Yuanyuan
Wang
,
Zhenhua
Niu
,
Yangyang
Dai
,
Peng
Mu
* and
Jian
Li
*
Key Laboratory of Eco-functional Polymer Materials of the Ministry of Education, College of Chemistry and Chemical Engineering, Northwest Normal University, Lanzhou 730070, P. R. China. E-mail: pengmu2019@nwnu.edu.cn; jianli83@126.com; Tel: +86 9317970806
First published on 27th January 2023
Transition metal carbides/nitrides (MXenes) are emerging two-dimensional (2D) materials that have been widely investigated in recent years. In general, these materials can be obtained from MAX phase ceramics after intercalation, etching, and exfoliation to obtain multilayer MXene nanosheet structures; moreover, they have abundant end-group functional groups on their surface. In recent years, the excellent high permeability, fine sieving ability and diverse processability of MXene series materials make the membranes prepared using them particularly suitable for membrane-based separation processes in the field of gas separation. 2D membranes enhance the diversity of the pristine membrane transport channels by regulating the gas transport channels through in-plane pores (intrinsic defects), in-plane slit-like pores, and planar to planar interlayer channels, endowing the membrane with the ability to effectively sieve gas energy efficiently. Herein, we review MXenes, a class of 2D nanomaterials, in terms of their unique structure, synthesis method, functionalization method, and the structure–property relationship of MXene-based gas separation membranes and list examples of MXene-based membranes used in the field of gas separation. By summarizing and analyzing the basic properties of MXenes and demonstrating their unique advantages compared to other 2D nanomaterials, we lay a foundation for the discussion of MXene-based membranes with outstanding carbon dioxide (CO2) capture performance and outline and exemplify the excellent separation performances of MXene-based gas separation membranes. Finally, the challenges associated with MXenes are briefly discussed and an outlook on the promising future of MXene-based membranes is presented. It is expected that this review will provide new insights and important guidance for future research on MXene materials in the field of gas separation.
At present, several solid-state materials are widely used in the field of gas separation, which exhibit a good performance, as shown in Table 1.
Material | Advantage | Prospect | Application | Ref. |
---|---|---|---|---|
Graphene | Single atoms and can be prepared as high permeability and thin membrane | Synthesis of high flux selective gas separation membranes | Ion-gated graphene film | 31 and 32 |
GO | Hydrophilic 2D crystalline nanostructures contains oxygen functional groups | Capable of efficient CO2 separation | SDBS-modified GO membrane for gas purification technology | 33 and 34 |
g-C3N4 | 2D layered material, capable of synthesizing ultra-thin layered nanochannels with selective loading of different active ions | Preparation of high selectivity separation membranes | A novel SILM was constructed by IL through nano-constrained [EMIm][AcO] in the 2D channel of g-C3N4 | 35–37 |
BNs | High specific surface area, abundant structural defects, low density and excellent chemical inertness | Preparation of high permeability separation membranes | A novel BN nanosheet-supported magnetic ionic liquid membrane (BN-SMILM) was constructed by confining nano MIL [P6,6,6,14] [FeCl4] to 2D nanochannels | 38–40 |
MOFs | Ligand compounds with tunable, designable and functionalizable nanospaces | Preparation of high permeability and high selectivity separation membranes | Design and preparation of novel MOF-based hybrid films on tubular ceramic substrates to form thin and compact MOF/silicone nanocomposite films | 41–43 |
COFs | An emerging class of porous crystalline materials with tailored functionality and carefully designed stable and ordered frameworks | Achieving efficient CO2 capture to mitigate the greenhouse effect | Most likely a viable alternative to MOF, thus meeting the multifaceted requirements for activation and conversion of CO2 | 44 and 45 |
… | … | … | … | … |
In addition to these common materials, with the development of scientific research, other types of materials are also used in the field of gas separation, such as 2D transition metal sulfides (TMDs).46 In summary, 2D materials with nanoscale thickness play an important role in membrane separation technology. In nanomaterial science, 2D nanostructures are very attractive for the fabrication of nanodevices due to their high surface-to-volume ratio and good compatibility with device design.47 Moreover, 2D materials enable the development of high-performance separation membranes due to their planar laminar flow structure, high spreading chord ratio and tunable surface features. Thus, they are important materials for advanced molecular separation. The extraordinary permeability of membranes prepared using these 2D materials opens up new avenues for the ultra-fast and highly selective separation of water and gases. Consequently, an increasing number of researchers have devoted their efforts to synthesizing and functionalizing 2D nanosheets in a controlled manner to obtain materials with enhanced performance.48–55
Interestingly, a new group of highly promising 2D materials, called transition metal carbides and nitrides (MXenes), have attracted interest from many researchers in the last few years due to their easy-to-produce 2D structure, tunable surface chemistry and interlayer spacing. Ti3C2Tx was first reported in 2011, and in the decade since, it has been increasingly widely used in various synthesis procedures and applications.56–59 As a new type of 2D ceramic nanosheet, MXenes are being investigated and widely applied in the fields of sensors, electrochemistry, medicine, biology, energy and electronics.60–63 Simultaneously, they have also been investigated for practical applications in various research fields, such as lubricants, photodetectors, solar cells, energy harvesting and storage, as shown in Fig. 1.64–71 Presently, MXenes are considered as molecular barriers with ultra-thin atoms because of their several atomic-thick layers. Consequently, they can be employed for the synthesis of outstanding high-performance barrier separation membranes, thus showing promise for realizing higher permeability properties.72,73 The unique properties of MXenes lead to new applications compared to other 2D membrane nanomaterials, such as graphene and zeolites. Generally, three strategies are employed for the preparation of MXene-based membranes: (1) MXenes are used as skeleton materials to directly prepare 2D membranes with a layered structure; (2) different polymers or nanomaterials are combined with MXenes to prepare composite membranes; and (3) MXenes are used as coating materials to modify the original support layer to prepare membranes. The MXene composite films prepared using the above-mentioned methods possess randomly stacked adjacent nanosheets, forming disordered interlayer “nanochannels” for mass transport between them. The interlayer stacking enables the passage of molecules, thus achieving the selective separation of large molecular compounds, while also allowing small molecules to move between the channels, which is a process known as “molecular sieving”.74–76 MXenes have high energy saving separation performance due to their structure and special chemical surfaces, and their modifiable property allow the prepared membranes to exhibit superior performances in a variety of separation sciences. This has created numerous opportunities for researchers to fabricate novel materials, such as energy-efficient membranes for various engineered separations.77 In recent years, the excellent chemical, mechanical, optical and separation properties such as remarkable flexibility, hydrophilic surface, high mechanical strength and good electrical conductivity of the MXene series materials have made them suitable for a wide range of membrane-based separation processes.78–84 Their applications include gas separation, pervaporation, desalination and solvent/water separation.85–88 Nonetheless, the application of MXenes in gas separation membranes is still in its infancy.
