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. 2018 Jun 26;8(41):23130–23151. doi: 10.1039/c8ra03156h

Separation and purification using GO and r-GO membranes

J Lyu 1, X Wen 1, U Kumar 1, Y You 1, V Chen 2, R K Joshi 1,✉
PMCID: PMC9081616  PMID: 35540136

Abstract

Many materials with varied characteristics have been used for water purification and separation applications. Recently discovered graphene oxide (GO), a two-dimensional derivative of graphene has been considered as a promising membrane material for water purification due to its excellent hydrophilicity, high water permeability, and excellent ionic/molecular separation properties. This review is focussed on the possible versatile applicability of GO membranes. It is also known that selective reduction of GO results in membranes with a pore size of ∼0.35 nm, ideally suited for desalination applications. This article presents the applicability of graphene-based membranes for multiple separation applications. This is indeed the first review article outlining a comparison of GO and r-GO membranes and discussing the suitability for applications based on the porosity of the membranes.

This review article outlines a comparison of GO and r-GO membranes for separation and purification applications.graphic file with name c8ra03156h-ga.jpg

1. Introduction

Membrane technology is a separation process which allows certain species to pass through the membrane while restricting the others depending on the properties of the membrane material. Membranes can be classified as dense and porous, according to the driving force and the mode of ionic and molecular movement through membranes. Traditionally it is known that different species permeate at different specific diffusion rates through membranes which depends on solubility, diffusivity,1 and porosity of the membrane as shown in Fig. 1. The smaller molecules could pass through the membrane while the others could be blocked depending on the pore size.2,3

Fig. 1. The transport mechanism for dense membranes (a) and porous membranes (b). Reproduced with permission from ref. 2. Copyright© 2017, Royal Society of Chemistry. Reproduced with permission from ref. 4. Copyright© 2010, John Wiley and Sons.

Fig. 1

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Filtration mechanism based on porous membranes can be further classified as microfiltration (MF, pore size 0.1–10 μm), ultrafiltration (UF, pore size 0.001–0.1 μm), reverse osmosis (RO, pore size < 10 Å) and nanofiltration (NF, pore size 0.5–2.0 nm) membranes.5

Ceramic and polymers are the most common porous membrane materials. Ceramic membranes possess excellent thermal and mechanical properties, but it is difficult to control the pore size precisely with cost-effectiveness.6 In comparison, the polymeric membranes are economic and therefore widely used in MF, UF, NF, and RO with fast permeation and high selectivity.7 However, polymers are hydrophobic, which can easily adsorb organic contaminants causing membrane fouling.8

In comparison to ceramic and polymeric membranes, the new class of membranes based on the recently discovered graphene oxide (GO) offers superior properties, such as high hydrophilicity, outstanding dispersion in water, nanopores, and excellent mechanical behaviour.9 Moreover, reduced graphene oxide (r-GO), another important derivative of graphene, with similar properties as GO has been used in membrane separation technology.

1.1. Graphene oxide

GO is an oxidized form of graphene (GN) that is considered to be the thinnest and strongest material with an extended one-atom-sheet of sp2-bonded carbon atoms.10–12 Graphite oxide which was synthesized from the oxidization of graphite13 can be converted into graphene oxide via exfoliation in ultra-sonicator.14 This is to mention that, the Hummers method is the most common approach for synthesizing graphite oxide, as it offers a high yield. Hummers and Offeman15 used KMnO4, concentrated H2SO4, and NaNO3 as a mixture oxidant to oxidize graphite for a certain time, in which the intermediate product (Mn2O7) is the main oxidant as shown in the equation taken from ref. 16:KMnO4 + 3H2SO4 → K+ + MnO3+ + H3O+ + 3HSO4−MnO3+ + MnO4− → Mn2O7

Graphite oxide consists of layers of GO and can be used to prepare GO flakes via an ultrasonication process.15 GO has a defective graphene plane as well as various oxygen-containing functionalities, such as carboxyl, hydroxyl, and epoxy groups.17 The most widely recognized structure of GO is shown in Fig. 2(b).

Fig. 2. (a) Graphene oxide suspension. Reproduced with permission from ref. 23. Copyright© 2012, Royal Society of Chemistry. (b) The structure of GO according to the Lerf–Klinowski model. Reproduced with permission from ref. 17. Copyright© 1998 Elsevier Science B.V. Reproduced with permission from ref. 24. Copyright© 2012, John Wiley and Sons.

Fig. 2

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The unique structure of GO results in its superior characteristics. Due to the existence of oxygen groups, GO becomes hydrophilic, which could cause GO flakes to form homogenous dispersions with pure water and other polar organic solvents. Fig. 3 shows the stability and solubility of GO in organic solvents.18 Meanwhile, the non-oxidized regions of GO flakes are hydrophobic as pure graphene, which could explain that GO is an amphiphilic material.19 As a result, GO nanosheets perform similar to the surfactants tending GO to stay at the interface of two phases for reducing the free energy.

Fig. 3. Pictures of GO in water and other solvents after sonication for 1 h. Reprinted with permission from (ref. 18). Copyright (2008) American Chemical Society.

Fig. 3

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In addition, GO is likely to react with various chemicals to modify its properties. Also, the defects caused by the functional groups could be beneficial for the passage of water molecules.20–22

1.2. Reduced graphene oxide

r-GO can be produced from GO by removing oxygen-carrying functionalities, which is also named as chemically modified graphene, functionalized graphene, chemically converted graphene, or reduced graphene.25 To date, the common reduction strategies include thermal reduction, chemical reduction, and solvothermal reduction.26

1.2.1. Thermal reduction

This method can further be divided into thermal annealing, microwave and photo irradiation.26 Reducing graphite oxide with a rapid heating (>2000 °C) in a non-oxygen furnace is the thermal annealing method. In this process, two stacked GO flakes could be easily peeled off at a pressure of 2.5 MPa.27 Meanwhile, with the high pressure and high temperature, a large amount of CO and CO2 will be released through removing oxygen from the oxygen-containing functional groups and carbon from the GO's graphene-like region. As a result, wrinkled r-GO flakes are possible to be yielded by furnace heating.14 The thermal annealing is a highly-effective GO reduction method, however, due to the release of CO and CO2, the graphene planes in r-GO nanoflakes prepared by the rapid annealing reduction could inevitably have an effect of structural damage, which leads to a lower conductivity in the r-GO product than that of pure graphene and a resistance for heating GO membranes that are deposited on a low melting-point substrate material. Also, it is obviously an energy-consuming route because it needs a high reaction temperature.28 In addition, with the development of novel heating methods, researchers have tried to synthesize r-GO with microwave- or photo-assistance, which can accelerate the reduction process.29 Zhu et al. spent less than 1 min to achieve the exfoliation and reduction of GO with the assistance of a microwave.29

