Mineralization of pentachlorophenol by ferrioxalate-assisted solar photo-Fenton process at mild pH (2023)

Table of Contents
Chemosphere Abstract Introduction Section snippets Chemicals Experimental procedures Comparative study of PCP mineralization Conclusions Acknowledgements References (38) Photostability and toxicity of pentachlorophenol and phenanthrene J.Hazard Mater. Innovative analytical method for the determination of underivatized tributyltin and pentachlorophenol in seawater by gas chromatography-triple quadrupole mass spectrometry Anal. Chim. Acta Homogeneous photo-Fenton processes at near neutral pH: a review Appl. Catal. B: Environ. The association of cancer risks with pentachlorophenol exposure: focusing on community population in the areas along certain section of Yangtze River in China Environ. Pollut. Study of the intensification of solar photo-Fenton degradation of carbamazepine with ferrioxalate complexes and ultrasound J.Hazard Mater. Treatment technologies used for the removal of As, Cr, Cu, PCP and/or PCDD/F from contaminated soil: a review J.Hazard Mater. Natural soil mineral nanoparticles are novel sorbents for pentachlorophenol and phenanthrene removal Environ. Pollut. Depletion of pentachlorophenol in soil microcosms with Byssochlamys nivea and Scopulariopsis brumptii as detoxification agents Chemosphere Effect of co-substrates on biogas production and anaerobic decomposition of pentachlorophenol Bioresour. Technol. The impact of alkali metal halide electron donor complexes in the photocatalytic degradation of pentachlorophenol J.Hazard Mater. The role of organic ligands in ferrous-induced photochemical degradation of 2,4-dichlorophenoxyacetic acid Chemosphere The effects of different types of crop straw on the transformation of pentachlorophenol in flooded paddy soil Environ. Pollut. Simultaneous pentachlorophenol decomposition and granular activated carbon regeneration assisted by microwave irradiation Carbon Insights into solar photo-Fenton process using iron(III)–organic ligand complexes applied to real textile wastewater treatment Chem. Eng. J. Catalytic degradation of Orange II in a ferrioxalate-assisted photo-Fenton process using a combined UV-A/C–solar pilot-plant system Appl. Catal. B: Environ. Photodegradation of Reactive Blue 4 solutions under ferrioxalate-assisted UV/solar photo-Fenton system with continuous addition of H2O2 and air injection Chem. Eng. J. Electrochemical mineralization of pentachlorophenol (PCP) by Ti/SnO2–Sb electrodes Chemosphere Thermodynamic analysis of the reactions of iron oxides: dissolution in oxalic acid Can. Metall. Q. Acomparative study on the removal of pentachlorophenol using copper-impregnated pumice and zeolite J.Environ. Chem. Eng. Cited by (28) Performance of heterogeneous Fenton catalyst from solid wastes for removal of emerging contaminant in water: A potential approach to circular economy Elimination of bisphenol A with visible light-enhanced peroxydisulfate activation process mediated by Fe<sup>3+</sup>-nitrilotriacetic acid complex An overview of chelate modified electro-Fenton processes Efficient decontamination of ciprofloxacin at neutral pH via visible light assisted Fenton–like process mediated by Fe(III)–GLDA complexation High-efficiency removal of tetracycline by carbon-bridge-doped g-C<inf>3</inf>N<inf>4</inf>/Fe<inf>3</inf>O<inf>4</inf> magnetic heterogeneous catalyst through photo-Fenton process A green solar photo-Fenton process for the degradation of carbamazepine using natural pyrite and organic acid with in-situ generated H<inf>2</inf>O<inf>2</inf> Recommended articles (6) Ascorbic acid induced activation of persulfate for pentachlorophenol degradation Enhancing CaO2 fenton-like process by Fe(II)-oxalic acid complexation for organic wastewater treatment Effect of a solar Fered-Fenton system using a recirculation reactor on biologically treated landfill leachate Benefits and limitations of using Fe(III)-EDDS for the treatment of highly contaminated water at near-neutral pH Treatment of landfill leachate using electrochemically assisted UV/chlorine process: Effect of operating conditions, molecular weight distribution and fluorescence EEM-PARAFAC analysis Photoelectro-Fenton as post-treatment for electrocoagulated benzophenone-3-loaded synthetic and urban wastewater

