| Literature DB >> 35323762 |
Syafiqah Syazwani Jaffar1, Suryani Saallah1, Mailin Misson1, Shafiquzzaman Siddiquee1, Jumardi Roslan2, Sariah Saalah3, Wuled Lenggoro4.
Abstract
Extensive research and development in the production of nanocellulose production, a green, bio-based, and renewable biomaterial has paved the way for the development of advanced functional materials for a multitude of applications. From a membrane technology perspective, the exceptional mechanical strength, high crystallinity, tunable surface chemistry, and anti-fouling behavior of nanocellulose, manifested from its structural and nanodimensional properties are particularly attractive. Thus, an opportunity has emerged to exploit these features to develop nanocellulose-based membranes for environmental applications. This review provides insights into the prospect of nanocellulose as a matrix or as an additive to enhance membrane performance in water filtration, environmental remediation, and the development of pollutant sensors and energy devices, focusing on the most recent progress from 2017 to 2022. A brief overview of the strategies to tailor the nanocellulose surface chemistry for the effective removal of specific pollutants and nanocellulose-based membrane fabrication approaches are also presented. The major challenges and future directions associated with the environmental applications of nanocellulose-based membranes are put into perspective, with primary emphasis on advanced multifunctional membranes.Entities:
Keywords: adsorbent; environmental remediation; membrane; nanocellulose; photocatalyst; water filtration
Year: 2022 PMID: 35323762 PMCID: PMC8950644 DOI: 10.3390/membranes12030287
Source DB: PubMed Journal: Membranes (Basel) ISSN: 2077-0375
Figure 1(a) Molecular structure of cellulose and (b) intramolecular (blue-dotted line) and intermolecular (red-dotted line) hydrogen bonding formation in cellulose.
Figure 2Overview of the highlights of the present review: desirable properties of nanocellulose, surface modification strategies, approaches for nanocellulose-based membrane fabrication and their environmental applications.
Density and mechanical properties of high-performance materials in comparison to nanocellulose.
| Material | Density, | Tensile Strength, σ | Elastic Modulus, E | Reference |
|---|---|---|---|---|
| Stainless steel 304 | 8.00 | 0.50–0.70 | 193 | [ |
| E-glass fiber | 2.54–2.60 | 0.52–3.79 | 72.40 | [ |
| TORAYCA carbon fiber | 1.79 | 7.00 | 324 | [ |
| Kevlar 49 Aramid fiber | 1.47 | 3.45 | 179 | [ |
| Nanocellulose | 1.6 | 2–7.7 | 110–220 | [ |
Mechanical properties of nanocomposites reinforced with nanocellulose.
