Functionalized Nanomaterials for Catalytic Application

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With the rapid development in nanotechnology, it is now possible to modulate the physical and chemical properties of nanomaterials with molecular recognition and catalytic functional applications. Such research efforts have resulted in a huge number of catalytic platforms for a broad range of analytes ranging from metal ions, small molecules, ionic liquid and nucleic acids down to proteins. Functionalized nanomaterials (FNMs) have important applications in the environmental, energy and healthcare sectors. Strategies for the synthesis of FNMs have contributed immensely to the textile, construction, cosmetics, biomedical and environmental industries among others.
This book highlights the design of functionalized nanomaterials with respect to recent progress in the industrial arena and their respective applications. It presents an inclusive overview encapsulating FNMs and their applications to give the reader a systematic and coherent picture of nearly all relevant up-to-date advancements. Herein, functionalization techniques and processes are presented to enhance nanomaterials that can substantially affect the performance of procedures already in use and can deliver exciting consumer products to match the current lifestyle of modern society.

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Figure 12 Electrocatalytic degradative action to protect the water system - фото 3

Figure 1.2 Electrocatalytic degradative action to protect the water system.

1.3 Electro-Fenton/Hetero Electro-Fenton as FNMs

Fenton’s redox chemistry employs ·OH released between the reacting species (H 2O 2+ Fe 2+) for the decomposition of target pollutants (TPs), where electro-Fenton (EF) or photoelectro Fenton (P-EF) have prominent roles. Hetero-EF (H-EF) utilizes solid nanocatalyst as a supporter for reducing H 2O 2→ ·OH. The disadvantage of small pH range (acidic) is overcome by solid supporters when used. The effluents released into the water system have a wide range of pH [47]. Micro-porous/meso-porous FNMs offer best solutions for degrading OPs in the water bodies. Research communities are focusing on this segment for protection of environmental crises using Fe/other transition metal/metal oxides as cathodic FNMs in H-EF methods.

Cathodic FNMs are got by (i) uni/multi step synthesis of low-density porous-solids (C aerogels), (ii) modified conducting FNMs with Fe, and (iii) carbonaceous solids supported with Fe or other components as FNMs [48–50]. Formation of sludge as Fe-hydroxides, as in normal Fentons, is retarded or inhibited, thus improving the efficiency and availability of catalyst for its activity. Hence, less energy utilization and a cost-effective approach is favored. Similarly, reusability and recyclability for many trials were observed while using cathodic FNMs of Fe 2O 3/N-C by [51] and Fe-Cu-C aerogel [52]. However, Fe when strengthened with other metals (transition) embedded in it, results in a redox reaction with catalytic decomposition, and is favored with the increase in efficacy of the electrocatalytic system to bring about degradation of TPs [53–55]. A figurative description of the functionalized catalytic activity is shown in Figure 1.3.

In a typical report of Cui, L. et al ., MO decomposition by H-EF was proved to be accelerated by FNM - Fe 3O 4/MWCNTs, when prepared by solvothermal process. Degradability of the TP was noted to be 90.3% (3 h) with reusability to 5 runs, at pH (3). This system with two compartments of FNM membrane required no external additives, but had a potency in green wastewater treatment techniques [56]. Zhao, H. et al . reported that Fe 3O 4@Fe 2O 3/ACA (activated C aerogel) as cathodic in this EF routine degraded (90%) of OP-pesticide imidacloprid (30 min) and TOC (60 min) in pH range of (3–9) [57]. Haber-Weiss model inferred that Fe 2+aided the decomposition of peroxide to form ·OH. ·OH and ·O 2−contribute for the degradation of OP. Mesoporous FNMs MnCo 2O 4-CF (C felt) as cathodic EF with excellent porosity and large modified surface area prepared showed a powerful degrading capacity for CIP (100%) an antibiotic in 5 h and TOC (75%) in 6 h [58]. Mn 2+/Mn 3+, Co 3+/Co 2+with e −transfers enhanced peroxide decomposition to form ·OH and ·OOH required for five cycles degradation.

Figure 13 ElectroFenton functionalized catalytic degradative activity for - фото 4

Figure 1.3 Electro-Fenton functionalized catalytic degradative activity for water bodies.

Table 1.1 Electro-Fenton (EF)/Hetero-Electro-Fenton (H-EF) catalyst as FNMs.