Chemosphere

Volume 217,

February 2019

, Pages 475-482

Author links open overlay panel, , ,

Abstract

This work reports the use of ferrioxalate complexes to assist solar photo-Fenton treatment of pentachlorophenol (PCP) in aqueous medium at mild pH, which inhibits the precipitation of iron hydroxides and allows working at a low iron dosage. The experimental parameters were optimized by assessing the effect of initial concentrations of H2O2 (0–2.5 mM) and Fe(II) (2–10 mg/L), pH (3.0–9.0) and iron/oxalic acid molar ratios (1:0–1:13.5) on total organic carbon (TOC) removal. Ferrioxalate-assisted solar photo-Fenton achieved 97.5% mineralization in 120 min, clearly outperforming conventional Fenton and solar photo-Fenton. The presence of photosensitive ferrioxalate complexes accounted for the enhancement, as a result of Fe(II) regeneration that accelerated the hydroxyl radical (Mineralization of pentachlorophenol by ferrioxalate-assisted solar photo-Fenton process at mild pH (3)OH) production. The time course of H2O2 and Fe(II) concentrations was evaluated under different iron/oxalic acid ratios. The five carboxylic acids determined by ion-exclusion HPLC and the eight aromatic by-products identified by GC-MS allowed the proposal of a degradation pathway that included hydroxylation, dechlorination and dimerization steps. Complete chloride ion release was achieved after 90 min of treatment.

Introduction

Chlorophenols, listed as priority pollutants by most water directives worldwide due to their high toxicity, are still massively employed in industrial and agricultural activities (Hechmi etal., 2016; Khuzwayo and Chirwa, 2017). Pentachlorophenol (PCP, C6HCl5O), the highest chlorinated phenol, is widely used as herbicide, fungicide, insecticide and disinfectant, showing main applications in agriculture, wood preservation and industry (Amendola etal., 2017; Tsoufis etal., 2017). Although large-scale manufacture and application of PCP have been banned in Taiwan and mainland China since 1984 and 1997, respectively, its presence in water and soil has been regularly reported in the last three decades (Shih etal., 2016). Due to its long-term persistence, high toxicity and carcinogenicity, wastewater contaminated with PCP must be conveniently treated before being discharged or reused (Cui etal., 2017).

The solubility of PCP, with pKa = 4.75 (He etal., 2015; Guemiza etal., 2017), is highly dependent on pH, being low at pH < 5.0 (≤14 mg/L) but very high at pH > 6.0 (>100 mg/L) since its anionic form is predominant. As a result, it has been detected in industrial wastewater of pH 9.0 at a concentration of 490 mg/L (Rahmani etal., 2018). Various technologies have been developed for the treatment of PCP in water, including biodegradation (Khan etal., 2017), adsorption (Zhou etal., 2014), chemical oxidation and reduction (Shih etal., 2016), electrochemical oxidation (Niu etal., 2013) and photocatalysis (Khuzwayo and Chirwa, 2017). Unfortunately, most of these methods exhibit several weaknesses like long treatment times required, high energy consumption, insufficient ability to ensure total removal and inefficient mineralization that causes the accumulation of toxic intermediates.

Nowadays, advanced oxidation processes (AOPs), including those based on Fenton's reaction, ozone and light irradiation, have been proven excellent to degrade highly recalcitrant organic compounds because of the action of hydroxyl radical (Mineralization of pentachlorophenol by ferrioxalate-assisted solar photo-Fenton process at mild pH (4)OH), which is the second strongest oxidant after fluorine with a high standard redox potential (E0= 2.80 V|SHE) (Martínez-Huitle etal., 2015). Among AOPs, Fenton's reaction is recognized as a very simple way to generate Mineralization of pentachlorophenol by ferrioxalate-assisted solar photo-Fenton process at mild pH (5)OH. However, inefficient Fe(II) regeneration usually results in the need of large amounts of such catalyst, which must be carefully managed upon treatment completion (Brillas etal., 2009). The addition of UV radiation gives rise to photo-Fenton process, which can readily regenerate Fe(II) and produce additional Mineralization of pentachlorophenol by ferrioxalate-assisted solar photo-Fenton process at mild pH (6)OH amounts (Eq. (1)), as well as photodecarboxylate the Fe(III) complexes generated during the oxidation of most organics (Eq. (2)) (Ye etal., 2016).[Fe(OH)]2++ → Fe2++Mineralization of pentachlorophenol by ferrioxalate-assisted solar photo-Fenton process at mild pH (7)OH[Fe(OOCR)]2++ → Fe2++CO2+RMineralization of pentachlorophenol by ferrioxalate-assisted solar photo-Fenton process at mild pH (8)

Nonetheless, conventional Fenton process with simple soluble salts presents two critical limitations: (i) it demands acidic conditions (pH 2.5–3.5) to maintain a high performance, which restricts the application of photo-Fenton process for wastewater treatment at large scale; and (ii) reaction (1) exhibits a quite low quantum yield for Fe(III) photoreduction (Φ(Fe(II)) = 0.14 ± 0.04 at 313 nm), and might also be inhibited by the reduced light penetration when treating colored solutions (Pignatello etal., 2006).