1.2.2. Chemical reagent reduction

Adding chemical reducing agents is beneficial for the reaction in a moderate condition rather than a high temperature and high pressure as the thermal method needs. Moreover, this process can be achieved in a liquid environment. Conventional reagents are hydrazine, metal hydrides (NaBH4), hydroiodic acid (HI), NaOH, etc. Stankovich et al.30 firstly demonstrated that GO can be chemically reduced by hydrazine. Currently, hydrazine is considered as the most common reductant. Metal hydrides are the other important reagents for the synthesis of r-GO. Unlike hydrazine which can reduce various oxygen-containing groups in an aqueous environment, NaBH4 is a strong reducing agent only in organic solvents, reported by Periasamy et al.31 Meanwhile, Periasamy et al.31 also expressed that NaBH4 can reduce C Created by potrace 1.16, written by Peter Selinger 2001-2019 O bond more effectively compared to other oxygen functionalities, such as carboxyl groups and epoxy groups. Pei et al.32 reported that HI can not only reduce GO membranes, but also maintain their stability. Even though many chemical reagents are toxic and non-environmentally friendly materials, this method is more energy efficient and more beneficial for the synthesis of r-GO membranes than the thermal reduction. Moreover, many researchers are gradually focusing on exploring green chemical reagents such as ascorbic acid (vitamin C), sugars, green tea, etc.33–35

1.2.3. Hydrothermal reduction

This reaction is another emerging reduction route, which is conducted in a sealed container at a certain temperature higher than boiling points of solvents. Under a high temperature condition, the concentration of H+ in solution will be increased, which results in the reduction of GO sheets. Zhou et al.36 illustrated that GO can be converted to stable r-GO aqueous dispersion with hydrothermal method at 50 °C. In this case, Zhou et al.36 also found that the GO suspension at pH = 11 could carry out r-GO solution, while an acidic GO solution (pH = 3) tends to the aggregation of r-GO flakes. Xu et al.37 successfully produced porous r-GO hydrogel via hydrothermal method at 180 °C for 12 h. The prepared r-GO hydrogel offers excellent electrochemical properties. In comparison with the above two reduction strategies, therefore, hydrothermal reduction is a green method and its setup is extreme simple. Moreover, the other advantage is that this method can produce r-GO products with different phases, stable r-GO suspensions graphene hydrogels, which can increase the value of applications.

In comparison with GO, r-GO exhibits more sp2 hybridization. Fig. 4 is the TEM image of monolayer graphene, GO, and r-GO, respectively, which indicates that r-GO possesses a more graphene-like structure than GO. However, unlike the monolayer graphene, r-GO contains defects and oxygen-containing functional groups.

Fig. 4. Aberration corrected TEM images of graphene (a), GO (b), and r-GO (c), in which the perfect sp2 carbon hybridization regions in green, the oxidized areas in grey, and the defects or pores in blue. Reproduced with permission from ref. 38. Copyright© 2010, John Wiley and Sons.

Fig. 4

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Due to the deoxygenation of graphene oxide, r-GO is less hydrophilic than GO. Therefore, an agglomeration phenomenon can easily take place when the highly reduced graphene oxide is dissolved into hydrophilic solvents.29 Surprisingly, various studies indicate that homogeneous r-GO aqueous dispersion could be synthesized. A successful study of r-GO colloid dispersion was demonstrated by Park and his co-workers.40 They obtained a well-dispersed r-GO aqueous solution by chemically reducing a GO suspension in a mixed solution of DMF/H2O.

In order to deeply understand the applications of GO and r-GO membranes for gas separation and water purification, the following contents will demonstrate the conventional synthesis methods, the applications in waste water treatment, sea water desalination, and gas separation using the separation mechanism of GO and r-GO membranes.

2. GO and r-GO membranes

2.1. Conventional synthesis methods for (r)GO-based membranes

Generally, the common synthesis routes of (r)GO-based membranes include spin coating, layer-by-layer self-assembly, and vacuum filtration methods. Moreover, (r)GO composite membranes are commonly prepared by coupling the blending method and the above basic approaches.

2.1.1. Spin coating method

Spin coating is a widely used method for the fabrication of (r)GO-assisted membranes.41,42 Commonly, the first step of spin coating is dropping GO suspension on a base. The second step is rotating the plate with high speed. Consequently, there will be a formation of thin liquid layer which is driven by a centrifugal force.43–45

Nair et al.46 synthesized ultrathin GO films with laminar structure by spin-coating method. They measured the distance between two laminates as ca. 10 Å. The GO semi-permeable membrane possessed an excellent selectivity. Wu et al.47 prepared excellent electrical reduced graphene oxide membrane by spin coating. Meanwhile, they adjusted the thickness of the fabricated membrane via changing the amount of reduced graphene oxide solution on the substrate. Becerril et al.42 compared the properties of different GO membranes prepared by three methods, spin-coating, drop-coating and solvent-induced precipitation. They used glass and quartz as substrate to fabricate GO films. As a result, the GO films fabricated by spin-coating were the thinnest among all products. Kim et al.41 compared the structure of GO membranes which were synthesized by two spinning methods. In the method one, a polymeric substrate contacted GO solution with surface-by-surface. Thereafter, rotating the polymeric substrate facilitated in the removal of extra water resulting in the formation of a thin membrane (Fig. 5(a)). In the other method, a certain amount of GO solution was dropped on the base followed by the spinning (Fig. 5(b)). As a result, as-prepared GO membranes via the second process have a more dense and uniform structure than membranes synthesized by the first method, because water molecules could be removed more by the later approach decreasing the inter-layer spacing of GO membranes and increasing capillary interaction between GO layers. Chang et al.48 coated several layers r-GO which was prepared by a low temperature thermal method, on a SiO2 substrate and the produced r-GO thin film have been used in the application of photodetection.

Fig. 5. (a) and (b) Preparation of GO membrane by two different spinning methods. Reproduced with permission from ref. 41. Copyright© 2013, American Association for the Advancement of Science. (c) Synthetic process of a novel GO membrane by LBL self-assembly method. Reprinted with permission from (ref. 67). Copyright (2009) American Chemical Society. (d) Ordered deposition of GO sheets by vacuum filtration; (e) the mechanism of physically packed GO nanosheets by vacuum filtration. Reproduced with permission from ref. 21. Copyright© 2014, American Association for the Advancement of Science.

Fig. 5

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Spin coating method can easily adjust the thickness and area of membranes by controlling the amount of (r)GO solution and the size of the substrate.

2.1.2. Vacuum filtration

Vacuum filtration process is continuously filtering GO suspension with a strong vacuum pressure and depositing freestanding GO membranes.39,49,50Fig. 5(d) illustrates that lamellar GO sheets can be uniformly deposited by vacuum filtration. The continuous suction force from vacuum pump is able to move water rapidly, which contributes to a strong electrostatic repulsion among GO flakes to overcome the agglomeration of graphene oxide with the formation of ordered laminated GO membranes.24 Mi21 reported pure GO membranes prepared by filtration in a vacuum condition are super tight, with an interlayer spacing of ∼0.3 nm. The thickness, pore size and the spacing between GO nanosheets is tunable.21 Early in 2007, Dikin et al.49 synthesized graphene oxide membranes via vacuum filtration. The thickness of the prepared products was at a micron level ranging from 1 to 30 μm, while they had a high average tensile modulus of 32 GPa. Years later, Eda et al.51 filtered graphene oxide colloidal solution through an ester membrane with pore size of ∼25 nm and obtained ultrathin GO films of ∼1 nm. Joshi et al.52 immersed their fabricated GO membrane in an ionic solution which resulted in the increased interlayer spacings of ca. 0.9 nm. Xu et al.53 filtered the mixed solution of Ti(SO4)2 and GO to obtain GO/TiO2 composite membrane with an average pore size of ∼3.5 nm. Moreover, You et al.54 applied various volumes of GO dispersion to form uniform GO membranes with different thicknesses that are from <1 μm to ca. 10 μm on porous PVDF templates by vacuum filtration.