Herein, we review the research related to 2D MXene nanomaterials and the separation membranes prepared using them. Firstly, the basic structure, synthesis and functionalization of MXenes are briefly introduced (section 2). Then, the properties of MXene-based films are summarized and reviewed, as well as the structure–property relationship (effect of structure on performance) of MXenes in their design and fabrication (section 3). Finally, a comprehensive summary of MXenes is presented, including the gas separation performance of various MXene membranes, their advantages and disadvantages in the field of gas separation, the remaining challenges that need to be urgently addressed, and the future prospect of this discipline (section 4).
Fig. 2 (a) MXene preparation process. (b) AFM of Ti3C2Tx MXene flakes. Reprinted with permission.75 Copyright 2018, Springer Nature. (c) XPS survey of Ti3C2Tx MXene. Reprinted with permission.97 Copyright 2018, Elsevier. (d) SEM of Ti3C2Tx MAX phase. (e) SEM of multilayer Ti3C2Tx MXene. Reprinted with permission.94 Copyright 2012, the American Chemical Society. (f) TEM of Ti3C2Tx MXene flakes. Reprinted with permission.95 Copyright 2016, the American Chemical Society. (g) EDX of Ti3C2Tx MXene. Reprinted with permission.96 Copyright 2018, Elsevier. |
(1) |
Ti3C2 + 2HF = Ti3C2(F)2 | (2) |
Ti3C2 + 2H2O = Ti3C2(OH)2 + H2 | (3) |
Ti3C2 + 2H2O = Ti3C2(O2) + 2H2 | (4) |
Fig. 4 Principle and product characterization by HF etching. (a) Schematic diagram of the exfoliation process of Ti3AlC2, showing the substitution of Al atoms by –OH after reaction with HF. (b) XRD images of Ti3AlC2 and ultrasonically exfoliated nanosheets before and after HF treatment. Reprinted with permission.113 Copyright 2011, John Wiley and Sons. (c) SEM images of: (i) Ti3AlC2 particles, which are typical of the unreacted MAX phase, (ii) Ti3C2Tx, (iii) Ti2CTx, (iv) Ta4C3Tx, (v) TiNbCTx, and (vi) Ti3CNTx. Reprinted with permission.94 Copyright 2012, the American Chemical Society. |
Fig. 4b shows the XRD spectrum of MAX during etching. It can be clearly seen that after reacting with HF, the characteristic peak of Ti3AlC2 at about 39° disappeared, and the (002) peak also shifted to a smaller angle. It can be calculated from the following Bragg eqn (5) that the etching process increased the original interlayer spacing of Ti3AlC2.115
nλ = 2dsinθ | (5) |
In the etching process, the HF concentration, etching temperature and etching time have important effects on the etching degree and morphology of products. Alhabeb et al. studied the etching of Ti3AlC2 at room temperature (RT) using HF etchants with different concentrations and different etching times (e.g., 5 wt% 24 h, 10 wt% 18 h, and 30 wt% 5 h). The results showed that the etching time of MAX was shortened and the etching efficiency was improved under the condition of high HF concentration. The morphology of the 5 wt% HF-etched product, as shown in Fig. 5a, was almost the same as that of the Ti3AlC2 precursor. The XRD image, as shown in Fig. 5b, shows the formation of Ti3C2Tx, which indicated that the formation of the accordion morphology was not a sign of the successful etching of MAX to obtain MXene.90 Although the morphology of Ti3C2Tx etched with HF at different concentrations was obviously different, the characteristic (002) peak of the product was also located at 9.0°, and the interlayer spacing was 9.7 Å, reflecting that there was no relationship between the fluffiness of the accordion-like structure and the interlayer spacing of the MXenes. Additionally, given that the surface end groups of Ti3C2Tx were formed during the etching process, the concentration of HF had a great influence on the type and content of surface end groups.116 As shown in Fig. 5c, the characteristic (00l) peak of Ti3AlC2 gradually disappeared when the etching time was extended and the etching temperature was increased. Ti3AlC2 was etched in 50 wt% HF for 2 h, and the characteristic peak at around 39° completely disappeared when the temperature reached 50 °C. To obtain the same result, complete etching of Ti3AlC2 was achieved by simply extending the etching time to 15 h at room temperature. In addition, the (002) peak of the prepared Ti3C2Tx shifted to a lower angle with an increase in the etching time, indicating that the interlayer spacing gradually increased.104 Hence, when using this method to synthesize MXenes, an appropriate HF concentration, etching time, temperature and other conditions should be selected according to different product requirements to better achieve the desired goal.
Fig. 5 Influence of different synthesis parameters on MXenes studied using the HF etching method. (a) Scanning electron microscopy images of Ti3AlC2 (MAX) powder, showing dense layered structures and multilayer Ti3C2Tx powder synthesized from 5, 10 and 30 wt% HF. (b) XRD spectra of Ti3C2Tx MXene powder and Ti3AlC2 powder synthesized from 5, 10 and 30 wt% HF etchants. Reprinted with permission.90 Copyright 2017, the American Chemical Society. (c) Diffractograms were obtained after etching the Ti3AlC2 powder using 50% HF solution, with diffractograms at different temperatures on the left and diffractograms at different times at room temperature on the right. Reprinted with permission.104 Copyright 2013, Elsevier. |
The HF etching method is simple, performed at low reaction temperature, and suitable for etching the MAX phase containing Al and some non-MAX phases. Nevertheless, HF etchants are an issue because of their high corrosion, toxicity, operational risks and adverse environmental impact. Moreover, the surface of the etched product has a large number of –F groups, which are not favorable for energy storage.117,118
LiF(aq) + HCl(aq) = HF(aq) + LiCl(aq) | (6) |
Due to the fact that the in situ HF etching process avoids the direct use of HF, this method has the advantages of simple operation, energy saving, and avoiding certain chemical risks during the etching process.
Acid/fluoride salt etching is the most common method for in situ HF etching, which refers to the selective etching of Ti3C2Tx on the MAX (Ti3AlC2) phase with hydrochloric acid and fluoride salt.103,107 When HCl/LiF is used as the etchant, the Li+ ions can be spontaneously embedded between MXene layers. The intercalation of the metal ions increases the layer spacing between the MXene sheets, thus weakening the interaction between them, which eventually leads to the delamination of the MXene sheets during the washing process after they are etched.90 In 2014, Ghidiu et al. first reported that HF was formed in situ with HCl/LiF solution at 40 °C for etching Ti3AlC2.120 This method had successfully produced Ti3C2Tx conductive clay with strong plasticity, which could be processed into films by rolling (Fig. 6a). The rollable MXene clay exhibited excellent elasticity, ultra-high toughness and good hydrophilicity, and it could be easily bent into an “M” shape and the electrical conductivity could be sustained up to 1500 S cm−1 (Fig. 6b–d). Similar to the process of direct HF etching, the process of forming HF etchant in situ with HCl/LiF for the synthesis of MXenes not only produced a multi-layer accordion-like morphology (Fig. 6e), but also enabled the surface of MXenes to be functionalized to produce rich surface terminal groups, such as –F, –OH, and –O. However, given that the latter reacts with acid and salt solution to produce HF, the obtained MXenes were inevitably accompanied by the insertion of water molecules, which led to a longer drying time for the product. The interlayer spacing of the MXenes obtained by in situ HF-forming etching was significantly reduced after drying due to the disappearance of water molecules inserted between the layers during the etching process (Fig. 6f).121,122 The type of surface end base has a great effect on the interlayer spacing. This is due to the strong hydrophobicity of –F, which repels water molecules, making the interlayer spacing of MXene negatively correlated with the number of –F. Specifically, when the content of –F group increases, the interlayer spacing of the MXene will decrease. Zhu et al. also used the LiF/HCl etching method to prepare MXenes, as shown in Fig. 6g.123 Briefly, 1.6 g of LiF was mixed with 20 mL of 9 M HCl. Subsequently, 1 g of Ti3AlC2 powder was added to the mixture and stirred continuously at 35 °C in a Teflon bottle for 24 h. After the etching process, it was washed repeatedly with deionized water to pH = 4–6. Finally, the product was sonicated under flowing inert gas conditions to obtain a layered Ti3C2Tx MXene suspension. In this work, given that LiF was relatively mild, it reacted with HCl to produce HF in situ. Thus, the danger associated with the direct addition of HF was avoided and the safety of the experiment improved.