To overcome these disadvantages, some chelating agents such as oxalate, citrate, ethylenediamine-N,N′-disuccinic acid (EDDS), ethylenediaminetetraacetic acid (EDTA) and nitrilotriacetic acid (NTA) have been investigated to upgrade the conventional photo-Fenton process (Klamerth etal., 2012; Manenti etal., 2015; Clarizia etal., 2017). Such compounds are able to form stable complexes with ferric ions, thereby maintaining the iron soluble at less acidic pH and acting as photoactive species that greatly enhance the performance of photo-Fenton process. Among these agents, oxalate has been shown to be preferred (Kwan and Chu, 2007). The advantages of ferrioxalate-assisted photo-Fenton as compared to other systems include (Luca etal., 2014; Souza etal., 2014; Clarizia etal., 2017): (i) the soluble ferrioxalate complex allows working at neutral pH values; (ii) this complex has a higher quantum yield for Fe(II) regeneration (Eqs. (3), (4)); (iii) it exhibits more intense light absorption, with a range up to 580 nm; and (iv) additional H2O2 production can occur from participation of dissolved oxygen (Eqs. (5), (6), (7), (8)). The reaction network can be summarized as follows (Souza etal., 2014; Clarizia etal., 2017):[Fe(C2O4)n]3−2n+ → Fe2++(n−1)C2O42−+C2O4Mineralization of pentachlorophenol by ferrioxalate-assisted solar photo-Fenton process at mild pH (9)C2O4Mineralization of pentachlorophenol by ferrioxalate-assisted solar photo-Fenton process at mild pH (10)+[Fe(C2O4)n]3−2n → Fe2++nC2O42−+2CO2C2O4Mineralization of pentachlorophenol by ferrioxalate-assisted solar photo-Fenton process at mild pH (11)+O2 → O2Mineralization of pentachlorophenol by ferrioxalate-assisted solar photo-Fenton process at mild pH (12)+2CO2Fe2++O2 → Fe3++O2Mineralization of pentachlorophenol by ferrioxalate-assisted solar photo-Fenton process at mild pH (13)O2Mineralization of pentachlorophenol by ferrioxalate-assisted solar photo-Fenton process at mild pH (14)+H+ ↔ HO2Mineralization of pentachlorophenol by ferrioxalate-assisted solar photo-Fenton process at mild pH (15)pKa = 4.82HO2Mineralization of pentachlorophenol by ferrioxalate-assisted solar photo-Fenton process at mild pH (16) → H2O2+O2

Considering the high energy consumption using artificial UV light sources, sunlight can be alternatively employed to operate the ferrioxalate-assisted solar photo-Fenton process, which has been proven to be an efficient wastewater treatment technology (Monteagudo etal., 2010a,b; Souza etal., 2014; Expósito etal., 2018). The present work investigates the mineralization and dechlorination of PCP by ferrioxalate-assisted solar photo-Fenton process at mild pH with a low iron concentration. The effect of main experiment parameters, such as initial concentrations of H2O2 and Fe(II), pH and iron/oxalic acid molar ratios on total organic carbon (TOC) abatement has been assessed, and the evolution of H2O2, Fe(II) and dissolved O2 has also been determined. In addition, a schematic reaction mechanism involving the iron cycle, radical reactions and PCP mineralization has been proposed. A possible pathway for the degradation of PCP is presented according to the identified intermediates.

Section snippets

Chemicals

PCP was purchased from Sigma Aldrich (97% purity) and used without further purification. Hydrogen peroxide, ferrous sulfate heptahydrate and oxalic acid dihydrate were obtained from Union Chemical, Merck and Sigma Aldrich, respectively. The solution pH was adjusted with diluted NaOH or H2SO4. Other chemicals used herein were of analytical grade. Laboratory-grade deionized water from a reverse osmosis system (resistivity > 18.2 MΩ cm) was used to prepare all aqueous solutions.

Experimental procedures

The experiments

Comparative study of PCP mineralization

First, a comparative study on the mineralization of PCP from an aqueous solution containing 50 mg/L (i.e., 14 mg/L TOC) at pH 5.0 by different processes was conducted. As shown in Fig.1, direct solar photolysis had no effect on TOC abatement for 120 min. This agrees with the low photodegradation rate constants at PCP concentrations of 0.4–2.1 mg/L, within the range of 4.9 × 10−2–7.1 × 10−2 h−1, which informs about the great persistence of this pollutant in the environment (Agbo etal., 2011).