Han et al.55 deposited chemically reduced graphene oxide flakes by vacuum filtration. The thickness of as-prepared GO membranes was between 22-53 nm and its interlayer spacing decreased to ca. 0.4 nm. By vacuum filtration, the thickness of GO films could be controlled easily. Yang et al.56 utilized HI vapours to chemically reduce their vacuum filtration prepared GO membranes for ions rejection application. Later, Yang57 enhanced the biofouling resistance property of the r-GO membranes. Recently, Zhang and his co-workers58 mixed oxidized carbon nanotube with r-GO dispersion which was synthesized by chemicals reduction, and the mixture solution was filtered for the deposition of rGO-OCNT membranes. Thebo et al.59 utilized vacuum filtration method to prepare r-GO/tannic acid and r-GO/theanine amino acid composite membranes, and they found that all membranes can show a super water permeability (>10 000 L m−2 h −1 bar−1) and stability in water.

To sum up, vacuum filtration method is easy to conduct, by which the thickness of membranes is controllable with adjusted concentration of GO suspension. However, GO papers are fragile when exfoliated from membrane base.

2.1.3. Layer-by-layer (LBL) self-assembly method

In this method, covalent bond and electrostatic interaction are the two main forces for the deposition of stable GO nanosheets.21 Due to the exitance of hydroxyl and carboxyl acid groups, GO flakes possess negative charge.39,60,61 Therefore, there is a strong electrostatic attraction between positively charged substrate and negatively charged GO nanosheets, promoting the deposition of GO sheets.62 Furthermore, these functional groups can react with various compounds achieving the LBL assembly process.63–65 According to GO's amphiphilic characteristic, the hydrophilic substrates benefit the assembly of GO films because they facilitate the formation of one-layer water molecule between the bottom-layer's graphene oxide sheet with substrate, which benefits ordered deposition of GO membranes.24 Otherwise, the pH value of the solution can also influence the microstructure of stacked GO films prepared by LBL assembly method. It is possible to present wrinkles and overlaps connecting the adjacent GO sheets when the GO suspension is acidic. On the contrary, alkaline solution can tend GO to evenly stay in solution rather than at the surface because of the stronger repulsive force, which is beneficial to reduce wrinkles and overlaps.66

Hu and Mi65 prepared a novel GO membrane by LBL method. In this case, 1,3,5-benzenetricarbonyl trichloride acted as linker and the polydopamine-coated polysulfone worked as a support. They demonstrated that the GO membrane had a high flux which is about 4–10 times higher than that of most commercial membranes. Yu et al.62 deposited GO on a polyethylene-terephthalate (PET) base, where the prepared films merely had 2–3 layers of reduced-GO sheets. Shen et al.67 firstly synthesized GO-acrylic acid with negative charges and GO-acryl amide with positive charges. Due to the electrostatic interaction between GO-acrylic acid and GO-acryl amide, they were successful to prepare laminar GO membrane by LBL self- assembly process, and the mechanism is demonstrated in Fig. 5(c).

Compared to vacuum filtration, LBL assembly method is more energy-saving. Meanwhile, the fabricated GO films are more stable than that prepared by vacuum pump.

2.1.4. Other methods

Plenty of alternative methods could be used for the fabrication of (r)GO membranes, such as drop coating, spray coating and dip coating.22,45 As for drop coating and spray coating, the main process of thin GO film formation is dripping or spraying GO dispersion on horizontal substrates and drying afterward.68 Gilje et al.69 spray-coated GO onto SiO2 substrate in which the prepared GO film is more uniform than that of drop-coating. Then, they chemical reduced the GO film with hydrazine at 80 °C. Dip coating is another traditional film preparation method, in which the substrate should be withdrawn vertically from the container. After drying the substrate, a thin membrane can be fabricated.70

Furthermore, blending method is an important approach for hybridization of (r)GO and other components, which is beneficial to synthesize advanced GO composite membranes. Wang et al.71 synthesized a mixture of GO and polyvinylidene Fluoride (PVDF) solution by blending process and prepared GO-PVDF films via casting, which increased the pure water flux from 233.11 L m−2 h−1 (pure PVDF membranes) to 457.86 L m−2 h−1. Zhao et al.72 successfully synthesized a GO/copper oxide/PVDF films with improved hydrophilicity and antibacterial ability of PVDF. Peng et al.73 blended r-GO with SiO2 and filtered the mixture on PVDF membrane. Authors reported that the novel r-GO composite film exhibits superior stability and recyclability for waste water purification.

2.2. Comparison of GO and r-GO membranes

The produced GO or r-GO sheets all exhibit outstanding mechanical properties because of the strong hydrogen bond in the interlayer of GO or r-GO layers. However, even though GO and r-GO have similar structure, GO membranes and r-GO membranes still have distinctions as well as similarities.

2.2.1. Laminated structure

It is a widely-known fact that GO, and r-GO membranes have a lamellar-like structure after the deposition of 2D (r)GO nanoflakes.25,46,49,74 The structures of GO and r-GO films are shown in Fig. 6(a)–(d).

Fig. 6. (a) 1 μm-thick pure GO membrane; (b) the cross-section SEM image of pure laminated GO membrane; (c) 0.2 μm-thick r-GO membrane; (d) the cross-section SEM image of pure laminated r-GO membrane; (e) stability of pure GO laminates, r-GO composites membranes in neutral, acidic and alkaline solution. (a) and (b) Reproduced with permission from ref. 46. Copyright© 2012, American Association for the Advancement of Science. (c) and (d) Reproduced with permission from ref. 74. Copyright© 2014, John Wiley and Sons.

Fig. 6

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2.2.2. Pore size

A critical reason for the utilization of r-GO membranes is that the pore size or interlayer spacing of r-GO films is largely smaller than GO membranes, so r-GO films could be more suitable for desalination. It has been widely reported that the d-spacing of pure GO laminates is ∼0.8 nm,32,52,75,76 while the value for r-GO membranes is only ∼0.35 nm.32,51,74 Joshi et al.52 demonstrated that GO membrane allowed the pure water to pass through but impeded solutes with hydrated diameters larger than the inter-layer spacing (0.9 nm) of GO membranes. However, Park et al. measured the interlayer spacing of GO powder, graphite powder, and r-GO powder.77 In this case, GO has the largest inter-sheet distance of 8.32 Å among the three materials, attributed to its abundant functional groups and inserted water molecules in wet state.78 In comparison, this value for r-GO is only 3.7–3.8 Å. A similar result demonstrated by Liu et al.74 indicated that the interlayer spacing of r-GO reduced by HI was ca. 3.5 Å, whilst that of GO is ca. 8.67 Å.

2.2.3. Permeability

GO membranes were considered as a semipermeable membrane with an extraordinary water permeate rate. In early 2012, Nair et al.46 firstly confirmed that water can transmit through GO membranes without impediment, while blocking other vapours and gases, even the small-sized Helium (He). Hu and Mi65 reported that the LBL self-assembly prepared GO films exhibit a super high water flux of 276 LMH/MPa. Moreover, You et al.54 demonstrated that GO films have a high constant water flux of 65 L m−2 h−1 bar−1. Li et al.79 demonstrated that a 3 nm GO membrane has a high water permeance of 1370 L m−2 h−1 bar−1, whilst the permeance of r-GO membranes is only 0.5 to 1 L m−2 h−1 bar−1. However, when the thickness of r-GO films decreases, water or other gas molecules are permeable.79 Liu et al.74 demonstrated that the water permeance of 100 nm thick r-GO membranes can reach to 57 L m−2 h−1 bar−1. Therefore, compared to r-GO membranes, GO membranes could be more effective for the separation of large size species from water because of GO membranes' higher water permeability.

