Literature DB >> 34693667

Photocatalytic Air Purification Using Functional Polymeric Carbon Nitrides.

Min Zhou1, Honghui Ou2, Shanrong Li3, Xing Qin1, Yuanxing Fang3, Shun-Cheng Lee4, Xinchen Wang3, Wingkei Ho1.   

Abstract

The techniques for the production of the environment have received attention because of the increasing air pollution, which results in a negative impact on the living environment of mankind. Over the decades, burgeoning interest in polymeric carbon nitride (PCN) based photocatalysts for heterogeneous catalysis of air pollutants has been witnessed, which is improved by harvesting visible light, layered/defective structures, functional groups, suitable/adjustable band positions, and existing Lewis basic sites. PCN-based photocatalytic air purification can reduce the negative impacts of the emission of air pollutants and convert the undesirable and harmful materials into value-added or nontoxic, or low-toxic chemicals. However, based on previous reports, the systematic summary and analysis of PCN-based photocatalysts in the catalytic elimination of air pollutants have not been reported. The research progress of functional PCN-based composite materials as photocatalysts for the removal of air pollutants is reviewed here. The working mechanisms of each enhancement modification are elucidated and discussed on structures (nanostructure, molecular structue, and composite) regarding their effects on light-absorption/utilization, reactant adsorption, intermediate/product desorption, charge kinetics, and reactive oxygen species production. Perspectives related to further challenges and directions as well as design strategies of PCN-based photocatalysts in the heterogeneous catalysis of air pollutants are also provided.
© 2021 The Authors. Advanced Science published by Wiley-VCH GmbH.

Entities:  

Keywords:  denitrification; desulfurization; photocatalytic air purification; polymeric carbon nitrides; volatile organic compound removal

Year:  2021        PMID: 34693667      PMCID: PMC8693081          DOI: 10.1002/advs.202102376

Source DB:  PubMed          Journal:  Adv Sci (Weinh)        ISSN: 2198-3844            Impact factor:   16.806


Introduction

With the increasing recognition of environmental issues, robust attention of the public has been paid to reduce air pollutants.[ , , , , ] The undesirable and harmful materials of air pollutants (e.g., nitrogen oxides (NO ), sulfur compounds, volatile organic compounds (VOC), and other species (carbon monoxide) enter the atmosphere from sources currently beyond human control.[ , , , , , , , , , , , , , , ] These man‐made air pollutants are primarily produced from counts of life and industry (e.g., transportation, fossil fuel combustion, vehicle exhaust, industrially processes, and miscellaneous).[ , , , ] The quantities effects generated from the harmful air pollutants may seriously damage the global environment, which may induce acid rain, thereby destructing the ozone layer by chlorofluorocarbons; and deteriorate the human/animal health, thereby causing respiratory problems; and increase the form of brown or hazy air or unpleasant smells.[ , , , , ] Recently, the control technologies (primarily related to the resources), including exhaust release treatment (e.g., advanced physical adsorption and catalytic particulate biofiltration), and exhaust after treatment (e.g., thermal catalysis), are used to achieve the emission reduction of air pollution.[ , , , , , ] These technologies allow us to increase the population and level of economic activity per person while decreasing the most measured air pollutants concentrations. Nevertheless, the sources of emissions control still have not dealt with the actual problem fundamentally because of the presence and production of air pollution.[ , , ] Developing an economic and environmental technology to address the fundamental problems on the air pollutants is necessary, particularly at low pollutant concentrations of part per billion (ppb) levels typically for indoor and outdoor air concentration. Therefore, recently, the fields of surface/interface chemistry regulations on the multiphase catalysis of air pollutants have advanced significantly to improve the quality of human life and economy, and scientific understanding of the effects and such pollutants is incomplete and is paid less attention to.[ , , , ] To date, numerous studies have reported that heterogeneous catalytic treatments used for atmospheric environmental issues are identified as the most efficient solution because of their high efficiency and selectivity.[ , , , , ] Among potential and green solutions, semiconductor‐based photocatalysis, which is widely used in atmospheric environment protection, has emerged with inestimable superiority because of its economic, renewable, clean, and safe properties.[ , , , , , , , ] Given the fundamental mechanism of multiphase photocatalysis removal of air pollutants (Figure  ), the process under irradiation can be simplified and divided into three steps: 1) light absorption (fs level, followed by generating the electron–hole couples), 2) reagents’ adsorption (ps–ns level, followed by separating the electron–hole couples), and 3) surface/interface redox reaction (ms–μs level, followed by desorption of the products).[ , , , , , ] In brief, factors such as the optical absorption performance of the semiconductor, the generation/separation/migration of light‐excited carriers, and the reactants adsorption and products desorption seriously affect the efficiency of the entire semiconductor photocatalytic‐based air purification.[ , , , ]
Figure 1

A) The mechanism of the semiconductor‐photocatalyzed reaction. Reproduced with permission.[ ] Copyright 2007, Royal Society of Chemistry. B) Reactive oxygen species are generated in the photoredox steps. Reproduced with permission.[ ] Copyright 2017, American Chemical Society.

