Abstract
Water pollution and fossil fuels are major issues in the context of climate change. Photocatalysis research is rising to develop green technologies for the remediation of pollutants and for energy production. Photocatalysis converts the light energy as photons into chemical energy using semiconducting materials. Different methods are utilised to synthesise these photocatalytic materials. Metal and coupled metal frameworks are applied for the production of photocatalytic materials. Here we review the synthesis and applications of photocatalysts for environmental decontamination and for production of biodiesel, methanol and hydrogen. Pollutants include dyes, pesticides, herbicides, phenols and antibiotics.
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Introduction
Water contamination considered being pertaining environmental issues gained pivotal attentiveness in recent years. Heavy metals, dyes and persistent organic pollutants are the three predominant pollutants occurring in nature. The presence of these pollutants in the environment even in minute amounts can pose ample health ailments in human resources. Waste discharges such as pesticide, pharmaceutical, textile and petrochemical industries routinely discharge these pollutants into the environment. Chronic toxicity, developmental and neurological disorders and cardiovascular and intestinal ailments are some of the health effects caused due to the chronic occurrence of these chemicals into the environment. Different conventional treatments exist to remediate the environmental pollutants. Some of these methods include membrane separation, solvent extraction, adsorption, filtration, electro kinetic remediation, flocculation, coagulation and precipitation (Kiruba et al. 2014; Anitha et al. 2015; Neeraj et al. 2016; Ahmad et al. 2020a; Hitam and Jalil 2020; Jeevanantham et al. 2019; Saravanan et al. 2020).
Few advanced oxidation processes include fenton reaction, photocatalysis, wet oxidation and sonolysis. Of these, photocatalysis is regarded as the suitable method due to its property of mineralising recalcitrant compounds. Photocatalysis has attracted extraordinary consideration because of its direct transformation of solar energy to the easy storage of hydrogen and CO2 conversion to hydrocarbon fuels (Li et al. 2018). The degradation mechanism of photocatalysis has been characterised by four ways (1) light ingestion to create electron–hole sets, (2) division of energised charges, (3) transferral of electrons to the external of photocatalysts and (4) usage of charges on a superficial level for redox responses. Photocatalysis has several advantages compared to other conventional methodologies such as efficient degradation of contaminants, wastewater treatment, environmental protection, clear surface of various material, air purification and no secondary pollution. Photocatalysis study comprises the generation of chemical energy from light energy which generates charge carriers provoking redox reactions which reduce the recalcitrant pollutants. The entire process involves three major steps, namely the generation of charges, separation of charged components and their consumption (Long et al. 2020; Anandan et al. 2020; Younis et al. 2020). Pollutant degradation using photocatalyst involves four major steps: mass transfer of pollutant molecules, excitation of pollutant molecules on the photocatalytic surface, degradation of pollutant molecules by oxidised compounds and desorption of decomposed compounds from photocatalytic surface to the bulk solution. Cost efficiency, non-toxic nature, absence of further pollution and high process efficiency are the advantages of employing photocatalytic process in environmental pollutants. Electron–hole pair separation efficiency and absorption signify the dependence of good photocatalytic materials. Some of the persistent organic pollutants such as pesticides, phenol, antibiotics and herbicides are also been remediated employing photocatalytic processes. For example, glyphosate herbicide and parathion pesticide have been removed using bismuth iron oxide-based photocatalyst and titanium-based photocatalyst, respectively. In general, photocatalytic materials are confined to specific substrates. After remediation process, they consequently assist in the dispersion and recuperation from environmental platforms. Well-designed photocatalytic substrates can enhance the photocatalytic efficiency of environment pollutant remediation (Di Paola et al. 2012; Meng et al. 2015; Ayodhya and Veerabhadram 2018; Zhao et al. 2019; Wood et al. 2019; Singh et al. 2013).
Fossil fuel consumption generates the large quantity of pollutant gases which may cause toxic effect (Cheng et al. 2017; Ren et al. 2018). One of the effective explications in sustainable energy resources is the development of hydrogen fuel from solar energy by conversion and splitting of water molecules. In contrast to traditional technologies, superior efficiency and performance in energy production were observed with photocatalytic technology (Huang et al. 2019; Zhang et al. 2019a; Li et al. 2019). Biodiesel, hydrogen and methanol are some of the fuels that are being produced by using different advanced oxidation processes. Studies such as biogas, hydrogen and ethanol production using pre-treated substrates using advanced oxidation processes show the increasing interest in the emerging of advanced oxidation processes for energy production (Tamilarasan et al. 2019; Kumar et al. 2019a; Yang and Wang 2019). Several photocatalytic materials have also been utilised for the production of bioenergy and biofuels such as biodiesel, methanol and hydrogen. Few photocatalysts used for the photocatalytic water splitting include titanium oxide, bismuth oxide and ferrous oxide (Lee et al. 2019; Helal et al. 2017; Hakobyan et al. 2019).
This review describes photocatalytic materials and processes for the elimination of environmental pollutants, for example metals, dyes and persistent organic pollutants. The findings of this review would appeal to various researchers and analysts who engross on the remediation of water pollutants employing new photocatalytic materials, generation of energy by photocatalytic processes and develop their explorations towards further explicating the advancements in photocatalytic processes. The mechanism of photocatalysis and in removal of pollutants is thoroughly interpreted. Several photocatalysts developed for the elimination of toxic contaminants have been described. Additionally, the photocatalytic processes for the generation of biofuels are portrayed in detail. Current limitations and future perspectives on the photocatalytic elimination of toxic contaminants and biofuel production are systematically discussed in this review article.
Principle of photocatalysis
Environmental pollutants can be eliminated by the process of light induced redox reactions known as photocatalysis. The exposure of photocatalyst surface to photon energy (hʋ) more than or equal to band gap energy (Ebg) results in the agitation of electrons from valence band to the conduction band consequently leading to electron–hole pair formation in both the bands, respectively. Positive hole generated in the valence band oxidises the pollutant or water molecules producing hydroxyl radical and the adsorbed oxygen on the photocatalyst is reduced by those excited electrons. In the conduction band, excited electrons possess strong reduction ability reacting with dissolved molecular oxygen in water or adsorbed oxygen on the surface of the photocatalytic material.
Organic pollutant degradation
In case of organic contaminant, hydroxyl free radical reacts on the organic group of the pollutant and converts the toxic pollutant into non-hazardous forms (Hasanpour and Hatami 2020; Ganguly et al. 2019):
Exciting agent and reducing agent are hʋ and \( h_{\text{VB}}^{ + } \), \( e_{\text{CB}}^{ - } \) is the photon energy required to excite the electrons.
Hydroxyl radical formation
Formation of super oxide radical anions and hydroperoxide radicals by reaction with oxygen
Degradation of organic pollutants by hydroxyl radical
The further process of degradation is initiated by hydroxyl radicals, hydrogen ions and superoxide anion radicals (Belver et al. 2019).
Heavy metal remediation
Usually heavy metals are the prevailing pollutants in water resources. Direct or indirect reduction takes place in photocatalytic removal of heavy metals.
Direct reduction of heavy metal species by photon energy.
In some cases, few metal species cannot be reduced directly or be transformed to higher oxidation state. Indirect reduction by donor intermediated reduction of heavy metals
By these reactions, heavy metals, dyes and organic pollutants can be removed in effective ways providing an alternative for conventional treatments. Metal ions or chemical species can be transformed from aqueous or contaminated solutions to photocatalytic surface removing their toxicity. Different metal ions are removed by slightly different photocatalytic mechanisms. Environmental applications of photocatalysis process are depicted in Fig. 1.
Photocatalytic remediation of environmental pollutants
Heavy metals
Globally, environmental pollution problems have been increasing every year since the industrial effluents such as organic pollutants, dyes, heavy metals and radioactive ions were discarded in the rivers, lakes and portable water. The toxicity of these pollutants causes illness to aquatic organisms and human health. These toxins are non-biodegradable. Among all these toxins, heavy metals are highly toxic and carcinogenic. They would accumulate in the food chain and affect our health. To remove these chemicals, many biological and chemical methods are used. However, photocatalytic removal processes were in practice and efficient (Sun et al. 2019; Dhandole et al. 2019). Ferric oxides are majorly used in many fields because of their stability and low cost. Three-dimensional ferric oxide hierarchical structure (3D Fe2O3) was synthesised for the removal of heavy metal. The 3D structure was prepared using ultrasound irradiation (Lee et al. 2018). The advantage of 3D Fe2O3 is that it has larger surface area, high stability and cost effective. As(V) and Cr(VI) are predominantly found in the water bodies. Source of the heavy metals for As(V) is Na2HAsO4.7H2O and for chromium is K2Cr2O7. 4 mg of 3D Fe2O3 and 25 mL of As(V) and Cr(VI) were taken and mixed well and kept in the room temperature for 15 h. Then the removal capacity of 3D structure was analysed by plasma atomic emission spectroscopy (PAEC). The removal rate for As(V) was 100% in 6 mg of commercial Fe2O3, whereas in 3D-Fe2O3 was 100% in 2 mg. TiO2 and ZnO were used as the source for preparing the nanoparticles for the removal of toxic contaminants. In this experiment (Shahzad et al. 2019a) CuCo2S4-modified MoSe2/BiVo4 composite was used as the photocatalyst. Hydrothermal process was used to prepare the monoclinic bismuth vanadate nanoparticles. Bi(NO3)3.H2O and NH4VO3 in 40 mL of deionised water and stirred continuously for 30 min followed by autoclave for 24 h at 180 °C. The nanoparticles were calcined at 400 °C for 3 h. From this, CuCO2S4-modified MoSe2/BiVO4 composite was prepared. To check the photocatalytic activity of the composite, chromium, copper, zinc, lead and cadmium were taken (0.1 mg of heavy metal in 100 mL of distilled water). The prepared composite also added to the container and stirred for 30 min and kept in the sunlight. The sample was drawn from the container, and removal of toxic was observed under ultraviolet visible adsorption spectrophotometry. The CuCo2S4-modified MoSe2/BiVO4 composite has photocatalytic activity under solar light irradiation.