Fig. 6 Typical morphology and properties of Ti3AlC2 etched by HCl/LiF mixture etchant. (a) MAX phase is etched in a solution of acid and fluorine salts and washed with water to bring the pH to neutral, obtaining a clay-like deposit that produces a conductive object of the desired shape after the operation. (b) Digital photograph showing the morphology of rolled Ti3C2Tx “clay” films. (c) Electrical conductivity of Ti3C2Tx “clay” films. (d) Contact angle measurement of Ti3C2Tx “clay” films. (e) Multi-layer MXene particles. Reprinted with permission.120 Copyright 2014, Springer Nature. (f) XRD patterns of Ti3C2 before and after drying at 80 °C. Reprinted with permission.121 Copyright 2013, The Royal Society of Chemistry. (g) Schematic diagram of the synthesis of Ti3C2Tx MXene nanosheets. Reprinted with permission.124 Copyright 2022, Elsevier. |
HF is not only volatile, but also dangerous to use. However, it can be replaced by the relatively mild NH4HF2. For the method of etching with NH4HF2 solution, Kim et al. first added Ti3AlC2 powder to an NH4HF2 solution and stirred it at room temperature for 24 h, and then washed the product to obtain etched MXenes.125 In 2014, Barsoum et al. reported the fabrication of Ti3C2 films by selectively etching Al in epitaxial Ti3AlC2 films deposited by sputtering using NH4HF2 as the etchant.105 The etching mechanism of this process can be summarized as eqn (7) and (8), as follows:
(7) |
(8) |
Given that fluoride salts are solid at high temperatures, they have a higher level of safety during operation compared to hydrogen fluoride. However, to date, this above-mentioned method has only been proposed for etching Ti3AlC2 and has not been explored for other MAX phases.
Feng et al. used NH4HF2 as the etchant and obtained an MXene with a large interlayer spacing. When Ti3C2 was used as the electrode, the large layer spacing provided more space for ions to be embedded to store ions.126 In this work, high-purity Ti3C2 MXene was prepared via a simple method, and the acquired Ti3C2 had a large layer spacing. Similar to the use of fluoride salts, NH4+ could increase the interlayer spacing by inserting MXene nanosheets.127 The Ti3C2 etched by NH4HF2 in this work exhibited an outstanding pseudocapacitance performance, which was 34% higher than that etched by HF. Thus, NH4HF2 etching can produce Ti3C2 electrodes with excellent regeneration performance, which provides an effective way to improve the desalination performance of capacitive deionization technology.
In addition to the above-mentioned two in situ HF etching methods, there are other methods with similar principles for etching MAX phases. For example, Wu et al. reported a new mixed etchant, namely, NH4F mixed with a low eutectic mixed solvent of choline chloride and oxalic acid, and then etched the MAX phase at different temperatures for 24 h via the hydrothermal process.128 In this process, oxalic acid reacted with NH4F to produce HF and destroy the Ti–Al bond in Ti3AlC2 to form multilayers of Ti3C2Tx MXene. While chloride ions were inserted in the interlayer of MXenes, the layer spacing increased. Wu and colleagues synthesized a Ti3C2Tx MXene with inhomogeneous layering by CoF2/HCl etching due to the intercalated Al3+ and Co2+ acting as the backbone of the interlayer spacing of MXene layers.129 In this study, the effect of the etching environment on the composition, interface, structure and thermodynamic properties of the Ti3C2Tx MXenes was investigated. Compared with HF/HCl, CoF2/HCl etching had more advantages, such as endowing Ti3C2Tx MXene with a wider interlayer distance distribution, increasing the number of intercalated cations, and reducing the degree of hydration. In addition, the increased interlayer space, size heterogeneity and reduced hydration led to a reduction in the interlayer van der Waals force interactions and weaker hydration effects. Thus, MXene with intercalated metal cations had a lower exothermic enthalpy (ΔHf). The results of this work further deepen the understanding of the energy, structure and interface properties of MXene.
MXenes, an emerging and promising class of 2D nanomaterials, have been intensively investigated by researchers since they were first reported in 2011. According to the different requirements of MXene material structure in different application fields, there are many methods to etch MXenes. Although most of the more commonly used etching methods rely on etchants, the use of etchants will have an impact on the etching results to some extent.130 In addition to the direct HF etching and in situ HF etching introduced above, there are many etching methods, such as electrochemical etching, alkali etching, and molten salt etching. In 2021, Luo et al. reported a simple one-step molten salt etching method for the preparation of Co-modified MXene.131 This method was also the first to use a non-fluorochemical method to obtain MXene with the ends completely wrapped in Cl. This experiment proved that the method had the unique advantage of using Cl as Tx, which can effectively improve the electrochemical performance of MXenes.130 In the case of the electrochemical etching method, it reduces the adverse effects of the etchant on the product given that it avoids the use of an etchant. Yang et al. demonstrated an efficient fluorine-free etching method using anodic etching with Ti3AlC2 as the precursor.132 The etching process was defined by eqn (9), as follows:
Ti3AlC2 − 3e− + 3Cl− = Ti3C2 + AlCl3 | (9) |
The rapid synthesis of MXene at room temperature was achieved by electrochemical etching, and it was also confirmed that the MXene obtained by electrochemical etching has good capacitive performance in all solid-state supercapacitors, indicating that the MXene obtained by this method was superior to that obtained by LiF/HCl etching. The formation of Ti–F bonds and Ti–O bonds during etching indicated the selective etching of Al. By etching with this method, stripped Ti3C2Tx nanosheets without any –F terminal functional group could be obtained due to the fluorine-free etching. The use of this method further broadens the application path of MXenes in electrochemistry.
