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A Review on Advanced Oxidation Processes for Effective Water Treatment

Nirmalendu Sekhar Mishra , Rajesh Reddy , Aneek Kuila , Ankita Rani , Priya Mukherjee , Ahmad Nawaz , and Saravanan Pichiah*

Environmental Nanotechnology Laboratory, Department of Environmental Science and Engineering, Indian Institute of Technology (ISM), Dhanbad 826004, Jharkhand, India.



Advanced oxidation processes (AOPs) such as fenton, ozonation, sonolysis, photocatalysis, UV photolysis, and wet air oxidation are one amongst the most suitable techniques for water and wastewater treatment. These, AOPs have also been chosen for the complete degradation of various categories of emerging pollutants that could not be managed by any conventional technologies. The mineralization is achieved by chemical reactions between the various reacting species generated and the pollutants. The present article provides a vivid view of the mechanistic features of various AOPs and its possible synergisation for process enhancement to achieve better treatment efficiency.


AOP; sonolysis; ozonation; UV; fenton; photo-fenton

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The availability of the earth’s fresh water resources has drastically depleted or contaminated due to improper water management, leading to the vulnerable situation. On the other hand the demand for safe potable water is increasing day-by-day due to the exponential growth of population and inability of the traditional treatment [1]. There are many traditional and contemporary purification techniques available or practiced for delivering safe water as per the local standards and these spans from basic filtration, adsorption to most advanced techniques; membrane separation and advanced oxidation processes (AOPs). Amongst the contemporary, the latter one is recognized as highly effective in delivery of safe drinking water free of organics, inorganics, and microbes. [2-3]. Owing to strong reactive oxygen species generation ability of AOPs it was considered for treating different types of water and wastewaters containing the various classification of pollutants including endocrine disrupting chemicals (EDCs), persistent organic pollutants (POPs), total organic carbon (TOC) and micropollutants [4-5].  This AOPs is a broad classification wherein consists of various techniques for the generation of reactive oxygen species and is shown in Figure 1.  In general, the realistic aim of any water purification techniques is to render water that is free of toxic matters (organic, inorganic and biological). In this regard, AOPs are characterized as best water treatment/purification processes that involve generation of hydroxyl radical (*OH) in sufficient quantity to affect water purification at standard temperature and pressure [6]. The significant advantage of AOPs over all existing chemical and biological processes is that they are totally “environmental-friendly” as they neither transfer pollutants from one phase to the other (as in chemical precipitation and adsorption) nor produce massive amounts of hazardous sludge [7-10]. The first AOP based water purification/treatment in full scale was proposed in early 1980s and followed by considerable achievements have been reported [11, 12]. Thus, the present review will emphasize on the various aspects of AOPs for efficient water management.

Figure 1: Classifications of Advanced Oxidation Process 

Figure 1: Classifications of Advanced Oxidation Process


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The enhanced degradation of various categories of pollutants by different AOPs has drawn attention from various research communities. The AOP allows the in-situ generation of various reactive oxygen species (ROS) via different process such as sonolysis, ozonation, UV, Fenton processes, etc. These ROS are subsequently utilized towards the degradation of the various categories of pollutants. The insights on the process parameters and degradation of different AOPs have been conferred. Thus, the present article consolidates the significant works that was reported by the various researchers for efficient water management.


It involves efficient utilization of ultrasonic sound with a frequency range of 20 KHz -10 MHz [13, 14]. It does not utilize any hazardous chemicals as mediator’s and hence regarded as eco friendly process. The organic molecules are degraded as a result of explosions of the cavitation bubbles formed as a result of ultrasonic/hydrodynamics. The generated cavitation bubbles tend to fluctuate in their size until get collapsed at their resonance size, leads to dissipation of the stored energy causing the explosions [13]. The formation of these cavitation bubbles highly dependents on the ultrasound frequency [15]. In general, lower frequencies leads to formation of lesser concentration of active bubbles due to presence of high water vapor content in the collapsing bubbles [15]. However, high frequency leads to collision among the active bubbles which generates smaller number of reactive species leading to lesser efficiency [15]. The schematic of working principle of Sonolysis is depicted in figure 2.

