MBenes for Advanced Water Treatment and Desalination Membranes: A Bibliometric, Materials Engineering, and Future Perspectives Review
Abstract
1. Background
2. Bibliometric Methodology and Global Research Landscape of MBenes (2017–2026)
2.1. Bibliometric Data Collection and Analysis Methodology
2.1.1. Database, Search Strategy, and Data Retrieval
2.1.2. Inclusion, Exclusion, and Screening Criteria
2.1.3. Data Cleaning and Descriptive Analysis
2.1.4. VOSviewer Network Analysis
2.1.5. Verification of Bibliometric and Technical Data
2.2. Publication Growth and Research Distribution
2.3. Subject-Area Distribution and Interdisciplinary Nature
2.4. Publication Outlets and Research Types
2.5. Emerging Trends and Challenges
2.6. Initial Phase (2017–2020): Conceptual Foundations
2.7. Growth and Expansion Phase (2021–2024): Rapid Diversification
2.8. High-Output and the Partial-Year Phase (2025–2026)
2.9. Overall Insights
2.10. Desalination Technologies and Their Challenges
2.11. Membrane Materials: Polysulfone and Its Limitations
2.12. Two-Dimensional (2D) Materials for Membrane Applications
2.12.1. Overview
2.12.2. Graphene and Graphene Oxide (GO)
2.12.3. Transition-Metal Dichalcogenides (TMDs)
2.13. MBenes: A New Frontier
2.14. Research Gap: Why MBenes Remain Underexplored in Water Treatment
3. Keyword Landscape and Research Focus
- Geographic and Institutional Contributions
- 2.
- Research Themes and Applications
3.1. Cluster List
- Cluster 1 (Synthesis, Structure, and Characterization): Focused on material preparation, structural properties, and experimental validation.
- Cluster 2 (Catalysis and Electronic Mechanisms): Centered on density functional theory (DFT) modeling, adsorption behavior, and catalytic activity.
- Cluster 3 (Electrochemical Applications and Energy Storage): Encompassing lithium/sodium-ion batteries, diffusion barriers, and electrode performance.
3.2. Cluster 1: Synthesis, Structural Characterization, and Fundamental Properties
3.3. Cluster 2: Catalytic Mechanisms, Electronic Properties, and Theoretical Modeling
3.4. Cluster 3: Electrochemical and Energy Storage Applications
3.5. Inter-Cluster Relationships and Cross-Domain Integration
- Synthesis (C1) develops new MBenes with tailored morphology and purity;
- Theory (C2) predicts catalytic and electronic properties via DFT, identifying promising compositions;
- Applications (C3) test these materials in batteries, supercapacitors, and electrocatalytic setups;
- The performance feedback then informs new synthesis modifications, closing the cycle.
3.6. Emerging Trends and Research Gaps
3.7. Hypothesized Advantages of MBenes and Requirements for Validation
3.8. Conceptual Framework Derived from the Bibliometric Network
- Material Genesis: MAB → MBene (etching and structural verification).
- Theoretical Screening: DFT predicts properties (band structure and adsorption energy).
- Functional Evaluation: Catalysis (HER/NRR) and energy storage (Li/Na-ion).
- Performance Optimization: Surface functionalization, doping, and hybridization.
- Application Diversification: Batteries, supercapacitors, sensors, possibly biomedical uses.
