed by many efforts to improve the exfoliation and functionalization processes of bulk MoS2. Although there is still a debate on the functionalization mechanism, it is well-known that the surface of MoS2 can be readily functionalized with thiol compounds by physisorption or direct coordination to S vacancies of MoS2 (Fig. 12a) [106, 107]. The functionalized MoS2 sheets presented diverse surface properties depending on the terminal groups of thiol ligands, and thus they were highly dispersible in a complex aqueous media [108]. In addition, since the surface of MoS2 sheets was partially oxidized during the exfoliation process, their surface was easily functionalized by a sol-gel reaction with silane compounds [109] or electrostatic interaction of polymers [63] and small molecules [110]. The non-covalent functionalization of MoS2 with poly organic dyes also greatly improved the membrane performance of laminated MoS2 sheets over their pristine counterpart [59]. These previous reports indicated the importance of surface functionalization of MoS2 sheets for application as a membrane material.

Fig. 12
figure12

a Surface functionalization of MoS2 sheets with thiol compounds [107]. Adapted with permission from ref [107]. Copyright 2013 for American Chemical Society. b Exfoliation and hydroxyl functionalization process of h-BN sheets by sonication-assisted hydrolysis [114]. Adapted with permission from ref [114] Copyright 2011 for American Chemical Society. c Exfoliation and amine functionalization of h-BN sheets by urea-assisted ball milling [121]. Adapted with permission from ref [121]. Copyright 2015 for Nature Publishing Group. d Exfoliation process of Ti3C2Tx sheets by chemical etching of MAX phases by using a fluoride-containing agents [126]. Adapted with permission from ref [126]. Copyright 2011 for John Wiley and Sons. e Functionalization of Ti3C2Tx sheets with phenylsulfonic groups by diazotization [130]. Adapted with permission from ref [130]. Copyright 2018 for Elsevier

Surface functionalization of h-BN

h-BN is an attractive 2D material for membrane applications owing to its unique and excellent properties such as high strength, insulation, thermal stability and conductivity and chemical inertness [111,112,113]. Those properties make it promising, but its extremely high chemical inertness has restricted its wide-spread application. Surface functionalization strategies for h-BN can be also classified into covalent and non-covalent approaches. The covalent approach is generally a one-step process in which the exfoliation and functionalization of BN sheets occur simultaneously. The aqueous exfoliation and functionalization of h-BN sheets with hydroxyl groups was achieved through a hydrolysis reaction by prolonged-sonication of h-BN in aqueous media (Fig. 12b) [114], refluxing in concentrated strong acids or bases [115, 116], solution-phase oxygen radical reaction [117], using urea with a ball milling process, using molten hydroxides [118], or direct hydrothermal reaction with hydrogen peroxide. The hydroxylated h-BN sheets can be diversely derivatized using a silylation reaction with various silane compounds [119, 120]. Despite those efforts, the membrane applications of h-BN sheets were restricted owing to their low exfoliation and production yield. By contrast, Lei et al. reported an efficient strategy to synthesize amine-functionalized h-BN (BN-NH2) on a large scale by ball-milling h-BN powder with urea, and the resulting BN-NH2 sheets were stably dispersed at a high concentration in aqueous media (Fig. 12c) [121]. Recently, they also demonstrated that the laminated BN-NH2 sheets can be harnessed as a stable and efficient molecular separation membrane for molecules dissolved in both aqueous and organic solvents with a high permeation rate under acidic, alkaline and oxidative conditions [50, 54]. In addition to laminated BN-NH2 sheets, it was also revealed that BN-NH2 sheets can be directly composited with polypiperazine (PPA) by interfacial polymerization, and the resulting composite membrane exhibited a 13.5% higher permeation rate than a bare PPA membrane without compromising rejection properties against organic molecules [122].