| Material | Nanocellulose Composition (%) | Tensile Strength (MPa) | Tensile Strain (%) | Young’s Modulus (GPa) | Reference |
|---|---|---|---|---|---|
| GO/CNF | 0 | 50.2 ± 6.3 | 4.8 ± 1.3 | 2.99 ± 0.31 | [ |
| 1 | 74.4 ± 2.8 | 4.8 ± 0.9 | 3.90 ± 0.84 | ||
| 4 | 80.0 ± 14.9 | 5.9 ± 2.5 | 4.13 ± 0.73 | ||
| SF/CNF | 0 | 66 ± 18.9 | 18.6 ± 8.5 | 1.2 ± 0.2 | [ |
| 5 | 111.1 ± 11.7 | 12.7 ± 0.4 | 2.0 ± 0.2 | ||
| 10 | 140.1 ± 14.3 | 12.3 ± 0.6 | 2.7 ± 0.2 | ||
| 15 | 143.5 ± 8.3 | 11.4 ± 1.6 | 3.0 ± 0.1 | ||
| PNC/Nafion | 0 | 11.5 | ~50 | 0.35 | [ |
| 3 | 15.15 | ~25 | 0.54 | ||
| 7.5 | 13.00 | ~20 | 0.75 | ||
| Celery CNF/Lignin/hemicellulose | 0 | 24.1 ± 0.9 | 0.5 ± 0.1 | 4.83 ± 0.10 | [ |
| 10 | 39.0 ± 4.1 | 0.6 ± 0.1 | 7.10 ± 0.31 | ||
| 20 | 72.5 ± 0.3 | 1.1 ± 0.2 | 6.42 ± 0.14 | ||
| 30 | 79.3 ± 3.4 | 1.4 ± 0.1 | 5.62 ± 0.24 | ||
| 50 | 85.2 ± 2.6 | 2.6 ± 0.3 | 3.25 ± 0.16 | ||
| PAN | 0 | 150 ± 10 | 44 ± 16 | 5.9 ± 0.4 | [ |
| PAN/c-CNC | 0.1 | 190 ± 10 | 21 ± 5 | 6.7 ± 0.4 | |
| PAN/s-CNC | 0.1 | 190 ± 10 | 19 ± 6 | 7.0 ± 0.2 | |
| PAN/s-CNF | 0.1 | 150 ± 2 | 22 ± 7 | 6.3 ± 0.4 | |
| CNC/PVA | 0 | 117 | 0.7 | 32 | [ |
| 0.5 | 98 | 1.4 | 26 | ||
| 1.0 | 105 | 12 | 15 | ||
| 1.5 | 104 | 5 | 20 | ||
| 2.0 | 118 | 7 | 20 | ||
| 4.0 | 132 | 10 | 30 | ||
| 6.0 | 155 | 1.4 | 38 | ||
| CMC/CNC | 0 | 6.10 ± 0.24 | 201.73 ± 0.15 | na | [ |
| 0.1 | 7.23 ± 0.71 | 101.05 ± 1.32 | |||
| 0.5 | 9.98 ± 0.55 | 70.53 ± 0.23 | |||
| 1 | 12.30 ± 0.30 | 89.53 ± 0.18 | |||
| PLA/LNC | 0 | 40 ± 1 | 70 ± 20 | 1.77 ± 0.10 | [ |
| 1 | 45 ± 3 | 30 ± 10 | 1.74 ± 0.14 | ||
| 3 | 26 ± 1 | >230 | 1.13 ± 0.10 | ||
| 5 | 27 ± 4 | >130 | 1.06 ± 0.06 | ||
| 10 | 21 ± 2 | 35 ± 10 | 1.01 ± 0.06 | ||
| 20 | 18 ± 2 | 30 ± 10 | 0.95 ± 0.03 | ||
| PEO/CNC | 0 | 14.2 ± 0.9 | 86 ± 14 | 0.76 ± 0.19 | [ |
| 1 | 15.9 ± 0.1 | 495 ± 43 | 0.82 ± 0.20 | ||
| 4 | 16.0 ± 0.8 | 504 ± 34 | 0.90 ± 0.14 | ||
| 7 | 17.6 ± 0.7 | 526 ± 40 | 0.94 ± 0.15 | ||
| 10 | 15.3 ± 0.2 | 416 ± 43 | 0.76 ± 0.33 | ||
| PEO/CNF | 1 | 17.7 ± 0.9 | 491 ± 21 | 0.90 ± 0.10 | [ |
| 4 | 20.8 ± 0.7 | 281 ± 56 | 0.99 ± 0.22 | ||
| 7 | 27.3 ± 0.9 | 340 ± 62 | 1.73 ± 0.10 | ||
| 10 | 14.4 ± 0.5 | 89 ± 55 | 1.24 ± 0.10 |
Figure 3Crystalline and amorphous regions of cellulose as well as the interfibrillar network among cellulose molecules.
Figure 4Mechanism of dispersion-induced disordering of the interfacial molecules between bundled microfibrils in a wood cellulosic structure that affect the crystallinity. Adapted from [47].
Figure 5Illustration of antifouling behavior of nanocellulose barrier layer on nanocomposite membrane.
Figure 6Chemical modification of nanocellulose.
Figure 7Mechanism of TEMPO-mediated oxidation.