Theoretically, one-atom-layer materials with highly dense pores show high water flux rate and ions selectivity. Suk and his co-workers demonstrated that pure water could continuously flow through graphene pores with diameters smaller than 1 nm by molecular dynamics simulation.80–82 With this same computational method, a research carried out by Cohen-Tanugi and Grossman82 showed that the single-layer graphene with defect pores was able to reject salt and the water permeability of the porous membranes could reach 2 to 3 orders of magnitude higher than that of traditional RO membranes. However, the preparation of one-layer graphene is restricted due to the lack of advanced technologies. On the contrary, pure GO and r-GO membranes, which possess a lamellar structure with nanochannels and pores, were easier to prepare via depositing micron-scaled layered GO crystallites.13 Moreover, GO or r-GO can also combine with various inorganics and mix with polymers, to improve the performance of (r)GO membranes and enlarge its application in water treatment and gas purification. Tables 1 and 2 demonstrates some GO and r-GO composite membranes for water treatment and gas separation, respectively, and their improved characteristics after adding inorganics or polymers. Therefore, the following sections will review various applications and separation mechanisms of (r)GO membranes in detail, which includes waste water purification, organic solvent nanofiltration, sea water desalination and gas separation.

(r)GO-inorganics (or polymers) composite membranes for water treatment.
Composites Water permeability Improved properties Ref.
Inorganics CNTs/GO 32 L m−2 h−1 bar−1 Enhance the strength and scratch resistance; over 99% of rejection rate for nanoparticles, proteins, sugars, and particularly humic acid 83
SWCNT/GO 720 L m−2 h−1 bar−1 High rejection rate for molecules with size larger than 1.8 nm 84
TiO2/GO 7 L m−2 h−1 Large specific surface area (489.2 m2 g−1 for as-prepared, <10 m2 g−1 for pure GO sheets); ∼100% of dye retention rate 53
TiO2/GO 78 L m−2 h−1 Excellent photocatalytic antifouling 85
Ag/GO Strong antibacterial ability (86% of Escherichia coli be inactivated in 2 h) 86
Ag/polydopamine (pDA) coated r-GO membrane 28.9 L m−2 h−1 Excellent antibiofouling ability 57
Polymers PVDF/GO 800 L m−2 h−1 Over 99% of rejection rate for kaolin in 0.5 h 87
PES/GO 57.6 L nm−2 h−1 Higher hydrophilicity than pure PES 88
pDA coated r-GO membrane 36.6 L m−2 h−1 Improvement of the hydrophilicity of r-GO; 92.0% of salt rejection rate in forward osmosis 56
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(r)GO-inorganics (or -polymers) composite membranes for gas separation.
Composites Separation Selectivity Improved properties Ref.
MoS2/GO H2/CO2 44.2 Higher selectivity than that of bare MoS2 membranes 89
ILs/GO CO2/N2 116 A stable process for the selectivity of CO2/N2 and the permeance of CO2 in 120 h; easer reparation for scalable GO membrane 90
Pebax/GO CO2/N2 91 A smaller interlayer-spacing (0.7 nm) than that of pure GO gas-separation membranes in wet state (0.79 nm) 91
Polyimide/ZIF-8@GO CO2/N2 65 Improvement for the permeance of CO2 contributed by the ZIF-8 92
PEI/GO H2/C3H8 280 Improvement for the preparation of GO membranes by layer by layer assembly method; 11-fold enhancement of H2/C3H8 compared to pure GO laminated films 93
Pebax/r-GO CO2/N2 104 Enhancement for the mixed gases selectivity 94
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3. (r)GO-based membranes for water purification

As a novel multifunctional material, GO-assisted membranes have emerged to deal with waste water as well as to improve desalination technique. Table 2 demonstrates some recent works on water treatment with GO-assisted membranes.

3.1. (r)GO-based membranes for waste water purification

The waste water membrane technology aims to remove dyes, metallic ions, bacterium contaminants. Han et al.55 used vacuum filtration method to prepare r-GO membranes in which some conventional membranes, such as PVDF, acted as substrates. The stacked r-GO films had a high water flux (21.8 L m−2 h−1 bar) but the thickness remained low (∼22 nm). The rejection rate of methyl blue (MB) and direct red 81 (DR 81) using the r-GO membrane is 99.8% and 99.9%, respectively. They reported that the pore size of r-GO sheets played the most important role in rejecting dyes as it is smaller than the size of dye molecules.55 Xu et al.95 doped TiO2 nanoparticles in GO solution to tune the size of channels and pores of lamellar GO sheets. They filtered GO–TiO2 mixed dispersion via vacuum filtration strategy and the as-prepared GO/TiO2 composite films could reject 100% of methyl orange (MO). According to blending method, Zinadini et al.96 fabricated polyethersulfone (PES)/GO hybrid membranes. In this case, GO improved the properties of bare PES, for example, the novel materials had excellent antifouling, hydrophilic ability. Furthermore, blending GO in PES could increase the pore size of prepared sheets, which may possibly increase its water flux, while the rejection rate of dyes would be reduced. Recently, Guan et al.97 combined 3D crystals (UiO-66) with 2D r-GO membranes, in which the 3D porous material improved the water permeability of r-GO membranes. In this work, the pure water permeability of UiO-66-rGO membranes reached to 33 L m−2 h−1 bar−1 and the dye rejection was ca. 89%. Zhang et al.98 deposited various nanoparticles@rGO mixtures including Fe3O4@rGO, UiO-66@rGO, and TiO2@rGO on inner surface of ceramic tubes. The authors demonstrated that these prepared NPs@rGO displayed a super high water permeance of ∼300 L m−2 h−1 bar−1 because NPs enlarge the interlayer spacing, and a high dyes and ions rejection.

Sun et al.99 synthesized GO membranes via simple drop-coating method where they studied the separation process of ions via the as-prepared freestanding GO film. They reported that the rejection abilities of heavy-metal ions were lower than that of non-heavy metal ions as there was a tight interaction (covalent bonds) between the oxygenated functional groups on GO sheets and heavy-metal ions. Joshi et al.52 used vacuum filtration method to prepare GO membranes. They reported that the permeability of GO membranes is related to ions size and the free stacking GO membranes can separate ions with diameter larger than 9 Å. Zhang et al.100 modified GO twice via cross-linking and amine-enrichment to obtain stable structure of GO membranes that were used to block ions. As a result, the novel membrane has a higher rejection rate of divalent cations than that of single valent cations because the prepared membranes are electrically neutral in solvent. As for the separation ability of GO-based membranes for ions, it is not only influenced by the pore or channel size but also related to types of ions charge (positive ions or negative ions).

In addition, the antibacterial activities of GO and r-GO are also reported. Hu et al.101 found that GO and r-GO membranes prepared by a simple vacuum filtration route have antibacterial ability which may possibly restrain the growth of Escherichia coli (E. coli). Liu et al.102 analyzed reasons for the antibacterial ability of GO and r-GO solutions. They cultivated E. coli cells in GO and r-GO suspensions. As a result, GO had a stronger antibacterial ability than that of r-GO because the membrane structure of GO flakes can destroy the structure of bacteria cells. Kanchanapally et al.103 were first to utilize nisin, which is an antimicrobials agent including many –NH2 groups, to combine with GO sheets. They were successful to prepare a novel 3D porous antibacterial membrane. This as-prepared film can be used in identifying, removing and killing methicillin-resistant Staphylococcus aureus (MRSA). Recently, Yi et al.54 prepared pure freestanding GO membrane by vacuum filtration to isolate natural organic matter (NOM) from raw water. On the one hand, the fabricated GO membranes carried out a high constant NOMs water flux (∼65 L m−2 h−1 bar−1 for the first 6 h). On the other hand, they confirmed that bare laminated GO membranes can reject ca. 100% of NOMs. The results are shown in Fig. 7.