A) The mechanism of the semiconductor‐photocatalyzed reaction. Reproduced with permission.[ ] Copyright 2007, Royal Society of Chemistry. B) Reactive oxygen species are generated in the photoredox steps. Reproduced with permission.[ ] Copyright 2017, American Chemical Society. In addition, the generation and utilization of reactive oxygen species (ROS) is a crucial process during the semiconductor photocatalysis‐based removal of air pollutants (Figure 1B).[ , , , , , ] In general, oxygen (O2, the second most abundant gas on the earth) as a moderate oxidant is considered as a “green” character with regard to active oxygen content (atom economy).[ , ] The excited electrons (e–) and holes (h+) will react with the O2 to generate different ROS (superoxide (O2 ⋅–), hydroxyl (⋅OH), hydrogen peroxide (H2O2), and singlet oxygen (1O2)), and the formation processes are shown in Equations (1)–(8).[ , , , , ] The formation potential and electron transfer of ROS production are also important factors that influenced the selection and efficiency of the photocatalysts Based on the above‐mentioned factors and requests for heterogeneous catalysis of air purification, a suitable and efficient photocatalyst shows great potential. Nevertheless, the most developed semiconductors exhibit a wide bandgap, resulting in low solar energy utilization efficiency.[ , , , , , ] The other photocatalysts have a high economic cost, complex synthetic process, certain toxicity, and inactivation, which remain a “bottleneck” of the photocatalysts.[ , , , , , ] Therefore, designing robust photocatalysts that are low‐cost, abundant, and facile in preparation, visible‐light‐responsive, efficient, sustainable, and stable in multiphase catalysis reaction is challenging. Recently, a metal‐lacking polymeric carbon nitride (PCN) has received interest in the research community, which can achieve the visible‐light‐driven water splitting with the assistance of sacrificial electrons donor/acceptor and co‐catalysts.[ , , , , , , ] A PCN is a linear polymer that the plane is composed of triazine and heptazine units connected by amino (–NH2) groups and the interlayers are stacked by van der Waals forces of covalent C–N bonds.[ , , , , , , ] Given the contribution of the atoms’ orbitals from the PCN, the photocatalytic redox reactions primarily occur in the carbon and nitrogen atoms.[ , , ] Based on previous literature, the PCN photocatalysts with heptazine ring structure demonstrate various advantages and potentials in the heterogeneous catalysis of air purification: 1) low synthesis cost and simple process can be easily achieved by thermally condensing the low‐cost, N‐prosperous and O‐lacking composites involving the core of C–N precursors (e.g., melamine (MA), dicyandiamide (DCDA), cyanamide (CA), urea (U), and thiourea (T)).[ , , , , ] 2) The suitable electronic band structure (2.7 eV) and band positions are satisfactory to activate the O2 into the O2 ⋅– and overcome the Gibbs free energy, which is less than zero of the catalytic reaction.[ , ] 3) The redshift of light absorption of the PCN can provide more chances to absorb photons and participate in the visible‐light‐driven heterogeneous catalysis of air purification.[ , , , ] 4) The high physicochemical/mechanical/chemical/thermal stabilities (attributed to its aromatic C–N heterocycles) of the PCNs reduce the inactivation and photo corrosion, thereby extending the life of the photocatalysts.[ , , , , ] 5) A similar layered structure with graphite for PCN provides a large reaction space, improves gas absorption/desorption, and shortens the transmission distance of photogenerated charges.[ , , , , , ] 6) The surface amino and hydroxyl groups of the PCN can serve as defects and surface engineering sites (anchoring inorganic/organic functional monomers), and the lone pair of the N atoms can delocalize the electrons to expand the π‐conjugated systems.[ , ] 7) Theoretical calculations indicate that the Lewis basic sites of PCNs can donate electrons to the adsorbed air pollutants and decrease the bond order of N–O/C–S–C/C–H, thereby facilitating the conversion of air pollutants.[ , , , ] Therefore, at present, PCN is considered as a potential and transformative photocatalyst used in reforming air pollutants. In addition, the pristine PCN photocatalysts have achieved success in heterogeneous catalysis of air purification, such as denitrification, desulfurization, and VOC removal.[ , , ] Nevertheless, due to the limited synthesis method and intrinsic polymer nature, the photocatalytic activity of pristine PCN is seriously far from the practical application because of the relatively low surface area, high exciton binding energy, sluggish charges kinetics, insufficient sunlight absorption, the low adsorption capacity of air pollutants, insufficient activation of air molecular, which greatly inhibiting its potential photocatalytic applications in air‐related revolution.[ , , ] Subsequently, considerable achievements have been emerged in advancing the efficiency based on PCN semiconductors in multiphase catalysis of air purification (Figure  ). The specific regulation strategies of the PCNs primarily focus on structure modification based on its intrinsic nature, including nanostructure modulation, electronic structure programming, and heterostructure construction.[ , , , ] The nanostructure of PCN can be easily modulated because of the van der Waals force that existed in the interlayers and surface functional groups through a series of synthetic methods (e.g., exfoliation, template, and solvothermal strategies) to push the mass transfer and charge kinetics.[ , , ] The sufficient flexibility of the structure and polymeric nature of PCN allows control by atomic and molecular doping (introducing external impurities) to regulate the electronic structure and improve the optical absorption, and ROS generation.[ , , , ] The suitable bandgap and tunable band positions of PCN can be matched with other semiconductors to construct heterojunctions, and the synergistic effects can reduce charge recombination, enhance photon absorption, and accelerate mass transfer.[ , , ] Designing the PCN‐based photocatalysts is of great importance for diversifying and spreading the application fields of air purification. However, based on previous reports, systematic reviews about air purification by using functional PCN‐based photocatalysts are still lacking.[ , , , ]
Figure 2

Systematic modifications of air purification using PCN‐based photocatalysts.

Systematic modifications of air purification using PCN‐based photocatalysts. Herein, the brief synthetic pathways and latest research approaches for advancing PCN‐based photocatalysts and the progress of the remediating air purification‐associated issues (e.g., denitrification, desulfurization, and VOC removal) are given in the review (Figure  ).[ , , , , , , , , , , , , , , , , , , , , , ] The structure regulation for optimizing optical absorption, charge kinetics, gas activation, adsorption of reactants/desorption of products are analyzed and discussed, which can be constructive and instructive for readers to deeply understand on structure‐activity relationship of the PCN‐based and other photocatalysts and be in turn helpful for exploring various photocatalysts. The current status to be changed, limits to be resolved, and long‐term directions to be developed for PCN‐based catalysts and composites are proposed to push the practical application in atmospheric environment remediation.
Figure 3

A brief timeline of the development of representative PCN‐based photocatalysts in air purification.

A brief timeline of the development of representative PCN‐based photocatalysts in air purification.

Formation of PCN Materials

Pristine PCN

The pristine PCN photocatalyst is commonly synthesized by thermally condensing that leads to a combination of polyaddition and polycondensation reactions of the low‐cost, N‐prosperous, and O‐lacking composites involving the core of C–N precursors (e.g., MA, DCDA, CA, U, and T).[ , , ]

Functional PCN

The size, dimension, morphology, crystallinity, optical/electronic characters, chemical composition, and catalysis properties of functional PCN photocatalysts can be modulated by tailoring the nanostructure, regulating the molecular structure, and constructing the composites.[ , , , , ] Herein, we review the effects of exfoliation strategy, template and template‐free method, atomic and molecular doping, and composites construction on the performance of PCN‐based photocatalysts.

Nanostructure

Exfoliation

Due to the stacking of the polymeric layers, the bulk PCN counterparts usually exhibit very low specific surface areas, reduced the carriers transfer, insufficient active sites, and decreased reactants adsorption, thus limiting the photocatalytic efficiency and application of PCN.[ ] To advance the utilization of PCN, low‐dimensional PCN with atomic or molecular size/dimension can be obtained through liquid exfoliation.[ , , ] It has been evidenced that the PCN nanosheets could be obtained with the assistance of organic solvents, acid, and base solutions. For instance, Yang et al. used isopropyl alcohol as a solvent and sonication‐assisted method to exfoliate the bulk PCN into ultrathin PCN nanosheets .(≈2 nm)[ ] In addition, the thermal‐oxidation etching route and thermal exfoliation with alkali metal salts are also extensively used to produce the low‐dimensional PCN nanomaterials. In 2012, Niu et al. directly calcinated the bulk PCN in the air to obtain the 2 nm PCN nanosheets.[ ] In a word, the exfoliation strategy successfully produces PCN nanosheets through breaking hydrogen bonds and van der Waals stacking in the bulk PCN and suppressing the nanosheets restacking by formatting the polar C–H bonds.

Template Method

With the aid of different templates (soft and hard templates), the PCN forms flexible structures and different morphologies, which are endowed with improved surface areas, active sites, and charge dynamics.[ , , , ] The PCN photocatalysts with mesoporous, porous, spherical, and tubular structures can be prepared by thermal condensing the mixture of silica templates (hard templates) and precursors contained carbon and nitrogen, etching by NH4HF2 (removing the silica templates). For instance, Zhang et al. used the SBA‐15 mesozeolite as the template and CA as the precursor to produce ordered mesoporous PCN.[ ] Sun et al. first employed core‐shell silica as the hard template to penetrate with CA, then thermal condensation to produce hollow PCN nanospheres.[ ] In addition, the PCN with desired porous structures and surface morphologies can be also produced through the greener soft templates (surfactants, amphiphilic block polymers, and ionic liquids).[ , , ] In 2010, Wang et al. used kinds of soft templates to successfully synthesize mesoporous PCN, which is endowed with high surface area and conductivity.[ ] Yan et al. used MA (as an unresponsive precursor) and Pluronic P123 (as a soft template) to achieve mesoporous PCN in 2012.[ ]

