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Chemistry » "Nitrification and Denitrification", book edited by Ivan X. Zhu, ISBN 978-953-51-3300-1, Print ISBN 978-953-51-3299-8, Published: July 5, 2017 under CC BY 3.0 license. © The Author(s).

Chapter 5

Denitrification in the Presence of Chlorophenols: Progress and Prospects

By Emir Martínez‐Gutiérrez, Anne‐Claire Texier, Flor de María Cuervo‐ López and Jorge Gómez
DOI: 10.5772/intechopen.68860

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Denitrification in the Presence of Chlorophenols: Progress and Prospects

Emir Martínez-Gutiérrez1, Anne-Claire Texier2, Flor de María Cuervo-López2 and Jorge Gómez2
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Diverse industrial effluents may contain recalcitrant compounds such as chlorophenols. Besides, excessive use of pesticides in agriculture is a major cause of the appearance of chlorophenols in surface and groundwater. To mitigate and control the effects of chlorophenols in the environment, various methods have been developed for their elimination. Biological processes represent a sustainable and economical alternative that can lead to the mineralization of chlorophenols and be effective for the removal of these pollutants from different water bodies, such as rivers, groundwater, and wastewater. Some studies have reported that chlorophenols mineralization and nitrate reduction may simultaneously be performed. Other works have suggested that a reductive dechlorination occurs such as the first step and later, the phenol formed is subsequently mineralized by denitrification. However, the published information can be confusing as the denitrifying process is often associated with the sole nitrate consumption without corroborating the total reduction of nitrate to N2. Additionally, there are alternative systems that combine biological process with a chemical or electrochemical process for chlorophenols removal. This chapter focuses on the advances accomplished in the study of the removal of chlorophenols under denitrifying conditions with the aim of having a clearer panorama of the treatment alternatives that can be applied for treatment of this type of effluents.

Keywords: denitrification, chlorophenols, rates, anaerobic, combined systems

1. Introduction

Human activities generate effluents from production processes and domestic activities which may contain nitrogen and carbon pollutants. This pollution alters the global nitrogen and carbon cycles. Inorganic nitrogen is mainly present in the aqueous effluents such as nitrate, nitrite, and ammonium, causing serious problems to ecosystems and to public health. These compounds can achieve high levels of toxicity to aquatic organisms and may promote the growth of aquatic plants, which accelerate the eutrophication process of water bodies [1]. The ingestion of nitrite and nitrate by infants can promote methemoglobinemia and the formation of nitrosamines, which might be carcinogens [2]. On the other hand, diverse industrial effluents may contain recalcitrant compounds such as chlorophenols, which are derivatives of phenol that contain one or more covalently bonded chlorine atoms. Chlorophenols have been utilized for wood preservation, as well as for manufacturing of pesticides, antiseptics, and dyes. However, the excessive use of pesticides in agriculture is one of the major causes of the appearance of chlorophenols in surface and groundwater [3]. Depending on their concentration, they can be toxic compounds, causing damage to the cell membranes as well as uncoupling oxidative phosphorylation [4].

To diminish the adverse effects of chlorophenols in the environment, various methods have been developed for their elimination, including physical, chemical, electrochemical, and biological processes. The first three methods appear to be faster, but everything indicates that they are expensive and generate collateral contamination, making them less environmentally friendly processes than the biological treatment. Biological processes represent a sustainable and cost‐effective alternative that can lead to the mineralization of chlorophenols and can be effective for the removal of these pollutants from different water bodies, such as rivers, groundwater, and wastewater. Most of the information on disposal of chlorophenols under anaerobic conditions has been obtained under methanogenic conditions. There is evidence that shows that removal of chlorophenols by methanogenic microbial consortia is initiated by a reductive dechlorination and ends with the formation of methane and CO2 [5], although more chlorinated chlorophenols are not always completely mineralized and less chlorinated compounds are obtained as end products [6]. Chlorophenol mineralization coupled to denitrification is still poorly documented. In this regard, there are few studies showing the possibility of chlorophenol consumption coupled to reduction of nitrate, although it is suggested that the pathway is different to reductive dechlorination [7]. Other studies suggested that reductive dechlorination occurs at first and later the phenol formed is subsequently mineralized by denitrification process [8]. However, the published information can be confusing, as the denitrifying process is often associated with the sole nitrate consumption without corroborating the total reduction of nitrate to N2.

