| Literature DB >> 30345212 |
Katrina Pui Yee Shak1, Yean Ling Pang1, Shee Keat Mah1.
Abstract
Among many other sustainable functional nanomaterials, nanocellulose is drawing increasing interest for use in environmental remediation technologies due to its numerous unique properties and functionalities. Nanocellulose is usually derived from the disintegration of naturally occurring polymers or produced by the action of bacteria. In this review, some invigorating perspectives on the challenges, future direction, and updates on the most relevant uses of nanocellulose in environmental remediation are discussed. The reported applications and properties of nanocellulose as an adsorbent, photocatalyst, flocculant, and membrane are reviewed in particular. However, additional effort will be required to implement and commercialize nanocellulose as a viable nanomaterial for remediation technologies. In this regard, the main challenges and limitations in working with nanocellulose-based materials are identified in an effort to improve the development and efficient use of nanocellulose in environmental remediation.Entities:
Keywords: adsorbent; environmental remediation; membrane; nanocellulose; nanomaterials; photocatalyst
Year: 2018 PMID: 30345212 PMCID: PMC6176822 DOI: 10.3762/bjnano.9.232
Source DB: PubMed Journal: Beilstein J Nanotechnol ISSN: 2190-4286 Impact factor: 3.649
Figure 1Size chart of nanocellulose based on material length (with microscopic images of various nanocellulose sources). Reprinted in part from Huang et al. [25], Nguyen et al. [26], Razalli et al. [27], and Kunusa et al. [28].
Figure 2The structures of (a) cellulose nanofibers (CNFs) and (b) cellulose nanocrystals (CNCs) produced from cellulose.
Figure 3Resultant chemical structures of nanocellulose prepared via (a) mechanical refining, enzymatic hydrolysis, hydrolysis using hydrochloric acid, (b) hydrolysis using sulphuric acid, and (c) TEMPO-oxidation.
Cellulose-based biopolymer adsorbents for various types of organic pollutants.
| Biopolymer adsorbent | Model pollutants | Adsorption capacity (mg/g) | Duration (min) | Ref. |
| calcium hydroxyapatite microfibrillated cellulose | Cr(VI) | 114.79 | 5 | [ |
| magnetic Fe3O4@SiO2@cellulose composite | Cr(VI) | 171.5 | 30 | [ |
| aminopropyltriethoxysilane-modified microfibrillated cellulose | Ni(II) | 159.88 | 300 | [ |
| cotton fibre functionalized with triethylenetetramine and carboxymethyl chitosan | Pb(II) | 144.93 | 120 | [ |
| poly(itaconic acid)–poly(methacrylic acid)-grafted-nanocellulose/nanobentonite composite | Co(II) | 350.8 | 120 | [ |
| U(VI) | 121.02 | 120 | [ | |
| MnO2-loaded biocomposite based on microcrystalline cellulose | Pb(II) | 247.5 | 180 | [ |
| sulphonated cellulose | Fe(III) | 98.7 | 30 | [ |
| sulphonated nanofibrillar cellulose | Pb(II) | 248.6 | 1200 | [ |
| cationic cellulose nanofibers functionalized with glycidyltrimethylammonium chloride | PO43− | 55 | [ | |
| nanocellulose-amino linked by maleic acid supported on magnetite | arsenic | 85.3 | 90 | [ |
| Fe3O4@cellulose core–shell magnetic biopolymer | congo red | 131 | 11 | [ |
| amino-functionalized nanocrystalline cellulose | acid red GR | 134.7 | 300 | [ |
| carboxylate-functionalized adsorbent based on cellulose nanocrystals | crystal violet | 243.90 | 240 | [ |
| functionalization of cellulose with hyperbranched polyethylenimine | congo red | 2100 | 60 | [ |
| cellulose nanocrystal–alginate hydrogel beads | methylene blue | 255.5 | 210 | [ |
| cellulose aerogel based on cationic cellulose nanofibrils | blue dye CR19 | 230 | 80 | [ |
Application of nanostructured cellulose-based hybrid photocatalysts in photocatalytic degradation of various types of organic pollutants.