Chemical and pharmaceutical industries discharge a large amount of heavy metals as effluent in rivers, lakes and also release CO2 in air which causes air pollution. In this (Chen et al. 2020) work, a new unfamiliar idea was introduced. The heavy metals are removed using adsorbents, and then the removed heavy metals are used as the photocatalyst for the reduction of CO2. Removal of heavy metal was attained by calcium silicate hydrate nanosheets. It was prepared using the rate controlled precipitation method. Four major heavy metals were selected (Cu2+, Zn2+, Ni2+, Pb2+). Calcium silicate hydrate nanosheets have high stability and high adsorbent capacity. The heavy metal solutions (Cu(NO3).3H2O, Zn(NO3)2.6H2O, Ni(NO3)2.6H2O, Pb(NO3)2) are added to 20 mg of calcium silicate hydrate ultrathin nanosheets and the experiment carried out at 25 °C and pH 5.0. The solution was stirred continuously. After 30 min, 1 mL of solution was centrifuged and to the supernatant 2% of HNO3 was added and the adsorption was viewed in atomic adsorption spectrometry. The removal of heavy metal in calcium silicate hydrate nanosheets was efficient, and sheets were washed with distilled water, ethanol and used as photocatalyst for the CO2 reduction. In another studies, rhodium and antimony codoped TiO2 nanorod (Rh–Sb TiO2) and titanate nanotube composite (RS-TONR/TNT) degrade organic pollutant and remove heavy metals in water under sunlight irradiation. Molten salt flux method was efficient for the synthesis of Rh–Sb codoped TiO2. For composite (RS-TONR/TNT) preparation, hydrothermal is considered to be convenient technique. Lead, copper, zinc and cadmium metal ions were chosen and added separately to the 25 mg/L of prepared composite. The solution was allowed for the adsorption process under the sunlight, and the ion concentration was observed in plasma atomic emission spectrometry. Lead ion has adsorbed in higher rate, and zinc ion was least adsorbed metals. Preparation methodology of TiO2 photocatalyst is listed in Table 1.
Cr(VI) is highly toxic and very difficult to remove from the water bodies (Zhang et al. 2019b). Nano-heterojunction (AgIn5S8/Bi2WO6) was prepared by adding Bi(NO3)3 and Na2WO4 solutions in AgIn5S8 of different mass percentage such as 5%, 10%, 15%. To study this removal experiment, pure Bi2WO6 and pure AgIn5S8 and AgIn5S8/Bi2WO6 were compared. The concentration of chromium was analysed by means of diphenyl carbazide method. Pure Bi2WO6 removes 54%, and AgIn5S8 removes 68% and 10% of AgIn5S8/Bi2WO6. Pure Bi2WO6 results in 22% reduction, 5%, 10% and 15% of AgIn5S8/Bi2WO6 terminate 43%, 54%, 64%, respectively, and pure AGIn5S8 shows 98% of chromium reduction.
Pyrite (FeS2) is natural iron sulphur mineral. In mineral separation process, the pyrite was discarded as tailing waste. It has higher capacity in the removal of environmental pollutants. Usually, FeS2 was used as semiconductor adsorbent. FeS2 was used as the photocatalyst for concurrent removal of heavy metals and dyes and degradation of the organic pollutant (Diao et al. 2015). For the photocatalytic reactions, 1 g/L of FeS2 was suspended into the solution containing malachite green and Cr(VI). Ultraviolet lamp was used for the photocatalytic irradiation, and the whole experiment was carried out in a reactor. Prior to the photocatalytic activity, the solution was subjected to the stirring process for 30 min using a magnetic stirrer. The initial concentration of malachite green dye and Cr(VI) ion was noted. The photocatalytic activity was carried out for 120 min. Organic pollutants were degraded separately using different photocatalyst. In this experiment (Yuqing et al. 2020), Z-scheme BiOCl–Ag–AgBr photocatalyst was synthesised to degrade organic pollutant. BiOCl nanosheets were synthesised by the modified solvothermal method. Then BiOCl–Ag was prepared using photodeposition method by loading Ag on BiOCl. Under solar irradiation, the experiment was carried out. 50 mg of photocatalyst was dispersed into 50 mL of Cr(VI) ion and phenol solution. After that, the experiment was carried out and samples were withdrawn and analysed using diphenyl carbazide colorimetric method. BiOCl–Ag–AgBr has high removal efficiency compared with others.
Dyes
Dyes are most common effluent that is discharged from the pharmaceutical, chemical and textiles industries. These effluents contain many toxic and carcinogenic compounds that cause illness to humans and ecosystems. Photocatalytic removal process is the excellent way to reduce the toxicity in the wastewater containing heavy metals and dyes and convert them into nontoxic compounds (Eckert et al. 2015). Many textile, chemicals and food industries release toxic dyes into the portable water and rivers. In this experiment (Soliman et al. 2017), transition metals and activated carbon were combined together and used for the removal of the crystal violet that was released from the industries. Activated carbon was prepared from the agriculture waste. Further the transition metals were doped on the surface of the activated carbon by ion exchange process. Different metal ions are used, namely cadmium, zinc, copper and lead. 5 g of activated carbon was added to each container containing 500 mL of metal solutions and kept in the shaker for 20 h. From each container, 1 g of sample was taken and 250 mL of crystal violet dye was added and kept in the dark for 20 h in the shaker and kept in solar light. The concentration of activated carbon was noted. The photocatalytic activity of these metal ions with activated carbon shows better results.
Sodium iron disulphide (NaFeS2) was a good semiconductor and utilised as a catalyst in wastewater treatment. In this (Dileepkumar et al. 2020) work, the photocatalytic material was prepared by hydrothermal process. During the synthesis of NaFeS2 and NaNO3, by-products are removed and the yield was around 55%.
Various experiments were carried out to check the photocatalytic effect of NaFeS2 on methylene blue dye. The NaFeS2 catalyst was added to the methylene blue dye solution and kept under ultraviolet radiation. The results show negligible decomposition of dye. 250 mL of methylene blue dye and indigo carmine dye were separately taken in the circular photoreactor and 60 mg of photocatalyst was added and kept in the ultraviolet radiation and the samples were drawn at a certain interval and the decomposition was observed. At 105 min, the methylene blue shows the maximum decomposition of dye 97% and indigo carmine shows 99% decolourisation of dye at 45 min. This experiment shows that when the time increases, the decolourisation also increases. Hence, NaFeS2 was considered to be a good photocatalytic material.
TiO2 was the most commonly used photocatalyst for the degradation of organic pollutants (Gusain et al. 2019). As per (Sood et al. 2015) work, titanium oxide quantum dots (TiO2 QD) were prepared by solgel process. The photocatalytic activity was done in the ultraviolet chamber using the batch reactor. To maintain the temperature of 25–30 °C, water circulation was given externally. The quantum dots and 25 mg/L of indigo carmine were taken to test the removal capacity. In the presence of catalyst, the removal study was found to be 93% in 120 min. This experiment concludes that TiO2 quantum dots were used as the photocatalytic material. Metal and metal oxides are used for the removal of the dye and organic pollutant. Copper oxide nanoparticles (Cu2O NPs) are used to remove the methylene blue dye from the aqueous solution. The raw materials used for the synthesis of Cu2O nanoparticles are Cu2+ and Terminalia arjuna bark extract. 100 g of bark was taken and washed with 100 mL of double-distilled water; the bark pieces were added, and the condenser was connected. The whole set-up was placed in the microwave irradiation for 7 min. From the stock solution, 10 mL was taken and 50 mL of Cu(NO3) was added and kept in the microwave irradiation. After certain period, the reaction between them takes place and Cu2O NPs were synthesised. 20 mg of Cu2O in 200 mL of methylene blue dye solution was stirred continuously. Readings were noted over certain period of time under ultraviolet–visible spectrophotometry (Kangralkar et al. 2019).