In 2018, Wang et al. reported for the first time that a titanium carbide (Ti3C2) MXene and commercial (P25) were used as a highly efficient non-noble metal co-catalyst for photocatalytic carbon dioxide reduction. The discovery in this work provided a new and highly active alternative to the common non-noble metal auxiliary catalysts for the photocatalytic reduction of carbon dioxide.151
MXene and P25, alkalized MXene and P25 were mixed evenly through magnetic stirring to obtain TC/P25 and TC-OH/P25 hybrids, respectively. As shown in Fig. 7a, the characteristic diffraction peaks of TC-OH/P25 were not found in the XRD pattern, which was due to the relatively low mass content of TC-OH in the hybrids and the weak crystallization. In addition, the diffraction peaks in the spectrogram indicated that the mixing of P25 with TC or TC-OH did not change its phase composition and crystal structure. Transmission electron microscopy (TEM) images (Fig. 7b) showed that the P25 nanoparticles were loaded on 2D TC-OH. According to the magnified HRTEM image shown in Fig. 7c, the plane space corresponding to the approximate distance between adjacent lattice stripes shows that there was a close interaction between P25 and TC-OH, which was more conducive to forming a connection between them. The activity of the TC-OH/P25 catalyst was further enhanced compared to TC/P25 due to the modification of TC by hydroxyl groups. As shown in Fig. 7d, 5TC-OH/P25 was 3 and 2.77 times more active than P25 alone for CO and CH4, respectively. The graph showed the adsorption behavior of CO2. The absorption of CO2 by TC-OH at room temperature was significantly higher than that of TC, indicating that the CO2 molecules were more easily adsorbed on the surface of TC-OH. The adsorption energy of CO2 on TC-F was −0.13 eV, which was much higher than that of CO2 on TC-OH of −0.44 eV (Fig. 7e and f, respectively). It is obvious that the higher adsorption capacity of TC-F for CO2 was due to the lower adsorption energy of CO2 on TC-OH. In this work, the authors successfully improved the photocatalytic CO2 reduction activity of P25 by using the Ti3C2 MXene, a cocatalyst without noble metals. In particular, the surface alkalinization of Ti3C2 MXene further significantly improved the photocatalytic activity and the selectivity for CH4 release. The data showed that alkalization of the MXene could make its surface functional and significantly improved its performance in applications.
Fig. 7 (a) XRD patterns of Ti3AlC2, TC, TC-OH particles and TCOH/P25 hybrids. (b) Typical SEM image of the 5TC-OH/P25 mixture. (c) HRTEM images of the interfacial structure of TC-OH and P25 NPs. (d) Under the irradiation of a 300 W xenon lamp, the release rate of CO and CH4 on P25, 5Pt/P25, 5TC/P25, 5TC-OH/P25. (e) CO2 adsorption behavior of TC and TC-OH. (f) Side view of CO2 adsorption models on 2 × 2 × 1 TC-F and 2 × 2 × 1 TC-OH super-cell. Reprinted with permission.151 Copyright 2018, John Wiley and Sons. |
Furthermore, Sun et al. prepared multilayer Ti3C2Tx MXene by selectively etching the Al layer of Ti3AlC2 with hydrofluoric acid according to the literature. Then, the alkaline intercalation of the Ti3C2Tx MXene was completed by magnetic stirring, filtering, washing and drying with LiOH, NaOH and KOH solutions, respectively. Finally, three types of alkylated MXene, LiOH–Ti3C2Tx, NaOH–Ti3C2Tx and KOH–Ti3C2Tx, were synthesized.152 In this work, some of the alkali-treated Ti3C2Tx MXenes were characterized and their adsorption properties for dyes were examined. As shown in Fig. 8a and b, the low peak width intensity in the XRD spectrum of pristine Ti3C2Tx showed that the Al in Ti3AlC2 was etched, leading to reduced crystallinity. After treatment with LiOH, NaOH and KOH, the characteristic peaks of Ti3C2Tx became significantly stronger. In addition, the (002) peak at 9.0° obviously shifted to a lower angle, which indicated that the introduction of additional ion pairs in Ti3C2Tx not only expanded its structure, but also increased the uniformity of the lamellae, especially NaOH–Ti3C2Tx and KOH–Ti3C2Tx. As shown in Fig. 8d(i–iii), the SEM micrographs of Ti3AlC2 and Ti3C2Tx clearly showed that the morphology of Ti3AlC2 changed from a dense layer structure to a stacked sheet material with different thickness after HF solution etching. The thickness of the sheets of the Alk-Ti3C2Tx lamellar structure varied widely, and the SEM image of LiOH–Ti3C2Tx showed that the sheets were stacked but had many large gaps; the thickness of the NaOH–Ti3C2Tx sheets was similar to that of the original Ti3C2Tx; and the multilayer sheets of KOH–Ti3C2Tx were not only thicker but also had narrow stacking gaps (Fig. 8d(iv–vi)). The different MXene forms may also affect the adsorption properties for dyes. As shown by the HRTEM images in Fig. 8e–h, the pristine Ti3C2Tx was multilayered and the monolayer thickness of MXene increased after the alkalization treatment due to the intercalation of alkali metal ions. Fig. 8c showed that with time, all three types of Alk-Ti3C2Tx had a faster MB removal rate than the pristine Ti3C2Tx. This work demonstrated that Alk-Ti3C2Tx obtained by alkaline treatment could significantly expand the layer spacing of MXenes and its surface functional groups were transformed, thus improved the adsorption capacity of MXenes.
Fig. 8 (a) XRD spectra of Ti3C2Tx under different alkaline treatments: (I) Ti3C2Tx, (II) LiOH–Ti3C2Tx, (III) NaOH–Ti3C2Tx, and (IV) KOH–Ti3C2Tx. (b) Enlarged view of the XRD spectrum in (a). (c) Curves of the removal rate of MB with time for different absorbents. (d) SEM images of Ti3AlC2, Ti3C2Tx and various Alk-Ti3C2Tx: (i) Ti3AlC2, (ii) Ti3C2Tx, (iii) enlargement of (b), (iv) LiOH–Ti3C2Tx, (v) NaOH–Ti3C2Tx, and (vi) KOH–Ti3C2Tx. HRTEM images of Ti3C2Tx and various alkalized Ti3C2Tx: (e) Ti3C2Tx, (f) LiOH–Ti3C2Tx, (g) NaOH–Ti3C2Tx and (h) KOH–Ti3C2Tx. Reprinted with permission.152 Copyright 2018, Elsevier. |
Xu et al. successfully introduced amino end groups on the surface of Ti3C2 MXene using a simple sealed thermal method, in which the amination process mainly replaced the hydroxyl groups on the surface of the pristine MXene with amino groups.153 In this work, the Ti3C2 MXene was obtained by etching Ti3AlC2 powder with LiF/HCl solution. Then, ammonia water with a certain pH was added to the obtained MXene, it was shook well, and then ultrasonicated and centrifuged. Next, the Ti3C2 MXene suspension containing a few amination layers was placed in the reaction still and heated at 70 °C for 4 h. Finally, it was washed and centrifuged to neutral, and the obtained precipitate was freeze-dried to obtain MXene-NH2 nanosheets (Fig. 9a). The AFM and TEM images showed that the MXene-NH2 nanosheets were not only uniform in size and thickness but also ultra-thin (Fig. 9b and c). In the XRD spectra, the shift in the (002) characteristic peaks indicated a decrease in the d-spacing of MXene-NH2 compared to the pristine MXene, verifying the change in the morphology and chemical composition of the pristine MXene and MXene-NH2 nanosheets (Fig. 9d). As shown in Fig. 9e, the UPS spectra of the conventional MXene and MXene-NH2 nanosheets confirmed that the electron transport behavior of MXene-NH2 films was still higher, although the work function of MXene-NH2 increased. Likewise, the conductivity of the pure MXene-NH2 film reached 21100 S m−1, but it was reduced by 82.5% compared to the conductivity of the conventional MXene film; nevertheless, its value was still quite large (Fig. 9g). The high conductivity of the MXene-NH2 film indicated its high electric power supply and good electromagnetic interference shielding effect (SE). The EMI SE value of the pure MXene-NH2 film in the X-band exceeded 60 dB. Compared with pure traditional MXene films, the EMI SE of MXene-NH2 was only 5 dB lower, which shows its application potential (Fig. 9f). As shown in Fig. 9h, the CMC molecule had strong mechanical properties due to the formation of hydrogen bonds between it and conventional MXenes. When the CMC molecules and MXene-NH2 nanosheets formed a thin film, stronger covalent bonds were formed between them in addition to the normal hydrogen bonds, which made the CMC/MXene-NH2 film simultaneously exhibit excellent flexibility, thus enhancing the tensile properties of CMC/MXene-NH2, and its mechanical properties were also improved. In summary, all these results indicate that the introduction of amino terminals on the surface of Ti3C2 MXene endows it excellent mechanical properties, which not only optimizes the properties of the original product, but also further expands its application scope.