Template‐Free Method

The supramolecular method, as a common template‐free method, is extensively used to synthesize nanostructured PCN materials (flower‐like and spherical structures) without a post‐treatment procedure for removing the template.[ , , , , ] The PCN with desired structure and morphologies can be controlled by tuning the monomers ratio, solvent types, temperature, precursor styles (hydrogen‐bonding donor–acceptor pairs). The key to this supramolecular method is to use the noncovalent interactions (hydrogen bonding) to form the desired ordered structural unit. For instance, the melamine mixed with cyanuric acid or trithiocyanuric acid can be used to produce ordered hollow PCN, layered PCN, PCN nanotubes through the supramolecular preorganization of hydrogen‐bonded molecular assemblies by Jun et al. and Shalom et al.[ , ]

Molecular Structure

The molecular structure of PCN photocatalysts can be regulated by introducing external impurities to manipulate the physical and chemical characters.[ , , , , , , , ] The introduction of external impurities is mainly divided into two types, including atomic doping (anions, metal cations, and co‐doping) and molecular doping (copolymerization). For instance, Liu et al. directly thermal condensing the PCN under an H2S atmosphere to obtain sulfur doped PCN.[ ] Zhang et al. thermal polymerization the mixture of the DCDA and barbituric acid to produce the organic groups anchored PCN.[ ] However, the atomic doping strategy may also induce some disadvantages (forming recombination center for charges) because of the broken symmetry and purities in the PCN.[ , ]

Composites

The PCN with flexible structure and polymeric nature endows tunable and close interconnection with other semiconductors to construct various PCN‐based composites.[ , , , ] The PCN‐based composites can be divided into the following types: Schottky heterojunctions, type I heterojunctions, type II heterojunctions, direct/indirect Z‐scheme heterojunctions, and S‐scheme heterojunctions. For instance, Pan et al. successfully fabricated an indirect Z‐scheme Fe2O3/reduced graphene oxide (RGO)/PCN, achieving efficient overall water splitting.[ ] Xia et al. designed an S‐scheme heterojunction composed of CeO2 and PCN, which showed highly efficient inactivation of bacteria with visible light.[ ]

Application of PCN in Environmental Catalysis

PCN for Denitrification

Various types of NO, NO2, N2O, N2O3 constitute NO , and the most (95%) of the NO is NO.[ , ] The toxic NO2 can be formed through oxidizing NO in the atmosphere as shown in the following equations[ , ] NO is generally released from natural processes (e.g., volcanic activity and organic matter decomposition) and human activities (e.g., exhausts release and fossil fuel combustion).[ , , ] Respiratory diseases and even death can be triggered and resulted from breathing the air containing toxic NO .[ , , ] Recently, physical adsorption (PA), catalytic redox (CR), and photocatalysis are proposed and developed for NO elimination (denitrification).[ , , , ] Owing to the shortcomings of expensive cost and secondary environmental pollution in PA and CR, photocatalytic oxidation denitrification (PODN) as the most convenient method at ppb levels (indoor air concentration) arouses great interest, which is scientific, economical, and environmentally friendly.[ , , , ] To date, various inorganic materials are developed in multiphase catalytic elimination of air pollution driven by solar energy and achievements have been made.[ , , , ] However, the noneconomical and nonpractical properties of the inorganic materials are far from the expectations and practical applications. PCN as a visible‐light‐responsive material was firstly applied for water decomposition by Wang et al., it became a popular and state‐of‐the‐art material for photocatalysis.[ ] Interestingly, Zhu et al. firstly introduced PCN into the NO decomposition under high temperature (above 400 °C), exhibiting 15.06% of NO conversion.[ ] Theoretical calculations indicated that the adsorbed NO could accept electrons from the Lewis basic sites of PCN and the energy of the N–O bond could be decreased, thereby promoting denitrification efficiency (Figure  ). This novel discovery indicated that the PCN as a growing and potential star could be used in NO conversion, and future works should focus on stabilizing and activating the PCN for usage at the economical attraction and yield considerable denitrification performance even under mild conditions. In 2013, Dong et al. used the PCN into the visible‐light‐driven NO (ppb levels) conversion (32.1% for the optimal PCN‐240 sample after 45 min of irradiation) under ambient temperature without any sacrificial agents by adjusting the pyrolysis time of PCN materials.[ ] The enhancement of crystallinity and surface areas of PCN could be achieved simultaneously, which were favorable factors for promoting the PODN activity. Given the suitable band positions of the PCN, the photoexcited electrons exhibited a remarkable capacity to reduce O2 into O2 ⋅–.[ , , , ] The intermediate products (NO2) are mineralized and convert to NO3 – with the ROS or h+, and the possible oxidation processes of NO on PCN are shown in the following equations[ , , , , , ]
Figure 4

Theoretical calculations of NO decomposition on PCN. Reproduced with permission.[ ] Copyright 2010, Royal Society of Chemistry.

Theoretical calculations of NO decomposition on PCN. Reproduced with permission.[ ] Copyright 2010, Royal Society of Chemistry. The specific formation of the intermediates during the PODN reaction on PCN is also important for exploring the reaction mechanism and process deeply, and the formation processes are shown in the following equations[ , , ] Although the pristine PCN exhibits remarkable potential for its utilization in NO abatement driven by solar energy, the practical application of PCN in PODN fields is strongly limited because of its thick layered structures, weak intermolecular van der Waals forces, or electrostatic forces existed between each layer and carbonization of either molecular or chemical precursors during the high‐temperature polymerization.[ , , ] In addressing the aforementioned problems, considerable effort has been made on PCN‐based photocatalysts by a nanostructure design (adjusting the polymerization process, incorporating the defective sites, controlling the morphologies, and transforming the types of the semiconductor).[ , , , , ] The electronic structure regulations are used to modify the light absorption of and the redox potentials through adding cations and anions and co‐doping, or molecular doping of PCN.[ , , , , , ] The heterostructure constructions through band alignment are also designed to accelerate the kinetics of charges, and the synergistic effects of multi‐components increase the adsorption of reactants/desorption of products, mass transfer, and ROS generation, thereby promoting the PODN efficiency.[ , , ] Recent progresses of PCN‐based photocatalysts with various structure modifications, which are used in POND, are shown in Table  .
Table 1

Summary of recently reported PCN‐based photocatalysts utilized in denitrification reaction

PhotocatalystsTypesExperimental conditionsLight sourceAnalyzerMain products and NO removal ratioRefs.
PCN (precursor regulation)Nanostructure design

Reactor: 4.5 L

Cat a) .: 0.1 g

Conc. b) : 600 ppb

Time c) : 30 min

100 W THL d) (λ > 420 nm)Model 42i‐TL e)

Products: NO3

η f) (NO): 26.2% (PCNM g) ), 32.2% (PCNU h) ), 29.2% (PCNT i) ), 22.2% (PCND j) )

[ 186 ]
Defective PCNT/PCNUNanostructure design

Reactor: 4.5 L

Cat.: 0.1 g

Conc.: 600 ppb

Time: 30 min

150 W THL

(λ > 420 nm)

Model 42i‐TL

Products: NO3

η(NO): 39.4% (PCNT); 40.4% (PCNU)

[ 187 ]
PCN (precursor mass regulation)Nanostructure design

Reactor: 4.5 L

Cat.: 0.2 g

Conc.: 600 ppb

Time: 30 min

150 W THL

(λ > 420 nm)

Model 42i‐TL

Products: NO3

η(NO): 48.3%

[ 188 ]
PCN (precursor temperature and time regulation)Nanostructure design

Reactor: 4.5 L

Cat.: 0.2 g

Conc.: 600 ppb

Time: 30 min

150 W THL

(λ > 420 nm)