As per (Zhang et al. 2015) work, TiO2/MoS2 was fabricated on zeolite using the ultrasonic hydrothermal process. Titanium tetrachloride (TiCl4) was used as titanium source, molybdenum sulphide (MoS2) as sensitiser. The photocatalytic activity of TiO2/MoS2@zeolite was tested using methyl orange as the toxic pollutant. The removal capacity was compared with Degussa P25. It was used as the referred photocatalyst to evaluate the photocatalytic activity. TiO2 is an efficient photocatalytic material for the removal process, and MoS2 acts as a semiconductor because of its stability towards photocorrosion. 4 mL of TiCl4 and MoS2 powder were added into the beaker using ultrasound process, and homogenised solution was obtained. Glycerol was added, and the solution was subjected to continuous mixing; finally, zeolite was added. The whole solution was transferred into the autoclave, and hydrothermal process was done. After the process, the photocatalyst was obtained. To check the activity of the photocatalyst, 20 mg/L of methyl orange and 125 mg of photocatalyst were added into 250 mL of organic solution. The solution was stirred continuously for 30 min prior to the reaction to attain the equilibrium. The experiment was carried out in a reactor under XG500 xenon long arc lamp at acidic pH. At every 10-min interval, the samples were withdrawn from the reactor and analysed by spectrophotometer at absorbance of 464 nm. The concentration of photocatalyst varies from 0.25 to 0.80 g/L. The removal is high in acidic pH as pH goes into basic the activity decreases. The results of photocatalyst were compared with pure zeolite, Degussa P25, TiO2@zeolite, and the removal was 1.5%, 55%, 77%, respectively. This result shows that TiO2/MoS2@zeolite has excellent activity over removal of the methyl orange dye. The Sm@POA–TP is an efficient and reusable catalyst (Manea et al. 2019). The removal of methylene blue and malachite green dye was studied using the Sm@POA–TP catalyst. The prepared POA was added to the solution mixed constantly and kept in the room temperature for 24 h. POA–TP mixture was filtered, washed with distilled water and dried in an oven to obtain the product. 0.01 M Sm(III) was doped on POA–TP at room temperature and stirred constantly for 2 h using a magnetic stirrer. Then the solution was washed with distilled water and dried to obtain the final product. Sm@POA–TP and 200 mg/100 mL of methylene blue, malachite green dyes were added into the reactor container, and 500 W light source was given. Then the reaction proceeds, and aliquots of samples were collected and analysed in ultraviolet–visible spectrophotoscopy. The removal was about 94% and 90% for methylene blue and malachite green dyes, respectively, after 4 h of light irradiation.
Persistent organic pollutants
Organic pollutants are originating from petrochemical plants, urban sewages, pharmaceutical industries and agro-industries activities. Petrochemical plants mainly release atomic hydrocarbon, detergents, antibiotics, phenols and its derivatives. These organic pollutants are released in aquaculture water, drinking water, rivers, soils and seas (Shahidi et al. 2015). Organic pollutants should be treated, and hazardous chemicals are removed before discharging the wastes from the industries.
Pesticides
Pesticide is one of the most common and hazardous organic pollutants used in agricultural lands. Pesticides are made up of organic and non-organic (chemicals) compounds which are used to destroy the pests in the land and protect the crops so that the farmers get higher yield. But due to the excessive use of the chemical pesticides, the toxic compound remains active in the farms and also in the crops which causes dreadful illness to the mankind. Many methods are in practices to degrade the toxicity of pesticides in the land such as nano-based catalyst, nanofiltration and nanocomposites (Khan and Pathak 2020).
Carbamate pesticides are widely used in agriculture fields to control pests. TiO2 is used as the photocatalyst which helps in the degradation of pesticides from the lands. From the work of Kanan et al. (2019), TiO2 has a unique structure in which the titanium ions have an active site that degrades the organic pollutants. At a specific optimum condition, the TiO2 gives the maximum degradation of pesticides. TiO2 shows 20% increased degradation activity along with the ultraviolet irradiation activity. Also when catalyst (H2O2) was added to the TiO2/UV, the degradation of carbamyl was recorded as 79% without catalyst the degradation was 41%. This shows that the TiO2 has maximum degradation at specific conditions such as catalyst, temperature, pH and ultraviolet irradiation. Monocrotophos and chlorpyrifos are widely used organo phosphorus pesticide. As per (Amalraj and Pius 2015) work, TiO2 nano-photocatalyst was synthesised using the solgel process. The photocatalyst and pesticides were mixed and placed in a glass jacket and immersed in the batch reactor. The variation of monocrotophos and chlorpyrifos concentration was determined using the ultraviolet–visible spectrophotometer. O2 and H2O are reacting on the TiO2 surface and thus forms an HO* radical, which has the ability to degrade the monocrotophos and chlorpyrifos. As per (Ayodhya and Veerabhadram 2019) work, ZnS nanoparticles are synthesised using a Schiff base which acts as a capping agent. Under ultraviolet irradiation, the chlorpyrifos degradation was evaluated using the Schiff base ZnS nanoparticles. The photocatalyst and the pollutant chlorpyrifos were mixed and the reaction carried out in the photoreactor. The mixture should attain the adsorption equilibrium, for that continuous mixing was done for 10 min. Then the set-up was kept in the ultraviolet light irradiation. The degradation of the chlorpyrifos was analysed, and the comparative study was done between the normal ZnS and Schiff base ZnS nanoparticles. Under ZnS, the degraded recorded as 56.34% in 60 min, whereas in Schiff base ZnS nanoparticles the degradation was 85.29%. The above results show that Schiff base capped ZnS NPs are used as a photocatalytic degradation material. Degradation of dicofol was experimented by using nanocomposite. The photocatalyst and the organic pollutant were combined and treated under ultraviolet light. Without photocatalyst, the degradation of pollutant was less. The nanocomposite catalytic activity remains active after 5 cycle of usage (Ahamad et al. 2019).
O,O-dimethyl-S-methyl carbamoyl methyl thiophosphate commonly known as omethoate is a type of pesticides majorly used in developing countries. Due to its high toxic content, biological and traditional methods are not used to degrade this compound. According to Mohamed et al. (2020) work, nanocomposite was prepared using silica fume-based MCM-41, cobalt oxide and pomegranate leaves extract. Pomegranate leaves extract acts as a reducing agent. 0.51 g of CTAB and 16.34 mL of NH3OH were dissolved in 25 mL of distilled water and stirred over a period of time. Further 0.75 g of silica fumes was added to the solution and mixed well for 30 min at 1000 rpm. After that, the solution was kept in the autoclave and heated at 100 °C for 24 h. After the filtration process, the MCM-41 was prepared. The pomegranate leaves were powdered, and 5 g of powder was added to the distilled water and boiled for 3 min and filtered to obtain the pomegranate leaves extract. 2 g of MCM-41 was added to the 50 mL of distilled water and stirred for 30 min, then 2.5 g of Co(NO3)2·H2O was added slowly, and 50 mL of pomegranate leaves extract was also added. The solution was stirred continuously for 12 h and filtered to obtain the nanocomposite. The experiment was carried out in a glass chamber with a metal halide lamp for light source. The green nanocomposite and omethoate were added into the reactor and kept in dark for 30 min to attain the equilibrium. After the reaction process, samples were collected and analysed by high-pressure liquid chromatography (HPLC). At different catalyst dosage such as 0.1, 0.15, 0.2 and 0.25 g at constant 100 mg/L of omethoate, complete degradation occurs at 100, 70, 60 and 50 min. Likewise, for different concentrations of omethoate from 50, 100, 150, 20, 250 mg/L at 0.25 nanocomposite complete degradation occurs at time of 30, 50, 80, 100 and 120 min. From the results, it clearly shows Co3O4/SF–MCM-41 has excellent photocatalytic activity. Parathion pesticide was widely used in the agricultural lands. TNP-Pd-Fe3O4/GO and used for the degradation study for the parathion pesticide present in the waste water (Saljooqi et al. 2020). Pd (Palladium) nanoparticles were used to stabilise TiO2 nanoplates. 100 mg of TNP-Pd nanosheet was dissolved in 20 mL ethanol, and 50 mg of Fe3O4 was dispersed in 50 mL of ethanol. Then one mixture was added into the other slowly and stirred for 6 h at 40 °C. The experiment was performed under ultraviolet light, and samples were collected and analysed under ultraviolet–visible spectroscopy at absorbance of 260 nm. The photoactivity of the difference nanoparticles was investigated, and titanium nanoplate and TNP-Pd degrade within 80 min and 60 min, respectively, whereas the TNP–Pd–Fe3O4 nanosheets degrade the pesticide in higher speed and takes lower time. The degradation efficiency was recorded as 98.5%, and the products obtained were CO2, SO42−, PO43−, H2O which were harmless for the environment.