The explosion of these bubbles leads to degradation of the pollutants via pyrolysis at extreme pressure and temperature (500–10,000 atm & 3,000– 5000 K respectively) [16, 17] subsequently leading to the generation of *OH by the dissociation of water molecules. Thus formed *OH further reacts with the pollutants leading to their simplest form [18, 19]. The degradation at the bubble-liquid interface is dominated by the *OH. Also, the migration of free radicals from the bubble–liquid interface into the bulk liquid leads to secondary reactions in it. It is facile sludge free process with no additional generation of secondary pollutants, promoting it as one of the most preferred techniques over photolysis, photo-Fenton and Fenton process, etc. [14]. Moreover, it has inherent ability to treat cloudy water and leads to the efficient degradation of volatile and sparingly soluble organic matters causing high turbidity [19]. Nevertheless, its lower viability due to higher energy consumption and lesser mineralization efficiency limitations directs towards intensifying with various other AOPs like photocatalysis (sono-photocatalysis), photo-fenton (sono-fenton), ozonolysis (sono-ozonation), sonophotolysis, etc.

Figure 2: Schematics of working principle of Sonolysis (a) Bubble interior (b) Liquid-bubble interface (c) Bulk solution 

Figure 2: Schematics of working principle of Sonolysis (a) Bubble interior (b) Liquid-bubble interface (c) Bulk solution


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The mineralization efficiency can also be enhanced by varying the operational parameters such as initial substrate concentration, pH, catalyst loading and ultrasonic power [20]. Among the intensified, sono-photolysis involves the synergistic effects of UV irradiation and ultrasound waves towards the mineralization of the pollutants in the absence of catalysts. Whereas, sono-photocatalysis involves the use of UV irradiation and ultrasound waves in the presence of a semiconductor photocatalyst. The synergistic effect of UV/ultrasonic waves leads to enhanced generation of the reactive radicals leading to improved mineralization efficiency. The enhanced generation was attributed to the formation of electron-hole pair as a result of excitation in the semiconductor photocatalyst [21]. Additionally, presence of photocatalyst improves the bubble cavitation phenomenon resulting in enhanced migration of the reactive species towards the liquid bulk region [21]. Thus, intensification of the above process leads to increased concentration of the free radicals as a result of ultrasound on the peroxide species [22]. In case of sono-ozonolysis, the mass transfer of the *OH and ozone are enhanced leading to in-situ generation of H2O2/HO* (each O3 molecules degrades generating 2*OH) [22] resulting effective mineralization of the pollutants.  The reactive species are generated as a consequence of cavitation phenomenon in water and thermolysis of ozone. The mineralization can be further enhanced either by increasing the pressure or adding peroxide [23]. The combination helps in achieving efficiency levels > 80% within a pH range of 5.5 – 6.5 [24]


Ozone is categorized as strong oxidant and a powerful disinfectant [25] after fluorine. Theoretically ozone has been reported to oxidize both inorganic and organic pollutants but practically ozone is highly selective towards pollutants [25]. Hence ozone is considered as an electrophile with high selectivity in its reaction [26]. Ozonation for water treatment is highly applicable for degrading microbes [26], decolorization [27, 28], micropollutants removal [29, 30], non-protonated amines [26] and taste and odor removal [26, 31]. This technique is commercially implemented in European countries like Switzerland, Germany and etc as an oxidizer and in wastewater treatment plants [32]. Ozone generator, cooling system for ozone generator, pre-treatment unit for dehydrating the air added into the Ozonator and post-treatment reactor for removing excess ozone in the off-gas are the units required for implementation of ozonation [33]. The schematic of a typical ozone reactor is shown in figure 3.

 Figure 3: A typical reactor assembly for ozonation. (A=Liquid circulation pump; B=Ozone liquid analyzer; C=Ozone gas analyzer) [34].

Figure 3: A typical reactor assembly for ozonation. (A=Liquid circulation pump; B=Ozone liquid analyzer; C=Ozone gas analyzer) [34].


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Aquatic phase reaction of Ozone

In water, ozone is wobbly and hence undertakes reaction with the elements of water components [25]. The ozone decomposition mechanism in water entangle complex sequence of atoms and single electron transport with intermediate *OH formation and further involves the formation of OH-, HO2, O2-, O3-, HO3, OH, O2 and HO4 entities as shown in figure 4. This ozone decomposition process can be accelerated by escalating the pH or hydrogen peroxide concentration [26]. It is well known that Ozone is the predominant disinfectant in water while OH and O3 both act as oxidants in the oxidation process in water with O3 being highly selective and *OH is being highly reactive [26]. Hence ozonation can simultaneously be used for disinfection and oxidation. In the inception ozone concentration in water decreases rapidly and then follows first-order kinetics while in the second phase of ozone decrease through oxidation following second-order kinetics [26, 35, 36].