Surface functionalization of MXene (Ti3C2Tx)

Ti3C2Tx is a representative material of the MXene family and the laminated MXene (Ti3C2Tx) sheets have been spotlighted as a promising material for membrane applications based on their well-ordered subnanometer channels [42], hydrophilicity, high water flux [123], salt rejection [124], and anti-biofouling properties [125]. MXene sheets have been generally synthesized by chemical etching of MAX phases using fluoride-containing agents (Fig. 12d), including HF [126, 127], LiF/HCl [128], NaHF2, Na4HF2, and KHF2 [129]. During the etching process, the composition of terminal –O, −OH and –F groups on MXenes varied with the chemical etchants, and it was recently found that LiF/HCl is an efficient etchant to synthesize MXene sheets with a large lateral dimension and a single-layered and –OH group terminated structure [128]. Therefore, the etching process can be regarded as a simultaneous process of exfoliation and surface functionalization for the large-scale production of hydroxylated MXene sheets. The surface of MXene sheets can be further modified with covalent and non-covalent approaches like graphene derivatives. As a covalent approach, Wang et al. reported that the diazotization reaction of MXene sheets sulfanilic acid diazonium salts resulted in enhanced colloidal stability [129] and electrochemical activity (Fig. 12e) [130]. In the case of non-covalent approaches, MXene sheets present a negative surface charge owing to their hydroxyl groups, and thus they can have electrostatic and hydrogen-bonding interactions with poly (diallyldimethylammonium chloride) (PDDA) and polyvinyl alcohol (PVA) [131]. In the same line, the surface of MXenes can be functionalized with polyethyleneimine (PEI) and polydimethylsiloxane (PDMS) and the resulting laminates of PEI- and PDMS-functionalized MXene sheets achieved improvement in mechanical/thermal stability and solvent resistances accompanied by the enhanced transfer of alcohols and the rejection rate of solutes [132]. In addition, the complexation of positively charged Fe (OH)3 colloids with MXene sheets through electrostatic interaction resulted in the formation of expanded nanochannels and then enhancement of the water flux and rejection rate for approximately 2.5 nm-sized molecules [133]. Those previous studies clearly indicated that the surface functionalization of MXene sheets provide more opportunities to develop a multifunctional and high-performance membrane material.

Nanocomposite membranes formed with 2D materials

Nanocomposites formed with 2D materials are also an extended version of the 2D-enabled membranes. At a high-level, these nanocomposites can be classified into two types: 1) Polymer-based nanocomposites and 2) 2D nanocomposites formed with elements other than polymers (GO + MOF, COF + MOF, or COF + COF …). In polymer-based nanocomposites formed with 2D materials, the mixed-matrix membrane (MMM) architecture and the thin film composite (TFC) are the most well-known and studied membrane structure. Thin film composite (TFC) is one of the most representative asymmetric membrane architecture that is made of very thin (usually less than 200 nm) dense polymeric layer (separating layer) is deposited on top of a porous support. Polyamide composited with polyethersulfone (PES) or polysulfone (PS) support membrane is widely used in water purification or desalination systems. For mass production of TFC membrane, various scalable fabrication techniques have been reported such as dual-layer slot coating [134] or the hollow fiber spinning [135]. Compared to TFC membranes, MMMs have better thermal and mechanical stability arising from incorporated nanoparticles (fillers) that reduce the impact of heating and membrane compaction. On the other hands, TFC membranes are described by much thinner separating layer thickness compared to MMMs, TFC membranes are often referred to as high permeance membranes. However, TFC membranes typically suffer from membrane compaction and fouling. To overcome these limitations, TFC membranes are modified with fillers (similar to MMM). The following TFC based composite membranes using 2D fillers have been reported. Li et al. [136] fabricated TFC reverse osmosis membrane modified by 2D laminar MoS2. Due to membrane surface modification of MoS2 nanosheets, the surface of MoS2-TFC membrane showed improved hydrophilicity and roughness. As a result, MoS2-TFC membrane showed high water flux with the anti-fouling property. Dong et al. [137] modified TFC by clay nanosheets. A cationic clay (montmorillonite, MMT) and an anionic clay (layered double hydroxide, LDH) were used for modification of TFC. Likewise, clay-TFC showed hydrophilicity and anti-fouling property because of hydrophilic clays. Especially, MMT and LDH incorporated TFC membranes showed significantly improved the anti-fouling property to protein and cationic surfactant due to their negatively charged surface.