Model 42i‐TL

Products: NO3

η(NO): 32.7%

[ 189 ]
PCN (add water into precursors)Nanostructure design

Reactor: 4.5 L

Cat.: 0.2 g

Conc.: 600 ppb

Time: 30 min

150 W THL

(λ > 420 nm)

Model 42i‐TL

Products: NO3

η(NO): 48.0%

[ 190 ]
Porous PCN (add water into precursors, then add HCl)Nanostructure design

Reactor: 4.5 L

Cat.: 0.15 g

Conc.: 600 ppb

Time: 30 min

LED lamp (λ = 448 nm)Chemiluminescence

Products: NO3

η(NO): 71.2%

[ 123 ]
Porous PCN nanosheets (thermal exfoliation in the air at different temperatures)Nanostructure design

Reactor: 4.5 L

Cat.: 0.1 g

Conc.: 600 ppb

Time: 60 min

150 W THL

(λ > 420 nm)

Model 42i‐TL

Products: NO3

η(NO): 33.9%

[ 112 ]
Porous PCN (repeated thermal treatment with pristine PCN two times in the air)Nanostructure design

Reactor: 4.5 L

Cat.: 0.2 g

Conc.: 600 ppb

Time: 30 min

LED lamp (λ > 420 nm)Model T200 k)

Products: NO3

η(NO): 65%

[ 191 ]
PCN (repeated thermal treatment with pristine PCN in the air)Nanostructure design

Reactor: 4.5 L

Cat.: 0.2 g

Conc.: 600 ppb

Time: 30 min

LED lamp (λ > 400 nm)Model T200

Products: NO3

η(NO): 68%

[ 181 ]
Porous PCN (add water with PCN during re‐thermal treatment in the air)Nanostructure design

Reactor: 4.5 L

Cat.: 0.2 g

Conc.: 600 ppb

Time: 30 min

150 W THL

(λ > 420 nm)

Model 42i‐TL

Products: NO3

η(NO): 51.2%

[ 176 ]
Porous PCN (add water and HCl into precursors)Nanostructure design

Reactor:0.785 L

Cat.: 0.05 g

Conc.: 600 ppb

Time: 30 min

LED lamp (λ = 448 nm)Model 42i‐TL

Products: NO3

η(NO): 80%

[ 192 ]
Porous PCN (add NH4HCO3 into precursors)Nanostructure design

Reactor: 4.5 L

Cat.: 0.05 g

Conc.: 600 ppb

Time: 30 min

300 W Xe lamp (λ > 420 nm)Model 42i‐TL

Products: NO3

η(NO): 42%

[ 113 ]
Porous PCN (add (NH4)2SO4 into precursors)Nanostructure design

Reactor: 4.5 L

Cat.: 0.2 g

Conc.: 600 ppb

Time: 30 min

150 W THL

(λ > 420 nm)

Model 42i‐TL

Products: NO3

η(NO): 47.1%

[ 193 ]
Porous PCN (add glyoxal into precursors)Nanostructure design

Reactor: 0.325 L

Cat.: 0.05 g

Conc.: 15 ppm

Time: 120 min

300 W Xe lamp (λ > 420 nm)Testo 350

Products: NO3

η(NO): 66.7%

[ 194 ]
Mesoporous PCNNanostructure design

Reactor: 4.5 L

Cat.: 0.1 g

Conc.: 600 ppb

Time: 30 min

150 W THL

(λ > 420 nm)

Model 42i‐TL

Products: NO3

η(NO): 40.7%

[ 195 ]
Flower‐like PCNNanostructure design

Reactor: 4.5 L

Cat.: 0.2 g

Conc.: 600 ppb

Time: 30 min

150 W LED lamp (λ > 400 nm)Model T200

Products: NO3

η(NO): 59.7%

[ 180 ]
N vacancy/porous PCN microtubesNanostructure design

Reactor: 4.5 L

Cat.: 0.1 g

Conc.: 400 ppb

Time: 30 min

300 W Xe lamp (λ > 400 nm)Model 42i‐TL

Products: NO3

η(NO): 32.8%

[ 196 ]
N3C vacancy/PCNNanostructure design

Reactor: 4.5 L

Cat.: 0.4 g

Conc.: 600 ppb

Time: 30 min

LED lamp (λ > 420 nm)Model T200

Products: NO3

η(NO): 40.3%

[ 177 ]
N3C vacancy/amorphous PCNNanostructure design

Reactor: 4.5 L

Cat.: 0.1 g

Conc.: 600 ppb

Time: 30 min

150 W THL (λ > 400 nm)Model T200

Products: NO3

η(NO): 57.1%

[ 139 ]
N defect/PCN (thermal treatment PCN under H2)Nanostructure design

Reactor: 0.45 L

Cat.: 0.1 g

Conc.: 600 ppm

Time: 30 min

150 W THL

(λ > 400 nm)

Model 42i‐TL

Products: NO3

η(NO): 41.84%

[ 197 ]
C vacancy/PCN (mix melamine with cyanuric acid)Nanostructure design

Reactor: 0.23 L

Cat.: 0.1 g

Conc.: 600 ppb

Time: 30 min

300 W Xe

lamp (λ > 420 nm)

GC‐14B l)

Products: N2

η(NO): 48%

[ 198 ]
C vacancy/PCN (calcinating PCN under CO2)Nanostructure design

Reactor: 4.5 L

Cat.: 0.2 g

Conc.: 600 ppb

Time: 30 min

150 W LED lamp (λ > 400 nm)Model T200

Products: NO3

η(NO): 59.0%

[ 199 ]
C vacancy/⋅OH/PCNNanostructure design

Reactor: 0.373 L

Cat.: 0.2 g

Conc.: 2 ppm

Time: 10 min

450 W ML m) (λ < 400 nm)ECL‐88A n)

Products: NO3

η(NO): 33%

[ 182 ]
P‐type PCNNanostructure design

Reactor: 4.5 L

Cat.: 0.05 g

Conc.: 600 ppb

Time: 30 min

Xe lamp (λ > 420 nm)Model 42i‐TL

Products: NO3

η(NO): 80%

[ 179 ]
Crystalline PCNNanostructure design

Reactor: 0.373 L

Cat.: unmarked

Conc.: 2 ppm

Time: unmarked

450 W ML (λ < 400 nm)ECL‐88A

Products: NO3

η(NO): 46%

[ 200 ]
PCN/Al2O3 Nanostructure design

Reactor: 4.5 L

Cat.: 0.2 g

Conc.: 600 ppb

Time: 30 min

300 W Xe lamp (λ > 420 nm)Model 42i‐TL

Products: NO3

η(NO): 77.1%

[ 62 ]
PCN‐NH2 (thermal treatment under H2/O2)Nanostructure design

Reactor: 4.5 L (

Cat.: 0.2 g

Conc.: 600 ppm

Time: 30 min

30 W LED lamp (λ > 420 nm)Model T200

Products: NO3

η(NO): 60.7% (H2)

[ 124 ]
Perfected π‐conjugated PCN (add NaOH, NaNO3, and NaHCO3 into precursors, respectively)Nanostructure design

Reactor: 4.5 L

Cat.: 0.1 g

Conc.: 600 ppb

Time: 6 min

350 W Xe lamp (λ > 400 nm)chemiluminescence

Products: NO3

η(NO): 53% (NaOH)

