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Evaluation and comparison of advanced oxidation processes for the degradation of 2,4-dichlorophenoxyacetic acid (2,4-D): a review

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Abstract

Organochlorine pesticides have generated public concern worldwide because of their toxicity to human health and the environment, even at low concentrations, and their persistence, being mostly nonbiodegradable. The use of 2,4-dichlorophenoxyacetic acid (2,4-D) has increased in recent decades, causing severe water contamination. Several treatments have been developed to degrade 2,4-D. This manuscript presents an overview of the physicochemical characteristics, uses, regulations, environmental and human health impacts of 2,4-D, and different advanced oxidation processes (AOPs) to degrade this organic compound, evaluating and comparing operation conditions, efficiencies, and intermediaries. Based on this review, 2,4-D degradation is highly efficient in ozonation (system O3/plasma, 99.8% in 30 min). Photocatalytic, photo-Fenton, and electrochemical processes have the optimal efficiencies of degradation and mineralization: 97%/79.67% (blue TiO2 nanotube arrays//UV), 100%/98% (Fe2+/H2O2/UV), and 100%/84.3% (MI-meso SnO2), respectively. The ozonation and electrochemical processes show high degradation efficiencies, but energy costs are also high, and photocatalysis is more expensive with a separation treatment used to recover the catalyst in the solution. The Fenton process is a viable economic-environmental option, but degradation efficiencies are often low (50–70%); however, they are increased when solar UV radiation is used (90–100%). AOPs are promising technologies for the degradation of organic pollutants in real wastewater, so evaluating their strengths and weaknesses is expected to help select viable operational conditions and obtain optimal efficiencies.

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Abbreviations

ATZ:

Atrazine

BQ:

Benzoquinone

BOD:

Biochemical oxygen demand

BDD:

Boron-doped diamond

CB-GF:

Carbon black modified graphite felt

Cat:

Catalyst

COD:

Chemical oxygen demand

Cl :

Chloride ions

ChHQ:

Chlorohydroquinone

CP:

Chlorophenol

CPA:

Chlorophenoxyacetic acid

CR:

Chlororesorcinol

CR:

Chlororesorcinol

Co/PMS:

Cobalt/peroxymonosulfate

Co-ppt:

Co-precipitation method

TiO2@MgO-Fe2O3 :

Core of TiO2-shell structure of MgO-Fe2O3 as the catalyst

J:

Current density

CE:

Current efficiency

I:

Current intensity

DCC:

Dichlorocatechol

DCP:

Dichlorophenol

DCPA:

Dichlorophenoxyacetic acid

DCR:

Dichlororesorcinol

DOC:

Dissolved organic carbon

EC50 :

Effective concentration 50

R:

Electrical resistance

ECMF:

Electrocatalytic ceramic membrane filtration

EAOP:

Electrochemical advanced oxidation process

EF:

Electro-Fenton

EO:

Electro-oxidation

FeOx:

Ferri-oxalate

GAC:

Granular activated carbon

GO:

Graphene oxide

GF:

Graphite felt

N1-EEGr-GF:

Graphite felt cathode modified with electrochemically exfoliated graphene doped with ammonium nitrate as the nitrogen source

HQ:

Hydroquinone

H-TiO2 vs C-TiO2 :

Hydrothermal TiO2 and commercial TiO2

Fe-Ni/AC:

Iron and nickel based bimetallic loaded activated carbon

Pb/b-PbO2 :

Lead dioxide coated on a lead bed

G/b-PbO2 :

Lead dioxide coated on graphite

SS316/b-PbO2 :

Lead dioxide coated on stainless steel 316

LC50 :

Lethal concentration 50

LD50 :

Lethal dose 50

LI:

Light intensity

LPMOCVD:

Low-pressure metal-organic chemical vapor deposition

MAC:

Maximum allowable concentration

Mw:

Microwave

MCE:

Mineralization current efficiency

MI-Meso SnO2 :

Molecular imprinted mesoporous SnO2 surface

MI-TiO2@SnO2-Sb:

Molecular imprinting TiO2 coated by electrochemical SnO2-Sb films

nZVI:

Nanoscale zero-valent iron

nZVIPs@SN-GO:

Nanoscale zero-valent iron particles stabilized by sulfur/nitrogen dual-doped GO

NOEC:

No observed effect concentration

t30W:

Normalized illumination time. Time refers to a constant solar UV power of 30W/m2

Ox:

Oxalate

PC:

Peroxi-coagulation

PMS:

Peroxymonosulfate

PA:

Phenoxyacetic acid

PEO:

Photoelectrochemical oxidation

PEP:

Photoelectro-peroxone

PF:

Photo-Fenton

Pt-MMO:

Platinized mixed metal oxide

PVC:

Polyvinyl chloride

PSPC:

Pulsed switching peroxi-coagulation

SCE:

Saturated calomel electrode (the reference electrode)

SPF:

Solar photo-Fenton

SS:

Stainless steel

SL:

Sunlight

TiO2 @CuFe2O4 :

TiO2 anchored on cupper ferrite as the catalyst

PMS:

Peroxymonosulfate

TiO2/ SGOTNT:

TiO2 nanotubes/silylated graphene oxide–based molecularly imprinted polymer as photocatalyst

TDS:

Total dissolved solids

TOC:

Total organic carbon

VF:

Vibrio fischeri

FeO/TiO2/AC:

Zero-valent iron/titanium dioxide based on activated carbon nanocomposite

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Availability of data and materials

All data generated or analyzed during this study are included in this article.

Funding

This work was supported by UAEM (project No. 6207/2020CIB) and CONACYT (CVU: 863657).

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Authors

Contributions

All authors contributed to the study conception and design. The literature search and data analysis were performed by Elia Alejandra Teutli-Sequeira, Fortunata Santoyo-Tepole, and Rocío Girón-Navarro. The first draft of the manuscript was written by Verónica Martínez-Miranda, Ivonne Linares-Hernández, and Rocío Girón-Navarro. All authors commented on previous versions of the manuscript. All authors read and approved the final manuscript.

Corresponding authors

Correspondence to Ivonne Linares-Hernández or Verónica Martínez-Miranda.

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Girón-Navarro, R., Linares-Hernández, I., Teutli-Sequeira, E.A. et al. Evaluation and comparison of advanced oxidation processes for the degradation of 2,4-dichlorophenoxyacetic acid (2,4-D): a review. Environ Sci Pollut Res 28, 26325–26358 (2021). https://doi.org/10.1007/s11356-021-13730-y

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