Considering that efficient removal of recalcitrant compounds such as chlorophenols requires detailed analysis, this chapter focuses on the advances accomplished in the study of the removal of chlorophenols under denitrifying conditions. First, the physicochemical characteristics of the chlorophenols that confer their recalcitrant and toxic properties are presented. Then, general aspects of denitrification, such as microbiology and biochemistry, as well as the influence of various environmental factors, are presented. In physiological terms, the elimination of chlorophenols under denitrifying conditions is discussed, presenting the different configurations of reactors studied, types of inoculum, as well as the different strategies used to increase their consumption. Finally, the recently studied systems that combine the biological process with a chemical or electrochemical process, in order to increase the consumption of chlorophenols without the generation of toxic waste, are also presented.

2. Physicochemical properties of chlorophenols

Chlorophenols are organochlorine compounds whose structure consists of a phenol and one or more chlorine atoms that are covalently bonded. In total, there are 19 types of chlorophenols differing from each other in the amount and position of the chlorine atoms. They can be subdivided into five groups: monochlorophenols, dichlorophenols, trichlorophenols, tetrachlorophenols, and pentachlorophenols. Most chlorophenols are solid at room temperature, with the exception of 2‐chlorophenol (2‐CP) which is liquid. They are compounds with strong odor and medicinal taste with very low organoleptic thresholds, being perceived in water at very small quantities (µg/L). Chlorophenols present high log Kow (octanol water partition coefficient) values and low solubility in water (Table 1). As chlorination level increases, their water solubility decreases and their acidity increases. Similarly, the log Kow also increases with the number of chlorine atoms, favoring their bioaccumulation [9]. Transport and transformation of chlorophenols in natural environments depend on pH, oxygen concentration, presence of other organic and inorganic substances, and temperature as well as their own structure [10].

Molecular weight (g/mol)128.56128.56163.0197.45197.45266.34
Solubility at 20oC (g/L)28274.50.4340.4340.014
Density (g/cm3)1.2621.22381.381.491.841.98
Log Kow2.
Vapor pressure at 20oC (mm Hg)0.990.
Melting point (oC)9.442–4442–4369115191
Boiling point (oC)174.9217210246288309

Table 1.

Physical and chemical properties of chlorophenols.

CP: chlorophenol, DCP: dichlorophenol, TCP: trichlorophenol, TTCP: tetrachlorophenol, and PCP: pentachlorophenol.

Apparently, toxicity of chlorophenols is related to the degree of chlorination and the proximity of chlorine to the hydroxyl group. Chlorophenols with chlorine in the ortho position show lower toxicity than chlorophenols with the same number of chlorine in the meta or para position [11]. Toxicity of chlorophenols may also be related to their log Kow [12], as toxicity increases with a higher lipophilicity. Toxic effects of chlorophenols have been related to membrane destruction and inhibition of oxidative phosphorylation. This blockade of oxidative phosphorylation can occur by different ways: interfering with the release of hydrogen to the electron transport chain, inhibition of the transfer of electrons along the electron transport chain to oxygen, interference with the release of oxygen to the terminal electron carrier, or inhibition of the activity of adenosine triphosphate (ATP) synthase [11].

3. Microbiology of denitrification

In order to carry out denitrification, which is defined as the biological dissimilative transformation of nitrate (NO3) or nitrite (NO2) into molecular nitrogen (N2) under anoxic conditions with energy conservation [13], an electron donor is required. Therefore, denitrifying microorganisms must have the ability for using nitrate or nitrite as electron acceptors to reduce them to molecular nitrogen. Organotrophic or autotrophic microorganisms are involved in denitrification process depending on their ability to use organic or inorganic compounds as electron sources, respectively. Their remarkable characteristic is their facultative anoxic respiration.