Figure 8Silylation process of nanocellulose.
Figure 9General procedures for the development of nanocellulose-based membranes through vacuum filtration, phase inversion, electrospinning, freeze drying, and interfacial polymerization.
Figure 10Setup of electrospinning system and mechanism of Cd2+ adsorption on the chitosan/PNC membrane.
Figure 11(a) Honeycomb structure produced by freeze drying of nanocellulose suspension and (b) mechanism of nanocellulose aggregation and ice-crystals growth along the freezing direction.
Figure 12Type of membrane filtration: microfiltration (MF), ultrafiltration (UF), nanofiltration (NF), and reverse osmosis (RO).
Different types of nanocellulose-based membranes for water filtration.
| Materials | Method of Preparation | Filtration Process | Sample | Performance | Reference |
|---|---|---|---|---|---|
| Nanocellulose/filter paper (NC/FP) composite membrane | Vacuum filtration | UF | Oily wastewater | Up to 97.14% retention rate; 46,279 L m−2 h−1 flux | [ |
| Metalized nanocellulose (silver and platinum as additive) | Vacuum filtration | FO | Nanopure water, urea, and wastewater | High water flux and solute rejection with wastewater sample | [ |
| Cellulose acetate membrane | Phase separation | UF | Wastewater | 207.32 L m−2 h−1 pure water permeability; 90.56% flux recovery ratio | [ |
| Cellulose acetate/copper oxide nanoparticles | Wet precipitation | UF | Wastewater | Improved hydrophilicity, water permeation, BSA separation, and antifouling performance | [ |
| Cellulose membrane | Thermally inducedphase separation | MF | Oily wastewater | 99% rejections to peanut oil and pump oil nanoemulsion | [ |
| Nanocellulose as modifer for hollow fiber | Addition of nanocellulose to internal coagulant | UF | Dye | Permeability increased 1.5 times; rejection increased from 96 to 99% | [ |
| Biocellulose nanofibers membrane | Biosynthetic process followed by a purification step involving alkali treatment | NF | Emulsified oily wastewater | 99% separation efficiency; permeate flux recovery ratio >94% | [ |
| Carbon nanofiber (CNF)/cellulosic membranes | Carboxylic and amine functionalized CNFs | FO | Desalination | 15 L m−2 h−1 water flux | [ |
| Cellulose triacetate (CTA) and novel thin film composite | Calcium alginate as a model foulant. | FO | Desalination | Physical cleaning was more efficient | [ |
| CNC and TOCNF coated polyethersulfone (PES) membrane | Layer-by-layer deposition | MF | Water | Improved antifouling and antibacterial properties | [ |
Nanocellulose-based adsorbents for the removal of specific pollutants.
| Membrane Material | Target Compound | Adsorption Capacity (mg/g) | Removal Efficiency (%) | Reference |
|---|---|---|---|---|
| Amino-modified nanocellulose | Boron | 120.9 | 86.73 | [ |
| (EFB)-based nanocellulose functionalized with activated carbon | Pb2+ | 24.94 | 86 | [ |
| Electrospun CS/PEO/PNC | Cd2+ | 62.3 | n.a | [ |
| TOCNF/graphene oxide/trimethylolpropane-tris-(2-methyl-1-aziridine) propionate | Pb2+ | 571 | n.a | [ |
| Cu2+ | 462 | |||
| Zn2+ | 361 | |||
| Cd2+ | 263 | |||
| Mn2+ | 208 | |||
| TOCNF/Si/NH2 | Cu2+ | 99.0 | 95.6 | [ |
| Cd2+ | 124.5 | 85.2 | ||
| Hg2+ | 242.1 | 96.9 | ||
| Magnetic grass nanocellulose | Cerium (III) | 353.04 | n.a | [ |
| Cellulose microcrystalline for TLC | Disperse yellow | n.a | 62.5 | [ |
| Cinnamon nanocellulose | Methyl orange | n.a | 90.4 ± 2.3 | [ |
| Cross-linked poly(2-methacryloyloxyethyl phosphorylcholine) and bacterial nanocellulose | Methylene blue | 4.44 ± 0.32 | n.a | [ |
| Methyl orange | 4.56 ± 0.43 | |||
| Electrospun PHA/CNC/Cs | Congo red | 18.95 | 75.8 | [ |
| EDTA-embedded nanocellulose | Methylene blue | n.a | 91.14 | [ |
| Acid-Resistant Chitosan/CNF | Methylene blue | 14.71 | n.a | [ |
| Nanocellulose/SiO2 | Tar | n.a | 92.23 | [ |
| Total particulate matter | 90.25 | |||
| Nicotine | 95.02 | |||
| CO | 20.63 |
Figure 13Mechanism of photocatalytic degradation of methylene blue by TiO2/GO/cellulose membrane.
