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Page 24 of 35  Xing et al. Microstructures 2023;3:2023031  https://dx.doi.org/10.20517/microstructures.2023.11



 Table 2. Summary of liquid molecular separation membranes

                                                                          Permeate flux
 Membrane  Base material  Assembly method  Interlayer spacing  Molecular  Dye rejection (%)  -2  -1  -1
                                                                          (L·m ·h ·bar )
 [103]
 uGNMs  Graphene  Vacuum filtration  sub-1-nm  DR 8,  > 99                21.8
 [182]
 PRGO/HNTs  Graphene oxide  Solvent evaporation  8.87 Å  RB 5,  97.9      11.3
 [183]
 GO(120) NFMs  Graphene oxide  Electro spraying  0.818 nm  EB,  99.99     11.13
 [14]
 c-GO/PAN  Graphene oxide  Vacuum filtration  7.6/7.15 Å  DR 80,   > 99   78.5-117.2
 [184]
 MCM0.6-75  MXene  Suction filtration  1.41 nm  Methylene blue,   100     44.97
 [185]
 HGM30  Graphene oxide  Vacuum filtration  0.77 nm  rhodamine B (RhB),  99.30  89.6
 [186]
 MXene/GO-B  MXene & graphene oxide  Vacuum filtration  5 Å  Brilliant blue,   100  0.23
 [187]
 GO/MXene  Graphene oxide & MXene   Filtration  7.3 Å-14.5 Å  Chrysoidine G,   ~ 97  71.9
 [188]
 MXene/GO  MXene & graphene oxide  Vacuum filtration  12.7 Å  Methylene blue,   98.56  16.69
 [189]
 10%MXene@CA  MXene)/cellulose acetate  Casting  ~ 6.68 Å  Rhodamine B,   92  256
 [190]
 21% Ag@MXene  MXene  Vacuum filtration  2.1 Å  Rhodamine B,   79.93      420



 permeability of > 2,200 Barrer and H /CO  selectivity of > 160, demonstrating excellent eventual commercialization potential [Figure 10C] . Carbon
                                                                                 [164]
 2
 2
 neutrality has become a hot topic in recent years. The separation of CO /N  is a prerequisite for CO  capture, leading to the successful synthesis of organic
 2
                             2
 2
 matter from CO . Zhou et al. cross-linked piperazine with GO, resulting in a membrane with a high affinity for CO , thus significantly improving the
 2
                                                     2
 [165]
 separation efficiency of CO /N  [Figure 10D] . The separation of hydrogen isotopes is vital for medical diagnosis and treatment. Lozada-Hidalgo et al.
 2
 2
                                                              [166]
 reported that graphene monolayers and BN membranes could separate hydrogen ion isotopes with a separation factor of about 10 . For a better comparison
 of related membranes, a summary of gas separation membranes is shown in Table 3.
 Ion sieving
 Recently, researchers have paid increasing attention to high-performance ion sieve membranes in addition to traditional separation methods. Membranes with

 various properties are required to meet the different needs of ion sieve membranes for applications such as water desalination, microcurrent, hydrogen
 production, and energy storage.



 In seawater desalination, stringent channel dimensions are necessary, with nanochannels often needing to be sub-nanometers in size to achieve ultra-high
 desalination efficiency. Chen et al. reported a graphene desalination membrane with sub-nanopores that achieved 99.99% NaCl rejection with an ultrafast

 water flux combined with evaporation methods [Figure 10E] . In energy storage applications, ion sieve membranes are often used as diaphragms, where
 [167]
 excellent ionic conductivity and electrical insulation are required. Ghazi et al. synthesize a MoS /celgard separator with outstanding lithium ion passage and
                      2
 polysulfide retention capacity, which can effectively inhibit the shuttle effect in lithium-sulfur batteries, significantly improving the battery performance .
                                                                                           [168]
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