Distribution of denitrifying microorganisms in nature is ubiquitous. Organotrophic and autotrophic denitrifiers belong to α‐, β‐, γ‐ and ε‐proteobacteria group which comprise both, Gram‐negative and Gram‐positive bacteria. Nevertheless, some members of Archae and Eukarya have shown the ability for reducing nitrate to N2 [14, 15]. Most of organotrophic and autotrophic denitrifiers grow under neutral and mesophilic conditions [16, 17]. Organotrophic denitrifiers have been found in natural ecosystems as soil [18], surface water [19], groundwater, and sediments [20]; in wastewater treatment plants; and in different types of reactor configurations treating synthetic wastewater under organotrophic [21], autotrophic [22], or mixotrophic conditions, where mixtures of both organic and inorganic electron sources are present [22, 23]. For illustration purposes, several denitrifying microorganisms and their physiological characteristics are included in Table 2.

GroupGenus/speciesElectron donorPhysiological characteristicsReference
α‐ProteobacteriaParacoccus/P. pantotrophusOrganic and sulfur compounds, H2Organotrophic, sulfur and hydrogen autotrophic denitrification[16, 24]
β‐ProteobacteriaThiobacillus thiophillusSulfide, sulfurSulfur autotrophic denitrification[25]
AzoarcusOrganic compoundsOrganotrophic denitrification[23, 26, 27]
ThaueraAcetate, sulfide, H2Organotrophic, sulfur and hydrogen autotrophic denitrification[21, 23]
Acidovorax spp.Glucose, acetate, H2Organotrophic and hydrogen autotrophic denitrification[21, 28, 29]
Flavobacterium spp.Glucose, acetateOrganotrophic denitrification[21, 28]
γ‐ProteobacteriaPseudomonas sp.Organic compounds, H2Organotrophic and hydrogen autotrophic denitrification[24]
Acinetobacter sp.H2Hydrogen autotrophic denitrification[30]
Aeromonas sp.H2Hydrogen autotrophic denitrification[31]
ε‐ProteobacteriaSulfurimonas lithotrophicumSulfurSulfur autotrophic denitrification[32]
Thiomicrospira CVOSulfur, H2Sulfur and hydrogen autotrophic denitrification[33]

Table 2.

Some denitrifying microorganisms and their physiological characteristics.

Genus βproteobacteria has been found dominant in many denitrification systems [34]. Thauera is a dominant Gram‐negative organotrophic bacterium belonging to βproteobacteria which has been identified in wastewater treatment systems [35], in an integrated system of three‐dimensional biofilm‐electrode reactor and sulfur autotrophic denitrification (3DBER‐SAD) under mixotrophic conditions [27]. Thauera has also been identified in sequential batch reactors where the heterotrophic and autotrophic denitrifying process was conducted [23] and in several denitrifying bioreactors under autotrophic conditions, suggesting its ability for autotrophic growth [23]. Acidovorax is a Gram‐negative bacterium which has the ability of using both acetate and hydrogen for denitrification [29]. Denitrifying bacteria, similar to Acidovorax and Azoarcus, a facultatively anaerobic, mesophilic, and Gram‐negative bacterium with the ability of growing with a variety of organic substrates [26], have been identified under mixotrophic denitrifying conditions [27]. Denitrifying species of Acidovorax spp. and Flavobacterium spp. have been detected in a soil column system amended with glucose [21]. Recently, the ability of Pseudomonas sp. C27 for conducting both organotrophic and autotrophic denitrification has been reported [22]. On the other hand, Thiobacillus denitrificans, an obligate autotrophy and facultative anaerobic bacterium, which can use elemental sulfur as an electron donor, has been isolated from natural environments, man‐made environments [17], and denitrifying reactors operated under mixotrophic conditions [27].

4. Biochemical aspects

Irrespective of whether the organic or autotrophic process is conducted, the denitrification process has been described as a modular organization in which every biochemical reaction is catalyzed by a specific reductase [36]. These reactions occur when no oxygen is available and the environment becomes anoxic [37]. According to Mariotti [38], the denitrification process can be described as Eq. (1) indicates.

2NO3+10e+12H+N2+6H2OΔG°=1120.5 KJ/reaction

This general equation can be decomposed into four enzymatic reactions. At first, nitrate is reduced to nitrite by nitrate reductase (Nar) (Eq. (2)). The reaction can take place in the cell membrane and periplasmic space. Affinity constant (Km) ranging from 0.15–15 mM and ΔG°’ of −163.2 KJ/reaction values have been reported for this reaction [39, 40]. UQH2 corresponds to reduced ubiquinone, UQ to ubiquinone, c2+ to reduced cytochrome, and c3+ to oxidized cytochrome.