Nanocellulose-based photocatalysts for pollutant degradation.
| Membrane Material | Degraded Compound | Photocatalytic Performance | Reference |
|---|---|---|---|
| Anatase TiO2/CNF | Methyl orange | 99.72% degradation within 30 min, no obvious activity loss after reused for five cycles | [ |
| CeO2/TiO2-CNC | Rhodamine B | Complete removal of MO and RhB, and reduction of Cr(VI) solution within 70, 50, and 60 min | [ |
| ZnO/NC | Enrofloxacin | 97% degradation efficiency within 120 min | [ |
| Ag3PO4/NC | Methyl orange | 90% degradation efficiency in DI and 70% in wastewater within 80 min | [ |
| Fe-doped ZnO/NC | Methylene blue | 98.84% degradation efficiency within 90 min, 92% degradation efficiency after reused for 5 cycles | [ |
| NC/γ–Fe2O3–ZrO2 | Congo red | Increase degradation efficiency from 80.0% to 98.5% in 30 min | [ |
| TiO2/CNC | o-chloranil | ~90% degradation after 2 h | [ |
| TiO2/CNC | Methyl orange | 100% degradation in less than 6 h | [ |
| CNF//PEI/Ag | Methylene blue | Up to 98% degradation efficiency after 10 times reuse, high water flux (up to 5 × 104 L·m−2 h−1) | [ |
Figure 14Mechanism of CO2/N2 separation using PVA/CNC as active layer.
Nanocellulose-based pollutant sensors.
| Type of Sensor | Material | Target Pollutant | Reference |
|---|---|---|---|
| Electrochemical sensor | Copper ions | [ | |
| Colorimetric sensor | Aromatic imide functionalized nanocellulose and branched polyethyleneimine | Fluoride | [ |
| Optical plasmonic chemosensor | Copper nanoparticles embedded with flexible nanocellulose | Cyanide | [ |
| Biosensor | Cyanobacterial C-phycocyanin (CPC)/TOCNF | Copper ions | [ |
| Optical sensor | In situ synthesized AgNPs embedded nanopaper | Chiral compounds | [ |
| Optical sensor | Carbon quantum dots embedded nanopaper | Iodide | [ |
| Electrochemical sensor | Rice-husk derived CNF and TOCNF/glycerol | Water soluble gases (ammonia, acetone, methane, hydrogen sulfide) | [ |
| Fluorescent sensor | Carbon Dots-Rhodamine B (CDs-RhB) nanohybrid on nanopaper | Cadmium (Cd), lead (Pb), mercury (Hg), copper (Cu) and iron (Fe) ions | [ |
| Optical sensor (SERS) | Gold nanorod/Silver nanocubes (AuNRs/AgNCs) embedded on bacterial nanocellulose network | 2,4,6-trinitrotoluene (TNT) | [ |
| Chemiresistive sensor | Nanocellulose/graphene oxide membrane attached to SnO2 | Hydrogen gas | [ |
Figure 15Mechanism of electricity generation in fuel cell.
Figure 16Schematic representation of piezoelectric nanogenerator (PENG) and triboelectric nanogenerator.