| Literature DB >> 36235196 |
Francisco J Cervantes1, Luis A Ramírez-Montoya1.
Abstract
Nanomaterials (NMs) have been extensively used in several environmental applications; however, their widespread dissemination at full scale is hindered by difficulties keeping them active in engineered systems. Thus, several strategies to immobilize NMs for their environmental utilization have been established and are described in the present review, emphasizing their role in the production of renewable energies, the removal of priority pollutants, as well as greenhouse gases, from industrial streams, by both biological and physicochemical processes. The challenges to optimize the application of immobilized NMs and the relevant research topics to consider in future research are also presented to encourage the scientific community to respond to current needs.Entities:
Keywords: biodegradation; bioenergy production; greenhouse gases; industrial wastewater treatment; recalcitrant contaminants
Mesh:
Substances:
Year: 2022 PMID: 36235196 PMCID: PMC9572314 DOI: 10.3390/molecules27196659
Source DB: PubMed Journal: Molecules ISSN: 1420-3049 Impact factor: 4.927
Figure 1Key environmental applications of immobilized nanomaterials (NMs). GHGs, greenhouse gases.
Application of immobilized nanomaterials for energy production.
| Immobilized NMs | Application | Achievement | Reference |
|---|---|---|---|
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| MNPs | Methane production from low-strength wastewater | 3.6-fold higher methane production as compared to the control bioreactor | [ |
| BIO | Methanogenic process | 42% higher production of methane as compared to control | [ |
| GO-OX | Methanogenic process | Higher COD and ammonium removal from protein-rich wastewater as compared to control | [ |
| MNPs | Fermentative production of ethanol | Ethanol productivity of 264 g/L-h from corn starch, maintained in several cycles | [ |
| MNPs | Fermentative production of ethanol from | Immobilized cellulase produced 5.3 g/L of ethanol along with the reuse of the nano-biocatalysts several times | [ |
| MNPs | Biodiesel production from algal oil | Yield reaching 94% was maintained several cycles under optimal conditions | [ |
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| Pd, Pt | Pd NPs immobilized together with different microorganisms to produce energy in BES | Enhanced production of hydrogen or electricity as compared to controls without NPs | [ |
| Co3S4-graphene | Lithium battery | Better cycling and greater reversible capacity as compared to the pristine Co3S4 electrode | [ |
| Ni(OH)2-graphene | Supercapacitor | Better electrode–electrolyte interaction, enhancing the conductivity of ions and electrons, resulting in a higher performance | [ |
| Graphene-CX | Aqueous supercapacitor | Combination of high porosity and electrical conductivity for 25% more capacitance and 100% more power than undoped CX at high current densities | [ |
| S-I Pd aerogel | Microfluidic fuel cell | First time microwave-assisted synthesis of Pd aerogels with enhanced power densities for formic acid electro-oxidation | [ |
BES, bio-electrochemical systems; BIO, biogenic iron oxide; COD, chemical oxygen demand; CX, carbon xerogel; GO-OX, graphene oxide-organic xerogel; MNPs, magnetic nanoparticles; NPs, nanoparticles; S-I, self-immobilized.
Figure 2Mechanisms involved in the degradation of recalcitrant pollutants mediated by immobilized NMs in bioprocesses (A) and in electrochemical systems (B). Bacteria reduce conductive NMs (e.g., nanotubes), which promote redox reactions driving the biodegradation of contaminants (A). Immobilized NMs in electrochemical systems produce reactive oxygen species (ROS), which stimulate the degradation of contaminants (B).
Application of immobilized nanomaterials for the removal of recalcitrant pollutants.