Fig. 7. (a): The blue line is the relationship between the penetration time and NOMs water flux of GO membranes (<1 μm thickness), green arrows illustrate the NOMs contents in permeate side lower than detection limit in the first 6 h; (b) the relationship of GO membranes thickness with the NOMs water flux and NOMs contents in permeate side. Reproduced with permission from ref. 54. Copyright© 2017 Elsevier Ltd.

Fig. 7

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3.2. (r)GO-based membranes for organic solvent dehydration

According to Nair et al.,46 GO membranes not only can block gases but also can resist the passage of organic vapours. In recent, therefore, many works are focusing on organic solvent nanofiltration through a pervaporation process. In pervaporation, the feed side which is a liquid mixture in contact with one side of a membrane and the permeation vapor can be removed from the other side of the membrane.104 Due to the different affinities and diffusivities in a film, the components of the mixture feed liquid can be separated.105

Huang et al.106 exhibited that GO membranes supported on a ceramic hollow fiber have a high water permeate rate for water-dimethyl carbonate solutions using pervaporation, in which the water content ranged from 2.6 wt% (feed side) to 95.2 wt% (permeate side). Later, Huang and co-workers107 modified the GO membrane. Authors deposited a highly hydrophilic polymer, N-deacetylated chitin (CS), onto GO laminates that have been coated on a ceramic α-Al2O3 hollow fiber for the water/n-butanol separation using pervaporation.107 In this work, the hydrophilic CS leads to attract more water molecules on the surface of the prepared CS@GO membrane and reduce organic contact with the membrane. As a result, Huang et al.107 obtained a high purity water permeate content of over 99.4% with a super high water flux of over 10 000 g m−2 h−1. The Fig. 8(a) and (b) shows the liquid mixture separation process using the CS@GO membrane and a photo of the membrane. Different from Hung, Lecaros et al.108 based on the hydrophilic property of GO rather than depositing another hydrophilic material onto GO membrane, to achieve acetic acid dehydration, in which poly(vinyl alcohol) (PVA) has been used as a cross-linker to reduce the swelling of GO films and enhance the preparation of a uniform GO membrane. As a result, the GO-PVA film possessed an excellent pervaporation performance, a good water flux of 463.9 g m−2 h−1 and a high water permeate of 97.7%.108 Similarly, Hua et al.109 used various cross-linkers to synthesize a series of GO membranes with different d-spacings for alcohol dehydration. The authors demonstrated that the GOF membranes exhibit a high water permeation of 99.7 wt% as well as an outstanding pervaporation stability for a long time of 160–200 h.

Fig. 8. (a) Schematic of a liquid mixture separation process with the CS@GO membrane. (b) A photograph of a CS@GO membrane. (c) A digital photograph of r-GO/CS membrane in lab scale; (d) a digital photograph of r-GO/CS membrane in large scale. (a) and (b) Reproduced with permission from ref. 107. Copyright© 2015, John Wiley and Sons. (c) and (d) Reproduced with permission from ref. 110. Copyright© 2017 Elsevier Ltd.

Fig. 8

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Additionally, r-GO also plays an important role in organic solvent dehydration. Hung et al.110 mixed chitosan (CS) into r-GO suspension and fabricated r-GO/CS membranes with an orderly stacked lamellar structure by the casting method. The r-GO/CS films can obtain 96 wt% of water in permeate side. Meanwhile, the r-GO composite membranes can be produced on a large scale which is beneficial for the industrial application, and the Fig. 8(c) and (d) illustrate two sizes of r-GO/CS membranes.

3.3. (r)GO-based membranes for desalination

Desalination is a promising technique to solve the fresh water scarcity issue based on isolating pure water from sea water. Recently, graphene-based membranes as a series of versatile materials were studied to improve the seawater desalination technique.82,111,112 Reverse osmosis (RO) was emerged as the greatest desalination technology, which displays a high salt rejection under a certain pressure condition.113 Furthermore, considering that RO is an energy-consuming process, many researchers are also interested in the forward osmosis (FO) technology for desalination. The main benefits of FO technique are low operation pressure, high rejection for various precises, and low membrane fouling problem.114,115

Nicolaï et al.116 utilized MD simulation method to demonstrate that freestanding GO membranes are possible to reject salt with 100% rejection rate in RO process. For experimental results, on the one hand, modifying conventional membranes by doping (r)GO-based materials is a widely used strategy for desalination. For example, Fathizadeh and co-workers117 incorporated polyamide membranes with 0.02 wt./v% nitrogen-modified GO (N-GOQD) to prepare a novel thin RO film that showed a high salt rejection rate of ca. 93%. Meanwhile, the water flux increased when the N-GOQD content grows from 0 to 0.02 wt/v%. Shi et al.118 doped small content of GO into cellulose acetate (CA). They prepared GO/CA composite membranes in which the water flux of the material improved by 129%, which is higher than that of bare CA. Feng et al.119 prepared GO/polyimide membrane via phase inversion process. These membranes displayed a high salt exclusion rate (99.9%) and water flux (36.1 kg m−2 h−1). Depending on LBL assembled method, Kim et al.120 produced aPES/GO/aminated GO nanocomposite membranes, and authors found that the prepared GO composite membrane shows an excellent salt rejection of 98.4% compared to the pure aPES membrane (94.3%) using a 32 000 ppm NaCl solution in feed side. In this work, Kim and co-workers120 also found the water flux of the aPES/GO/aGO membrane is relatively low in a reverse osmosis (RO) process because of the existence of nanoparticle and sulfonated poly material. Recently, depending on the interfacial polymerization route, Li's group121 synthesized polyamide (PA)-GO hybrid reverse osmosis membranes with high NaCl rejection (>99.7%), good antifouling and long-term stability. Authors stated that the d-spacing of GO membranes was declined because the oxygen-carrying groups of GO reacted in the polymerization process as well. Also, the polymerization reaction enhanced the stability of GO membranes. Qian et al.122 applied pervaporation technique which is another promising method to separate salt from high-salinity water using chitosan (CS)/graphene oxide MMMs and the authors illustrated that the diffusivity of salt in the CS/GO MMM is lower than water molecules, leading to a high salt rejection of 99.9%. Additionally, there are some publications on r-GO composite membranes for desalination. Safarpour et al.123 inserted 0.02 wt% of r-GO/TiO2 nanocomposite into MPD/TMC polyamide membranes to improve the NaCl rejection of bare MPD/TMC polyamide membranes.