Herbicides
Pesticides and herbicides are mainly used in the agricultural land to control the pest attack which affects the yield of the crops. Higher usage of these chemicals over a prolonged period of time affects the soil fertility and the water resources. Among all herbicide 2, 4-dichlorophenoxyacetic is more toxic and carcinogenic. The degradation of this compound is difficult to remove because of its stability and less water solubility nature. The best method for the removal of herbicide pollutants is the photocatalytic degradation process (Sobahi 2017). Using Pt/TiO2 nanoparticles, the 2,4-D (2,4-dichlorophenoxyacetic acid) and 2,4-DP ((2,4-dichlorophenoxy)propionic acid) herbicides were degraded. Using the solgel method, TiO2 and Pt were synthesised. Cylindrical quartz glass of 10:20 height and diameter of photoreactor was used for the degradation process. After the process, the degradation was analysed using ultraviolet–visible spectroscopy. The degradation of pollutants is high in platinum-loaded titanium oxide than the free titanium oxide (Abdennouri et al. 2015).
High dose usage of herbicides leads to the contamination of the water bodies and soils. It can be effectively degraded using photocatalytic activity. As per (Zahedi et al. 2015) work, N,S codoped TiO2 thin films were used for the degradation of paraquat herbicide. Initially, TiO2 is prepared using the solgel process, and from TiO2 the thin films of TiO2 were prepared by using glass beads as the base. The surface of the glass beads should be free from organic and non-organic material, for that the beads were washed in deionised water and dried. The glass beads are then soaked in the TiO2 solution for 10 min and air-dried to obtain the immobilised TiO2. The degradation was performed in the photoreactor. The beads were arranged in the bottom of the reactor, and through an external valve the pollutant was added and samples were drawn from the reactor and analysed. The results show that under the sunlight degradation was 54.84%; on other hand, under ultraviolet the degradation of herbicides was observed as 74.1%.
Herbicides are categorised under pesticide pollutants. It also contaminates the water bodies. Diquat is a type of herbicide marketed as dibromide salt. In this experiment (Shibin et al. 2015), The ZnO acts as the photocatalyst and the reactor vessel consists of 50 mg/L of diquat solution, 0.6 mg/L of ZnO and external water supply was given to maintain the temperature. The set-up was kept in the solar light. During this process, OH* radicals are formed on the surface of the ZnO and it is tested by photoluminescence. The photocatalytic activity of ZnO degrades 58% of diquat pollutant in 5 h. Hence, ZnO is used as the photocatalytic agent. S-triazine is degraded using TiO2 suspension as a photocatalyst. Herbicide is used as an additive in paints to reduce the algae growth. This experiment was carried out in a stirred tank reactor. 10 mg/L of S-triazine herbicide and 100 mg/L of TiO2 into the reactor and agitated continuously and then kept in dark for 30 min before placing it in the sunlight. At every 10-min interval, samples were taken and TiO2 particles were removed using nanofiltration and samples were dried. The sample was analysed using gas chromatography. The results show that TiO2 perform the degradation activity effectively under sunlight (Konstantinou et al. 2001).
To increase the crop yield and inhibit the insect pest, herbicides are predominantly used (Mkhalid 2016). Using hydrothermal process, tungsten trioxide was synthesised and palladium (Pd) metal was decorated on the surface by photo-assisted process. The photocatalytic activity of the catalyst was checked by degrading (2,4-D) 2,4-dichlorophenoxyacetic acid under ultraviolet irradiation. Degradation capacity of both tungsten trioxide and Pd–WO3 was separately dispersed in 200 mL of 2,-D solution and subjected to uniform stirring before the photocatalytic activity. After certain time intervals, samples were taken and analysed using HPLC. The degradation percentage of Pd after 90 min along with tungsten trioxide for 0.0, 0.05, 0.10, 0.15 wt% was 73%, 79%, 85% and 100%. Reusability efficiency was checked and shows constant degradation activity for 5 cycles. Glyphosate (N-(phosphonomethyl) glycine) was an active organo phosphorus compound; due to its strong soil binding capacity and high resistant to the molecules, degradation by biological process was difficult. As per Cao et al. (2019) work, phosphonomethyl glycine was degraded using magnetic BiOBr/Fe3O4 nanocomposite as the catalyst. The catalyst was synthesised using the solvothermal method. A 500-W xenon lamp was fitted in the centre of the circulating plate and water circulated around the vessel. 0.08 g of catalyst was added to 20 mL of phosphonomethyl glycine. 8 tubes are fitted around the lamp. Air flow in the form of bubbles was sent into the tubes, and continuous stirring is done during the reaction and also before the reaction for homogenous mixture. After the photocatalytic activity, the magnetic catalyst was separated using a magnet. The samples were withdrawn and analysed under ion chromatography. The results show that 9% degradation for BiOBr/Fe3O4 and it was compared with pure BiOBr and Fe3O4 and the results were 85% and 5%, respectively. From the study, it was concluded that magnetic BiOBr/Fe3O4 has higher degradation capacity and it can be used as the photocatalyst. Up to 5 repeated cycles of degradation process, the photocatalyst has an average of 90% degradation; this shows it has reusable property.
Phenols
Phenol and phenolic compounds are considered to be major organic pollutant in the water bodies and cause ill effects in the aquatic system. Phenol is the most abundant organic pollutant in wastewater. Many methods are used for the removal of toxic phenol from the water environment. Photocatalytic degradation is one of the successful methods. Semiconductor is usually used as a photocatalyst (Dewidar et al. 2018).
The phenolic compounds are mainly released from petroleum and pharmaceutical industries, and they remain toxic for a longer period. In this (Shet and Vidya 2016) study, the phenol was degraded by the fluidised bed reactor using immobilised nanoparticles. Phenol was stored in the tank and pumped into the reactor through the peristatic pump. The reactor was packed with glass beads up to 5 cm. Above the glass beads, a thin cellulose acetate film flakes with immobilised nanoparticles are placed. The immobilised nanoparticles were synthesised from Ag and TiO2 using the one-pot synthesis method. Ag@TiO2 is a core shell structured nanoparticle. 1000 mL of 10 mg/L of phenol is distilled in water, and the set-up was kept in the open terrace and was operated in between 10 AM to 5 PM to obtain the sunlight. The phenol degradation was observed. In the absence of catalyst, the phenol removal is noted as 113%. Hence it is concluded that Ag@TiO2 can be used as the solar photo-catalytic degradation of phenol.
Solar degradation is commonly used for phenol degradation, but it is very less effective because of large band gap. In Al-Hamdi et al. (2016) study work, the photocatalytic degradation of phenol was studied by HPLC. Initially, antimony (Sb)-doped tin dioxide (SnO2) nanoparticles were synthesised using the solgel process at a low temperature and photocatalytic activity for phenol was studied under ultraviolet light and solar irradiation. Sb and SnO2 are n type dopant and n type semiconductor, respectively. By using different concentrations of Sb doped on the SnO2, the photocatalytic activity of nanoparticles is checked and phenol was used as the test contaminant. From the results obtained, the Sb–SnO2 nanoparticles degrade almost 95% phenol concentration and they can also be used in the photocatalysis field. Ag3PO4-BiOCl1−xBrx composites were synthesised using a facile two-step process. The degradation process was done using the synthesised material under sunlight irradiation. Ag3PO4 is coated on the BiOCl1−xBrx. The composite was placed under solar irradiation, and the degradation activity was carried out. A 300-W Xe lamp was the light source. In phenol solution, the photocatalyst was added and the suspension was irradiated and the results were obtained. Only Ag3PO4 material under the solar light showed 7.3% degradation in 75 min. At 75 min of irradiation, BiOCl0.75Br0.25 showed 72.4% degradation and the composite of ratio Ag3PO4-BiOCl0.75Br0.25 (1:5) degraded almost 97.9% of phenol as per (Qi et al. 2018) work. From the work, it is concluded that Ag3PO4-BiOCl0.75Br0.25 has the photocatalytic activity to degrade the phenol. In seawater, the degradation of phenol was obtained using carbon-modified titanium dioxide (CM-n-TiO2) nanoparticles under ultraviolet light and solar light. In Shaban et al. (2013) work, initially the unmodified titanium oxide and carbon-modified titanium oxide nanoparticles were synthesised using the solgel method. Seawater sample was taken and initial phenol concentrations were noted. The nanoparticles were added to the sample and the photocatalytic experiment was performed over a period of time and the phenol degradation was observed. In regular unmodified n-TiO2, the degradation of phenol was 42.26% in 240 min, whereas in modified CM-n-TiO2 under both ultraviolet and solar light it shows effective degradation. Complete degradation occurs in ultraviolet light in 180 min. This shows that the carbon-modified titanium oxide nanoparticle has efficient degradation of phenol and degrade at an optimum pH assortment of 3.0.