Figure 4: Ozonation reaction in water matrix [25]

Figure 4: Ozonation reaction in water matrix [25]


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The half-life of dissolved ozone varies from seconds to hours depending upon the water [26, 28, 37] pH, alkalinity, natural organic matter content [26, 28]. Among the three the natural organic matter can react with ozone or scavenge *OH i.e. directly or indirectly affecting ozone stability [26]. It has been reported that ozone is potent to react with substances directly or indirectly with *OH even at neutral pH as hydrogen peroxide, superoxide ions [25]. Ozone, *OH or the blend of the two and subsumed throughout the ozonation of organic and inorganic compounds. Ozone oxidation is enhanced by electron donating groups like –CH3, O-, -OCH3 [26, 32] and is reduced by electron withdrawing groups like –Cl, -NO2 [26]. Sulfidic groups and compounds containing amino groups and double bond also exhibit high ozone reactivity while the reactivity with the saturated compounds is low being accumulated during the ozonation process [26]. Low reactivity is also observed in the reaction of ozone with methyl and ethyl ether. Two electron oxidation liberating oxygen atom from ozone is followed in ozonation for oxidizing inorganic compounds [26, 38, 39]. The oxidation potential decreases with protonation of species due to decrease in nucleophilicity [26]. Hence the Ozonation can be effectively applied to varieties of pollutants as shown in the Table 1.

Table 1: Various categories of pollutants degraded by ozonation






Microbial (cyanobacteria) product










Vinyl chloride


[26, 42]






Nitrilotriacetate (NTA)



Ethylenediaminetetraacetate (EDTA)





















17 α – ethinyl estradiol






Deproteinated amines








Inorganic micropollutants












Influence of process conditions

Higher dosage of ozone at elevated pH with low bromide concentration increases the abatement efficiency of micro-pollutants [29]. While low alkalinity and low dissolved oxygen concentrations decrease the oxidation capacity of the system [26]. For active compounds like diclofenac, sulfamethoxazole, carbamazepine, trimethoprim, hydrochlorothiazide, phenazone, tramadol, metoprolol etc. with ozone and *OH are independent of pH change without variation in degradation efficiency; however elevated pH readily converts O3 resulting in the abatement of ozone-resistant [29].

Limitation of Ozonation

Low oxidation by ozone is reported for chlorinated benzenes, geosmin, and methylisoborneol (MIB), trihalomethanes (THMs) etc [25]. Cryptosporidium paravum oocyst are a resistant microbe against disinfection requiring higher amount ozone exposure and hence forms undesirable by-products in drinking water [26, 47]. Ammonia removal by ozone is slow as it possesses weak oxidation potential [26]. It has been seen that the oxidation products produced by ozonation can have unknown toxic matters however these are in low concentration as compared to parental compounds having negligible antimicrobial and estrogenic activities. The toxic matter includes formaldehyde, ketones, phenols, nitromethanes and carcinogens like bromates, N-nitrodimethylamine (NDMA) [32, 48]. Bromate a potential carcinogen formation occurs when ozone and *OH react with bromide in the liquid phase. Apart from all the high costs of ozone as a reagent is a major limiting factor in implementing ozonation.


Ozone combined with hydrogen peroxide has emerged as a new dimension in water treatment which can oxidize both inorganic and organic substances more effectively than standalone process. The first studies for wastewater treatment by using O3/H2O2 were performed by simultaneous by Nakayama et. al., and Hango While, Brunet and Duguet, performed for treating drinking water [51]. Studies showed that H2O2 application in ozonation enhanced the organic substance and Trihalomethanes (THM) precursor oxidation. Its addition increases the ozone transfer rate [51, 52-56], follows a single electron transfer forming HO2- which initiates the ozone decomposition cycle forming *OH. The H2O2 incorporation in ozonation especially increases the color removing efficiency but treating drinking water, the oxidation of pesticides, aromatic compounds, and chlorinated solvents mainly applies O3/H2O2 [50, 61]. Benefits of O3/H2O2 usage include shorter reaction time, allowing higher application of ozone doses and low agglomeration of ozone at the reactor outlet. Process conditions like reaction time increment after ozone addition, intensifying pH and applying hydrogen peroxide can enhance the oxidation property of ozone. However, increase in reaction time and pH is not economically viable however H2O2 being a low-cost reagent most commonly applied in drinking water treatment for achieving higher efficiency. Ozone decomposition by H2O2 incorporation is initiated by *OH and superoxide formation [26]. In case of treating surface waters using conventional ozonation and O3/H2O2 much difference was not observed in the transformation of ozone to HO*. But in case of groundwater, containing para-chlorobenzoic acid (pCBA) the oxidation of it by conventional ozone is 20% and was increased to 50 % by incorporating H2O2 along with O3 [26]. Compounds like geosmin and 2-methylisobrneol (MIB) produced by algae are also difficult to oxidize by ozone as they contain saturated ring system. However, they are well suited to be treated by O3/H2O2 having high oxidation rate constant [26].The Bromate formation is low in O3/H2O2 process than the conventional ozonation [51].