The original concept of the mixed-matrix membrane has evolved from the idea that incorporated filler materials can enhance either the permeability or the selectivity of the polymeric matrix—eventually overcoming the selectivity-permeability trade-off of conventional polymer based membranes. A wide range of fillers has been adopted in MMMs, ranging from nonporous inorganic nanoparticles to highly microporous frameworks including, MOFs and zeolites. Two dimensional materials (graphene, graphene oxide, MXene, 2D MOF, 2D zeolite …) with a high aspect ratio can also be incorporated into a mixed-matrix membrane opening up the possibility to form “ultrathin” composite membrane layers. These 2D fillers provide a tortuous diffusion pathway via stacked lamellar structures. Moreover, it is possible for few nano-meter thick 2D fillers to form a mixed-matrix with a larger volume fraction, which is not possible with the conventional 3D shape fillers.

GO based MMMs

Among various 2D materials, the graphene and graphene oxide family are the most studied materials in nanocomposites such as mixed-matrix membranes. In particular, due to its affinity toward a polymeric matrix and versatile functionality, graphene oxides have been one of the most popular filler choices in the fabrication of MMM. One important issue related to GO synthesis is the non-uniform lateral sizes of the fabricated GO nanosheets. Shen et al. [138] showed the size effects of graphene oxide on the separation performance of MMMs using the small (100–200 nm)−/medium (1–2 μm)−/large (5–10 μm)-lateral sized GO. Researchers used polyether-block-amide (PEBA, Pebax®) as a polymeric matrix and investigated the chain mobility of the GO incorporated polymer matrix. The mobility of the polymer chains was restricted with increasing lateral size of GO, while large-sized GO showed poor dispersion properties in a polymer solution. MMM fabricated with 1–2 μm lateral sized GO exhibited excellent and stable separation of the CO2/N2 pair with CO2 permeability up to 110 Barrer and CO2/N2 selectivity up to 80. Dong et al. [139] reported the use of porous reduced graphene oxide obtained by a dehydration reaction using NaOH as a filler for MMM fabricated with PEBA (Pebax®). Incorporation of the lamellar structure of the porous rGO was advantageous in selectivity enhancement for the CO2/N2 pair, since the hydrated lamellar structure of rGO favorably adsorbed CO2 over N2. Furthermore, the reduction degree of the porous rGO controlled the permeability through the composite membrane by creating enlarged transport pathways for gas molecules. In summary, their MMM showed CO2 permeability up to 119 Barrer and CO2/N2 selectivity up to 100. Shen et al. [140] reported polyvinylamine (PVAm) and chitosan (Cs) based MMM using graphene oxide grafted with hyperbranched polyethyleneimine (HPEI-GO). Amine functionalization via incorporation of HPEI on GO sheets not only enhanced the polymer-GO adhesion properties but also increased the CO2 sorption capacity through reversible chemisorption. Their membrane showed a slightly increased CO2/N2 selectivity (~ 107) with moderate-to-low permeance of 36 GPU. Li et al. [141] introduced the polyethylene glycol- and polyethyleneimine-functionalized GO sheets (PEG-PEI-GO) to form a mixed-matrix membrane with Pebax®. Ethylene oxide and amine functional groups from PEG and PEI, respectively, had an excellent affinity toward CO2. The mixed-matrix membrane showed a much-improved separation performance with CO2 permeability up to 1330 Barrer with CO2/CH4 selectivity up to 45 and CO2/N2 selectivity up to 120 (Fig. 13).

Fig. 13
figure13

a Diffusion coefficient and selectivity, b solubility coefficient and selectivity of N2, CH4, and CO2 in pure polymer membrane, GO based MMM and functionalized GO based MMM. c Robeson plot for CO2/CH4 separation. d Robeson plot for CO2/N2 separation [141]. Adapted with permission from ref [141]. Copyright 2015 for American Chemical Society