[ 201 ]
Crystalline CNNanostructure design

Reactor: 0.16 mL

Cat.: 0.1 g

Conc.: 2 ppm

Time: 10 min

450 W ML (λ > 400 nm)ECL‐88A

Products: NO3

η(NO): ≈45%

[ 200 ]
TAP p) /PCNElectronic structure regulation

Reactor: 4.5 L

Cat.: 0.1 g

Conc.: 600 ppb

Time: 40 min

30 W LED lamp (λ > 420 nm)Model T200

Products: NO3

η(NO): 59.4%

[ 115 ]
B/PCNElectronic structure regulation

Reactor: 4.5 L

Cat.: 0.1 g

Conc.: 400 ppb

Time: 30 min

300 W Xe lamp (λ > 420 nm)Model 42c o)

Products: NO3

η(NO): 30.4%

[ 117 ]
Defective borate/PCN (NaBH4 treat PCN)Nanostructure design

Reactor: 4.5 L

Cat.: 0.2 g

Conc.: 500 ppb

Time: 30 min

300 W HL (420–700 nm)Model 42i‐TL

Products: NO3

η(NO): 56.4%

[ 202 ]
C/PCNElectronic structure regulation

Reactor: 4.5 L

Cat.: 0.2 g

Conc.: 600 ppb

Time: 30 min

100 W THL (420–700 nm)Model 42i‐TL

Products: NO3

η(NO): 50.1%

[ 203 ]
P/PCNElectronic structure regulation

Reactor: 4.5 L

Cat.: 0.2 g

Conc.: 500 ppb

Time: 30 min

150 W THL (420–700 nm)Model 42i‐TL

Products: NO3

η(NO): 42.3%

[ 204 ]
K/PCNElectronic structure regulation

Reactor: 4.5 L

Cat.: 0.2 g

Conc.: 600 ppb

Time: 30 min

150 W THL

(λ > 420 nm)

Model 42i‐TL

Products: NO3

η(NO): 44.25%

[ 125 ]
Ca/PCNElectronic structure regulation

Reactor: 4.5 L

Cat.: 0.2 g

Conc.: 500 ppb

Time: 30 min

150 W THL (λ > 420 nm)Model 42i‐TL

Products: NO3

η(NO): 54.78%

[ 174 ]
Cs/PCNElectronic structure regulation

Reactor: 4.5 L

Cat.: 0.2 g

Conc.: 600 ppb

Time: 30 min

150 W THL (420–700 nm)Model 42i‐TL Column 1

Products: NO3

η(NO): 51.11%

[ 205 ]
Sr/PCN (Sr(NO3)2 as the source of Sr)Electronic structure regulation

Reactor: 4.5 L

Cat.: 0.2 g

Conc.: 600 ppb

Time: 30 min

150 W THL (λ > 420 nm)Model 42i‐TL

Products: NO3

η(NO): 53.1%

[ 206 ]
Sr/PCN (multi‐site doped Sr(NO3)2)Electronic structure regulation

Reactor: 0.785 L

Cat.: 0.05 g

Conc.: 600 ppb

Time: 30 min

300 W Xe lamp (λ > 420 nm)Model 42i‐TL

Products: NO3

η(NO): 55%

[ 207 ]
Sr/PCN (celestite as the source of Sr)Electronic structure regulation

Reactor: 0.785 L

Cat.: 0.05 g

Conc.: 600 ppb

Time: 30 min

30 W LED lamp (λ > 420 nm)Model 42i‐TL

Products: NO3

η(NO): 67.5%

[ 208 ]
Group IIA element ions/PCNElectronic structure regulation

Reactor: 0.785 L

Cat.: 0.05 g

Conc.: 600 ppb

Time: 30 min

Xe lamp (λ > 420 nm)Model 42i‐TL

Products: NO3

η(NO): 62% (Ba/PCN)

[ 136 ]
Pd nanoparticles/PCNElectronic structure regulation

Reactor: 4.5 L

Cat.: 0.2 g

Conc.: 600 ppb

Time: 30 min

150 W THL

(λ > 420 nm)

Model 42i‐TL

Products: NO3

η(NO): 60.6%

[ 209 ]
Pd QDs q) /PCNElectronic structure regulation

Reactor: 4.5 L

Cat.: 0.15 g

Conc.: 600 ppb

Time: 40 min

LED lamp (λ = 448 nm)Model T200

Products: NO3

η(NO): 72%

[ 210 ]
O/Ba co‐doped PCNElectronic structure regulation

Reactor: 4.5 L

Cat.: 0.2 g

Conc.: 500 ppb

Time: 30 min

150 W THL

(λ > 420 nm)

Model 42i‐TL

Products: NO3

η(NO): ≈58%

[ 211 ]
O/La co‐doped PCNElectronic structure regulation

Reactor: 4.5 L

Cat.: 0.1 g

Conc.: 500 ppb

Time: 30 min

150 W THL

(λ > 420 nm)

Model 42i‐TL

Products: NO3

η(NO): 50.4%

[ 183 ]
K+/NO3 co‐doped PCNElectronic structure regulation

Reactor: 4.5 L

Cat.: 0.2 g

Conc.: 500 ppb

Time: 30 min

150 W THL

(λ > 420 nm)

Model 42i‐TL

Products: NO3

η(NO): 40.33%

[ 128 ]
GO r) /PCN aerogelHeterostructure construction

Reactor: 4.5 L

Cat.: 0.2 g

Conc.: 500 ppb

Time: 30 min

150 W halide lamp (λ > 420 nm)Model 42i‐TL

Products: NO3

η(NO): 46.1%

[ 137 ]
G s) /MPCN t) (GO/MPCN)Heterostructure construction

Reactor: 4.5 L

Cat.: 0.1 g

Conc.: 600 ppb

Time: 30 min

150 W THL

(λ > 420 nm)

Model 42i‐TL

Products: NO3

η(NO): 64.9% (G/MPCN), 60.7% (GO/MPCN)

[ 212 ]
RGO u) /hollow PCNS/carbonized polymer nanofibersHeterostructure construction

Reactor: 1.6 L

Cat.: 0.05 g

Conc.: 600 ppb

Time: 30 min

20 W lamp (λ > 420 nm)Model 42i‐TL

Products: NO3

η(NO): 64%

[ 213 ]
Ag/PCNHeterostructure construction

Reactor: 4.5 L

Cat.: 0.2 g

Conc.: 600 ppb

Time: 30 min

300 W THL (λ > 420 nm)Model 42i‐TL

Products: NO3

η(NO): 54.3%

[ 214 ]
Au/PCNHeterostructure construction

Reactor: 4.5 L

Cat.: 0.2 g

Conc.: 500 ppb

Time: 30 min

150 W THL

(λ > 420 nm)

Model 42i‐TL

Products: NO3

η(NO): 41.0%

[ 65 ]
Cu/PCNHeterostructure construction

Reactor: 0.785 L

Cat.: 0.2 g

Conc.: 600 ppb

Time: 30 min

300 W Xe lamp (λ > 420 nm)Model 42i‐TL Column 1

Products: NO3

η(NO): 51.0%

[ 162 ]
Bi/PCNHeterostructure construction

Reactor: 4.5 L

Cat.: 0.2 g

Conc.: 600 ppb

Time: 30 min

LED lamp

(λ = 448 nm))

Model T200

Products: NO3

η(NO): 65%

[ 215 ]
Bi nanoparticles/PCNHeterostructure construction

Reactor: 4.5 L

Cat.: 0.2 g

Conc.: 500 ppb

Time: 30 min

150 W THL

(λ > 420 nm)

Model 42i‐TL

Products: NO3

η(NO): 60.8%

[ 173 ]
Bi Spheres/PCNHeterostructure construction

Reactor: 4.5 L

Cat.: 0.2 g

Conc.: 600 ppb

Time: 30 min

150 W THL

(λ > 420 nm)