Homogeneous and heterogeneous catalyst addition in ozonation process also plays a key role in enhancing the oxidation reaction [57]. Metal oxides like Fe2O3, Al2O3-Me, TiO2-Me, MnO2, Ru/CeO2 and metal ions like Fe2+, Fe3+, Mn2+, etc. have been used as catalysts [57]. Successful removal of chemical oxygen demand, organochlorides, and total organic carbon had been achieved by combining iron and manganese [57, 58]. Combinations like O3/TiO2, Ru/CeO2/O3 [33], Al2O3/O3 showed better efficacy in removing total organic matters [57]. Granular activated carbon is also considered as a catalyst for the destruction of bio-refractory compounds [57, 60].

UV bases AOP

The UV treatment is generally applied as a tertiary for killing the microbes and degradation of those aquatic organic compounds which can absorb UV light. On the absorption of UV light, the electrons in the pollutant excite from the ground state to the excited state, (equation. 1) from where the electrons are transferred to an oxygen molecule which converts both O2 and the pollutant molecule into a radical (equation. 2). The radical being a highly reactive species oxidizes other molecules to acquire a stable form.

P  → P*                            (1)

P* + O2 → P+* + O2-*         (2)

UV light can also result in the homolytic cleavage of the chemical bond of the pollutants resulting in the formation of two radicals (equation. 3). UV light with a wavelength less than 190 nm can effectively break highly stable C-F bond whereas wavelength in the range 210-230 nm can break C-Cl bond. The radicals formed can then react with oxygen (equation. 4) or may take part in the further oxidation-reduction reactions with the other dissolve molecules.

R  → X → R* + X*                      (3)

R* + O2 → RO2                          (4)

High energy UV lights with a wavelength smaller than 190 nm can photolyze water molecule to form *OH (equation. 5), that subsequently oxidize other organic substrates. [61]

H2O + hv → 2HO*                    (5)

Lamps like Mercury arc with different UV light emitting intensities are used for generation of the UV radiation. These are generally of three types: Low pressure, medium and high-pressure lamp. The former is monochromatic in nature and emit light of wavelength 253.7nm. Medium and high pressure lamps emit a wide range of wavelengths in the UV region and penetrate deeper because of their higher intensity and take less time for the completion of the treatment. The limitation with the application of them is that they are energy intensive. [62] Lamps like Pulse radiation lamps and Excimer lamps were also utilized for generation of UV irradiation. [63]. The main component of UV treatment system includes lamps, ballast and a reactor. Mercury arc lamps are generally used as the UV lamps. Ballast is a support device, which mainly performs two functions: first, they provide appropriate voltage for the reliable starting of the lamp; secondly, they maintain a continuous current flow to the lamp, to prevent the lamps from short-circuiting. Finally, the Reactor, they are of two types: contact and non-contact reactor. The contact reactors are the one in which the UV lamps remain in submerged condition. The lamps are generally enclosed within quartz sleeves in order to prevent them from damages. Non-contact reactors are the one in which a transparent material is placed between the water sample and the lamps. The lamps can be positioned either in perpendicular or parallel to the wastewater flow direction. [62, 64]. The major strength of this process is eco-friendly and shorter treatment time. It also does not require the use chemicals; therefore, no residual products are left after the treatment [62]. This technique has been applied for the degradation of numerous organic compounds, including EDCs (Endocrine disrupting chemicals) and various industrial solvents. It is an effective method for degrading NDMA (N-nitrosodimethylamine) a well-known potent carcinogen and mostly found in wastewater in trace amounts [65-67]. Sakai et al (2012) found 222 nm Kr- Excimer – UV lamps to be a better option for NDMA degradation in the place of low pressure (LP) and filtered medium pressure lamps (FMP). [68] Sanches et. al. 2010 utilized low-pressure UV lamps to check the degradation of five pesticides viz: Alachlor, Atrazine, Diuron, Pentachlorophenol, Chlorphenvinphos and Isoproturon. More than 50% of all the pesticides were completely degraded by the conventional low-pressure mercury lamp except Isoproturon. The low quantum yield of Isoproturon, in spite of having high molar absorption coefficient, can be a reason behind its less degradation. [69]. Various categories of pollutants treated by UV photolysis are summarized in Table 2.