Due to the hydrophilicity of the GO sheets, mixed-matrix membranes formed with GO generally have good aqueous or liquid stability, and GO based MMMs are frequently used in water purification or pervaporative separations. The current state-of-the-art membrane process for desalination is illustrated by the interfacial-polymerized polyamide thin film composites. Yin et al. [142] constructed a polyamide thin-film nanocomposite using a GO based polyamide mixed-matrix membrane. Typical interfacial polymerization of polyamide film was performed on the polysulfone support layer with m-phenylenediamine (MPD) and trimesol chloride (TMC). GO nanosheets were dispersed in a TMC-hexane solution layer and the GO was incorporated into the polymeric matrix of the polyamide thin film. Incorporation of the GO nanosheets enhanced salt rejection (NaCl: 93.8%, NaSO4: 97.3%) and water flux (59.4 Lm− 2 h− 1) through restricted interlayer spacing (~ 0.83 nm) of the lamellar structure and further increased the water permeability through the hydrophilic water channel of the GO. Instead of forming a thin-film composite, GO nanosheets were also exploited in a conventional MMM platform for water purification. Ganesh et al. [143] reported the salt rejection of GO based MMM using polysulfone as a polymeric matrix. Insertion of GO into the polymeric matrix have induced the formation of macrovoids in membranes, which is responsible for high water flux. In addition, Yang et al. [144] used graphene dispersed polydimethylsiloxane (PDMS) MMM for pervaporative desulfurization. Due to the abundant population of the π electrons on the graphene nanosheets, CH- π interaction between the high aspect ratio graphene and the PDMS chain was available. A π-π interaction between the thiophene and graphene was also constructed, and a favorable interfacial structure between GO and PDMS was consequently formed. The GO/PDMS membrane showed an improved flux of ~ 6 kg m− 2 h− 1 and a selectivity of ~ 3.5 for applications in pervaporative desulfurization as well as separation of aromatics-containing mixtures.

2D MOF based MMMs

Microporous materials have also been a popular choice for filler material in the fabrication of mixed-matrix membranes. Among various microporous frameworks, MOFs have distinctive advantages over classical zeolite families due to their favorable interaction with a polymeric matrix. MOFs form highly dispersed polymer solutions and can be fabricated into a dense film with significantly reduced interfacial gaps [145]. On the other hand, conventional zeolites form a “sieve-in-a-cage” structure due to its immiscibility with the organic phase [146] (c.f., a polymeric matrix). Rodenas et al. [147] reported the Cu (BDC) (BDC: 1,4-benzenedicarboxylate) MOF based mixed-matrix membrane for CO2/CH4 separation especially focusing on the use of MOF nanosheets as a filler. Bulk (3D) MOF crystals leave a significant fraction of the composite volume unoccupied due to their bulky nature, but 2D MOF lamellae are uniformly distributed over the entire MMM. This uniform distribution of nanosheets throughout the matrix is translated as improved separation performance by eliminating the unselective transport pathways. Moreover, unlike isotropic fillers (nanocrystals or bulk MOF crystals) that cause swelling of the polymer matrix on the uptake of the highly plasticizing CO2, nanosheet loaded MMMs effectively suppressed the swelling and therefore maintained a high CO2/CH4 separation factor (up to 90) at a transmembrane pressure up to 8 bar. Shete et al. [148] also reported the use of Cu (BDC) nanosheets in mixed-matrix membranes. Cu (BDC) nanosheets were prepared in the bottom-up direct synthesis and the synthesized nanosheets had aspect ratios as high as 100 (average lateral size 2.5 μm and thickness of 25 nm). Polyimide (Matrimid®) was used to provide a polymeric matrix and a Cu (BDC) nanosheet dispersed MMM showed much-improved separation performance in terms of CO2/CH4 selectivity compared to neat polyimide membranes. Jungle-gym-like [149] Cu2(ndc)2(dabco) (ndc: 1,4-naphthalenedicarboxylate, dabco: 1.4-diazabicyclo[2.2.2]octane) nanosheets were reported and these nanosheets were blended with polybenzimidazole (PBI) to form a mixed-matrix membrane used in a pre-combustion CO2 capture process. Similar to Cu (BDC), Cu2(ndc)2(dabco) nanosheets showed a larger improvement when incorporated into a MMM compared to bulk 3D crystals. For a high-pressure (up to 5 bars of CO2) pre-combustion CO2 capture process, the mixed-matrix membrane showed H2 permeability up to 6.1 Barrer with H2/CO2 selectivity up to 26. The concept of the mixed-matrix membrane has been further expanded to microporous, rigid polymers such as “polymers of intrinsic microporosity (PIMs)”. Cheng et al. [150] reported a PIM-1 based mixed-matrix membrane with Cu (BDC) nanosheets. Notably, ultrathin mixed-matrix membranes with a thickness of 660 nm have been fabricated with 2D nanosheets and achieved high CO2 permeance (up to 400 GPU) with moderate CO2/CH4 selectivity (up to 15). MMMs with a thickness of 60 μm had a relatively low performance in terms of CO2 permeance (up to 196 GPU) with low CO2/CH4 selectivity. The effect of nanosheets on separation performance of MMMs is dramatically compared further by two model MOFs. Samarasinghe et al. [151] fabricated MMMs containing both 2D nanosheets (Cu (BDC)) and 3D bulk crystals (ZIF-8, ZIF: zeolitic-imidazole framework). MMMs were successfully fabricated without significant defects and showed both enhanced CO2 permeability and CO2/CH4 permselectivity compared to a filler-free polymeric membrane. By incorporating the 2D and 3D fillers together, the disadvantage of the 2D filler (low CO2 diffusivity) can be easily overcome as 3D filler can increase CO2 diffusivity. Moreover, the MMM containing both 2D and 3D fillers incorporated the benefit of the 2D fillers, which is the effective enhancement of selectivity. As a result, this MMM showed improved separation performance with high permeability (3D fillers) and high selectivity (2D fillers).