Using ultrathin magnesium oxide-coated Ag/TiO2 (Silver/Titanium oxide) nanoparticles, the degradation of phenol experiment was carried out (Scott et al. 2018). TiO2 nanorods were synthesised by using hydrothermal process. Further, Ag/TiO2 nanoparticles were prepared by coating Ag nanoparticles on TiO2 nanorods and then a thin layer of magnesium oxide was coated on Ag/TiO2 using atomic layer deposition process. To inspect the activity of photocatalyst, 10 mg of photocatalyst was added to the 50 mL solution of 15 mg/L of phenol and kept in the ultraviolet irradiation. After 30 min, the sample was collected and the catalyst was filtered. By increasing the layer of magnesium oxide on Ag/TiO2, the light absorbance was increased that enhances the photocatalytic activity. The efficient thickness of magnesium oxide for the degradation of the phenol was determined by the followed protocol. 0, 1, 5, 10 and 20 cycles of atomic layer deposition were tested. It is confirmed that 5 cycles of magnesium oxide coated on Ag/TiO2 were efficient. The degradation capacity has reached 95% in 120 min. After 5 cycles of atomic layer deposition, the degradation graph gradually decreases. Only Ag/TiO2 nanoparticles act as catalyst, the degradation was 87%.
In the experiment (Rani and Shanker 2018), a natural surfactant water (Aegele marmelos leaf extract) was synthesised and used along with bimetallic oxide as a photocatalyst. The bimetallic oxide used in the experiment was Ni–CuO, Cu·Cr2O4 (copper chromate) and NCrO3. Fresh A. marmelos leaves were collected, ground and dissolved in deionised water to obtain the plant extract. Equimolar amount of leaf extract was added to the 2nd metal salt solution (0.05 M, 100 mL) and dropwise the solution is added to the 1st solution (0.05 M, 100 mL) under continuous stirring for 2 h at 80 °C. Further dilute ammonium solution was added to the metal oxide mixture until the precipitation occurs. The solution is filtered, washed and dried. 5–25 mg of bimetallic nanocomposite of different doses on selected phenol solution of concentration varied from 1 × 10−4 M to 1.8 × 10−4 M at different pH (3.0, 5.0, 7.0, 9.0 and 11.0). Final sample solution has 15 mg of catalyst and 50 mg/L of phenol at neutral pH under solar irradiation. After the process, the samples were collected and examined under ultraviolet–visible spectrophotometer. Lower concentration of 1x10−4M shows the effective result. At high concentration, the phenolic compound absorbs sunlight rather than photocatalyst. The effective degradation of bimetallic oxide is in the order: 3-aminophenol > phenol > 2,4-dinitrophenol. The reusability property of catalyst was investigated; the photocatalyst was removed and then subjected to acetone and the deionised water washing and dried at 60 °C for 30 min. Slightly efficiency variation in 3-nitrophenol adsorption. After the 10th cycle, 93% Ni–CuO, 91% NiCrO and 88% CuCrO degradation was recorded. High degradation was observed in NiCuO at neutral pH.
Antibiotics
Antibiotics are manufactured in pharmaceutical industries and used in the hospitals. Unused, remaining and expired antibiotics are discharged in the lands and water. It affects the ecosystem and the fertility of the soil. Macrolide antibiotics are commonly found antibiotics in the water worldwide, due to its low water solubility nature (Babic et al. 2017). Antibiotics residues are not properly treated through wastewater treatment plants. Titanium oxide is most commonly used for the degradation of organic pollutants because of its effective photocatalytic activity and low cost (Do et al. 2019; Oliva et al. 2020).
As per Lei et al. (2020) work, antibiotics are degraded using photocatalyst. Fluoroquinolone antibiotics are degraded using inverse opal potassium-doped carbon nitride (IO K-CN). Fluoroquinolone includes levoflavin and norfloxacin. SiO2 photocatalysts is used as a template for IO K-CN preparation. K undoped (IO CN) was used as the control.
Control: 50 g antibiotic in water matrix in 20 min dark. Then it is allowed to irradiate under the xenon lamp of 300 W. After irradiation, the samples were collected and the levoflavin and norfloxacin were analysed using HPLC. Photocatalytic degradation: 50 mg photocatalyst in 50 mL antibiotic and kept in 20 min dark. Then, the procedure continues as the same as control and the samples were analysed. All IO K-CN showed better results; in particular, IO K-CN (7.5) has shown the highest degradation. In Qu et al. (2019) work, surface functionalised N,S-doped carbon quantum dot (N,S-CQD) was designed and synthesised by the hydrothermal process, where the carbon source is cysteine. The quantum dot was inserted in ZnO nanoflowers. 20 mL of organic pollutant solution was added to the photocatalytic device, and 10 mg of ZnO/N,S-CQDs sample was added to attain the adsorption equilibrium. Then, the sample was irradiated by sunlight and the sample was examined by the ultraviolet–visible spectrophotometer. Finally, the wok concluded that the organic pollutant removal was 79% after 120 min of ZnO/N,S-QCDs under ultraviolet irradiation, whereas 22.8% in ZnO and 9.3% in carbon-doped quantum dots.
Perylene diimide supramolecular photocatalyst is a 3D network structure, which has higher degradation capacity and adsorption. Firstly, the 3D network perylene diimide supra-molecular photocatalyst was prepared and the reaction for the degradation takes place in a multichannel photochemical reactor system. 25 mg of photocatalyst dissolves in 50 mL of antibiotic solution. Before exposing into the ultraviolet radiation the mixture was analysed in ultraviolet–visible spectrophotometry. The degradation capacity of 3D network perylene diimide supramolecular photocatalyst for tetracycline was found as 0.433/h. Thus, 3D network perylene diimide supramolecular photocatalyst has the degradation activity (Zhang et al. 2020). The synthesised double shelled ZnSnO3 hollow cubes acts as photocatalyst (Dong et al. 2019). It was prepared by co-precipitation method. Solution A: 0.4 g stannic chloride and 5 mL of ethanol solution. Solution B: 0.15 g sodium citrate, 0.1 g zinc chloride and 10 mL distilled water. After preparation of 2 solutions both were mixed well and 20 mL of 0.4 M NaOH solution was added, stirred for 1 h. Further, 10 mL 2 M NaOH was added to the mixture to form ZnSn(OH)6 double-shelled cubes. This catalyst not only degrades ciprofloxacin, but also degrades other pollutant such as toxic dyes. The experiment was carried out in reactor with 300 W xenon. 25 mg of photocatalyst and 50 mL of pollutant solution were mixed and poured into the reactor for the degradation reaction. At different intervals, samples were collected, filtered in centrifuge and analysed in ultraviolet–visible spectroscopy. The pollutant degradation was recorded as 85.9%, 37.5%, 96.52%, 48.3%, 34.8% for ciprofloxacin, sulphamonomethoxine, methylene blue, rhodamine B and methyl orange, respectively. Using hydrothermal method; Ag2O/Bi12GeO20 heterostructure were synthesised and acts as photocatalyst for the removal of toxic contaminants (Ruan et al. 2018). The degradation results were compared with pure Bi12GeO20 material to check the efficiency of the photocatalyst. To obtain the Bi12GeO20, the suspension was centrifuged and dried. Followed by heterostructure preparation, Bi12GeO20, distilled water and 0.6 g NaOH solution were added and stirred for 1 h; further, 0.0013 mol AgNO3 was added under dark condition and stirred constantly for 12 h to obtain the heterostructure product. 50 mg of photocatalyst was added with 100 mL of tetracycline, ciprofloxacin and levofloxacin solution and sonicated for 15 min. To attain the equilibrium of the solution, it was kept in the dark for 30 min. After the reaction, samples were collected and examined under ultraviolet–visible spectroscopy. The recorded results were compared with pure Bi12GeO20 and found that for tetracycline, ciprofloxacin and levofloxacin the degradation rate was 4.5, 3.5 and 4.7 faster, thus confirming that it has efficient degradation capacity. Different photocatalysts used for pollutant degradation are listed in Table 2. Figure 2 shows that heavy metals and organic pollutants degradation by photocatalysis process.