A subsequent reduction of nitrite to nitric oxide is carried out by one of two nitrite reductases (Nir, CuNir) or the cytochrome cd1,both located at the periplasmic space (Eq. (3) and (4)). Km values of 3.13–750 µM [41, 42] and 6–46 µM [39, 41] are reported for Nir/CuNir or cd1, respectively, whereas ΔG°’ of −73.2 KJ/reaction correspond to this stage.




Afterward, in the cell membrane, nitric oxide is reduced to nitrous oxide by the enzyme nitric oxide reductase (Nor) (Eq. (5)). Km values of 0.25–60 µM are reported for Nor enzyme with a ΔG°’ of −306.3 KJ/reaction [43, 44].


Finally, nitrous oxide is reduced to N2 by the enzyme nitrous oxide reductase (Nos), which is located at the periplasmic space (Eq. (6)). Km values of 2–6 µM are reported for this enzyme with a ΔG°’ of −306.3 KJ/reaction [45].


5. Denitrification and its environment

Denitrification performance is controlled by many environmental factors such as concentration, type and solubility of the substrate, C/N ratio, temperature, and pH, among other factors. These environmental variables determine the metabolic behavior, being the effect of each factor different on the biochemistry and physiology of the microorganisms [39, 46]. In this regard, experimental data have suggested that a C/N ratio close to the stoichiometric value is required for complete denitrification [47]. In this respect, many authors have made recommendations to adjust the C/N, S/N ratio for denitrification processes [36, 48]. Tiedje [49] observed that an excess of reducer source induced the reduction of nitrate to ammonium. Denitrification is an exergonic process where the energy formation depends on the type of reducer source. Degradation of monochlorophenols coupled to denitrification is also an exergonic process (Table 3). This makes denitrification a potential microbial biomass producer. Nonetheless, wastewater treatment should be a dissimilatory process where the pollutants might be essentially removed through catabolic processes.

CompoundEquationΔG°’ (KJ/reaction)
Acetic acidCH3COOH + 1.6NO3− → 2CO2 + 0.8N2 + 1.6OH + 1.2H2O−843
GlucoseC6H12O6 + 4.8NO3− → 2.4N2 + 6HCO3− + 1.2H+ + 2.4H2O−2686
PhenolC6H6O + 5.6NO3− + 0.2H2O → 2.8N2 +6HCO3− + 0.4H+−2818
MethanolCH3OH + NO3− → 0.5N2 + CO2 + 2H2O−582
p‐CresolC7H8O + 6.8NO3− → 3.4N2 + 7HCO3− + 0.2H+ + 0.4H2O−3422
TolueneC7H8 + 7.2NO3− + 0.2H+ → 3.6N2 + 7HCO3− + 0.6H2O−3524
XyleneC8H10 + 8.4NO3− + 0.4H+ → 4.2N2 + 8HCO3− + 1.2H2O−4136
SulfideS2− + 2NO3− + 4H+ → SO42− + N2 + 2H2O−922
MonochlorophenolC6H5ClO + 5.2NO3− + 1.4H2O → 2.6N2 + 6HCO3− + 1.8H+ + Cl−2742

Table 3.

Stoichiometric reactions of the denitrifying respiratory process using different electron sources and their ΔG°’ values (according to Cuervo‐López et al. [36]).

Oxygen is generally considered as a denitrifying inhibitor [50]. Likewise, according to O2 and nitrate potential redox, a competition effect can occur between these oxidants. It has been reported that nitrate could be reduced even in the presence of O2 [51]. On the other hand, the denitrifying process can be carried out in a temperature range between 5 and 35°C. However, it has been observed that at low temperatures, the emissions of nitrous oxide increase whereas N2 formation decreases [52].

pH is an independent variable that affects denitrification process at different levels [46, 53]. The common pH value employed for denitrification is around 7. At low pH values, an inhibition on the reduction of nitrous oxide occurs, causing an accumulation of nitrous oxide and a decrease in N2 formation [54, 55]. Denitrification can also be influenced by the speciation and bioavailability of the chemical compounds used as reducer sources. Thus, physicochemical conditions must be controlled in order to have a faster and efficient denitrifying process.