MXene based MMMs

Similar to other 2D materials, single- or few-layered flakes of MXene nanosheets are capable of forming nanocomposites with polymers. The hydrophilic nature of the MXene nanosheet makes it possible to form a highly stable dispersion in various aqueous or organic media (e.g., aprotic polar solvents) to fabricate 2D nanocomposite membranes [152]. Formation of the highly stable dispersion in organic solvents is directly translated into the formation of non-segregating polymer solutions for further scalable membrane processing. Moreover, as discussed in the earlier sections, the lamellar structure of the 2D MXenes are characterized by the extremely short transport pathway and the large volume of the nanochannel, and nanocomposite membranes based on MXene nanosheets are able to enhance membrane separation performances. Therefore, MMMs based on MXene nanosheets often show very high water permeance (> 1000 Lm− 2h− 1bar− 1) with a favorable dye rejection rate (90% for Evans blue of molecular weight 960, 97% for Cytochrome C of molecular weight 12,000) [133]. Due to its stability under harsh chemical environments, studies on MMMs based on 2D MXenes have focused on liquid phase separations. Han et al. [153] reported a 2D Ti3C2Tx (T: functional groups, O, OH, and/or F) based mixed-matrix membrane and its application in water purification by forward osmosis. 2D MXene was prepared by etching and ultrasonic treatment on its parent Ti3AlC2 structure. The as-synthesized MXene nanosheets displayed a very loose lamellar structure, which provided a preferential transport channel for liquid molecules. It directly affected the water permeance of the fabricated MMM with polyethersulfone (PES). The PES/MXene membrane showed excellent water flux (~ 115 Lm− 2 h− 1) with high dye rejection (~ 92% for Congo Red with a molecular weight of 697). Ti3C2Tx nanosheet based mixed-matrix membranes were further tested in dehydration of conventional organic solvents. Submicron-Thick chitosan (Cs)/MXene mixed-matrix membrane was fabricated on porous polyacrylonitrile (PAN) substrate via a spin-coating method. The loose interlayer channels in the MXene provided a fast and selective transport pathway for water molecules. Their Cs/MXene mixed-matrix membrane showed a total flux of 1.4–1.5 kg m− 2 h− 1 and selectivity up to 1400, 4800, and 900 for dehydration of ethanol, ethyl acetate and dimethyl carbonate at 50 °C, respectively. Han et al. [154] also reported the MXene based cross-linked P84 copolyimide mixed-matrix membrane with improved solvent resistance. Organic solvent nanofiltration (OSN) was demonstrated using a triethylenetetramine (TETA) crosslinked P84/MXene mixed-matrix membrane. The water channel of MXene with good hydrophilicity played a positive role in the overall membrane performance. As a result, this membrane showed high flux (268 Lm− 2 h− 1) and perfect rejection (100%) to gentian violet with a molecular weight of 408. Moreover, the separation performance did not change during 18 days of immersion in acetone, methanol, and DMF, respectively.