3.9. Mapping the Future of MBene Research
4. Comparative Analysis
4.1. Synthesis and Properties of MBenes
4.2. Incorporating MBenes into Polysulfone Membranes
4.3. Fouling and Antifouling Properties
4.4. Energy Efficiency and Sustainability
4.5. Applications Beyond Desalination
4.6. Economic Feasibility and Scalability
5. Integrated Evidence Synthesis and Translational Roadmap
5.1. Evidence Maturity and Research Gaps
5.2. From MBene Synthesis to Membrane Testing
5.3. Standardized Validation and Practical Translation
6. Conclusions
Author Contributions
Funding
Institutional Review Board Statement
Informed Consent Statement
Data Availability Statement
Conflicts of Interest
References
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| Material | Membrane Configuration | Process, Feed, and Test Conditions | Reported Performance | Evidence Level | Refs. |
|---|---|---|---|---|---|
| Graphene | Oxygen plasma–etched, suspended nanoporous single-layer graphene | Pressure-driven water transport at 40 °C and an estimated pressure difference of approximately 17 kPa; separate osmotic-pressure experiments | Nearly 100% salt rejection for low-defect-density membranes; water flux up to approximately (106) g m−2 s−1 under the pressure-driven experimental configuration | Direct experimental evidence; specialized nanoscale configuration | [10,56] |
| Graphene oxide–graphene | Approximately 5-micrometer-thick swelling-controlled GO–graphene laminate | Forward osmosis; 0.1 M NaCl feed and 3 M sugar draw solution | Approximately 97% NaCl rejection and 0.5 L m−2 h−1 water flux | Direct experimental evidence | [57] |
| MoS2 | Approximately 1-micrometer-thick peptide-functionalized porous MoS2 nanosheet/nanodisk laminate on an alumina support | Forward osmosis; 0.5 M NaCl feed and 2 M sucrose draw solution; continuous testing | >99% initial NaCl rejection; >95% rejection over 30 days; approximately 5 L m−2 h−1 water permeance for the selected laminate | Direct experimental evidence | [11,60] |
| Ti3C2Tx MXene | Approximately 1.1-micrometer-thick Al3+-intercalated Ti3C2Tx lamellar membrane supported on PES | NaCl solutions from 0.2 to 2.0 M and synthetic seawater containing KCl, NaCl, Na2SO4, CaCl2, and MgCl2; aqueous testing up to 400 h | Approximately 89.5–99.6% NaCl rejection and 1.1–8.5 L m−2 h−1 water flux, depending on membrane and feed conditions | Direct experimental MXene evidence; not MBene evidence | [9,22] |
| MBenes | MoAl1−xB photothermal layer integrated with a thermally insulated nylon support | Solar interfacial steam generation under one-sun irradiation; seawater, brine, and selected contaminated-water feeds | Evaporation rate of 1.59 kg m−2 h−1 and reported efficiency of 96.66% under one-sun irradiation | Direct experimental solar-evaporation evidence; not a pressure-driven RO, NF, or UF test | [12] |
| Material Class | Membrane-Level Evidence | Experimentally Demonstrated Findings | Principal Limitations of Interpretation | Evidence Classification | Refs. |
|---|---|---|---|---|---|
| Graphene | Available for nanoporous single-layer membranes | High salt exclusion and rapid water transport have been demonstrated in specialized nanoscale experimental systems | Small active area, defect control, unusual test geometry, and scale-up limitations prevent direct comparison with conventional membranes | Direct experimental membrane evidence | [10,56] |
| Graphene oxide | Available for lamellar and composite membranes | Controlled interlayer spacing can enable ion sieving and high NaCl rejection | Performance depends strongly on swelling control, membrane thickness, cross-linking, feed concentration, and operating mode | Direct experimental membrane evidence | [52,53,57,59] |
| TMDs, particularly MoS2 | Available for functionalized and porous lamellar membranes | Salt rejection, water transport, and extended aqueous stability have been experimentally demonstrated | Performance varies with functionalization, surface charge, pore size, interlayer structure, support, and FO or RO operation | Direct experimental membrane evidence | [11,54,60,62] |
| MXenes, particularly Ti3C2Tx | Available for lamellar, intercalated, and composite membranes | Ion sieving, water transport, antibacterial activity, and swelling control have been experimentally investigated | Oxidation, swelling, termination chemistry, intercalation, membrane thickness, and long-term stability remain condition-dependent | Direct experimental MXene membrane evidence | [9,21,22,107] |
| MBenes | Available for solar interfacial evaporators; insufficient for pressure-driven desalination membranes | Photothermal evaporation and freshwater production have been demonstrated in layered and composite MBene systems | Solar evaporation is not directly comparable with RO, NF, or UF; composition, support, irradiance, feed, and collection conditions differ | Direct experimental solar-evaporation evidence; pressure-driven membrane performance not established | [12,13,43] |
| Evidence Level | What Is Currently Available | Permitted Interpretation | Evidence Still Required | Refs. |
|---|---|---|---|---|
| Direct MBene water application | Early MBene solar-evaporation studies are application-specific. | Demonstrates photothermal water production in the tested architecture. | Independent replication; water quality, salt management, durability, and standardized energy balance. | [121] |