Fig. 9 (a) Schematic diagram of the preparation of aminated Ti3C2 MXene. (b) AFM images and (c) TEM images of MXene-NH2 nanosheets. (d) XRD patterns of conventional MXene and MXene-NH2 films. (e) UPS spectra of valence band region of conventional MXene and MXene-NH2 nanosheets. (f) EMI SE of each thin film in the X-band. (g) Electrical conductivity of MXene and MXene-NH2 films. (h) Schematic diagram of mechanical property enhancement mechanism. Reprinted with permission.153 Copyright 2021, Elsevier. |
Zhang et al. considered that the lack of active adsorption sites definitely affects the adsorption performance of ordinary MXene adsorbents, and thus it is necessary to functionalize the surface of MXenes to optimize their performance. In this work, the researchers prepared a novel MXene-based adsorbent (Ti3C2-SL) by combining Ti3C2 terminated with a conjugated amino group and sodium lignosulfonate through a simple substitution reaction with hexachlorocyclotriphosphonitrile (HCCP) as the linkage point.154 Through detection, Ti3C2-SL could be used as an adsorbent to adsorb doxorubicin hydrochloride (DOX). Experiments showed that Ti3C2-SL could adsorb DOX rapidly and its adsorption amount was significantly higher than that of the unmodified Ti3C2, which was about four times that of the original Ti3C2. Furthermore, Ti3C2-SL had a good application prospect in removing environmental pollutants due to its simple preparation process and significant performance enhancement, and thus this work will significantly advance the environmental applications of MXene-based composites.
Soroush et al. used [3-(2-aminoethylamino)-propyl] trimethoxysilane (AEAPTMS) for the amino functionalization of the surface of Ti3C2Tx MXene.155 In this work, the functionalization of MXene caused its zeta potential to change from −35 mV to +25 mV at neutral pH, and this change in the potential caused the MXene able to prepare self-assembled films in situ. The results of this work showed that AEAPTMS-Ti3C2Tx is a pH-responsive nanomaterial due to the existence of amino groups on its surface and its ability to adsorb or desorb protons with a change in pH.
Besides, in the work by Zhang and colleagues, it was reported for the first time that MXenes (Ti3C2Tx) and levodopa (DOPA) could be prepared as MXene-based polymer composites (Ti3C2Tx-PDOPA) after simple mixing under rather mild reaction conditions.156 In the reaction system, as DOPA can adhere to the surface of MXenes by self-polymerization, resulting in the ability to introduce multiple carboxyl groups during the polymerization process and formation of poly-(DOPA). The resulting Ti3C2Tx-PDOPA composite was used as an adsorbent, which not only possessed a higher adsorption capacity for heavy metal ions than the pristine Ti3C2Tx, but could also be further functionalized with other functional materials through subsequent reactions. Because the functionalization of pristine MXenes leads to the introduction of many reactive groups, a variety of composites based on MXenes can be prepared.
Briefly, the amine functionalization approach not only extends the scope of MXenes for more applications in different fields, such as fuel cells, dye adsorbents and antimicrobial coatings, but is also applicable to other MXene structures and composites.
Because of the rapid development of industrialization, the depletion of fresh water resources is significant.157 It is well known that the wastewater produced by the dyeing industry has a complex composition and mainly contains dyestuffs with a high salt content, making wastewater treatment complicated and challenging.158–161 Therefore, various methods have been studied and developed to treat the wastewater generated from printing and dyeing. Zhang et al. reported that Ti3C2 nanosheets were obtained by etching Al from the Ti3AlC2 MAX phase by in situ-forming HF etchant, and the surface of the Ti3C2 nanosheets was modified with sulfonic acid groups through the direct reaction of diazonium salt and Ti3C2 sheets, as shown in Fig. 10a.162 Meanwhile, the adsorption behavior and adsorption capacity of Ti3C2 and functionalized Ti3C2 on methylene blue (MB) were further investigated and compared in this work. The SEM images showed that the pristine Ti3C2 was a multi-layer 2D nanomaterial with a packaged and stacked lamellar structure, and the interlayer spacing was about 200 nm (Fig. 10d). The apparent granular-structured surface is shown in Fig. 10e, which was due to the modification of Ti3C2 by the aryl diazonium salt, that is, the benzene sulfonic acid group functionalized the surface of Ti3C2. The comparison of the TEM images of the pristine Ti3C2 and Ti3C2–SO3H showed that the transparency of the nanosheets was further improved after surface modification (Fig. 10f and g). The presence of sulfur was observed in the XPS spectra of both samples (Fig. 10b), where the vibrational peaks caused by the asymmetric stretching of the SO band appeared at 1211 and 1130 cm−1 in the FT-IR spectra (Fig. 10i). Furthermore, the weight loss of more than 50% of Ti3C2–SO3H was observed in the TGA curves (Fig. 10j), and the (002) peak was sharpened and shifted to a lower angle in the XRD spectra (Fig. 10h), indicating that Ti3C2 was successfully sulfonated by benzene sulfonic acid. As shown in Fig. 10c, compared with the adsorption capacity of the virgin Ti3C2 MXene of 21.10 mg g−1 for MB in water, that of the benzene sulfonic acid group-functionalized MXene for MB in water was 111.11 mg g−1, which is five times higher than that of the pristine MXene. This study demonstrated that Ti3C2–SO3H is a promising and efficient adsorbent for the removal of organic dyes from the aqueous environment.