Final comments

Rigid, microporous materials and membranes are emerging as a viable class of materials for energy-efficient separation processes. The combination of molecular specificity and chemical resistance put them to meet the challenges inherent in these types of difficult molecular separations. 2D materials like graphene and graphene oxide have already been shown to be successfully fabricated in membrane architecture to separate a number of different gas and liquid mixtures, and there is a rapid growth of sorption and transport data available for these materials that are helping to guide the design of new 2D materials such as MXene, BN, MoS2, and 2D MOFs. However, much of the permeation data through the 2D-enabled membranes is still being gathered under different testing conditions that are not directly translatable to separation performance found in conventional polymeric membranes. Critically, the majority of these 2D materials have not yet been explored in various separation applications, therefore further research input is needed in this area.

We believe that future biofuel production, biorefining, and pharmaceutical separation will continue to integrate more membrane processes into its conventional processes. In pharmaceutical separation process, the highly selective membrane material is needed to remove either APIs (Active Pharmaceutical Ingredients), impurities, or to recover high-value catalysts utilized during synthesis. Optimized reuse of spent organic solvent is also achievable by ultrathin 2D-enabled membranes, where high solvent permeability and resistance required. A key asset of the 2D-enabled membrane is its high permeability (or permeance) that is directly translated into high-productivity of separation processes. Therefore, 2D-enabled membranes are expected to show promising applications in the field that requires organic solvent separations. However, long-term permeation stability and relative robustness of the 2D-enabled membranes should be fully understood for these applications. Biofuel production and biorefining require energy-efficient removal of oxygenate species from various complex feeds. In this regards, 2D-enabled membranes with the hydrophobic surface are required to reduce the energy cost associated with the pervaporative recovery of bioalcohols from fermentation broths. Especially, membrane biofouling from the feed becomes an important issue to ensure the performance lifetime of the membranes. Hence, there is a critical need for fouling-related studies on 2D membranes that focusing on the interaction between biomolecules and different 2D nanosheets since the fouling mechanism on these membranes are relatively unexplored. Although the petrochemical industry has been implementing membrane processes, with more robust and selective membranes further low-energy petrochemical platform can be achieved. Since many of the 2D nanosheets are derived (exfoliated) from its parent chemically-resistant 3D frameworks, these nanosheets are also “solvent-ready” that will find vast applications where chemical resistance is required. Control over the swelling degree is essential to maintain stable separation performance over an extended time period [155]. These chemically and mechanically robust materials will withstand the harsh chemical conditions required to achieve liquid phase hydrocarbon separations. With refined selectivity, 2D-enabled membranes can further be used in reverse osmosis molecular differentiation of organic solvents that have been demonstrated with carbon molecular sieve hollow fiber membranes [156]. Furthermore, since the different 2D building blocks that have different molecular weight cutoffs, membrane cascade systems could be used to successively fractionate complex feeds.

Scalability and quality of the 2D membranes are also critical requirements for industrial applications. Class 1 and 2 membranes can potentially be processed via roll-to-roll production technique on porous flat support or even onto the hollow fiber support. Whereas class 3 membranes at this stage of development are deemed less-scalable. One important issue with class 3 membrane is that CVD grown materials still suffers from intrinsic defects, grain boundaries, and wrinkles that contribute to defective pathways. Even though with very small pinhole defects can compromise membrane performance in selectivity. Atomic-level surface contamination and the mechanism of the pinhole defect formation during synthesis should further be understood. While the majority of 2D-enabled membrane research has focused on developing new membrane materials, this is insufficient to transition these materials from lab scale to commercialization. One important issue is testing 2D-enabled membranes with more realistic feed mixtures. A membrane’s pure component behavior is often not representative of its mixed component performance due to non-ideal component interactions. The development of user testbeds or dedicated user facilities for 2D-enabled membrane prototype testing would also be beneficial for the membrane-based separation areas. This would allow for more rigorous and uniform testing of promising new materials and reduce the cost. In addition to improved testing standards, a diverse portfolio of membranes will be needed to tackle the separation challenges of the future. For 2D-enabled membranes, varied approahces to membrane research and development will be needed to ensure the success of the membrane separations field. We believe these 2D-enabled membranes will continue to revolutionize the field of membrane-based separations by overcoming the limitations posed by conventional materials.