On the other hand, many researchers are devoted to preparing r-GO laminates for the rejection of Na+ and Cl− ions. Abraham et al.20 studied the effect of channel size between GO laminates on ions exclusion. They synthesized GO/r-GO composites for minimising the swelling of membranes and controlling the channel size in diameter of ca. 0.4 nm and the produced membrane offers a high salt rejection rate of 97%.20 Based on the property of a narrow d-spacing of r-GO membranes, Jia and co-workers124 prepared r-GO films with two reduction steps for salt rejection. The first step was using iron powder that is a mild and “green” reductant and the second step applied hydrazine. In order to obtain r-GO suspension, Jia et al.124 added sulphonation after the first step to introduce the negatively charged SO3− in r-GO flakes and avoid an aggregation phenomenon, and the produced r-GO laminates by vacuum filtration displayed a high removal rate for NaCl (83.4%). Furthermore, Liu et al.74 successfully synthesized r-GO laminates by chemical reducing GO membranes and the authors reported that the interlayer spacing of the prepared r-GO sheets is merely 0.35 nm which exhibit a low Na+ permeation of ∼0.2 mol h−1 m−2. Yang et al.56 partly reduced GO to prepare r-GO membranes with small interlayer spacing (0.345 nm). Then, polydopamine, a hydrophilic material was coated on r-GO sheets for enhancing the hydrophilic ability. After FO experiments of the prepared membrane, pDA–rGO membrane has an excellent water flux (36.6 L m−2 h−1) and a high salt rejection rate (92%) (Table 3).

Summary of recent research on water treatment with (r)GO-assisted membranes.

Targets Membrane materials Synthesis methods Rejection Water permeability Ref.
Dye Methyl orange Pure GO Electrospraying coating 100% 11.13 L m−2 h−1 bar−1 125
Malachite green GO/N+-nylon Drop coating 98% 126
Methyl red Pure GO Vacuum filtration >97% 18.5 L m−2 h−1 bar−1 127
Sunset yellow GO/PFS/pore former Casting 62.3% 245 L m−2 h−1 bar−1 128
Methyl blue GO/oxidized CNTs LBL self-assembly 99.30% 21.71 L m−2 h−1 bar−1 129
Direct blue 14 PEN/GO-PDA Coating 99.80% 99.7 L m−2 h−1 130
Ions Cu(ii) Reduced GO/PDA Vacuum filtration 95.64% ca. 200 L m−2 h−1 131
Cu(ii) PDA/RGO/HNTs Vacuum filtration 99.74% 237.67 L m−2 h−1 132
Cr(ii) GO/chitosan/PSF/PVP Casting ca. 95% 41 L m−2 h−1 133
Cr(ii) PDA/RGO/HNTs Vacuum filtration 99.01% 237.67 L m−2 h−1 132
Na2SO4 GO/CN/TiO-CNT LBL-assembly 67% 16 L m−2 h−1 bar−1 134
NaCl Ag/PDA-rGO Vacuum filtration 66% 28.9 L m−2 h−1 57
Others Bovine serum albumin GO/quaternized PSF >95% 686.16 L m−2 h−1 135
Bisphenol A GO/CN/TiO-CNT LBL-assembly 82% 16 L m−2 h−1 bar−1 134
Oil GO/PDA/MCEM Vacuum filtration 96% ca. 73 L m−2 h−1 bar−1 136
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4. GO and r-GO membranes for gas separation

In addition to water purification, gas separation is another promising application for GO-based membranes. In the study of the water and gases transport for tight GO membranes, Nair demonstrated that He gas could be blocked by these membranes.46 However, with the regulation of related humidity and pore sizes of GO films, gases can be allowed to flow into the GO-based membranes.41

For gas separation, there are two important parameters to define the performance of a membrane. One is the gas permeance rate or permeability which is the speed of target gases travelling through a membrane, and the other is gas selectivity which is the extent for the desired gases separating from the mixture gases. Kim et al.41 experimentally confirmed that GO-based membranes are able to be utilized into gas separation. They synthesized bare GO membranes by two methods. One was coating several laminates of GO to obtain less tight films, while the other method is spin-coating which offered super interlocked membranes. As a result (shown in Fig. 9), they found that the gas permeance through GO membranes was influenced by the water content in membranes. There was a higher gas permeance in a dry state than that in a wet environment. For the GO membranes fabricated by method one, their gas transport performance depended on the molecular weight of the gases. The other highly interlocked GO sheets exhibited a remarkable permeability for CO2 and the order for the penetration of various gases was CO2 > H2 ≥ He > CH4 > O2 > N2. In this case, the CO2 permeability reached a high result of ca. 8500 GPU and the selectivity of CO2/N2 mixtures for GO membranes prepared by the second method was approximately 20.

Fig. 9. (a): The impact of the environment humidity and gas molecular weight on the gas permeance performance of method one GO membranes; (b) the relation between the permeation time and H2, CO2 and H2/CO2 selectivity for method one films; (c) the impact of the environment humidity and the sizes of gases on the gas permeance performance of method two GO membranes; (d) the relationship between CO2 permeability and the CO2/N2 selectivity under various related humidity conditions and there is a comparison with various commercial membranes (CMS, TZPIM, TR, PIM, Zeolite and Silica). Reproduced with permission from ref. 41. Copyright© 2013, American Association for the Advancement of Science.

Fig. 9

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Li et al.79 fabricated GO membranes with different thicknesses by the vacuum filtration method. They reported that the permeant trend of various gases through laminated GO membrane with a ca. 18 nm thickness was H2 > He > CH4 > CO > O2 > N2 > CO2. Meanwhile, they obtained a super high permeance for H2 and He to pass through a 1.8 nm thickness GO membrane with ca. 1000 × 10−10 mol (m2 s Pa)−1.79 Surprisingly, the as-prepared GO membranes also showed an excellent selectivity for 50 : 50H2/CO2, which was over 2000 at room temperature. The selectivity for H2/N2 using GO membranes with different thicknesses was higher than that of commercial membranes. In addition, they found that with the increase of GO membranes' thickness from 1.8 nm to 180 nm the permeance of H2 and N2 would decrease.79 The results are demonstrated in Fig. 10. Shen et al.93 coupled PEI with GO to synthesize GO composite membrane by LBL self-assembly. Due to the intercalation of PEI molecules, the interlayer-spacing of GO/PEI hybrid film (0.76 nm) is slightly higher than that of pure GO sheet (0.72 nm). In this case, as-prepared membranes exhibited a super high selectivity of H2/CO2 and H2/C3H4, which are 6- and 11- fold higher than pristine GO membranes, respectively. Meanwhile, the GO/PEI hybrid membrane also showed excellent mechanical properties; its elasticity modules was ca. 210 MPa while that of bare GO membrane was approximately 150 MPa.93

Fig. 10. (a): The permeability of GO membrane with 18 nm thickness for various gases of different diameters; (b): the influence of the thickness of prepared membranes on the permeance of H2 and He; (c) the relation between H2 permeance and the selectivity of H2/CO2 using various commercial porous membranes and fabricated GO membranes ((1) silica, (2) silicon carbide, (3) MFI Zeolite, (4) ZIF-7, (5) zeolite composite, (6) MFI zeolite, (7) DDR zeolite, (8) silica-titania, (9) MOF, (10) GO). Reproduced with permission from ref. 79. Copyright© 2013, American Association for the Advancement of Science.

Fig. 10

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In addition, Lin and Grossman137 analysed r-GO ultra-thin films for separation with MD techniques. In this work, the authors proved that more nanopores will be created after a thermal reduction and a higher epoxy/hydroxyl ratio and higher annealing temperature can lead to the enlargement of the pore size because more CO or CO2 gases will be released. Meanwhile Lin et al.137 explored that the porous r-GO membrane can only allow the transmission of CO2, whilst resisting CH4. Later, Dong et al.94 synthesized r-GO/Pebax MMMs for the separation of CO2/N2, and they utilized the narrow gas flow channels (∼0.34 nm) of the prepared membrane to enhance the selectivity that is 104. Recently, various attempts have been made by the researchers to modify pure GO or r-GO membrane for gas separation. Therefore, Table 4 replays various recent works on the gas separation of r-GO membranes and their composite films.