Fig. 10 (a) Schematic diagram of the preparation of Ti3C2 and Ti3C2–SO3H. (b) XPS wide scan spectra of pristine Ti3C2 and Ti3C2–SO3H. (c) Effect of contact time on the adsorbed MB on pristine Ti3C2 and Ti3C2–SO3H. SEM images of (d) virgin Ti3C2 and (e) Ti3C2–SO3H. TEM images of (f) virgin Ti3C2 and (g) Ti3C2–SO3H. (h) XRD patterns of virgin Ti3C2 and Ti3C2–SO3H. (i) FT-IR spectra of virgin Ti3C2 and Ti3C2–SO3H. (j) TGA curves of virgin Ti3C2 and Ti3C2–SO3H. Reprinted with permission.162 Copyright 2019, Elsevier. |
Pu et al. embedded sodium lignosulfonate (LS), which contained abundant hydrophilic groups (sulfonic acid groups and phenolic hydroxyl groups), and MoS2 nanosheets in MXene nanosheets for functionalization.163 The researchers prepared 2D MoS2@LS-MXene composite membranes with high water permeability and outstanding dye separation properties via the pressure-assisted self-assembly technique, as shown in Fig. 11a. The MXene nanosheets added with deionized water were ultrasonically dispersed, and after the dispersion was uniform, LS was added with magnetic stirring for a certain time, resulting in the functionalization of the MXene nanosheets. Subsequently, specific concentrations of MoS2 dispersion liquid were added for sonication to obtain precursor solutions of different compositions, after which MXene-based composite films were prepared. The hydrophilicity and permeability of the membranes were tested by water contact angle (CA) and pure water flux measurements (Fig. 11c). Given that LS is a biological macromolecule containing sulfonic acid groups and many phenolic hydroxyl groups, it endowed the prepared composite membranes with good hydrophilic properties. Consequently, with an increase in LS content, the water contact angle of the composite film decreased, indicating an increase in hydrophilicity. The enhanced hydrophilicity also improved the breathability of the membrane. Because the membrane with hydrophilic surface could prevent the accumulation of contaminants in water on its surface, its antifouling ability was improved. The XRD patterns of the three samples showed (Fig. 11d) that the (002) peaks of the MXene nanosheets after LS treatment were not only broadened but also shifted to a lower angle, indicating an increase in the layer spacing of the composite films. The increased interlayer spacing and hydrophilicity provided a suitable environment for the rapid permeation of water molecules, indicating that the water flux of the composite membrane became larger. As shown in Fig. 11f and g, to examine the separation performance of the MXene composite membranes, the researchers used Congo red and rhodamine B to simulate dye wastewater vapors. It was clearly observed that the layer spacing of the MXene composite membranes increased with an increase in LS content, and the removal rates of CR and RhB were improved for all the membranes. The composite membranes removed both Congo red and rhodamine B in mixed solutions at more than 95% compared to the single component dyes (Fig. 11h). The result showed that the MXene composite membranes had a good performance for dye/salt separation. In addition, the composite membrane could be recycled again after washing, and the recycling also showed that the composite membrane had good flux recovery performance. Fig. 11b shows the flux recovery of the M-3 membrane after CR permeation and DI water cleaning. It can be seen that the flux of the composite membrane still recovered well when cleaned with detergent for 10 min at each cycle. Also, the separation mechanism of the composite membranes showed that when the composite membranes had an appropriate interlayer spacing, smaller-sized saline hydrated ions could permeate them, while larger-sized dye molecules were repelled, thus achieving mutual separation (Fig. 11e). The functionalized composite films obtained in this work not only exhibited good stability and fouling resistance, but this study also provided novel design ideas for the preparation of high-performance materials.
Fig. 11 (a) Scheme for the preparation of MoS2@LS-MXene composite films by pressure-assisted self-assembly. (b) FRR data of M-3. (c) CA of all membranes. (d) XRD patterns of M-0, M-1, and M-3. (e) Separation mechanism of MoS2@LS-MXene composite membranes. Removal rates of dyes by different membranes: (f) CR and (g) RhB, and (h) separation of dye/salt mixture with M-3. Reprinted with permission.163 Copyright 2022, Elsevier. |
In summary, it is not difficult to see that there are numerous ways to functionalize MXenes. In addition to functionalization with surface groups, it is also possible to functionally optimize the defects of MXenes with substances that are also 2D materials.163 It is sufficient to prove that the products obtained from the functionalization of MXenes have excellent performance, which not only broadens the application direction and field of MXenes, but also makes MXenes extremely potential for development.
Well-designed methods for the preparation of membranes are essential to achieve the goal of efficient separation processes. According to the actual needs, great progress has been achieved in the past few years by combining different methods to design membranes accurately and rationally. Under vacuum filtration conditions, the fabricated membranes form nanochannels of different lengths and widths due to the high aspect ratio of MXenes, and these nanochannels provide pathways for gas diffusion (Fig. 14c).168 Consequently, changing the interlayer distance and length of the nanochannels will allow different types of gases to pass through the membrane and also change the gas permeability, which in turn will achieve the purpose of gas separation. In MXene separation membranes, CO2 will be adsorbed in the MXene nanochannels, which prevents its transport, thus capturing CO2.85 MXenes have been progressively combined with stand-alone or film-composite polymers to prepare separation membranes. This method can increase the affinity between CO2 and the matrix. Because the nanochannels formed by MXene nanosheets contribute to molecular sieving and provide a more tortuous path for gas transport in the membrane, MXene-based gas separation membranes can improve the selectivity and permeability of the corresponding MXene MMMs.77 Compared with other existing 2D separation membranes (such as ZIFs and MOFs), MXene-based membranes may have the same selectivity and higher permeability. In addition, research has shown that lamellar MXene-based films exhibit excellent reproducibility, good mechanical properties, and stable separation performance due to their ordered nanochannels in the long-term continuous separation process.75
As shown in Fig. 12a, Ti3C2Tz MXene was embedded in Pebax-1657 block copolymer in the work by Ahmad et al. The mixture of these two substances formed good nano-channels to achieve the fast and selective transport of CO2, and the mixed matrix membrane also showed an excellent CO2 separation performance. Besides, the experimental scheme of mixing the MXene and polymer in the experiment could also mitigate the oxidation of the MXene.85 In the work by Li and colleagues, the Ti3C2Tx MXene was combined with Pebax to prepare a mixed matrix membrane for the separation of CO2.169 According to the scanning electron microscopy images of the cross section of the membranes, as shown in Fig. 12f and g, the MXene in the matrix was uniformly dispersed at 1% loading, while the cross-section was relatively smooth at 5% loading. The FTIR spectrum of the Pebax-MXene films, which characterized the interaction between the filler and the matrix, showed a slight shift in the peaks for the Pebax-MXene films at 3302 cm−1 and 1640 cm−1. The shift in these bands suggested that the interaction between the surface end groups of MXene and the Pebax chain may be hydrogen bonding (Fig. 12b–d). As shown in Fig. 12e, the CO2 permeability of the Pebax-MXene membrane was significantly greater in the wet state than in the dry state, and this state was related to the fact that the membrane swelled when wet. When the content of MXene in the membrane increased from 2% to 5%, the CO2/N2 selectivity of the membrane in the wet state clearly tended to increase, which was obviously different from the trend in the dry state. However, in general, Pebax-MXene membranes exhibit a high separation performance due to the abundance of functional groups on the MXene surface.