6. Biodegradation of chlorophenols under denitrifying conditions

Chlorophenols are generally degraded under anaerobic conditions through the first reductive dechlorination step, which consists of the substitution of chlorine atoms by hydrogen atoms (Eq. (7)).


This stage is catalyzed by specific dehalogenases enzymes. The majority of the known reductive dehalogenases belong to the CprA/PceA family and contain one corrinoid and two iron‐sulfur clusters as cofactors [56]. Reductive dechlorination requires the addition of electron donors. There are other cases in which chlorophenols are used as carbon and energy sources for microorganisms [57]. Under methanogenic conditions, mineralization of various chlorophenols to CO2 and methane has been observed [5]. However, it is unclear if reductive dechlorination would be involved in the degradation of chlorophenols under denitrifying conditions. In fact, different pathways that do not involve the dechlorination reductive step have been suggested [7].

The study of chlorophenols under denitrifying conditions has been mainly evaluated using monochlorophenols. Chang et al. [58] used a biofilm to remove 2‐CP under denitrifying conditions in batch cultures. They observed that the nitrate disappeared in 16 h, and there was a consumption of 2‐CP. However, there was no formation of phenol in this period, suggesting that 2‐CP was not dechlorinated in the presence of nitrate. Phenol was produced only after the disappearance of nitrate, suggesting that nitrate competed with 2‐CP as an electron acceptor. A similar behavior was observed by Sanford and Tiedje [8], who evaluated, in serological bottles, the elimination of 2‐CP in the presence of nitrate and acetate. They observed that the consumption of 2‐CP was inhibited by the presence of nitrate and was only carried out when nitrate disappeared or was found in concentrations lower than 104 mg/L. Yu et al. [59] studied the effect of nitrate addition on the reductive dechlorination of pentachlorophenol (PCP) and found that low concentrations of nitrate (0–62 mg/L) can enhance reductive dechlorination of PCP, whereas high concentrations (310–1860 mg/L) provoke a contrary effect. Thus, reductive dechlorination could be carried out at low concentrations of nitrate. On the other hand, Häggblom et al. [60] studied the removal of three monochlorophenols in batch cultures under denitrifying conditions. Only 2‐CP was eliminated in 110 days; nevertheless, they did not detect the formation of phenol as a product of reductive dechlorination. Bae et al. [7] also studied the elimination of monochlorophenols and dichlorophenols under denitrifying conditions in batch cultures, finding that 4‐chlorophenol (4‐CP), 2,4‐dichlorophenol (2,4‐DCP), and 2,6‐dichlorophenol (2,6‐DCP) were not biodegraded, whereas 2‐CP and 3‐chlorophenol (3‐CP) were mineralized and the presence of nitrate was essential. The authors reported that 2‐CP was oxidized to CO2 under denitrifying conditions and suggested the presence of a population capable of eliminating 2‐CP by a mechanism that does not involve reductive dechlorination.

As observed in Table 4, most of the studies with chlorophenols have been carried out in batch assays and only few types of reactors have been evaluated under denitrifying conditions. Moussavi et al. [61] evaluated the elimination of 2‐CP in a granular anoxic baffled reactor (AnBR) increasing the concentration of 2‐CP up to 500 mg/L without affecting the efficiency of 2‐CP removal, so this could be a feasible process at low cost. Wang et al. [62] evaluated the removal of PCP in a packed reactor with corncob as both carbon source and biofilm support and obtained efficiencies of nitrate and PCP removal above 90%.

Chlorophenol (mg/L)Type of reactorInoculumElectron donorRemoval efficiency of CPsRemoval efficiency of nitrateProductsReference
2‐CP (12.8)Batch (serum bottle)SedimentNa2S.9H2O______[60]
2‐CP, 3‐CP, or 4‐CP (25.7)BatchSoilAcetate, volatile fatty acids____Phenol, benzoate[8]
2‐CP (12.8)BatchAcclimated sludgeNa2S.9H2O______[7]
3‐CP (2.0–5.2)Up‐flow columnsActivated sludgeNa2S.9H2O27–100%__Phenol, benzoate[65]
2‐CP(25)Batch (gas‐permeable silicone membrane bioreactor)Hydrogenotrophic biofilm (acclimated)H2Around 100%Around 100%Phenol[58]
4‐CP, 2,4 DCP (5)Sequencing batch reactorsAcclimated biomassMilk powder plus yeast extract______[66]
PCP (5 mg/L)Laboratory‐scale reactor packedBiofilmCorncob40–91%98%3‐CP, phenol[62]
2‐CP (50–500)Anoxic baffled reactorActivated sludge (enrichment)>99%____[61]
PCP (1–5)Batch (serum bottles)SoilLactic acidAround 100%Around 100%__[59]

Table 4.