Table 2: Various categories of pollutants treated by UV photolysis


Specific Pollutant


Trace Organic Chemical




Diclofenac, Antipyrine, Chlorotetracycline, Norfloxacin, Caffeine, Dipyridamole, Diltiazem, Clofibric acid, Acetamiprid


sulfamethoxazole (SMX), oxytetracycline (OTC) and ciprofloxacin (CIP)





Atrazine, Diuron, Alachlor, Pentachlorophenol, Chlorphenvinphos


Anabolic-androgenic steroid







The limitations of the technique are the *OH formed by the action of UV, sometimes leads to the partial degradation of the organic contaminants, leaving behind the intermediates concentration in a higher level at the place of CO2 and H2O. The higher concentration of Total Suspended Solids (TSS) and particulate material (e.g. humic compounds and iron) lags the treatment. Further, it is energy intensive and expensive as compared to the other tertiary processes like chlorination [62].

UV/O3 Process

Treatment by combining UV and O3 is a well-established advanced oxidation technology. This technique is more advantageous than the individual UV and O3 technologies since it combines the advantages of both. The ultraviolet light coming in contact with the ozone (O3) breaks it to form *OH, through the following reaction steps [75]:

O3 + H2O + hv → H2O2 + O2                 (6)

H2O2 + hv → 2OH*                        (7)

2O3 + H2O→ 2OH*                   (8)

The *OH formed, then either completely mineralizes the organic substances to form CO2 or H2O or form some easily degradable intermediate substances. Being an unstable and reactive molecule, O3 gas is generated in-situ in the experiment. Thus, the generated O3 is then sparged into the reactor in which UV lamps are installed. [75, 76]. These UV lamps are enclosed within Quartz sleeves in the contact reactors, which ensure better transmission of UV. In the non-contact type UV lamp and wastewater are separated by a transparent separator. Schematics of a UV reactor configuration are shown in figure 5.

 Figure 5: Schematic representation of a UV reactor consisting of two UV Banks [77]

Figure 5: Schematic representation of a UV reactor consisting of two UV Banks [77]

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In most of the studies, it was found that the UV/O3 treatment was successful in TOC and COD reduction besides its pollutant degradation capacity. [75, 78-80].  In a study performed by Hassan et. al. (2017), it was found that the color removal was higher for UV/O3 in comparison to individual treatment with O3. [80]. Tehrani et. al. (2010) studied the removal of Reactive Blue 19 dye through the UV/O3 and O3 treatment. In their study, it was found that the UV/O3 treatment was more effective in COD removal than the O3. It was also found that decolourization decreased as the initial concentration of dye was increased. [78] The factors which can affect the treatment includes: pH, initial pollutant concentration, the turbidity of the solution, amount of O3 dose, amount of UV dose, types of UV lamps used for the process, reaction time, scavengers present in the water [80-82]. Table 4 enlists some selected pollutants removed effectively by UV/O3 treatment

Table 3: Selected Pollutants Removed By UV/O3 Treatment


Specific pollutant










Direct Yellow 50













Other organic chemicals



Bisphenol A



Fenton Processes

The Fenton is one of the prominent AOP and the chemistry of reactions related to this includes reactions of peroxides (H2O2) with Fe2+ to generate reactive oxygen species that can degrade the organic as well as inorganic matter in aqueous phase. Fenton chemistry dates back to 1894 when the activation of H2O2 by ferrous salts was reported for oxidizing tartaric acid by Henry J.Fenton [89].In 1934 it was proposed by Haber and Weiss [90] that there is a formation of *OH due to the Fenton reaction. This *OH has an oxidation potential of 2.73V. Hence it is one of the most active and powerful oxidants, which can be used in the degradation of most organic compounds including emerging [91].