Photocatalysts and processes for fuel generation
Methanol
Methanol is an alcohol which is also used as fuel for various purposes. It has less energy density and is less expensive but also more toxic compared with ethanol. So, when it is used as fuel, there is always a mixture of other fuels with methanol. This fuel can be synthesised with carbon dioxide, and hydrogen and bio methanol can be produced by gasification of organic substrates. It is used in cooking, racing cars and combustion engines in many countries. For a higher yield in photocatalytic reactions, the factors that can influence are higher surface area of catalyst, high light absorption, prolonged presence of catalyst and selectivity. Amorphous FeOOH coupled with m-WO3 has been used as photocatalyst for the fuel generation was prepared by KIT-6 silica in Juan et al. (2020) and Yang et al. (2020). Many parameters of the catalyst material were analysed, like crystalline structure, morphology, catalytic performances, and textural properties; most of them showed positive results. Only methanol was observed in higher amounts, and other few compounds were present in trace amounts. The conversion rate of CH4 was increasing with the input FeOOH. Also, it was found that the conversion of m-WO3 with FeOOH was 3 times greater than without it. The CH4 conversion increase was probably due to the coating of FeOOH which probably enhances photocatalysis. As there were different proportions of FeOOH used, the most preferred one, i.e. having the highest yield, was 1.98% with a selectivity of 91%. Moreover, the incident light intensity was found to be one of the factors influencing the activity of the photocatalyst. When the intensity was low, the yield was low as well, and when intensity was increased, the oxidation of methane occurred. But when the intensity is increased very high, the selectivity for methanol got reduced and carbon dioxide was increased. After this, the stability of the catalyst was analysed, and results showed that the catalyst performance was slightly reduced, while recycling run was done. In conclusion, anchoring was proven to be advantageous.
As per Kumar et al. (2019b)’s work, methanol was seen the highest product column and other by-products like formic acid were not found. Here, three catalysts have been used: CoPc–COOH, g-C3N4, and g-C3N4/CoPc–COOH which were studied, and the yield for each of them was calculated. The combined catalyst (g-C3N4/CoPc–COOH) gave the highest yield leaving behind a very far second CoPc–COOH. After this, the different proportions of g-C3N4/CoPc–COOH were tested: 5%, 10%, and 15%. The 10% was found to have higher yield due to less concentration of photosensitiser in 5% and excess concentration of 15% which led to leaching. For checking whether the yield was because of photoreduction of CO2 or not, blank experiments were conducted: Firstly, photoreduction with and without photocatalyst, and secondly, photoreduction by photocatalyst in dark. And all the results pointed to the photoreduction of CO2 using photocatalyst for methanol production. Then, isotope labelling, stability testing was also performed, and results were positive. Finally, the interaction between -COOH group and carbon nitrate atoms were proven to be the reason for better yield.
Another photocatalyst used by Liu et al. (2017), CdIn2S4 and CdInS4/mpg-C3N4 composites produced methanol as a product. The bare CdIn2S4 produced significantly lower yield than the combined one, and the increase in mpg-C3N4 (mesoporous g-C3N4) enhanced the yield too. But, after a certain amount (20 wt%) the production rate drops down. This probably caused either due to excess content of mpg-C3N4 which may have filled the active sites or due to photoinduced recombination of charges. The results indicated that CdInS4/20% mpg-C3N4 has a larger specific area than the compared CdInS4/20% bulk-C3N4 because of higher active and adsorption sites. Lastly, the composite material has shown high durability, stability, and yield than others.
In David et al. (2019) and Olowoyo et al. (2019), there are many photocatalysts with different properties and performed the conversion of carbon dioxide to methanol. As per results, the reduced graphene oxide containing materials produced higher yields and excess RGO content also can contribute to lower products because of reduced graphene oxide acts as a competitor to TiO2 in higher amounts. So, the optimisation was done and 5% of reduced graphene oxide in 5.0 RGO-TiO2 was observed to be highest. This reaction was a success probably because of reduced graphene oxide which acted as a sensitiser of TiO2 which increase light activity. On the whole, the experiments showed the different paths for the future of these materials used in the light-based phenomenon.
TiO2, activated carbon fibre–TiO2, and NiO–TiO2/activated carbon filter were used as photocatalysts for methanol production. And the results showed that bare TiO2 displayed a lesser yield, whereas others showed higher methanol production. This increased production was seen due to immobilisations on the activated carbon fibre surfaces accompanied by electronic conductivity (Sharma and Lee 2017). NiO–TiO2/activated carbon fibre has shown the highest product formation of the three. NiO–TiO2/activated carbon fibre produced best results because of increased breakage of electron–hole pairs, larger surface area which supported diffusion, and enhanced effect of light shattering. The material NiO–TiO2/activated carbon fibre was also proved to be stable and effective after 10 regenerations.
Methanol production by photocatalysis needs not be done necessarily by specific composites. A different approach to this has been performed in an experiment by Wang et al. (2016), where the pH has been considered the most crucial and pyridine catalysis has been employed. pH 5.0 was found to be optimum at a time of 6 h, whereas at pH of 4.0 and 6.0, the yield was very less because H+ amount was not enough or in excess, respectively. The mechanism observed was pyridine and CO2 combined to form PyCOOH via a series of proton and electron transfers. As a result, the pyridine catalysis yield has been noticed to have good results and may be used in future for fuel generations. Au/Ti0.82Si0.18O2, Au/Ti0.76Si0.24O2, Au/Ti0.72Si0.28O2, Au/P25 (TiO2) and Au/TiO2 were used by Yadav et al. (2018) for photocatalysis. Au/TixSi1−xO2 generated higher yields than others. And Au/Ti0.72Si0.28O2 produced the highest compared with Au/Ti0.76Si0.24O2 and Au/Ti0.82Si0.18O2, and the reason for this was small nanoparticles of Au, TiO2, and metal interaction which were proved in various results obtained from the analysis. In conclusion, the Si-doped TiO2 was evident to be reasonable for enhanced activity.
Biodiesel
Owing to universal energy crisis, biodiesel has become an alternative energy source (Roslindawati et al. 2017). For the biodiesel production, novel photocatalytic materials have been utilised in trans-esterification of substrates. Novel CaO/TiO2 (calcium oxide-titanium dioxide) catalysts was prepared by photochemical mechanism and utilised for the production of biodiesel from microalgal biomass. Biodiesel production was performed in a reactor with methanol and Chlorella vulgaris biomass powder for 1 h at a fixed pressure range. Significant compounds such as fatty acid methyl esters were observed to be present in the resultant analysis, and the biodiesel yield was increased to around 51.6% (Aghilinategh et al. 2019). Another study was explored using ZnO/SiO2 catalyst with Jatropha Curcas crude oil as substrate. Broadly, the biodiesel generation involves two primary steps: free fatty acid photo-esterification and alkali catalysed trans-esterification. In the first step, photocatalytic experiments were performed in a ultraviolet photoreactor with optimal reaction conditions. The mechanism of photocatalytic trans-esterification process is as follows: free fatty acids and methanol transfer and adsorption from the solution to the photocatalyst surface, adsorbed phase reaction such as redox reactions to form radicals, formation of fatty acid esters, desorption of the formed esters and their corresponding transfer to the liquid phase. The synthesised photocatalyst used was efficient and reusable for around 10 biodiesel production cycles. The process infers the heterogenic photocatalysis nature of biodiesel production (Corro et al. 2013). Another photocatalysts such as Cr/SiO2 and TiCl2 photocatalysts were employed for the trans-esterification process for biodiesel production. In the former catalyst, existence of chromium ion groups assists in the absorption of photons and generation of electron–hole pairs thus performing trans-esterification and photo-esterification of methanol. Extraction of lipids from Nannochloropsis was carried out using photocatalysis process. Consecutively, reactive oxygen species are produced which disrupts the cell membrane releasing lipids. The generated radicals were further used for trans-esterification of the lipids. Gas chromatography mass spectrometry (GCMS) analysis inferred the presence of benzene methanol, cyclohexane, etc. (Corro et al. 2017; Shwetharani and Balakrishna 2016). Thus the above studies confirm the efficiency of photocatalysts for biodiesel production. However, studies have to be explored for improving the efficiency of the photocatalysts for biofuel production.
Hydrogen
Hydrogen is a zero-emission fuel, which has been used in vehicles for many years. It has been produced using various methods, either from fossil fuels, by steam methane reforming or gasification or electrolysis processes, or by solar fuel cells. It is sometimes hazardous because it has low ignition and high combustion energies, so, it may leak from the container. In Sun et al. (2020a), bare Cu2O, pure CZTS (Cu2ZnSnS4), CZTS/Cu2O-1, CZTS/Cu2O-2, and CZTS/Cu2O-3 have been compared for photocatalytic hydrogen production. As per the results, bare Cu2O has a negligible amount of hydrogen yield, whereas bare CZTS generated higher production rates. The synergistic effect of CZTS and Cu2O increased the yield relatively. CZTS/Cu2O-2 had maximum hydrogen generation, which was 7.7 times greater than the CZTS result. CZTS/Cu2O-2 was tested based on its stability, and analysis disclosed that they were highly stable and efficient. Hydrogen generation can be done with the help of methanol/glycerol using the photocatalysts TiO2, Pt/TiO2, 1% CNT–Pt/TiO2 (C–TiO2/g-C3N4), 5% CNT–Pt/TiO2, 10% CNT–Pt/TiO2 and 20% CNT–Pt/TiO2 (Naffati et al. 2020). The carbon naotube-TiO2 hybrids were more effective than Pt–TiO2, because of enhanced photo-efficiency in the composites. And the highest yield was obtained by 1% CNT–Pt/TiO2 with 2327 and 2019 μmol g−1 using methanol and glycerol, respectively. However, more than 1% carbon nanotubes composites showed decreased hydrogen evolution and 20% showed the lowest yield. Thus, the study shows that when the carbon nanotube content is too high, the light penetration becomes difficult, and it is important to know the optimum amount required for higher production.