Biodegradation of different chlorophenols under denitrifying conditions.

In conclusion, mineralization of chlorophenols coupled to denitrification is rarely documented as the total oxidation of chlorophenols to CO2 and reduction of nitrate to N2 have not been corroborated. The available information is controversial as several works evidenced that the presence of nitrate inhibits the transformation of chlorophenols [8, 63], while other authors indicate that reductive dechlorination can be carried out at low concentrations of nitrate [59]. In fact, other studies evidenced that mineralization of chlorophenols is linked to denitrification, and the presence of nitrate was necessary for the biodegradation [7, 64]. In addition, the denitrifying process is often evaluated by the sole nitrate consumption without verifying its total reduction to N2. Therefore, it is necessary to carry out more studies which evaluate the process through response variables such as removal efficiencies, yields of product formation, and rates in order to characterize and better understand the process.

6.1. Strategies for improving the consumption of chlorophenols

It has been pointed out that the main difficulty for the elimination of chlorophenols is the strong stability that the carbon‐halogen bond of the aromatic compound confers to its structure [67]. Thus, in many cases, the biodegradation is slow. Several strategies for increasing the consumption of chlorophenols have been proposed, although most of them have been conducted under aerobic and anaerobic conditions and in minor proportions under denitrifying conditions.

Some strategies have been proposed to increase the efficiency and/or rate of chlorophenols consumption. These include the sludge adaptation to pollutants, the use of genetically modified microorganisms, and the addition of alternative carbon sources [68]. It has been also suggested that the addition of readily oxidized carbon sources could exert various beneficial effects, such as decreasing toxicity, acting as an enzyme‐inducing agent, or providing reducing power for the consumption of recalcitrant organic compounds [6971]. Furthermore, Puyol et al. [72] observed accumulation of different intermediates depending on the co‐substrate used. When methanol, ethanol, or volatile fatty acids were used as co‐substrates, 4‐chlorophenol was accumulated while 2,4‐dichlorophenol was accumulated when lactate was used as the co‐substrate.

Under denitrifying conditions, Hu et al. [66] found that the presence of co‐substrates caused a significant decrease in the degradation rate of 4‐chlorophenol (by 4 times) while the biodegradation rate of 2,4‐dichlorophenol increased by 4.2 times. Therefore, it could be said that the use of co‐substrates does not always have a positive effect on the biodegradation of recalcitrant compounds. The compounds used as co‐substrates include compounds of easy oxidation and compounds with a structure similar to chlorophenols. Regarding this, Martínez‐Gutiérrez et al. [73] evaluated the effects of phenol and acetate on the mineralization of 2‐CP by a denitrifying sludge in batch assays. When phenol was used as a co‐substrate, the specific rate of 2‐CP consumption increased by 2.6 times, regarding to a control assay without co‐substrate. When acetate was used, the specific rate of 2‐CP consumption increased by 9 times, suggesting that the addition of co‐substrates is a good alternative for improving the biodegradation of chlorophenols. These results also suggest that the effects of co‐substrates addition depend on several factors: type of both the co‐substrate and chlorophenol employed, inoculum source, and experimental conditions.