Homogeneous Fenton reactions

The Fenton process is an easy and economical method to generate highly reactive oxygen species for degrading contaminants. H2O2 is safe and easy to handle, comparatively cheap and easily decomposes into water and oxygen. Similarly, iron is also cheaper and safe to use. This mechanism of decomposition of H2O2 was later revised by Barb et al. [92-94] to introduce the chain reactions of the Fenton process. The proposed mechanism which involves the breaking down of H2O2 to produce *OH /free radical is a sequence of seven reactions in an acidic medium under dark conditions [95]. The reactions are as follows:

Fe2+ + H2O2 → Fe3+ + OH + *OH


Fe3+ + H2O2 → Fe2+ + HO·2 + H+


*OH + H2O2 → HO·2 + H2O


*OH + Fe2+ → Fe3+ + OH


Fe3+ + HO·2 → Fe2+ + O2H+


Fe2+ + HO·2 + H+ → Fe3+ + H2O2


HO·2 + HO·2 → H2O2 + O2



*OH, which is the required oxidant for degradation of the contaminants is produced by reaction 9. Reaction 10, therefore, becomes the rate-limiting reaction because it is slower than proceeding by several orders of magnitude. The organic compounds (RH / R) can be oxidized by any one or combinations of the following: (1) *OH, (2) abstraction of hydrogen (R*), (3) addition of hydroxyl (*ROH) [96].

RH + *OH → H2O + R* → Further oxidation


R + *OH → *ROH → Further oxidation



*OH, can be scavenged by either Fe2+ or H2O2 as shown in equation 10 and 11. Hence optimization of Fe2+ / H2O2 is to be carried for reducing the scavenging of ·OH. Whereas, the produced Fe3+ precipitates to form ferric oxy-hydroxides as the pH increases from its optimum generating an undesirable sludge giving problems in practical applications [97, 98]. Additionally, the drawbacks of application of Fenton process for large-scale wastewater treatment include pH dependency (effective only in the range of pH 2 to 5), generation of iron-based sludge, the necessity of its expensive post-treatment and finally neutralizing the treated water before disposal [99]. Therefore, further research is required on modified Fenton processes such as photo Fenton which can increase the reaction rate by light irradiation. Sometimes the use of chelating agents provides optimum pH for Fenton reactions. Chelating ligands compete favorably with hydroxide ion; hence increase the pH range over which compounds are soluble. The reaction kinetics is as similar to Fenton oxidation at the optimum pH. Various chelators include Fe3+-CIP chelate, deferioxamine, cyclodextrin, nitrilotriacetic acid (NTA) and ethylenediaminetetraacetic acid (EDTA) [100-103] were adopted. However, additional research is required to identify chelating agents that can increase the rate of oxidation, stability, and eco-friendliness.

Photo – Fenton Process

Irradiating Fenton reaction solutions with ultraviolet and visible light increases its reaction rate and the efficiency towards waste degradation [99]. The increase in efficiency is correlated to the photochemistry of Fe3+ complexes [Fe3+(OH)-] + and [Fe3+(RCO2)-]2+ to dissociate into Fe2+. The photochemistry of Fe3+ gives an advantage to Fenton processes because the reduced Fe2+ reacts with H2O2 forming *OH as per reaction 9 [104]. The photo-Fenton reaction reaches its optimum around pH 2.8 and as the pH increases above this the Fe3+ precipitates as oxyhydroxides and as pH decreases below the optimum, the concentration of Fe(OH)2+ will decline [105]. The Photolysis of hydrogen peroxide takes place under UV light irradiation as shown (equation 18):

H2O2 + hν → 2HO*                      (18)

Although the quantum yield by photolysis of hydrogen peroxide shown in reaction 10 is good, due to the weak absorption of light irradiation by H2O2, its activity in photo Fenton reactions is not significant. Similar to Fenton, photo-Fenton has the drawbacks of high cost for sludge processing and the requirement of narrow pH range, limits its application in waste/wastewater treatment [97, 106].

Heterogenous Photocatalysts

Heterogeneous photocatalysis is different compared to other treatment methods involving oxidation and reduction simultaneously, with the use of light irradiation and a light absorbing photocatalyst. Various compounds can utilize light irradiation to catalytically undergo photolysis to produce redox reactions. These compounds usually have a band structure with empty conduction and a filled valence band [89]. Once light irradiation is incident on a semiconductor and if the energy of photons exceeds the energy gap of the semiconductor, electrons are excited from valence band to the conduction band leaving behind the holes [90, 91]. The activated electrons in the valence band and holes in the conduction reacts with water generating *OH, superoxide (*O2-) and peroxide radicals (*OOH). These radicals further degrade various pollutants to obtain products such as CO2 and H2O [92-94]. The mechanism of photocatalysis and degradation of contaminants is illustrated in figure 6.