FNMs as catalyst | Type | Year Process | Current/Voltage Parametric expressions Solution evolved (% degradation) | Reusable cycles Remarks Ref.
BGA-GDE | EF | 2019 Hydrothermal | 4.5 mA cm −2 pH (3–9) | 60 min BPA (~89.65%) | 5 TOC (~90%) | 5 ·OH | pseudo-1 st-order kinetics [62]
RGO-Ce/WO 3NS/CF | EF | 2018 Hydrothermal | 300–400 mA pH (3) | 1h CIP (100%) | 5 ·O 2−, H 2O 2, ·OH | Ce-WO 3improved adsorption [63]
ACF-HPC | EF | 2019 Hydrothermal, carbonization | (16, 20, 24) mA cm −2 pH (3, 7, 9) | 40, 180 min Phenol (93.8%) | 5TOC (85.7%) | 5 Enhanced formation of H 2O 2, ·OH | Low-cost [64]
Fe-C/PTFE | H-EF | 2015 Ultra-sonification | 100 mA pH (6.7) |120 min 2,4-DCP (95%) | pseudo-1 st-order kinetics | promoters: H 2O 2, ·OH | Cheap [65]
N-C (NF) as (c PANI/GF2) | EF | 2019 Carbonization (PANI) |−0.6 V pH (3) |180 min Mineralization (42%) | Florfenicol (99%)| Phenol (85%) | MO (100%) | 5 Activation: H 2O 2→ ·OH [66]
FeO x/NHPC750 | H-EF | 2020 Hydrothermal, carbonization | (−3.30, −4.42, −3.77) mA cm −2| −0.6 V pH (6) |90 min ATZ (96%) | Rh B (99%) | 2,4-DCP (99%) | Sulfamethoxazole (95%) | Phenol (99%) | 5 Cleavage of O-O bond | Assists H 2O 2| Fe 2++ O 2→ Fe 3++ ·O 2− [67]
(Co, S, P)/MWCNTs | P-EF |2019 Hydrothermal | 40 mA cm −2 pH (3) |360 min Bronopol (100%) |TOC (77%) | 3 Contributors: sunlight, ·OH, BDD ( ·OH) | [68]
Mn/Fe@porous C (PC)-CP cathode | H-EF | 2019 Carbonization | 40 mA pH (2–8) |120 min, 240 min TCS (100%) | TOC (~57%) | 6 Regeneration: Fe 2+/Mn 2+/3+| e-transfer: Fe 2+/ 3+, Mn 2+/ 3+/ 4+,pseudo-0-order kinetics [69]
3DG/Cu@C | H-EF | 2020 Hydrothermal, calcination | 30 mA pH (3–9) | 150 min Rh B (100%) | CIP (100%) | 2,4-DCP (100%) | PCA (89.8%) | BPA (96.1%) | CAP (82.6%) | 5 Contributors: ·OH, ·O 2−| e- transfer: Cu 2+/ + [70]
C felt/Fe-Oxides | H-EF | P-EF | 2016 Electro-deposition | 21.7 mA cm −2 pH (3) |120 min MG (98%) | 10 ·OH, BDD - activators | UVA | pseudo-1 st-order kinetics | [71]
(N-G@CNT | EF | 2108 Hydrothermal | variable | −0.2 V pH (3) |180 min DMP (100%) | 20TOC (40.4%) Fe 2++ H 2O 2→ Fe 3++ e −| pseudo-1 st-order kinetics [72]
F-rGO/SS membrane | EF | 2019 Electrophoretic deposition | 170 mA | −0.5 V pH (3) | PCM (37%) | 5 e -transfer-enhanced by rGO | low-cost membrane [73]
G-CNT-CE | EF | 2014 Electrophoretic deposition | 0.18 A pH (3) |210 min Acid Red 14 (91.22%) |Acid Blue 92 (93.45%) pseudo-1 st-order kinetics | pseudo-2 nd-order kinetics [74]
Fc-ErGO | EF | 2018 Electrochemical | −1.5 V | (−0.75, −1.0, −1.5, −2.5) V pH (3) | 15 min | pH (7) | 120 Min CIP (99%) | 5 ·OH | pseudo-1 st-order kinetics [75]
FeOCl-CNT | EF | 2020 Thermal-induced | −0.8 V pH (wide) | TC (99.5%) | Fe 3+/Fe 2+| H 2O 2+ ·OH → H 2O + ·OOH [76]
3D GA/Ti wire | EF | 2018 Hydrothermal | [0 – (−95.5)] mA cm −2 pH (2) |120 min EDTA-Ni (m73.2%) | 5 π-π interaction | pseudo-1 st-order kinetics [77]

H-EF system with Fe oxides surrounded by Cu and N on HPC (hollow porous C) as cathodic FeO x/CuN xHPC was inferred to give a good degradability for phenol (100%/90 min/variable pH) and (81%/120 min/pH6). Slow redox reaction (Fe 2+/Fe 3+) favored e −movement, and formation of ·OH, that were essentials for degradation in this ambient condition [59]. In a similar fashion a three-layered H-EF catalyst as FMN “CFP@PANI@Fe 3O 4” engineered using electrodeposition-solvothermal method was proven for the removal of 4-NP (100%/60 min/4 runs) at an acidic pH (3) and TOC (51.2%/7 runs) at the same pH [60]. Enrichment of electrocatalytic capacity was attributed to formation of Fe 3O 4on the functionalized surface of the conducting layers. Wang, Y. et al . fabricated γ-FeOOH GPCA cathodic EF-catalyst for experimenting the degradability of the antibiotic sulfamethoxazole (~90%/5runs). Twelve degraded products by, hydroxylation, isomerization, and oxidation reactions were identified using chromatographic trials [61]. Table 1.1depicts trials developed by some research personalities.

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