TiO2 coupled with g-C3N4 has been utilised as photocatalysts for the production of hydrogen (Han et al. 2019). The amount of hydrogen evolution is highest for C-Ti/CN-10, where it clearly indicates that more than bare C–TiO2. The photocatalytic activity of C–TiO2 and g-C3N4 was 24 and 8 times lower than that of C–TiO2/g-C3N4 composites. In Nagajyothi et al. (2020)’s work, the ZnFe2O4 and MoS2 were two materials that were combined to form an effective catalyst. And the findings showed that 2-ZFO/MS/Pt-10 (ZnFeO4/MoS2) had the highest yield, and the next after which was 2-ZFO/MS/Pt-15 followed by 2-ZFO/MS/Pt-5. The hybrid’s performance was justified by the following reasons, large surface area, quicker electron transfers, co-catalyst interactions with water, redox activity of Zn and Fe ions, and separation potentials of the combinations used. In this study also, it is exhibited that the hybrids or composites have more efficiency than the pure and they enhance the stability of the material used for hydrogen generation.
Janus nanofibre heterojunction photocatalyst (JNHP), T-NP, B-NP, M-NP (TiO2/C, Bi2WO6/C) were analysed in the experiment by Sun et al. (2020b). JNHP-2 was observed to have the highest yield of hydrogen, and M-NP was lower which is described by the fact that B-NP and T-NP are not completely fused. Consecutive rounds of photocatalysis were carried to check the quality of JNHP-2, and the results showed that the photocatalyst had good stability, flexibility, and other properties. In a wavelength of 320 ≤ λ ≤ 780 nm, JNHP produced more yield than in 420 ≤ λ ≤ 780 nm that is 16.32 mmol h−1 g−1. Furthermore, there was no usage of metals as cocatalyst in this process. 1Pt–TiO2-2 and TiO2-2–1Pt have been compared with TiO2 in Chung et al. (2019) and the results showed that the combinations used produced good outputs, but it cannot be clearly explained which of the combinations is more preferred. Also, when NaOH was used, the investigation of the procedure exposed that the addition of the base decreased the photocatalytic activity, which moreover led to the conclusion that it is better to include washing step for higher hydrogen yield. In another study (Gil et al. 2020), ZnS–ZnO/ZnAl-LDH composites were used in different proportions, i.e. ZA-S1, ZA-S2, ZA-S3, and ZA-S4. Sulphur ions and ZA material were proven to be responsible for a higher hydrogen yield rate. But the excess sulphur presence lowered the yield as well. Among the hybrids, ZA-S3 produced the highest amount of hydrogen, followed by ZA-S4, ZA-S2, and ZA-S1. Only ZA did not produce any hydrogen because of the large bandgap of ZnAl-LDH.
Sm-doped ZnO/g-C3N4 composites have been used by Rakibuddin and Kim (2020) in various combinations like SAZOC-5, SAZOC-10 and SAZOC-15. After the analysis, SAZOC 10 was observed having the largest hydrogen evolution then SAZOC 15, SAZOC 5, g-C3N4, and Sm-ZnO. While stability testing, there was no decrease in the hydrogen production rate until 8 h. After 8 h, due to leaching, there was a small reduction in hydrogen reduction. Overall, the material SAZOC10 had good stability and photocatalytic properties. In Shahzad et al. (2019b), WO3, WO3/4% fullerene, WO3–/0.5% fullerene, Ni3B/Ni (OH)2 and WO3/2% fullerene Ni3B/Ni (OH)2 were represented by S1, S2, S3, S4, S5 and S6, respectively. And the highest evolution of H2 was seen in S5 followed by S6 than S4, S3, S2 and S1. After stability testing, the results collected showed that S5 was highly efficient and reusable and doping indeed helps in increasing the yield of hydrogen and separation characteristics. M–M (mechanical mixing) Er3+: Y3Al5O12@Nb2O5/In2O3, C–D (coating-demolding) Er3+: Y3Al5O12@ Nb2O5/In2O3 and C-D Er3+: Y3Al5O12@ Nb2O5/Pt/In2O3 were prepared for Z scheme photocatalysis (Xing et al. 2020). The two C–D schemes had a higher production rate than the M–M scheme. The differences in the scheme were due to Pt conducted between Nb05 and In2O3 and makes electron’s faster transfer to valence band. Pure TiO2 NPs and Au/TiO2 composites were compared in a recent study (Wang et al. 2020). The different composites used were 0.1 g/L Au/TiO2, 0.5 g/L Au/TiO2, 1 g/L Au/TiO2. The various yields produced were examined and the results were 1 g/L Au/TiO2 > 0.5 g/L Au/TiO2 > 0.1 g/L Au/TiO2 > pure TiO2. On the whole, the noble metal material produced 1 g/L Au/TiO2 exhibited the highest yield. Cl-Ta2O5-x microspheres were taken by Yu et al. (2020) for performing photocatalytic hydrogen generation. The microspheres arrest the light, inside them and then generate hydrogen. Among the microspheres used, Cl-Ta2O5-x-200 shows significantly higher stability. The content of hydrogen evolutions tended to increase when the number of microspheres was increased from the methanol solution. Finally, the other analysis results were obtained and the material was proved to be stable photocatalyst. Photocatalytic hydrogen generation by MoO3@MoS2/TiO2 was performed by Zhang et al. (2019c). The same composites were used at different temperature using M-10T i.e. M-310T (at 310 °C), M-320T (at 320 °C), M-330T (at 330 °C), M-340T (at 340 °C), M-350T (at 350 °C), and M-360T (at 360 º C) along with 1.3 montmorillonite and TiO2 for comparison. The quenching temperature was decreased which further resulted in the increase in yield from 2234 to 4691 μmol h−1 g−1. Hydrogen yield of distinct photocatalysts used for hydrogen production is shown in Table 3. In conclusion, the quenching method was established to be advantageous and it also increases sites of adsorption and efficiency. Biofuel production by the photocatalysts is shown in Fig. 3.
Limitations
Even though photocatalysis has many advantages, there are an equal number of challenges which makes the current photocatalysis as a less usable option. When it comes to materials used in photocatalysis, the material must be suitable for photocatalysis in all possible ways. But there are only limited ones which can be used because many lack any one main factor. For example, semiconductors with sulphides, oxides, or nitrides can be used for photocatalysis, but some have a small range for absorption and others are not stable in the aqueous medium (Mishra and Chun 2015). Metal oxides have been used as photocatalyst widely too, but they also have some disadvantages like less adsorption, lower recovery, less reusability and higher recombination rates (Mohamed et al. 2020). TiO2-based elements have been widely used for photocatalysis, and they have many advantages. However, they show poor performance when used alone, and they also possess comparatively less oxygen production, fast recombination rate, and poor charge transportation. Another problem is that the ultraviolet with high energy band entering the earth is already less and TiO2 requires very high energy to get activated. Hence, the productivity of TiO2 is reduced (Adekoya et al. 2017). It is also said to have lower quantum yield, less adsorption potential, and surface area (Lum et al. 2019). Similarly, ZnO also has lower adsorption potential and is non-porous. ZnO is very unstable in both alkaline and acidic conditions and gets accumulated to bulk easily.
When there is the use of microbes while fuel generation, the challenges increase because of many reasons. One of them is by-products; this can be a major problem when we want to extract particular gas, e.g. hydrogen, and the extra product, e.g. carbon dioxide. This can make the process tedious and difficult. Also, the residues produced may influence product production as microbial pathways can be influenced by various factors. For these types of problems, the need for newer and better reactors and engineered microbes are required. Water-splitting processes have been used along with photocatalysis to extract hydrogen. Alsayegh et al. (2018) have explained the challenges that are faced while this process briefly. When hydrogen and oxygen are separated physically using a reactor, there is a consequence of explosion along with the recovery process which is costly and tedious.
Although the nano-photocatalysts are proven to be highly efficient, some challenges limit their usage too, Chen et al. (2019) have highlighted the same. Inorganic nano-photocatalysts have lower charge transport and organic possess weak interactions. Moreover, the heterostructures should be studied in-depth and their function in the catalysis should also be identified for better results. After the quantitative and qualitative prediction of the material, we can be able to use this for pollutant removals or fuel generation in industrial scales. Other problems with nanoparticles (Mamba et al. 2019) are the accumulation of photocatalysts, low recovery rates and metal leaching. Even though there have been many solutions that are emerging, the requirement of metal-free or low metal catalysts that are less hazardous is always present. When we take an industrial perspective into account, the cost, efficiency and life of the material can majorly affect the product. The price always matters when quantity increases, so a cheap catalyst is the primary aim, but many photocatalysts are either doped or mixed with elements like gold (Yadav et al. 2018) and platinum (Chung et al. 2019) which not only increases the efficiency but also increases the cost. And the combined materials used become harder to study and also adds money to the process. Additionally, the photocatalyst is used in large scales for fuel generation, therefore are supposed to have higher life. But, most of the photocatalysts are only efficient for 2–3 cycles, after which the fuel production reduces. Hence, these limitations have to be overcome in further explications.