 Figure 6: Schematic representation Photocatalysis of mechanism

Figure 6: Schematic representation Photocatalysis of mechanism


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The heterogonous photocatalyst materials consist of TiO2, ZnO, Fe2O3, WO3, SnO2, ZrO2, CdS ZnS, etc. Among them, TiO2 is the most extensively used heterogonous photocatalyst due to its easy availability, cheapness and high chemical stability. The other classification of photocatalyst also experimented for its applicability. Owing to the limitation of utilizing the visible light the conventional photocatalyst materials were hybridized with suitable cocatalyst.  Table 4 shows the various hybridized heterogeneous photocatalysts utilized for waste degradation.

Table 4: Various photocatalysts studied for degrading different pollutants

Sl. No. Photocatalyst Pollutant Removal efficiency Ref.
1. Graphene oxide/WS2/Mg doped ZnO nanocomposite. Rhodamine B (RhB) 90% in 5 min [98]
2. Pd-TiO2 photocatalyst Amoxicillin (AMX) 97.5% in 5h [107]
3. Hexagonal WS2 platelets Rhodamine B 98% in 105min [99]
4. Ag+, Fe3+ and Zn2+ intercalated cadmium(II) metal organic frameworks 2-cholrophenol (2CP) 93% in 5h [104]

Reduced graphene oxide and Ag wrapped TiO2

Bisphenol A (BPA)

69.1% in 5h



Graphene bridged Ag3PO4/Ag/BiVO4 photocatalyst


94.96% removal in 60min



Magnetic biochar supported g-C3N4/FeVO4


methyl paraben (MeP) and 2-cholrophenol (2-CP)

98.4% MeP removal and

90.7% 2-CP removal



In-based MOF/graphene oxide

Amoxicillin (AMX)

93% AMX removal, 80% TOC removal



Magnetic RGO/ZnO/ZnFe2O4 composite

Methylene Blue (MB)

98.64% in 60min



Fe3O4 nanoparticles and oxalate complex 


97.61% in 3h



Copper zinc tin sulfide (CZTS) nanoparticles Methylene blue (MB) dye 50% in 45min [108]


Reticulated ZnO Acid Red 88 dye 79% in 180min [109]


α-Fe2O3 nanosheets

Bisphenol S 91% in 120min [110]


Ag/TiO2 photocatalyst

Amoxicillin (AMX), 2,4-dichlorophenol (DCP)

63.48% AMX & 60.23% 2,4-DCP in 5h



Fenton reactions using Heterogeneous catalysts

In conventional Fenton process removal of dissolved iron from the treated water is one of the biggest challenges which prompted the use of heterogeneous catalysts along with Fenton process. The investigation has been carried out on the use of supported iron catalysts to decrease sludge formation and to increase the pH range over which the Fenton reaction is effective. In Heterogeneous catalysts supported Fenton process reactant molecules get adsorbed on the active sites present on the surface of the catalyst. The products get desorbed after the reaction takes place [112].  The use of goethite (-FeOOH), hematite (-Fe2O3), FeS2/SiO2, Ilmenite (FeTiO3) and Titanomagnetite (Fe3TiO4) as heterogeneous Fenton catalysts has been studied by various researchers [113-116]. The advantage of an ideal heterogeneous catalyst is its ability to separate from water and function in wide range of pH.  Various pollutants degraded using Fenton/ Heterogeneous catalysts are tabulated in table 5.

Table 5: Pollutants degraded using Fenton/ Heterogeneous catalysts

Sl. No

Fenton/ Heterogeneous catalysts


Removal Efficiency



Photo-Fenton/ magnetite and EDDS

Bisphenol A (BPA)

BPA = 70% in 11h



Bioelectro-Fenton /carbon felt cathode /boron-doped diamond anode

Pharmaceutical wastewater

COD = 60%, 5-fluorouracil = 88%, caffeine = 43% in 3days



Fenton/ FeS2/SiO2


Ciproflaxacin = 99% in 60 min



Fenton/ ferric sludge

Landfill leachate

BOD7 = 99%, COD = 86%




Micropollutants from municipal wastewater

Micropollutants = 40%



Fenton with graphene modified iron sludge as catalyst

Rhodamine B (RhB), acid red G (ARG), metronidazole

RhB = 99%, ARG = 98.5%, metronidazole = 91.8%



Photo Fenton oxidation with zeolite as catalyst


Paracetamol removal = ~99%, TOC removal = 60% in 5h



Other AOPs

The above discussed processes are the most prominence among the AOPs with practical applicability. Apart there are few like wet air oxidation (WAO), supercritical wet oxidation process (SWOP) process and electron beam radiation. Off this WAO utilizes the molecular oxygen or air as oxidizer in high pressure and temperature environment. This extreme condition allows the generation of free radicals that decomposes the waste [123]. Thus temperature and pressure are the controlling factor for WAO process. Most of the organic acids excluding acetic and propionic acid [124] are converted to CO2 at high temperature. Figure 7 depicts the simple functionalities of wet oxidation.