Model 42i‐TL

Products: NO3

η(NO): 59.7%

[ 216 ]
OPCN/K‐PCNHeterostructure construction

Reactor: 4.5 L

Cat.: 0.2 g

Conc.: 550 ppb

Time: 30 min

150 W THL

(λ > 420 nm)

Model 42i‐TL

Products: NO3

η(NO): 54%

[ 64 ]
PCNM/PCNUHeterostructure construction

Reactor: 4.5 L

Cat.: 0.1 g

Conc.: 600 ppb

Time: 30 min

150 W THL

(λ > 420 nm)

Model 42i‐TL

Products: NO3

η(NO): 41.3%

[ 217 ]
SnO2 QDs/PCNHeterostructure construction

Reactor: 8.4 L

Cat.: 0.4 g

Conc.: 400 ppb

Time: 30 min

150 W THL

(λ > 420 nm)

Model 42i‐TL

Products: NO3

η(NO): 68%

[ 218 ]
(BiO)2CO3/PCNHeterostructure construction

Reactor: 4.5 L

Cat.: 0.1 g

Conc.: 600 ppb

Time: 30 min

150 W THL

(λ > 420 nm)

Model 42i‐TL

Products: NO3

η(NO): 53.28%

[ 185 ]
Bi2O2CO3/PCNHeterostructure construction

Reactor: 4.5 L

Cat.: 0.1 g

Conc.: 400 ppb

Time: 30 min

300 W Xe lamp (λ > 420 nm)Model 42c‐TL

Products: NO3

η(NO): 34.8%

[ 126 ]
2D/2D BiOBr/PCNHeterostructure construction

Reactor: 4.5 L

Cat.: 0.1 g

Conc.: 660 ppb

Time: 30 min

100 W THL (λ > 420 nm)Model 42c‐TL

Products: NO3

η(NO): 32.7%

[ 219 ]
CeO2/PCNHeterostructure construction

Reactor: 4.5 L

Cat.: 0.15 g

Conc.: 450 ppb

Time: 30 min

300 W THL (λ > 420 nm)Model 42c‐TL

Products: NO3

η(NO): 35%

[ 220 ]
LaCO3OH/PCNHeterostructure construction

Reactor: 4.5 L

Cat.: 0.1 g

Conc.: 400 ppb

Time: 30 min

300 W Xe lamp (λ > 420 nm)Model 42i‐TL

Products: NO3

η(NO): 30.3%

[ 114 ]
Ti3+‐TiO2/PCN filmsHeterostructure construction

Reactor: 0.85 L

Cat.: unmarked

Conc.: 400 ppb

Time: 30 min

300 W Xe lamp (λ > 420 nm)Chemiluminescence

Products: NO3

η(NO): 25.8%

[ 221 ]
PCNT/PCNUHeterostructure construction

Reactor: 4.5 L

Cat.: 0.1 g

Conc.: 600 ppb

Time: 30 min

150 W Xe lamp (λ > 420 nm)Model 42i‐TL

Products: NO3

η(NO): 47.6%

[ 222 ]
Ni3(Co(CN)6)2/PCNHeterostructure construction

Reactor: 2.26 L

Cat.: 0.1 g

Conc.: 600 ppb

Time: 30 min

300 W Xe lamp (λ > 420 nm)Model 42i‐TL

Products: NO3

η(NO): 59.1%

[ 223 ]
Illite/PCNHeterostructure construction

Reactor: 4.5 L

Cat.: 0.05 g

Conc.: 660 ppb

Time: 6 min

300 W Xe lamp (λ > 420 nm)Model 42i‐TL

Products: NO3

η(NO): 63%

[ 224 ]
PdCl2/PCNHeterostructure construction

Reactor: 4.5 L

Cat.: 0.2 g

Conc.: 1100 ppb

Time: 30 min

30 W emitting diode (λ > 420 nm)Model T200

Products: NO3

η(NO): 65%

[ 225 ]
S‐TiO2 v) /PCNHeterostructure construction

Reactor: unmarked

Cat.: 1 g

Conc.: 1ppm

Time: 60 min

Fluorescent lamps (λ > 420 nm)CM2041, Casella

Products: NO3

η(NO): 25%

[ 226 ]
rTiO2 w) /PCN QDsHeterostructure construction

Reactor: 4.5 L

Cat.: 0.2 g

Conc.: 600 ppb

Time: 30 min

LED lamp (λ > 420 nm)Model T200

Products: NO3

η(NO): 37.4%

[ 127 ]
W18O49/PCNHeterostructure construction

Reactor: 0.785 L

Cat.: 0.05 g

Conc.: 600 ppb

Time: 30 min

300 W Xe lamp (λ > 420 nm)Model 42i‐TL

Products: NO3

η(NO): 83.55%

[ 227 ]
PI x) /PCNHeterostructure construction

Reactor: 0.785 L

Cat.: 0.05 g

Conc.: 600 ppb

Time: 10 min

300 W Xe lamp (λ > 420 nm)Model 42i‐TL

Products: NO3

η(NO): 47%

[ 184 ]
AgVO3/PCN/G aerogelHeterostructure construction

Reactor: 2.26 L

Cat.: 0.1 g

Conc.: 600 ppm

Time: 30 min

300 W Xe lamp (λ > 420 nm)Model 42i‐TL

Products: NO3

η(NO): 65%

[ 175 ]
2D/2D BiOIO3/I/PCNHeterostructure construction

Reactor: 2.26 L

Cat.: 0.1 g

Conc.: 600 ppb

Time: 30 min

300 W Xe lamp (λ > 420 nm)Model 42i‐TL

Products: NO3

η(NO): 57%

[ 228 ]
RGO/PI/PCNHeterostructure construction

Reactor: 0.785 L

Cat.: 0.02 g

Conc.: 600 ppb

Time: 30 min

300 W Xe lamp (λ > 420 nm)Model 42i‐TL

Products: NO3

η(NO): 60%

[ 70 ]
Ag3PO4/Ag/PCNHeterostructure construction

Reactor: 4.5 L

Cat.: 0.3 g

Conc.: 400 ppm

Time: 90 min

300 W Xe lamp (λ > 420 nm)SERVOPRO 4900

Products: NO3

η(NO): 74%

[ 229 ]
Sb2WO6/PCNHeterostructure construction

Reactor: 8.4 L

Cat.: 0.05 g

Conc.: 400 ppb

Time: 30 min

Xe lamp (λ > 420 nm)FT‐IR spectrometer

Products: NO3

η(NO): 68%

[ 230 ]
BP/PCN‐MOFComposite construction

Reactor: 2.26 L

Cat.: 150 mg

Conc.: 600 ppb

Time: 30 min

Xe lamp (λ > 420 nm)Model 42i‐TL

Products: NO3

η(NO): 74%

[ 231 ]
O vacancy‐BiOBr /PCNComposite construction

Reactor: 2.26 L

Cat.: 0.1 g

Conc.: 600 ppb

Time: 30 min

300 W Xe lamp (λ > 420 nm)Model 42i‐TL

Products: NO3

η(NO): 63%

[ 134 ]
GO‐InVO4/PCN QDs aerogelComposite construction

Reactor: 2.26 L

Cat.: 50 mg

Conc.: 600 ppb

Time: 30 min

300 W Xe lamp (λ > 420 nm)Model 42i‐TL

Products: NO3

η(NO): 65%

[ 131 ]
Co3O4/PCNComposite construction

Reactor: 2.26 L

Cat.: 100 mg

Conc.: 600 ppb

Time: 30 min

300 W Xe lamp (λ > 420 nm)Model 42i‐TL

Products: NO3

η(NO): 57%

[ 132 ]

Initial concentration of NO (Conc.)