| Type of catalyst | Model pollutants | Light source | Photocatalytic degradation efficiency (%) and reaction time (min) | Ref. |
| graphene oxide and TiO2 nanoparticle incorporated alginate/carboxymethyl cellulose nanocomposite | 30 mL of 30 mg/L congo red | solar light with average intensity of ≈900 W/m2 | 98%, 240 min | [ |
| nanoscale zinc oxide incorporated graphene oxide/nanocellulose composite | 25 mL 2–4 mg/L ciprofloxacin | solar light 100 mW/cm2 | 98%, 40 min | [ |
| ZnO/cellulose nanocomposite | 50 mL 3.25 g/L methylene blue | UV lamp with unknown wavelength and intensity | 79%, 300 min | [ |
| hydroxypropyl cellulose/molybdenum disulphide nanocomposite hydrogels | 250 mL methylene blue | sunlight | 90%, 180 min | [ |
| TiO2–hydroxypropyl methyl cellulose nanocomposite | 100 mL 10 ppm 4-nitrophenol | 250 W halogen lamp (main range 400–800 nm) | 85%, 180 min | [ |
| graphene oxide/TiO2/bacterial cellulose nanocomposite | 100 mL 10 mg/L methyl orange | UV lamp (365 nm, 175 W) | 100%, 120 min | [ |
| alginate/carboxymethyl cellulose/TiO2 nanocomposite hydrogel | 30 mL 30 mg/L congo red | sunlight | 91.5%, 240 min | [ |
| nanocrystalline TiO2 on cellulose fabric | 99.995% CO2 at flow rate 300 mL/min for 1 h | four UVA lamps (8 W each lamp) λ = 365 nm | 194.0 ppm/g and 50.8 ppm/g for CO and CH4, 360 min | [ |
| CdS nanoparticle/bacterial cellulose nanofibers | 200 mL 20 ppm methyl orange | 300 W Xe lamp with a cut-off of λ < 420 nm | 82%, 90 min | [ |
| cellulose fibre supported zinc phthalocyanine | 10 mL of 50 μM basic green 1 | 100 W lamp visible light, λ > 400 nm | 98%, 90 min | [ |
| immobilized Cu2O nanoparticles in cellulose/graphene oxide composite film | 10 mg/L methyl orange | sunlight (cloudy, 20 °C) | 72%, 300 min | [ |
| N-doped TiO2 nanorods in regenerated cellulose thin films | 150 mL 40 mg/L methylene blue | UV lamp at λ = 312 nm, 30 W | 96%, 360 min | [ |
| electrospun cellulose acetate membrane supported Ag@AgCl | methyl orange | 500 W Xe arc lamp equipped with a UV cut-off filter (λ > 420 nm) | 73% , 160 min | [ |
| immobilized TiO2 nanoparticles and laccase on bacterial cellulose membrane | 3 mL 15 mg/L reactive red X-3B | UV irradiation with unknown wavelength and intensity | 95%, 180 min | [ |
| graphene oxide/TiO2 based ultrafiltration cellulose membranes | 3.40 × 10−5 mol/L diphenhydramine at flow rate of ≈0.25 mL/min | UV irradiation 350 nm and 33 mW/cm2 | 65%, 240 min | [ |
Application of cellulose-based flocculants in wastewater treatment.
| Flocculant | Model pollutant | Analytical test | Optimum result (%) | Ref. |
| anionic sodium carboxymethylcellulose | natural surface water | turbidity | 93 | [ |
| anionic dicarboxylic acid nanocellulose | municipal wastewater | turbidity | 80 | [ |
| crystalline nanocellulose grafted with cationic pyridinium functional groups | freshwater microalgae | microalgae biomass | 95 | [ |
| nanofibrillated into cationic nanocelluloses | activated sludge | turbidity | 90 | [ |
| cationic dialdehyde cellulosic nanofibrils | kaolin wastewater | colloid aggregation | 95 | [ |
| anionic sulphonated nanocelluloses | municipal wastewater | turbidity | 80 | [ |
| hydroxypropyl methyl cellulose grafted with polyacrylamide | mine wastewater | turbidity | 94 | [ |
| cationic pyridinium cellulose nanocrystals | microalgal biomass | flocculation efficiency | 100 | [ |
| cationic cellulose nanofibrils | municipal activated sludge | turbidity | 90 | [ |
| anionic carboxylated cellulose nanocrystals | kaolin suspension | turbidity | 80.9 | [ |
| rod-shaped cellulose nanocrystals | flocculation and phase separation of bacteria | aggregation percentage | 100 | [ |
| poly( | kaolin suspension | turbidity | 69–91 | [ |
Application of nanocellulose material in membrane technology for environmental remediation.
| Membrane application | Cellulose type | Membrane fabrication feature | Membrane type | Operating condition | Membrane performance | Ref. |
| wastewater treatment (to remove urea) | nanocellulose | metalized nanocellulose composites–thin film composite membrane (MNC-TFC) | forward osmosis membrane | crossflow forward osmosis | water flux (LMH/bar): | [ |
| removal of heavy metals (ion exchange of Cd(II) ions) | cellulose nanofibers | regenerated cellulose nanofiber membrane with poly(glycidyl | ion exchange membrane | dead-end filtration | maximum Cd binding capacity, | [ |
| carbon dioxide capture | cellulose nanofibers | casting of pure microfibrillated cellulose membrane (MFC) and MFC–polyvinylamin (Lup) 50/50 wt/wt nanocompositemembrane | gas permeation membrane | gas permeation with constant humidity control; temperature, 35 °C; low pressure condition, 1 bar | selectivity: | [ |
| removal of metal ions (removal of Ag+, Cu2+ and Fe2+/ Fe3+ ions) | cellulose nanofibers; cellulose nanocrystals (cellulose sludge based (SL) and bioethanol based (BE)); | support layer fabricated by vacuum filtration of cellulose nanofibers (CNF) and active layer fabricated by dip coating of cellulose nanocrystals (CNC) | ultrafiltration membrane | crossflow filtration | removal (%): | [ |
| adsorption of metal ions | cellulose nanofibers; cellulose nanocrystals (cellulose sludge based (SL) and bioethanol based (BE)); | support layer fabricated by vacuum filtration of cellulose sludge (S) or cellulose sludge with nanocellulose nanocrystal (SL) and active layer fabricated by further vacuum filtration of cellulose nanocrystals (CNC); in situ TEMPO functionalization on active layer | ultrafiltration membrane | crossflow filtration | adsorption capacity (mg/g): | [ |
| removal of dyes | cellulose nanocrystals | casting of cellulose nanocrystals and chitosan solution | ultrafiltration membrane | dead-end filtration | removal (%): | [ |
Figure 4The morphology of MNC forward osmosis membranes with amino silane functionality as well as Pt and Ag nanoparticles. The ridge-and-valley morphology is commonly attributed to polyamide membranes. Reprinted (adapted) with permission from [146], copyright 2017 American Chemical Society.