Abbreviations

ACF:

Acid fuchsin

APIs:

Active Pharmaceutical Ingredients

BDBA:

1,4-benzenediboronic acid

BDC:

1,4-benzenedicarboxylate

BN:

Boron Nitride

BPEI:

Branched polyethyleneimine

BSA:

Bovine serum albumin

COF:

Covalent-organic framework

CR:

Congo Red dye

Cs:

Chitosan

CVD:

Chemical-vapor deposition

dabco:

1.4-diazabicyclo[2.2.2] octane

EB:

Ethidium bromide

EB:

Evans blue

EtOH:

Ethanol

FO:

Forward osmosis

GO:

Graphene oxide

h-BN:

Hexagonal boron nitride

HPEI:

Hyperbranched polyethyleneimine

LB:

Langmuir-Blodgett

LbL:

Layer-by-layer

LDH:

Layered double hydroxide

MB:

Methylene blue

MeOH:

Methanol

MMM:

Mixed-matrix membrane

MMT:

Montmorillonite

MOF:

Metal-organic framework

MoS2 :

Molybdenum Disulfide

MPD:

m-phenylenediamine

MSF:

Multi-stage flash

MWCO:

Molecular weight cutoff

MWRO:

Molecular weight retention onset

ndc:

1,4-naphthalenedicarboxylate

NF:

Nanofiltration

OSN:

Organic solvent nanofiltration

Pa:

p-phenylenediamine

PAAH:

Poly(allylamine hydrochloride)

PAN:

Polyacrylonitrile

PBI:

Polybenzimidazole

PDDA:

Poly(diallyldimethylammonium chloride)

PDMS:

Polydimethylsiloxane

PEBA, Pebax®:

Polyether-block-amide

PEG-PEI-GO:

Polyethyleneimine-functionalized GO sheets

PEI:

Polyethyleneimine

PES:

Polyethersulfone

PIMs:

Polymers of intrinsic microporosity

PPA:

Polypiperazine

PS:

Polysulfone

PVA:

Polyvinyl alcohol

PVAm:

Polyvinylamine

PVDF:

Polyvinylidene fluoride

R6G:

Rhodamine 6G

rGO:

Reduced graphene oxide

RhB:

Rhodamine B

RO:

Reverse osmosis

S-rGO:

Solvated reduced graphene oxide

TD:

4,4′-p-Phenylenedianiline

TETA:

Triethylenetetramine

TFC:

Thin film composite

TMC:

Trimesol chloride

TMD:

Transition metal dichalcogenide

Tp:

1,3,5-triformylphloroglucinol

ZIF:

Zeolitic-imidazole framework

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Acknowledgments

This research was supported by Basic Science Research Program through the National Research Foundation of Korea (NRF) funded by the Ministry of Science, ICT & Future Planning (NRF-2018R1C1B6002461). Also, this work was supported by the "International Collaborative Energy Technology R&D Program" of the Korea Institute of Energy Technology Evaluation and Planning (KETEP) granted financial resource from the Ministry of Trade, Industry & Energy, Republic of Korea (No. 20188550000580).

Funding

This research was supported by Basic Science Research Program through the National Research Foundation of Korea (NRF) funded by the Ministry of Science, ICT & Future Planning (NRF-2018R1C1B6002461). Also, this work was supported by the "International Collaborative Energy Technology R&D Program" of the Korea Institute of Energy Technology Evaluation and Planning (KETEP) granted financial resource from the Ministry of Trade, Industry & Energy, Republic of Korea (No. 20188550000580).

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DK designed and coordinated the research and drafted the manuscript. HT participated in the analysis of the emerging 2D materials and classification of 2D membranes and drafted the manuscript. JJ participated in the analysis of nanocomposites fabricated with 2D materials and drafted the manuscript. AC and YKK participated in the analysis of surface chemistry and modification of 2D materials and drafted the manuscript. All authors read and approved the final manuscript.

Correspondence to Young Kwan Kim or Dong-Yeun Koh.

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Keywords

  • Two-dimensional material
  • Membrane based separation process
  • Membrane fabrication