Fig. 12 (a) Design of Pebax/MXene membrane. Reprinted with permission.85 Copyright 2020, the American Chemical Society. (b)–(d) FTIR spectrum of Pebax-MXene films. (e) Gas transport characteristics of Pebax-MXene films under dry and wet conditions. (f) Cross sectional scanning electron microscopy images of Pebax-MXene-1% membrane and (g) Pebax-Mxene-5% membrane. Reprinted with permission,169 Copyright 2021, Elsevier. |
In addition to the above-mentioned separation membranes prepared using MXenes and polymer Pebax, other MXene-based membranes have also been extensively used in the field of gas separation. According to the outstanding structural characteristics and unique chemical surface of MXenes, researchers have designed MXene-based films combined with different substances. For example, Ding et al. used vacuum-assisted filtration in a laboratory study to place MXene nanosheets on anodic aluminum oxide carriers and could separate the MXene films “independently”. Furthermore, it was reported that the peeled MXene films showed good flexibility.75 Li and colleagues conducted an in-depth study on gas diffusion in MXene interlayer nanochannels through MD simulations to understand the selective diffusion of gases in MXene interlayer nanochannels at the molecular level. In this work, the diffusion behavior of many different gas molecules in MXene membranes with different structures was investigated, and the results showed that the effect of different MXene membrane structures on gas diffusion was significant.170
Furthermore, functional liquids, such as ionic liquids (IL), have the ability to achieve the purpose of separating different gases and enclosing undesirable defects in the packing due to their different solubility based on gases. Therefore, it is a very effective method to embed them in 2D layered membranes for the separation of gases with similar kinetic diameters. Considering this, Li et al. used a simple method to sulfonate MXene, followed by embedding the typical ionic liquid 1-butyl-3-methylimidazolium tetrafluoroborate ([BMIM][BF4]) in the ionized nanochannels of the sulfonated MXene nanosheet lamellar membrane to separate CO2 and N2 molecules.171 In this work, inspired by catechol-metal chelation, Ti3C2Tx MXene nanosheets containing a large number of unsaturated Ti atoms were chosen as the main building blocks to facilitate the homogeneous introduction of sulfonic acid groups (–SO3H). Also, a method of ionization was proposed, i.e., the modification of the nanochannels of the lamellar membrane with disodium 4,5-dihydroxy-1,3-benzenedisulfonate, which is a catechol derivative. The method allowed the IL to be stably immobilized in the nanochannels and achieved effective separation of CO2. The membranes prepared using the MXene modified by sulfonic acid groups had intrinsic advantages compared to previously reported liquid-immobilized lamellar membranes.172 The membrane with the best performance had a certain interlayer spacing and high absorptivity for IL, endowing it with high permeability to CO2 and high selectivity for CO2/N2. Besides, the IL loss rate of the membranes prepared by growing sulfonic acid groups in the nanochannels of MXene under high pressure (5 bar) significantly decreased within seven days compared to the unsulfonated MXene, indicating that the MXene functionalized with sulfonic acid groups showed good stability for IL storage. In conclusion, the membranes reported in this work not only had comparable permeate flux and stability, but also were expected to contribute to the development of liquid-based membranes.
In 2022, Wei et al. first reported the preparation of a freestanding MXene-ZIF-8 bilayer hydrogen separation membrane.173 To achieve MXene layer assembly and ZIF-8 growth, the researchers combined electrophoretic deposition (EPD) and fast current-driven synthesis (FCDS). As shown in Fig. 13a, this method resulted in the synthesis of independent MXene-ZIF-8 bilayer composite membranes in a relatively short period, enabling the simple and rapid production of membranes, while overcoming the time-consuming drawback of the traditional vacuum filtration and thermal synthesis methods. This figure showed that the thinner 2D layered MXene was obtained in a short time through EPD. Secondly, based on the MXene layer as the conductive substrate, a certain thickness of ZIF-8 layer was rapidly grown on the MXene layer using FCDS. The final MXene-ZIF-8 bilayer composite membrane could be used as a suspension membrane for gas separation. In the experiment, a single gas permeation test was performed for the MXene membrane and MXene-ZIF-8 bilayer composite membrane. The results indicated that the H2/CO2 selectivity of the pure MXene membrane exceeded the Knudsen selectivity, and the permeability of N2 and CH4 was higher than that of CO2 due to the adsorption of CO2 by the MXene (Fig. 13c). The MXene-ZIF-8 bilayer composite membrane, which grew a ZIF-8 layer, showed an almost twofold increase in H2/CO2 selectivity and a nearly threefold improvement in H2/C3H8 selectivity compared to the pure MXene membrane (Fig. 13d). This suggested that the combination of MXene nanosheets layer with ZIF-8 helped to improve the gas separation performance of the membrane. As shown in Fig. 13e, the gas separation performance curve of the MXene-ZIF-8 bilayer composite membrane for H2/CO2 at different temperatures clearly showed that the CO2 permeability increased with an increase in temperature. Subsequently, the researchers conducted a long-time H2/CO2 separation test on the MXene-ZIF-8 bilayer composite membrane, and the results showed that its permeability for H2 and CO2 remained almost unchanged during more than 100 h of operation. Simultaneously, the H2/CO2 selectivity was only slightly reduced, which confirmed the excellent stability of the MXene-ZIF-8 double-layer composite membrane (Fig. 13f). In addition, the excellent crystal structure of the ZIF-8 layer, the SEM image of the tightly bound MXene-ZIF-8 bilayer, and the elemental mapping of Zn and Ti in the MXene-ZIF-8 bilayer composite film indicated that the composite films still had a satisfactory and stable structure after long-time gas separation (Fig. 13b). The MXene-ZIF-8 bilayer composite membrane prepared in this work had the advantages of high synthesis efficiency, superior H2/CO2 selectivity, and extremely fast membrane preparation time. Simultaneously, the concept of designing membrane structures can be extended to other double-layer membranes, which provides a new idea for the development of membrane preparation.
Fig. 13 (a) Schematic diagram of the rapid synthesis of MXene-ZIF-8 bilayer composite membrane. (b) (i)–(iii) SEM images of the ZIF-8 layer, MXene layer interface and MXene-ZIF-8 bilayer composite film cross-section; (iv) are elemental mappings of Zn and Ti corresponding to (iii). Single gas permeability and selectivity of (c) MXene membranes and (d) MXene-ZIF-8 bilayer composite membranes. (e) Separation performance of MXene-ZIF-8 bilayer composite membranes for H2/CO2 mixtures at different temperatures. (f) Long-term separation performance of MXene-ZIF-8 bilayer composite membranes for H2/CO2 mixtures. Reprinted with permission.173 Copyright 2022, Elsevier. |
In summary, with the increasing in-depth research on MXenes, there are more in-depth studies and innovative design ideas for the preparation of MXene-based gas separation membranes, which further illustrates the application and development potential of 2D nanomaterial MXenes in gas separation membranes.