7. Coupled systems for chlorophenol degradation

Recently, other strategies have been developed for the elimination of recalcitrant compounds using systems that combine advanced oxidation (AOP) or electrochemical processes with biological processes. Daghio et al. [74] evaluated the degradation of toluene using bio‐electrochemical reactors obtaining a current power of 431 mA/m2. Yeruva et al. [75] evaluated the integration of a sequencing batch reactor (SBR) and a bio‐electrochemical treatment system (BET) for the treatment of petrochemical wastewater under anoxic conditions, obtaining high degradation and power generation (17.12 mW/m2). The application of an electrochemical treatment can diminish the time required for the treatment of chlorinated pesticides in the biological process [76]. A sequential biological advanced oxidation process was used for the degradation of 2,4‐dichlorophenol, consisting of an up‐flow anaerobic sludge blanket (UASB) reactor and a UV/H2O2/TiO2 system, obtaining 52.7% of degradation in only 6 h [77]. However, the degradation of chlorophenols with nitrate using combined systems has been scarcely evaluated. In this sense, Arellano‐González et al. [78] evaluated an electrochemical‐biological combined system where the reductive dechlorination was carried out in an ECCOCEL‐type (Pd‐Ni/Ti electrode) reactor that achieved 100% transformation of 2‐CP into phenol. Then, the phenol formed was mineralized by a biological denitrification process. The total time required for 2‐CP conversion into CO2 was 7.5 h.

8. Perspectives

Biodegradation processes of chlorophenols have been studied extensively because they are more economical and friendly environmental processes in comparison with physicochemical, AOP, and electrochemical processes. The information presented in this review shows that denitrification might be an efficient biological process for the treatment of effluents contaminated with nitrogen and chlorophenols. It has been also reported that biological processes may achieve the complete removal of many types of chlorophenols under aerobic and anaerobic conditions, but they do not always lead to mineralization. It is crucial considering that biodegradation processes can generate more toxic and recalcitrant intermediates than the original pollutant, and the partial oxidation of recalcitrant molecules should be prevented, favoring their mineralization. In this review, it is shown that recent experimental evidences demonstrated the possibility to use denitrification for 2‐CP mineralization associated with the reduction of nitrate to nitrogen gas. These results suggest that denitrification might be used for the mineralization of chlorophenols producing CO2 and N2 as final products and obtaining high removal efficiencies. However, more studies on chlorophenols biodegradation by denitrifying processes are needed, especially with mixtures of chlorophenols. More studies on physiological, kinetic, and biochemical aspects of denitrification are also required to identify the limiting steps of the biodegradation metabolic pathways and to better understand how controlling denitrifying processes in bioreactors without the formation of undesirable by‐products.

Another important aspect is that it has been shown that chlorophenols biodegradation by denitrifying microorganisms is very slow. As a consequence, the application of denitrification processes for chlorophenols removal is still limited, requiring very long acclimation and retention times, especially for the treatment of wastewaters contaminated with high chlorophenol concentrations. Different treatment alternatives have been proposed in order to increase the rate and efficiency of chlorophenol consumption and among them are adaptation to the pollutants, utilization of genetically modified microorganisms, and addition of alternative sources of energy. However, in spite of the addition of co‐substrates, the time required for complete mineralization of chlorophenols can be still very long compared to those obtained in physicochemical processes. In recent years, there have been proposals for coupling oxidation processes (AOP or electrochemical) to biological processes such as denitrification to combine benefits of both types of treatment and establish more efficient, more rapid, less expensive, and environmentally friendly treatment trains for degradation of recalcitrant compounds in wastewater. One alternative is the pretreatment of chlorophenols containing effluents through chemical or electrochemical processes to make them more easily degradable in a sequencing denitrifying biological treatment. Recent results showed that times can be considerably reduced for the complete mineralization of 2‐CP in an electrochemical‐biological combined system, where an electrocatalytic dehydrogenation process (reductive dechlorination) was coupled to a biological denitrification process in sequential ECCOCEL‐type (Pd‐Ni/Ti electrode) and rotating cylinder denitrifying reactors. The total time required for 2-CP mineralization in the combined electrochemical-biological process was close to the previously reported times for electrochemical and AOP processes, but in this case, an efficient process was obtained without accumulation of by‐products or generation of excessive energy costs due to the selective electrochemical pretreatment. This study showed that the use of electrochemical reductive pretreatment combined with denitrification could be a promising technology for the removal of recalcitrant molecules, such as chlorophenols, from wastewater by more efficient, rapid, and environmentally friendly processes. However, more studies are required in order to get an insight about the denitrification of electrochemically pretreated effluents in different combined systems, different configurations of reactors, and in the presence of different mixtures of chlorophenols and types of co‐substrates.


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