Conclusions

Promising results were obtained for the mineralization of PCP at near-neutral pH using a low iron concentration by the ferrioxalate-assisted solar photo-Fenton process. More than 95% TOC abatement were achieved in 120 min. The optimized operation parameters were: 5 mg/L Fe(II), 1.5 mM H2O2, pH 5.0 and iron/oxalic acid molar ratio of 1:6. The presence of oxalic acid greatly enhances the performance of solar photo-Fenton process due to various reasons: (i) the ferrioxalate complex ensures the

Acknowledgements

This work was supported by Natural Science Foundation of Hubei Province, China (Grant 2012FFA089) and the National Science Council of the Republic of China (No. NSC 102-2622-E-006-004-CC2). The authors also thank financial support from project CTQ2016-78616-R (AEI/FEDER, EU) and PhD scholarship awarded to Z.H. Ye (State Scholarship Fund, CSC, China).

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      This study evaluates the use of the Fe(III)-EDDS complexing agent as an alternative to conventional acidic pH photo-Fenton for the treatment of the pesticide imidacloprid in natural water. The main objective is to estimate whether Fe(III)-EDDS is a viable alternative when treating waters containing high concentrations of contaminants. To this end, the mode of action of Fe(III)-EDDS is examined in the presence of carbonates, at different aeration conditions and at different temperatures. The role of HO2Mineralization of pentachlorophenol by ferrioxalate-assisted solar photo-Fenton process at mild pH (24)/O2Mineralization of pentachlorophenol by ferrioxalate-assisted solar photo-Fenton process at mild pH (25) radical species and some aspects of the Fe(III)-EDDS complexation mechanism are discussed. Degradation kinetics and toxicities of generated intermediates are compared between Fe(III)-EDDS and conventional photo-Fenton treatment. An overview of the benefits and limitations of the process is presented.

    • Research article

      Treatment of landfill leachate using electrochemically assisted UV/chlorine process: Effect of operating conditions, molecular weight distribution and fluorescence EEM-PARAFAC analysis

      Chemical Engineering Journal, Volume 286, 2016, pp. 508-516

      Leachate, a highly polluted wastewater, is generated from landfill containing complex compositions which have great impact on the environment. The advanced treatment of biochemically treated landfill leachate using electrochemically assisted UV/chlorine process (UEC) in a flow reactor was investigated. The effects of pH and current density on COD and NH3-N removal by UEC process were evaluated. At the pH value of 5.0, current density of 60mA/cm2, the removal efficiencies for COD and NH3-N were observed as 77% and 87%, respectively. The electrochemical process alone (EC) could obtain relatively high NH3-N removal but very low COD removal, compared with which, the UEC process significantly promoted the removal efficiency of COD while that of NH3-N increased to a very limited extent. Most of NH3-N was converted into N2 and little nitrogen compounds and chloramines were remained in the leachate after 8h treatment. Moreover, the variations of active chlorine and chloride ions were monitored in the EC and UEC systems, and a possible mechanism was proposed for the UEC process. The in situ electro-generated active chlorine and photo-generated radical species should be responsible for the efficient degradation of landfill leachate. The total energy consumption and current efficiency were 216.5 (kWh/kg COD) and 17.5%, respectively, for 8h treatment. In addition, the molecular weight (MW) percentage distribution analysis and PARAFAC analysis of excitation emission matrix (EEM) fluorescence spectroscopy indicated that the organic matters in the leachate were significantly degraded into the fractions with small molecular weight.

    • Research article

      Photoelectro-Fenton as post-treatment for electrocoagulated benzophenone-3-loaded synthetic and urban wastewater

      Journal of Cleaner Production, Volume 208, 2019, pp. 1393-1402

      The removal of benzophenone-3 (BP-3), a ubiquitous pollutant in municipal wastewater treatment facilities, was optimal by means of a sequential electrocoagulation (EC)/UVA photoelectro-Fenton (PEF) treatment. Overall mineralization was attained upon combination of EC (Fe/Fe cell, 15 mA cm−2, 20 min) with PEF (boron-doped diamond/air-diffusion cell, 33.3 mA cm−2, 720 min), being superior to EC/electro-Fenton (EF) and requiring shorter time than single PEF. In EC, an Al/Al cell yielded the largest removal of BP-3 in a simulated matrix at pH 11.0 due to precipitation of its neutral form caused by a substantial pH drop, with optimum current density of 15 mA cm−2. EC of BP-3-loaded urban wastewater at natural pH was quite effective also with a Fe/Fe cell, being preferred since it provided the required metal catalyst for subsequent treatment. Among the electrochemical advanced oxidation processes tested, PEF was superior to electrochemical oxidation with electrogenerated H2O2 (EO-H2O2) and EF, especially when using the boron-doped diamond instead of a RuO2-based anode, due to the oxidation of generated active chlorine and hydroxyl radicals, along with the photolytic action of UVA irradiation. GC-MS revealed the formation of 14 cyclic products in PEF treatment, two of them being also formed during EC.

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