| Immobilized NMs | Removed/Transformed Contaminants | Achievement | Reference |
|---|---|---|---|
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| |||
| Pd in MEC | TCE | 93% removal efficiency vs. only 48% in the absence of Pd | [ |
| Pd in AGS | IOP | 81% removal of IOP vs. only 61% in the absence of Pd | [ |
| Pd in AGS | NP and Cr6+ | Up to 20-fold higher conversion in Pd-amended system as compared to control without Pd | [ |
| Pd in AGS | Azo dyes | Up to 10-fold increase in reduction rate as compared to control | [ |
| GSC | NB | 30–50% higher removal of NB in the presence of graphene as compared to control | [ |
| MGONS | IOP | 82% removal efficiency vs. only 51% in the absence of MGONS | [ |
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| Fe/Co in NPC | Organic pollutants | Removal of 91% within 60 min and mineralization efficiency of 90% within 240 min under neutral conditions, good stability and reusability, with low metal leaching | [ |
| Fe3O4 in MOF | Organic pollutants in OLL | 66.67% COD removal efficiency and degradation of heterocycles, phenols, and esters with increase in low-molecular-weight organics abundance | [ |
| Cu-GOr in CF | DCF | 100% DCF degradation within 1 h at 1 V constant biased potential | [ |
| Fe3O4 in CCB | Dyes | Up to 2-fold increased degradation rate as compared to Fe3O4 only | [ |
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| La/TiO2 in L | DMP | 74.4% removal vs. only 60.1% in the absence of La and only 18.3% in the absence of La/TiO2 | [ |
| Mn-CCMN | Dyes | Development of an effective and reusable photocatalyst for industrial wastewater treatment | [ |
| ZnO in AC | Dyes | Promoting removal effect when adsorption and solar photocatalysis are simultaneously used for dye removal | [ |
AC, activated carbon; AGS, anaerobic granular sludge; CCB, conductive carbon black; CCMN, chitosan conjugated magnetic nano-biocomposite; CF, carbon film; DCF, diclofenac; DMP, dimethyl phthalate: GSC, graphene-sludge composite; IOP, iopromide; L, lithium silicon powder; MEC, microbial electrolysis cell; MGONS, magnetic graphene oxide nano-sacs; MOF, metal organic framework; NB, nitrobenzene; NP, nitrophenol; NPC, nitrogen-doped porous carbon rods; OLL, old landfill leachate; GOR, reduced graphene oxide; TCE, tri-chloro-ethylene.
Figure 3Scheme of nanoparticle immobilization on different supporting materials for the treatment of polluted discharges through adsorption processes. AB, antibiotic; AC, activated carbon; AG, aerogel; AM, alkali-metal-based material; CNT, carbon nanotube; EP, emerging pollutant; HG, hydrogel; HM, heavy metal; MC, monolithic carbon; MO, metal oxide; MOF, metal organic framework; MNP, magnetic nanoparticle; OP, organic pollutant; OPC, ordered porous carbon; POP, persistent organic pollutant; QD, quantum dot; ZVM, zero valent metal.
Adsorption of pollutants using immobilized nanomaterials.
| Supporting Material | Nanomaterial | Pollutants | Q (mg/g) | SSA (m2/g) | Reference | ||
|---|---|---|---|---|---|---|---|
| Support | Composite | Support | Composite | ||||
| A-Chitosan | Ni2+ | Pb2+ | 21.0 | 50.3 | NA | NA | [ |
| Bamboo BC | MgO | Phosphate | 1.3 | 370 | NA | 399 | [ |
| Chitosan | Fe0 | Bisphenol-A | NA | 65.2 | NA | NA | [ |
| Chitosan | Bio-CuO | Congo red, Eriochrome black T | NA | 119.7, 235.7 | 15.84 | 25.3 | [ |
| CNT | MgO | Hg2+ | NA | 58.8 | 91.3 | 110.4 | [ |
| Corn stem BC | Fe-Mn | As2+ | 2.9 | 8.3 | 60.9 | 208.6 | [ |
| Douglas fir BC | α-Fe2O3, Fe3O4 | Nitrate, fluoride | NA | 15.5, 9.0 | 663 | 494 | [ |
| HCS BC | Fe0 | Pb2+, Cu2+, Zn2+ | NA | 195.1, 161.9, 109.7 | 1216 | 603.4 | [ |
| MOF-WC | Co | Congo red, Methylene blue | 613.6, 469.5 | 1117.0, 805.1 | NA | 170.4 | [ |
| Polydopamine | Graphene and Fe3O4 | Methylene blue | 110 | 140.3 | NA | 85.6 | [ |
| PC | Co | Sr2+ | NA | 3.21 | NA | NA | [ |
| Silica | HC | Cd2+, Pb2+, Ni2 | NA | 0.5, 8.9, 13.5 | 195 | 197 | [ |
| Silica | Au | Toluene | NA | 1360 | 465.3 | 367.4 | [ |
| Silica aerogel | La(OH)3 | Phosphate | 19.2 | 153.8 | 561.0 | 252.7 | [ |
A, aminophosphorylated; BC, biochar; CNT, carbon nanotubes carbon; HC, hydrophilic carbon; HCS, hydrophilic corn stalk; MOF-WC, metal–organic-framework wood composite; NA, not available; PC, phosphorylated chitosan.