Summary of recent research on gas separation with (r)GO-assisted membranesa.

Membrane materials Synthesis methods Membrane thickness Gas selectivity Gas permeability, barrer Ref.
Pure GO Spin coating 20 nm H2/CO2: ca. 240 H2: 3.4 × 10−7 mol (m2 s−1 Pa) 138
GO/K2B4O7/PES Vacuum filtration — CO2/CH4: 75 CO2: 650 GPU 139
GO/PEBA Casting — CO2/N2: 80 CO2: 110 barrer 140
ZIF-8/GO Contra-diffusion 100 nm H2/C3H8: 405 H2: 5.46 × 10−8 mol (m2 s−1 Pa) 141
H2/N2: 11.1
UiO-66-NH2/GO Vacuum filtration 1.9 μm H2/N2: 9.75 H2: 3.9 × 10−8 mol (m2 s−1 Pa) 142
H2/CO2: 6.35
(PDMS)/GO Casting and thermal treatment ca. 100 μm CO2/N2: 24 CO2: 27.7 barrer 143
Pebax/ZIF-8/GO Casting and thermal treatment 55–65 μm CO2/N2: 47.6 CO2: 249 barrer 144
Pebax/r-GO Solution-casting 45–60 μm CO2/N2: 104 CO2: 119 barrer 94
Pure GO Spray coating 1 μm H2/CO2: 20.9 H2: 2.7 × 10−8 mol (m2 s−1 Pa) 141
PEI/GO LBL assembly 1 μm H2/CO2: 30 H2: 1000 barrer 93
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a

1 GPU = 1 × 10−6 (STP) cm3/(cm2 s cmHg); 1 barrer = 10−10 cm3 (STP) cm/(cm2 s cmHg); STP: standard temperature and pressure.

5. Filtration mechanisms using laminar-structure (r)GO membranes

5.1. The mechanism for water purification

GO membranes offer a high-water permeability and remarkable selectivity.20,34,65 First of all, scientists have reported that the reason for fast water flow rate of GO is the existence of the pristine regions (hydrophobic areas). The theory is similar to the passage of water through smooth CNT.145 On the one hand, the larger slip length of CNT will have a higher water molecules' speed.146 Falk et al.147 predicted the graphene possesses a high slip length (80 nm) in theory. On the other hand, water diffusion in hydrophobic parts of GO laminates' nano-channels is similar to the single-file diffusion type.148 It leads to the transportation mode of one-chain water molecules combined with H-bonding (the motion illustrated in Fig. 11(a)). Furthermore, water molecules in this diffusion mode can be transferred to tiny ice crystals, which cause a weak attraction between water molecules and GO pristine layers and promote the passage of water.149 Consequently, water in non-oxidized area, which is a graphene-like region, has a high pass velocity.

Fig. 11. (a) The schematic of monolayer water molecules in single-file type; (b) transport theories of water molecules through pristine regions and oxidized regions of GO membrane. (c) Transport process of molecules with different sizes. (a) Reproduced with permission from ref. 146, licenses address https://www.creativecommons.org/licenses/by/3.0/legalcode. (b) Reproduced with permission from ref. 46. Copyright© 2012, American Association for the Advancement of Science.

Fig. 11

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In addition, the structure of nanocapillaries in GO membranes contribute to the entrance of pure water into inter-channels or defect pores of GO membranes.150 A strong capillary-like pressure proves that ions and molecules flow through GO channels.55 Nair et al.46 simulated the water dynamics in GO layers. Fig. 11(b) shows that there are oxidized and pristine parts in every GO sheet. They explained that the capillary-like pressure was possibly formed by pristine graphene layers, so water molecules can move faster in pristine regions than in oxidized areas. Meanwhile, the hydrogen bond between oxygen-containing functional groups and water molecules acts as the driving force for water molecules moving inside the membranes.

For the selectivity of GO membranes, Fig. 11(c) illustrates its permeation and separation mechanism.20,34,65 The nano-level defects and channels in GO films play a key role in molecules rejection. Theoretically, the interlayer spacing of GO sheets is ∼0.8 nm in a dry environment. Even though, it will be enlarged to ∼1.3 nm in an aqueous environment, it still can resist most of particles with different diameters and allow pure water molecules to pass through.52 Therefore, GO membranes are able to deal with all sorts of water contaminants.

Additionally, thanks to the adjustable GO inter-channels, GO membranes are ideal for both waste water treatment and sea water desalination. With the decrease of nanochannels, the ions and molecules permeation rate will reduce rapidly, while it is hard to influence the water permeation.20 Mi reported that when a membrane's spacing is below 0.7 nm, it can be used in desalination because the diameter of hydrated Na+ is ca. 0.72 nm.21 When the channel size of a membrane is smaller than 2 nm, it can only be used in waste water treatment. At the same time, various works have claimed that the inter-layer spacing of GO sheets is tunable via partly reducing GO flakes or inserting different molecules with various diameters.

Additionally, the humidity can impact GO membranes' inter-sheet distance because of a swelling phenomenon. Abraham et al.20 confirmed the swelling effect clearly. Fig. 12(a) demonstrates that the interlayer spacing is increasing depending on the increase of relative humidity (RH) of fabrication surrounding. When the RH is 0%, GO laminates' interlayer spacing is ca. 0.64 nm, while it is approximately 1.37 nm when immersed in water.

Fig. 12. (a) The influence of humidity on GO sheets' interlayer spacing, carried out by XRD (inset); (b) interlayer spacings of pure graphene oxide membranes (GOMs) after immersing in pure water and other solutions (KCl, NaCl, CaCl2, LiCl and MgCl2); (c): Interlayer spacings of GOMs soaked K+ after dropped in the same ions solutions; (d) the sizes of various r-GO membranes' interlayer-spacing; (e) water loss from containers covered by GO, thermal-reduced GO, HI-reduced GO, and VC-reduced GO films; (f) the moisture permeability of GO and various r-GO films. (a) Reproduced with permission from ref. 20. Copyright© 2017, Springer Nature. (b) and (c) reproduced from ref. 22. Copyright© 2017, Springer Nature. (d)–(f) adapted from ref. 151. Copyright© 2014, Springer Nature.

Fig. 12

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Chen et al.22 were successful to control the interlayer spacing by various cations. They compared the spacings of pure GO membranes (GOMs) immersed in DI-water and ions solutions with that of KCl-GOMs immersed in the same solutions. The result illustrates that the interlayer spacings of KCl-GOMs dropped in different salt solutions have a visible decrease. Importantly, all of the interlayer distances are almost equal to that of pure GOM immersed in KCl solution (Fig. 12(b) and (c)). Yang et al.56 decreased GO's interlayer distance from 0.7 nm to 0.345 nm via reducing GO. At the same time, in order to keep the reduced GO membranes water permeation rate, Yang56 coated dopamine on the top of GO membranes to improve its hydrophilicity. They obtained a high salt rejection (92%) and water flux (36.6 L m−2 h−1 bar−1).