Conclusion
Photocatalytic systems for the remediation of environmental pollutants have been exemplified as an efficient technique from various research studies. Currently, novel photocatalysts have been developed and used for the pollutant removal, but the cost of the material synthesis has to be minimised by further studies. The wide range of usage in removal of persistent organic pollutants such as antibiotics, pesticides and herbicides was noted with novel photocatalysts developed. Though energy generation using photocatalytic processes was found to be effective, production of by-products along with the main product limits their efficiency. The development of biofuel has emerged in recent years making microbial species as essential substrate along with photocatalyst for biofuel production. Microbial pathways influence the photocatalytic mechanism which has to be explored in future researches. Most of the photocatalysts are developed from metals which may further lead to polluted environment. Hence the alternative environment friendly photocatalytic materials have to be developed to mitigate the ecological effects. Also future explications in photocatalytic removal of environmental pollutants should focus on the optimising reaction parameters using mathematical modelling.
Abbreviations
- 3D Fe2O3 :
-
Three-dimensional ferric oxide
- As(V):
-
Arsenate
- Cr(VI):
-
Hexavalent chromium
- Na2HAsO4·7H2O:
-
Disodium hydrogen arsenate heptahydrate
- K2Cr2O7 :
-
Potassium dichromate
- PAEC:
-
Plasma atomic emission spectroscopy
- Fe2O3 :
-
Ferric oxide
- TiO2 :
-
Titanium dioxide
- ZnO:
-
Zinc oxide
- CuCo2S4 :
-
Copper cobalt sulphide
- MoSe2/BiVo4 :
-
Molybdenum diselenide/bismuth vanadate
- Bi(NO3)3.H2O:
-
Bismuth(III) nitrate monohydrate
- NH4VO3 :
-
Ammonium metavanadate
- CO2 :
-
Carbon dioxide
- Cu2+ :
-
Copper(II) ion
- Zn2+ :
-
Zinc(II) ion
- Ni2+ :
-
Nickel(II) ion
- Pb2+ :
-
Lead(II) ion
- Cu(NO3)·3H2O:
-
Copper(II) nitrate trihydrate
- Zn(NO3)2·6H2O:
-
Zinc nitrate hexahydrate
- Ni(NO3)2·6H2O:
-
Nickel(II) nitrate hexahydrate
- Pb(NO3)2 :
-
Lead(II) nitrate
- pH:
-
Potential of hydrogen
- HNO3 :
-
Nitric acid
- Rh–Sb TiO2 :
-
Rhodium and antimony co-doped titanium dioxide
- RS-TONR/TNT:
-
Rhodium/antimony co-doped titanium oxide nanorod and titanate nanotube
- Cr(III):
-
Trivalent chromium
- Bi(NO3)3 :
-
Bismuth(III) nitrate
- Na2WO4 :
-
Sodium tungstate
- AgIn5S8 :
-
Silver indium sulphide
- Bi2WO6 :
-
Bismuth tungstate
- FeS2 :
-
Iron disulphide
- BiOCl–Ag–AgBr:
-
Bismuth oxychloride silver bromide
- BiOCl:
-
Bismuth oxychloride
- NaFeS2 :
-
Sodium iron disulphide
- NaNO3 :
-
Sodium nitrate
- TiO2 QD:
-
Titanium oxide quantum dots
- Cu2O NPs:
-
Copper oxide nanoparticles
- Cu2O:
-
Cuprous oxide
- Cu(NO3):
-
Copper(I) nitrate
- TiO2/MoS2 :
-
Titanium oxide molybdenum sulphide
- TiCl4 :
-
Titanium tetrachloride
- MoS2 :
-
Molybdenum sulphide
- Sm@POA–TP:
-
Samarium codoped poly o-anisidine titanium phosphate
- POA–TP:
-
Poly o-anisidine titanium phosphate
- H2O2 :
-
Hydrogen peroxide
- ZnS:
-
Zinc sulphide
- CTAB:
-
Cetyl trimethyl ammonium bromide
- NH3OH:
-
Ammonium hydroxide
- MCM-41:
-
Mobil composition of matter 41
- Co(NO3)2·H2O:
-
Cobaltous nitrate hexahydrate
- HPLC:
-
High pressure liquid chromatography
- Co3O4/SF–MCM-41:
-
Cobalt tetraoxide silica fume Mobile composition of matter 41
- TNP–Pd–Fe3O4/GO:
-
Titanium nanoplate palladium-doped ferric oxide graphene oxide
- Fe3O4 :
-
Ferrosoferric oxide
- SO4 2− :
-
Sulphate
- PO4 3− :
-
Phosphate
- Pt/TiO2 :
-
Platinum-doped titanium dioxide
- 2,4 DP:
-
2,4-Dichlorophenoxyacetic acid
- Pd–WO3 :
-
Palladium tungsten oxide
- BiOBr/Fe3O4 :
-
Bismuth oxybromide-doped ferric oxide
- Ag@TiO2 :
-
Silver titanium dioxide
- SnO2 :
-
Tin dioxide
- Sb–SnO2 :
-
Antimony-doped tin dioxide
- Ag3PO4-BiOCl1−xBrx :
-
Trisilver phosphate-doped bismuth oxychloride bromide
- CM-n-TiO2 :
-
Carbon-modified titanium dioxide
- Ag/TiO2 :
-
Silver/Titanium oxide
- Ni–CuO:
-
Nickel-doped copper oxide
- Cu·Cr2O4 :
-
Copper chromite
- NiCuO:
-
Nickel-doped copper oxide
- NiCrO:
-
Nickel-doped chromium oxide
- CuCrO:
-
Copper-doped chromium oxide
- IO K-CN:
-
Hypoiodite potassium-doped carbon nitride
- IO CN:
-
Hypoiodite-doped carbon nitride
- N,S-CQD:
-
N,S-doped carbon quantum dot
- ZnO/N,S-CQDs:
-
Zinc oxide N,S-doped carbon quantum dot
- ZnSnO3 :
-
Zinc stannate
- NaOH:
-
Sodium hydroxide
- ZnSn(OH)6 :
-
Tin zinc hydroxide
- Ag2O/Bi12GeO20 :
-
Silver oxide-doped bismuth germanium oxide
- AgNO3 :
-
Silver nitrate
- FeOOH:
-
Ferric hydroxide oxide
- CoPc–COOH:
-
Cobalt phthalocyanine tetracarboxylic acid
- g-C3N4 :
-
Graphitic carbon nitride
- CdIn2S4 :
-
Cadmium indium sulphide
- CdInS4/mpg-C3N4 :
-
Cadmium indium sulphide-doped mesoporous graphitic carbon nitride
- RGO:
-
Reduced graphene oxide
- NiO–TiO2 :
-
Nickel oxide-doped titanium dioxide
- PyCOOH:
-
Pyrene-1-carboxylic acid
- CaO/TiO2 :
-
Calcium oxide-titanium dioxide
- ZnO/SiO2 :
-
Zinc oxide-doped silicon dioxide
- Cr/SiO2 :
-
Chromium-doped silicon dioxide
- TiCl2 :
-
Titanium chloride
- GCMS:
-
Gas chromatography mass spectrometry
- CZTS:
-
Copper zinc tin sulphide
- CNT–Pt/TiO2 :
-
Carbon nanotube platinum-doped titanium dioxide
- ZnFe2O4 :
-
Zinc ferrite
- JNHP:
-
Janus nanofibre heterojunction photocatalyst
- ZnAl-LDH:
-
Zinc aluminium-layered double hydroxide
- Ni3B/Ni (OH)2 :
-
Nickel boride nickel hydroxide
- Y3Al5O12@Nb2O5/In2O3 :
-
Yttrium aluminium oxide-doped niobium pentoxide indium(III) oxide
- Au/TiO2 :
-
Gold-doped titanium dioxide
- Cl-Ta2O5-x:
-
Chlorine doping tantalum oxide
- MoO3@MoS2/TiO2 :
-
Molybdenum trioxide-coated molybdenum disulphide-doped titanium dioxide
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Saravanan, A., Kumar, P.S., Vo, DV.N. et al. Photocatalysis for removal of environmental pollutants and fuel production: a review. Environ Chem Lett 19, 441–463 (2021). https://doi.org/10.1007/s10311-020-01077-8
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DOI: https://doi.org/10.1007/s10311-020-01077-8