| Direct MBene membrane | No validated pressure-driven MBene RO/NF/UF dataset was identified. | Report as an explicit evidence gap; do not estimate performance from analogous evidence. | Defined membrane composition, active area, feed, pressure, temperature, duration, and matched control. | [118,120] |
| MBene material experiments | Multiple precursor-conversion and exfoliation routes with structural characterization. | Supports claims about synthesis feasibility and route-dependent composition. | Batch yield, impurity balance, surface terminations, aqueous aging, and reproducibility. | [109,110,111,112] |
| Computational MBene evidence | Predicted structures and application-relevant properties. | Generates mechanisms and screening priorities. | Experimentally verified structure, defects, terminations, and transport under realistic water chemistry. | [117,119] |
| 2D-material analogous evidence | MXene and graphene studies demonstrate tunable nanoscale transport. | Guides variables, controls, and characterization choices. | Direct testing with true MBenes under matched conditions. | [113,114,115,116,117] |
| Translation evidence | No MBene membrane pilot or module-level evidence. | Defines a research target, not a present capability. | Scale-up, long-term operation, safety, TEA and LCA against commercial benchmarks. | [119,120] |
| Stage/Route | Variables to Record | Required Verification | Membrane Relevance | Refs. |
|---|---|---|---|---|
| Topochemical conversion | Parent phase; reagent sequence; temperature; time; separation yield. | XRD phase analysis; microscopy; composition; mass balance. | Residual precursor or oxide can change transport and apparent stability. | [109] |
| Controlled decomposition | Atmosphere; heating profile; precursor size; product porosity. | Phase fractions; pore-size evidence; surface area; morphology. | Porosity may aid transport but must be distinguished from interflake defects. | [110] |
| Gaseous-HCl conversion | Gas concentration/flow; temperature; exposure; washing. | Conversion extent; residual Al/Cl; particle dimensions; yield. | Scalability and safe reagent handling must be assessed before membrane fabrication. | [111] |
| Alkaline hydrothermal etching | Base concentration; solid/liquid ratio; time; temperature; delamination. | XRD, XPS, AFM/TEM; surface chemistry; colloidal stability. | Termination and flake-size distributions affect dispersion and channel assembly. | [112] |
| Membrane assembly | Support; deposition method; loading; thickness; drying; cross-linking. | Cross-section; defects; wet spacing; adhesion; active area. | Matched blanks isolate the MBene contribution from support and processing effects. | [113,114,115,116] |
| Transport testing | Feed composition; pressure/osmotic gradient; temperature; flow; duration. | Permeance/flux; rejection/selectivity; uncertainty; mass balance; repeats. | Common conditions and definitions are necessary for defensible comparisons. | [118,120] |
| Reporting Domain | Minimum Information | Required Controls/Replication | Decision Output | Refs. |
|---|---|---|---|---|
| Material identity | Precursor and product phases; composition; terminations; flake size/thickness; yield. | ≥3 independent batches; retained raw patterns/spectra; impurity and mass balance. | Reproducible MBene identity or return to synthesis. | [109,110,111,112] |
| Membrane construction | Configuration; support; deposition; loading; active area; dry/wet thickness; conditioning. | Matched support/polymer blank; replicated coupons; defect inspection. | Attributable membrane structure or redesign. | [113,114,115,116] |
| Feed and operation | Solutes; concentrations; pH; conductivity; temperature; pressure/gradient; flow; recovery. | Calibrated instruments; stabilization criterion; complete mass balance. | Comparable test boundary conditions. | [118,120] |
| Performance | Flux and permeance; rejection/selectivity; uncertainty; time-resolved data. | ≥3 independent membranes; commercial or established benchmark under the same conditions. | Effect size with confidence and benchmark position. | [118,119,120] |
| Durability and safety | Continuous duration; cycles; cleaning; wet aging; oxidation; leaching; post-test structure. | Blank leaching control; before/after chemistry; failure-mode record. | Stable, recoverable, and contained performance or hold. | [116,120] |
| Translation | Material/energy inventory; scale-up yield; waste; module assumptions; TEA/LCA boundaries. | Sensitivity analysis; transparent baseline; commercial comparator. | Go, hold, or stop decision with limiting variables. | [119,120] |
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Almulla, A.A.; Dweiri, F.T. MBenes for Advanced Water Treatment and Desalination Membranes: A Bibliometric, Materials Engineering, and Future Perspectives Review. Membranes 2026, 16, 258. https://doi.org/10.3390/membranes16080258
Almulla AA, Dweiri FT. MBenes for Advanced Water Treatment and Desalination Membranes: A Bibliometric, Materials Engineering, and Future Perspectives Review. Membranes. 2026; 16(8):258. https://doi.org/10.3390/membranes16080258
Chicago/Turabian StyleAlmulla, Asam Amin, and Fikri T. Dweiri. 2026. "MBenes for Advanced Water Treatment and Desalination Membranes: A Bibliometric, Materials Engineering, and Future Perspectives Review" Membranes 16, no. 8: 258. https://doi.org/10.3390/membranes16080258
APA StyleAlmulla, A. A., & Dweiri, F. T. (2026). MBenes for Advanced Water Treatment and Desalination Membranes: A Bibliometric, Materials Engineering, and Future Perspectives Review. Membranes, 16(8), 258. https://doi.org/10.3390/membranes16080258