 Figure 7: Flow operational diagram of WAO process

Figure 7: Flow operational diagram of WAO process


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Huge operational expenditure and investment is required to maintain a WAO system as it handles an extreme reaction environment. Figure 8 illustrates Reactor design adopted for WAO system.

 Figure 8: Reactor design for SWOP system

Figure 8: Reactor design for SWOP system


Click here to View figure


SWOP employs supercritical condition refers to the extreme temperature and pressurized condition, where water changes its polarity and became a non-polar solvent to get miscible with the organic part. In supercritical condition, water can be mixed with the oxygen creating a homogeneous mixture which is perfect medium for organic degradation. When organic compounds and oxygen are dissolved in water above the critical point they are immediately brought into intimate molecular contact in a single homogeneous phase. With no interface transport limitations at sufficiently high temperatures, the kinetics is fast and the oxidation reaction proceeds rapidly to completion. This supercritical water oxidation (SCOW) is also referred as hydrothermal oxidation (HTO). This process uses hydrogen peroxide in a homogeneous mixture to oxidize the toxic effluents above the critical point of water. If the organic material is in solid phase it requires the heterogeneous catalytic SCOW. It is most efficient method in case of environmental remediation as complete removal of oxidisable material can be achieved by this process. Till date inorganic substances like ammonia or cyanides can also be converted to CO2, H2O, and N2. SCOW consists of four steps, starting from pressurizing the reagent, reaction, salt separation and depressurization. Wastewater and oxidant are mixed and fed in the SCOW reactor. The oxidants are normally heated before reaction and this reaction condition allows the exothermic reaction between the waste and oxidant. The heat energy obtained in the oxidation reaction helps to activate the reagent optimally to oxidizable condition. After the treatment the salt precipitation is visible inside the reactor, because of reduced salt solubility. Though the process requires high energy, this demand can be recovered by utilization of this hot stream for preheating or energy production. A number of works that study in depth the organic reactions in SCW, focusing on the influence of the properties of water and in the kinetics modelling, has been developed over the last few years. The table 6 consists of the list of some organizations that have incorporated SCOW plant for water treatment. Figure 9 shows the schematics of a SWOP process for water/wastewater treatment while the table 6 lists the organization that incorporated the same.

 Figure 9: Schematics of SCOW

Figure 9: Schematics of SCOW


Click here to View figure


Table 6: List of some organizations that have incorporated SCOW plant for water treatment


Treated Effluent

Removal efficiency


ETH Zurich



TOC rem. 99.9%


ITC-CPV Karlsruhe


Ethanol, Na2SO4, Paper mill waste effluents

TOC rem. 99.9%


Sandia’s EER


Isopropyl alcohol

Military smokes and dye formulations

No Na2SO4 deposits in the

transpiring wall


Pine Bluff Arsenal


Isopropyl alcohol

Sugar and Na2SO4

Solutions Military smokes and dye


TOC rem. 99.9%


U.S. Navy/Army’s Dugway Proving

Ground Facility

(Utah, USA)

Naval wastes (Cl- and Fl- containing) (71 h) Chemical weapons (231 h)

TOC rem.> 99.9%

(Trials for Blue Grass chemical weapons destruction)


CEA (France)


TOC rem.   99.9%




The review explicitly discussed on the robustness of various AOPs that has been extensively used for water management. Their treatment efficiency depended on various process parameters that were clearly reviewed. However, limitations such as high operational costs, high energy consumption and lower generation of the reactive species initiated the need for process intensifications. The strength of the intensified system clarified their role on treating various pollutants. Though various AOPs for water treatment are discussed, the Heterogeneous Photocatalysis is most widely preferred over the rest of the processes for real-time applications. Over all the review presented the clear scenario of the AOPs for water and wastewater treatment with a benefit to the community.


The corresponding author is grateful to Science and Engineering Research Board (SERB), Department of science and Technology for the financial support received under Early Career Research Award with grant code ECR/2016/001400.


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