Fig. 14 Schematic diagrams of two mass transport mechanisms (a) through in-plane fissure-like pores (A) and interlayer channels (B). (b) Voids formed between the less ordered MXene nanosheets. Reprinted with permission.176 Copyright 2022, the American Chemical Society. (c) Separation mechanism of MXene-based membrane. Reprinted with permission.77 Copyright 2020, John Wiley and Sons. (d) Schematic diagram of adjacent MXene nanosheets. Reprinted with permission.75 Copyright 2018, Springer Nature. (e) Schematic diagram of the selective permeation of H2 and CO2 in MXene membrane. Reprinted with permission.73 Copyright 2018, John Wiley and Sons. |
Due to the fact that the adjacent nanosheets in a 2D layered membrane are usually stacked randomly, they form disordered nanochannels, which can hinder the efficient separation of the target gas. Therefore, it is necessary to fabricate MXene lamellar membranes with regularly arranged and ordered sub-nanochannels. Wang et al. prepared Ti3C2Tx nanosheets with lateral dimensions of around 1 μm by improving the method of preparing nanosheets using a mixed solution of LiF and HCl. Then, on an anodic aluminum oxide (AAO) substrate with a pore diameter of 200 nm, a self-supporting membrane was prepared by vacuum-assisted filtration.75 Because of the abundant surface end groups of the MXene, the membrane exhibited an H2 permeate flux of 2200 Barrer and H2/CO2 selectivity of over 160, a performance that exceeded that of most membrane materials available at the time. The performance achieved to such an extent, in addition to the interaction between the surface end groups and the gas molecules, is also largely dependent on the size sieving effect of the sub-nanometer interlayer channels on H2 and CO2.
The above-mentioned work achieved the modulation of MXene interlayer spacing and the stacking mode of interlayer nanosheets through chemical modification and intramolecular interactions (electrostatic interactions, hydrogen bonding and covalent bonding), thus preparing MXene nanomembranes with outstanding CO2 separation performances.
When the etchant used for synthesizing MXene is different, it also has an effect on the layer spacing of the MXene. For example, when etching MXene with HCl-LiF solution, Li+ will be interpolated between the MXene layers, thus synthesizing MXene with relatively large lattice parameters.120 In their work, Wang et al. uniformly combined Fe(OH)3 nanoparticles with a diameter of 4–5 nm with the MXene surface by electrostatic interaction, and then removed the excess nanofillers with HCl solution to obtain 2D nanochannels with a layer spacing of 2–5 nm.184 The MXene membranes obtained by this method showed outstanding permeability and stability. The showed that the width of the MXene nanochannels could be controlled by cationic intercalation, which in turn led to the better performance of the MXene membranes. Meng et al. intercalated Ni2+ in MXene nanosheet layers, and then assembled the modified MXene nanosheets with Al2O3 hollow fibers to form molecular sieve membranes (MSMs) through a vacuum-assisted filtration and drying process (Fig. 15a).185 The membrane had an H2 and CO2 selectivity of 615 and H2 permeability of 8.35 × 10−8 mol m−2 s−1 Pa−1 at room temperature. Compared with the Ti3C2Tx/Al2O3 hollow fiber membrane without intercalated cations, due to the strong interaction between the negatively charged MXene nanosheets and Ni2+, the interlayer spacing of the MXene was regulated. Consequently, the selectivity and permeability of the membrane prepared after Ni2+ intercalation were significantly improved. Also, the membrane continued to operate for 200 h and still had a stable gas separation performance. This work showed that the Ti3C2Tx/Al2O3 hollow fiber membranes prepared after Ni2+ intercalation have a broad prospect for industrial applications.
Fig. 15 (a) Schematic diagram of Ni2+–Ti3C2Tx/Al2O3 hollow fiber membrane for separation of hydrogen and carbon dioxide mixtures. Reprinted with permission.185 Copyright 2020, Springer Nature. (b) Schematic diagram of the preparation of MXene-assisted ZIF-67 film on Al2O3 disc. Reprinted with permission.186 Copyright 2022, Elsevier. (c) Schematic diagram of self-cross-linked MXene hollow fiber membrane for H2/CO2 separation. Reprinted with permission.187 Copyright 2021, Elsevier. |
Because of the abundance of end groups on the surface of MXenes, cation intercalation produces a certain interaction with it, causing the intercalated modified MXene membranes to exhibit more outstanding gas separation performance and stability. Consequently, changing the structure of the MXene layers by cationic intercalation plays a decisive role in the separation performance of the prepared MXene membranes.
The above-mentioned studies showed the potential of combining MXenes with other 2D materials for the preparation of high-performance gas separation membranes. However, thus far, this route has not been widely explored and applied in the field of gas separation. Also, this means that MXenes have a broader scope for development and application in the field of high-performance separation/purification.
Inorganic hollow fibers are a good substrate for the large-scale preparation of 2D material membranes; however, if 2D materials are inefficiently stacked on hollow fibers, it will lead to an oversized interlayer space and extremely low sieving performance. Xu and colleagues prepared self-crosslinked MXene hollow fiber membranes with good gas separation performance and stability from yttrium-stabilized zirconia (YSZ) hollow fibers via a simple heat treatment and self-crosslinking process.187 As shown in Fig. 15c, the prepared self-cross-linked MXene hollow fiber membranes were capable of forming sieving-capable nanochannels between adjacent MXene nanosheets due to the abundance of end-group groups on the MXene surface. The preparation process resulted in a regular reduction in the interlayer spacing of the MXene films during the heat treatment crosslinking, which led to a significant improvement of their H2/CO2 separation performance. Meanwhile, the operational stability of the prepared self-crosslinked MXene/YSZ (SM/YSZ) hollow fiber membranes was highly competitive.
As mentioned above, the structure of MXenes is inextricably linked to their properties and the performance of the prepared membranes. Whether it is the functionalization of MXenes, cationic intercalation, functionalization of other materials or combination with other 2D materials, these are essentially adjustments to the structure of MXenes, especially their interlayer spacing. The structurally altered MXene membranes almost always exhibit superior separation performance and stability compared to the original MXene membranes. However, obviously, there are still relatively few MXene membranes with outstanding performance for gas separation, which indicates that although they have great potential for development, there is still a long way to go for their research and exploration.
In addition, the tendency of layered MXenes nanocrystals to restack reduces the interlayer distance and open surface area, thus limiting their further application as adsorbents. Molecular sieve membranes with sufficient and homogeneous nanochannels to break the permeation-selectivity equilibrium are ideal for efficient gas separation, and the resulting 2D materials offer new avenues for membrane development. However, for 2D layered membranes, the randomly stacked adjacent nanosheets usually form disordered interlayer nanochannels between them, hindering the efficient separation performance of the membranes. Hence, it remains challenging to prepare layered membranes with highly ordered nanochannel structures for fast and accurate molecular sieving.
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