For the pure r-GO membrane, generally the water permeation is likely lower than that of the GO laminate because the d-spacing of a r-GO membrane is merely ∼0.35 nm that is too narrow to allow water, gases and other molecules transmitting through the membrane. For example, Su et al.151 deposited freestanding GO and r-GO films with a thickness of ∼0.5 μm and the authors confirmed that the bare GO membrane is permeable for water while all the r-GO membranes are almost impermeable (the results are shown in Fig. 12). They explained the narrower interlayer spacing is a main reason, meanwhile Su et al.151 reported the defects created by reduction in r-GO could be the only diffusion pathway. The authors demonstrated that the interlayer spacing of three r-GO films, thermal-reduced GO film, HI-reduced GO film and CV-reduced GO film, are similar in Fig. 11. However, the thermal-reduced GO membrane can allow some water molecules transmitting rather than the other chemical-reduced GO films entirely blocking water (shown in Fig. 12(e) and (f)) because a thermal reduction process is possible to release CO or CO2 creating more defects. Moreover, Lin et al.137 proved that a thermal reduction method is attributed to form nanopore in r-GO flakes with MD simulation.

In addition, the ultrathin r-GO membranes are able to allow the passage of water molecules which have been reported by Liu et al.74 The authors synthesized freestanding 100 nm thin r-GO membranes and the water permeability of the prepared film is 57 L m−2 h−1. Meanwhile, the ultrathin r-GO film displayed a high Na+ rejection. Su et al.151 also obtained a high ion rejection for HI-reduced GO film. According to Liu,74 the high rejection was attributed to the narrow distance between r-GO layers and the water pathway is also the inter-channels which is same as GO laminates.

5.2. The mechanism for gas separation

The major conventional gas separation membranes are nonporous membranes, such as polymeric membranes, which are dependent on the solution-diffusion mechanism.152 However, some porous membranes with nano-level apertures can also be used in gas separation. When the diameter of target gas is larger than the pore size, the gas would be impeded, which is considered as the molecular sieving process.153 Furthermore, when the pores are below 1 μm,154 the gas transport mechanism could be regarded as the Knudsen diffusion. Knudsen diffusion for gases indicates that within a diffusion in solid circumstance, if the pore size is equal to or smaller than the mean free path of the gases, these gas molecules are more likely to collide with the wall of the solid's pores rather than collide with each other. Thus, the resistance for gas permeance mainly depends on the collision between gas molecules and the pores wall. It is expressed as the following equation:93,1555.2.where J is the permeance rate through the membrane, KB is the Boltzmann constant, Mw, P and T are the molecular weight, the pressure and the temperature, respectively. Therefore, the gas permeance is inversely proportional to the square root of gas molecule weight.

Due to the porous structure of GO or r-GO films, the gas permeance mechanism could be regarded as the Knudsen transport. Guan et al.156 used pure GO membranes prepared by spray coating to investigate gas permeation and separation. They expressed that the results for H2, CH4, N2, and O2 had a Knudsen diffusion behaviour because the molecular sizes of these tested gases are smaller than the interlayer spacing of GO sheets (0.49 nm). Meanwhile, authors reported that the permeance for CO2 is relatively low because of the membrane adsorption performance of CO2. Kim et al.41 prepared pure GO films by two methods (Fig. 5), in which the GO membranes fabricated by the method one exhibited a heterogeneous microstructure because of the electrostatic repulsion force between the edges of GO flakes. Authors concluded that the gases' diffusion processes obeyed the Knudsen law except CO2. With the increase of molecular weight, the gas permeances for various gases with different molecular weight were decreasing. Moreover, they explained that GO membranes would absorb CO2 because of the attraction force between CO2 and carboxyl or hydroxyl on r-GO flakes, which has also been reported by other research.52,54,119,157 The results from Kim are demonstrated in Fig. 9(a).

Besides the inversely proportional relation between the gas permeance and the gas molecular weight, Kim and his co-workers41 expressed that increasing the number of pores on GO basal planes can improve the gas permeability. In this work, the prepared r-GO membrane after a heating treatment exhibited more pores and narrower inter-channel distance than pure GO films because of the movement of oxygen-containing functionalities and the release of CO2 and CO from GO films. According to the Fig. 13(a), at 130 °C to 140 °C the amount of CO2 reached the peak, which created more pores on r-GO flakes and led to a rapid growth of He permeance. Meanwhile, there was a similar tendency of H2 permeance as He as a function of temperature in this case. Fig. 13(b) also shows a slight increase in the CO2 permeability at the temperatures above 140 °C.41

Fig. 13. Two gas transport pathways in laminar GO membranes. Reproduced with permission from ref. 158. Copyright© 2018 Elsevier B.V.

Fig. 13

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Additionally, Li et al.79 concluded that the permeation of hydrogen and helium can be reduced with the increase in the thickness of GO membranes from 1.8 nm to 180 nm. The result also verified Nair's work that the He gas can be blocked by 500 nm-thick GO membranes. In this content, Li et al.79 also found that the size of the inter-layer spacing of GO membranes was not a major factor for the gas permeability unlike water filtration process where it plays an important role. Authors measured the permeance rates of various gases though GO membranes and r-GO membranes, respectively, and they obtained similar results.

In recent, Ibrahim and Lin158 explored the mechanism of gas separation through GO laminates. Different from the previous result that CO2 permeation through GO membranes disobeyed Knudsen diffusion, the permeation processes for large gas molecule, such as CH4, N2, and CO2, performed a Knudsen diffusion behaviour, while that for small gases (H2 and He) were higher than the gases' theoretical Knudsen permeance. The two authors explained that there were two possible pathways for gas transport in GO membranes, which are demonstrated in Fig. 13. The model A is a winding path that consists of inter-channels, defects on GO basal planes, and nano-gaps between adjacent GO flakes. The model B is an approximately straight narrow tunnel. Therefore, the overall gas permeance for a GO membrane is contributed to the two pathways. At room temperature, the major large gases transmitted through the pathway A because its diffusion activation energy (Ed) in the model A is smaller than that in the second transport road and the gas flow through passageway B can be ignored. Thus, the diffusion for large gas molecules was same as the Knudsen diffusion. However, besides a high permeability of H2 and He through the pathway A, the small gases permeance through pathway B also showed a considerable value.

Compared with other uniform porous membranes, the gas separation mechanism for GO or r-GO laminates remains unclear because the actual micro-structures of r-GO membranes are different when the conditions for r-GO suspensions or the membrane synthesis method change.

6. Conclusions

In summary, GO has been considered as a promising membrane material for water purification and separation applications with its excellent hydrophilicity, considerable defects, pores structure, and nanosized flakes. Through some physical routes, such as spin coating, drop coating, dip coating, layer-by-layer deposition and vacuum filtration, GO flakes can be stacked uniformly to form GO membranes with laminar structure.

It is noteworthy that the nano-channels of multilayer GO sheets are controllable, which can be realized by reduction to form r-GO or reaction with polymers or nanoparticles. These modifications of GO are likely to overcome the swelling phenomenon of GO sheets in water environment. Thanks to the tunable inter-sheet distance, the laminated membranes can achieve the selection of gases and separate pollutants with different sizes from waste water, even the small hydrated sodium ions. In the future, there is no doubt that GO related membranes are favourable candidates for blocking ions and molecules. Still, further studies need to be done like the ionic/molecular transport behaviour along the nano-channels of GO membranes and the trade-off between ionic/molecular selectivity and permeability in GO related membranes.

Conflicts of interest

There are no conflicts to declare.

Supplementary Material

References

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