The mass of the photocatalysts (Cat.)

Irradiation time (Time)

Tungsten halogen lamp (THL)

Thermo Environmental Instruments Inc., model 42i‐TL (Model 42i‐TL)

The removal efficiency η (%) of pollutant was calculated as: η (%) = (1 − C/C 0) × 100%

The melamine as the precursor (PCNM)

The urea as the precursor (PCNU)

The thiourea as the precursor (PCNT)

The dicyanamide as the precursor (PCND)

Model T200, Advanced Pollution Instrumentation (Model T200)

Gas chromatograph, GC‐14B Shimadzu Corp., Japan (GC‐14B)

Mercury lamp (ML)

Yanaco, ECL‐88A (ECL‐88A)

Model 42c, Thermo Environmental Instruments Inc., Franklin, MA, USA (Model 42c)

2,4,6‐Triaminopyrimidine (TAP)

Quantum dots (QDs)

Graphene oxide (GO)

Graphene (G)

Mesoporous PCN (MPCN)

Reduced graphene oxide (RGO)

Sludges TiO2 (S‐TiO2)

Rutile TiO2 (rTiO2)

Perylene imides (PI).

Summary of recently reported PCN‐based photocatalysts utilized in denitrification reaction Reactor: 4.5 L Cat .: 0.1 g Conc. : 600 ppb Time : 30 min Products: NO3 – η (NO): 26.2% (PCNM ), 32.2% (PCNU ), 29.2% (PCNT ), 22.2% (PCND ) Reactor: 4.5 L Cat.: 0.1 g Conc.: 600 ppb Time: 30 min 150 W THL (λ > 420 nm) Products: NO3 – η(NO): 39.4% (PCNT); 40.4% (PCNU) Reactor: 4.5 L Cat.: 0.2 g Conc.: 600 ppb Time: 30 min 150 W THL (λ > 420 nm) Products: NO3 – η(NO): 48.3% Reactor: 4.5 L Cat.: 0.2 g Conc.: 600 ppb Time: 30 min 150 W THL (λ > 420 nm) Products: NO3 – η(NO): 32.7% Reactor: 4.5 L Cat.: 0.2 g Conc.: 600 ppb Time: 30 min 150 W THL (λ > 420 nm) Products: NO3 – η(NO): 48.0% Reactor: 4.5 L Cat.: 0.15 g Conc.: 600 ppb Time: 30 min Products: NO3 – η(NO): 71.2% Reactor: 4.5 L Cat.: 0.1 g Conc.: 600 ppb Time: 60 min 150 W THL (λ > 420 nm) Products: NO3 – η(NO): 33.9% Reactor: 4.5 L Cat.: 0.2 g Conc.: 600 ppb Time: 30 min Products: NO3 – η(NO): 65% Reactor: 4.5 L Cat.: 0.2 g Conc.: 600 ppb Time: 30 min Products: NO3 – η(NO): 68% Reactor: 4.5 L Cat.: 0.2 g Conc.: 600 ppb Time: 30 min 150 W THL (λ > 420 nm) Products: NO3 – η(NO): 51.2% Reactor:0.785 L Cat.: 0.05 g Conc.: 600 ppb Time: 30 min Products: NO3 – η(NO): 80% Reactor: 4.5 L Cat.: 0.05 g Conc.: 600 ppb Time: 30 min Products: NO3 – η(NO): 42% Reactor: 4.5 L Cat.: 0.2 g Conc.: 600 ppb Time: 30 min 150 W THL (λ > 420 nm) Products: NO3 – η(NO): 47.1% Reactor: 0.325 L Cat.: 0.05 g Conc.: 15 ppm Time: 120 min Products: NO3 – η(NO): 66.7% Reactor: 4.5 L Cat.: 0.1 g Conc.: 600 ppb Time: 30 min 150 W THL (λ > 420 nm) Products: NO3 – η(NO): 40.7% Reactor: 4.5 L Cat.: 0.2 g Conc.: 600 ppb Time: 30 min Products: NO3 – η(NO): 59.7% Reactor: 4.5 L Cat.: 0.1 g Conc.: 400 ppb Time: 30 min Products: NO3 – η(NO): 32.8% Reactor: 4.5 L Cat.: 0.4 g Conc.: 600 ppb Time: 30 min Products: NO3 – η(NO): 40.3% Reactor: 4.5 L Cat.: 0.1 g Conc.: 600 ppb Time: 30 min Products: NO3 – η(NO): 57.1% Reactor: 0.45 L Cat.: 0.1 g Conc.: 600 ppm Time: 30 min 150 W THL (λ > 400 nm) Products: NO3 – η(NO): 41.84% Reactor: 0.23 L Cat.: 0.1 g Conc.: 600 ppb Time: 30 min 300 W Xe lamp (λ > 420 nm) Products: N2 η(NO): 48% Reactor: 4.5 L Cat.: 0.2 g Conc.: 600 ppb Time: 30 min Products: NO3 – η(NO): 59.0% Reactor: 0.373 L Cat.: 0.2 g Conc.: 2 ppm Time: 10 min Products: NO3 – η(NO): 33% Reactor: 4.5 L Cat.: 0.05 g Conc.: 600 ppb Time: 30 min Products: NO3 – η(NO): 80% Reactor: 0.373 L Cat.: unmarked Conc.: 2 ppm Time: unmarked Products: NO3 – η(NO): 46% Reactor: 4.5 L Cat.: 0.2 g Conc.: 600 ppb Time: 30 min Products: NO3 – η(NO): 77.1% Reactor: 4.5 L ( Cat.: 0.2 g Conc.: 600 ppm Time: 30 min Products: NO3 – η(NO): 60.7% (H2) Reactor: 4.5 L Cat.: 0.1 g Conc.: 600 ppb Time: 6 min Products: NO3 – η(NO): 53% (NaOH) Reactor: 0.16 mL Cat.: 0.1 g Conc.: 2 ppm Time: 10 min Products: NO3 – η(NO): ≈45% Reactor: 4.5 L Cat.: 0.1 g Conc.: 600 ppb Time: 40 min Products: NO3 – η(NO): 59.4% Reactor: 4.5 L Cat.: 0.1 g Conc.: 400 ppb Time: 30 min Products: NO3 – η(NO): 30.4% Reactor: 4.5 L Cat.: 0.2 g Conc.: 500 ppb Time: 30 min Products: NO3 – η(NO): 56.4% Reactor: 4.5 L Cat.: 0.2 g Conc.: 600 ppb Time: 30 min Products: NO3 – η(NO): 50.1% Reactor: 4.5 L Cat.: 0.2 g Conc.: 500 ppb Time: 30 min Products: NO3 – η(NO): 42.3% Reactor: 4.5 L Cat.: 0.2 g Conc.: 600 ppb Time: 30 min 150 W THL (λ > 420 nm) Products: NO3 – η(NO): 44.25% Reactor: 4.5 L Cat.: 0.2 g Conc.: 500 ppb Time: 30 min Products: NO3 – η(NO): 54.78% Reactor: 4.5 L Cat.: 0.2 g Conc.: 600 ppb Time: 30 min Products: NO3 – η(NO): 51.11% Reactor: 4.5 L Cat.: 0.2 g Conc.: 600 ppb Time: 30 min Products: NO3 – η(NO): 53.1% Reactor: 0.785 L Cat.: 0.05 g Conc.: 600 ppb Time: 30 min Products: NO3 – η(NO): 55% Reactor: 0.785 L Cat.: 0.05 g Conc.: 600 ppb Time: 30 min Products: NO3 – η(NO): 67.5% Reactor: 0.785 L Cat.: 0.05 g Conc.: 600 ppb Time: 30 min Products: NO3 – η(NO): 62% (Ba/PCN) Reactor: 4.5 L Cat.: 0.2 g Conc.: 600 ppb Time: 30 min 150 W THL (λ > 420 nm) Products: NO3 – η(NO): 60.6% Reactor: 4.5 L Cat.: 0.15 g Conc.: 600 ppb Time: 40 min Products: NO3 – η(NO): 72% Reactor: 4.5 L Cat.: 0.2 g Conc.: 500 ppb Time: 30 min 150 W THL (λ > 420 nm) Products: NO3 – η(NO): ≈58% Reactor: 4.5 L Cat.: 0.1 g Conc.: 500 ppb Time: 30 min 150 W THL (λ > 420 nm) Products: NO3 – η(NO): 50.4% Reactor: 4.5 L Cat.: 0.2 g Conc.: 500 ppb Time: 30 min 150 W THL (λ > 420 nm) Products: NO3 – η(NO): 40.33% Reactor: 4.5 L Cat.: 0.2 g Conc.: 500 ppb Time: 30 min Products: NO3 – η(NO): 46.1% Reactor: 4.5 L Cat.: 0.1 g Conc.: 600 ppb Time: 30 min 150 W THL (λ > 420 nm) Products: NO3 – η(NO): 64.9% (G/MPCN), 60.7% (GO/MPCN) Reactor: 1.6 L Cat.: 0.05 g Conc.: 600 ppb Time: 30 min Products: NO3 – η(NO): 64% Reactor: 4.5 L Cat.: 0.2 g Conc.: 600 ppb Time: 30 min Products: NO3 – η(NO): 54.3% Reactor: 4.5 L Cat.: 0.2 g Conc.: 500 ppb Time: 30 min 150 W THL (λ > 420 nm) Products: NO3 – η(NO): 41.0% Reactor: 0.785 L Cat.: 0.2 g Conc.: 600 ppb Time: 30 min Products: NO3 – η(NO): 51.0% Reactor: 4.5 L Cat.: 0.2 g Conc.: 600 ppb Time: 30 min LED lamp (λ = 448 nm)) Products: NO3 – η(NO): 65% Reactor: 4.5 L Cat.: 0.2 g Conc.: 500 ppb Time: 30 min 150 W THL (λ > 420 nm) Products: NO3 – η(NO): 60.8% Reactor: 4.5 L Cat.: 0.2 g Conc.: 600 ppb Time: 30 min 150 W THL (λ > 420 nm) Products: NO3 – η(NO): 59.7% Reactor: 4.5 L Cat.: 0.2 g Conc.: 550 ppb Time: 30 min 150 W THL (λ > 420 nm) Products: NO3 – η(NO): 54% Reactor: 4.5 L Cat.: 0.1 g Conc.: 600 ppb Time: 30 min 150 W THL (λ > 420 nm) Products: NO3 – η(NO): 41.3% Reactor: 8.4 L Cat.: 0.4 g Conc.: 400 ppb Time: 30 min 150 W THL (λ > 420 nm) Products: NO3 – η(NO): 68% Reactor: 4.5 L Cat.: 0.1 g Conc.: 600 ppb Time: 30 min 150 W THL (λ > 420 nm) Products: NO3 – η(NO): 53.28% Reactor: 4.5 L Cat.: 0.1 g Conc.: 400 ppb Time: 30 min Products: NO3 – η(NO): 34.8% Reactor: 4.5 L Cat.: 0.1 g Conc.: 660 ppb Time: 30 min Products: NO3 – η(NO): 32.7% Reactor: 4.5 L Cat.: 0.15 g Conc.: 450 ppb Time: 30 min Products: NO3 – η(NO): 35% Reactor: 4.5 L Cat.: 0.1 g Conc.: 400 ppb Time: 30 min Products: NO3 – η(NO): 30.3% Reactor: 0.85 L Cat.: unmarked Conc.: 400 ppb Time: 30 min Products: NO3 – η(NO): 25.8% Reactor: 4.5 L Cat.: 0.1 g Conc.: 600 ppb Time: 30 min Products: NO3 – η(NO): 47.6% Reactor: 2.26 L Cat.: 0.1 g Conc.: 600 ppb Time: 30 min Products: NO3 – η(NO): 59.1% Reactor: 4.5 L Cat.: 0.05 g Conc.: 660 ppb Time: 6 min Products: NO3 – η(NO): 63% Reactor: 4.5 L Cat.: 0.2 g Conc.: 1100 ppb Time: 30 min Products: NO3 – η(NO): 65% Reactor: unmarked Cat.: 1 g Conc.: 1ppm Time: 60 min Products: NO3 – η(NO): 25% Reactor: 4.5 L Cat.: 0.2 g Conc.: 600 ppb Time: 30 min Products: NO3 – η(NO): 37.4% Reactor: 0.785 L Cat.: 0.05 g Conc.: 600 ppb Time: 30 min Products: NO3 – η(NO): 83.55% Reactor: 0.785 L Cat.: 0.05 g Conc.: 600 ppb Time: 10 min Products: NO3 – η(NO): 47% Reactor: 2.26 L Cat.: 0.1 g Conc.: 600 ppm Time: 30 min Products: NO3 – η(NO): 65% Reactor: 2.26 L Cat.: 0.1 g Conc.: 600 ppb Time: 30 min Products: NO3 – η(NO): 57% Reactor: 0.785 L Cat.: 0.02 g Conc.: 600 ppb Time: 30 min Products: NO3 – η(NO): 60% Reactor: 4.5 L Cat.: 0.3 g Conc.: 400 ppm Time: 90 min Products: NO3 – η(NO): 74% Reactor: 8.4 L Cat.: 0.05 g Conc.: 400 ppb Time: 30 min Products: NO3 – η(NO): 68% Reactor: 2.26 L Cat.: 150 mg Conc.: 600 ppb Time: 30 min Products: NO3 – η(NO): 74% Reactor: 2.26 L Cat.: 0.1 g Conc.: 600 ppb Time: 30 min Products: NO3 – η(NO): 63% Reactor: 2.26 L Cat.: 50 mg Conc.: 600 ppb Time: 30 min Products: NO3 – η(NO): 65% Reactor: 2.26 L Cat.: 100 mg Conc.: 600 ppb Time: 30 min Products: NO3 – η(NO): 57% Initial concentration of NO (Conc.) The mass of the photocatalysts (Cat.) Irradiation time (Time) Tungsten halogen lamp (THL) Thermo Environmental Instruments Inc., model 42i‐TL (Model 42i‐TL) The removal efficiency η (%) of pollutant was calculated as: η (%) = (1 − C/C 0) × 100% The melamine as the precursor (PCNM) The urea as the precursor (PCNU) The thiourea as the precursor (PCNT) The dicyanamide as the precursor (PCND) Model T200, Advanced Pollution Instrumentation (Model T200) Gas chromatograph, GC‐14B Shimadzu Corp., Japan (GC‐14B) Mercury lamp (ML) Yanaco, ECL‐88A (ECL‐88A) Model 42c, Thermo Environmental Instruments Inc., Franklin, MA, USA (Model 42c) 2,4,6‐Triaminopyrimidine (TAP) Quantum dots (QDs) Graphene oxide (GO) Graphene (G) Mesoporous PCN (MPCN) Reduced graphene oxide (RGO) Sludges TiO2 (S‐TiO2) Rutile TiO2 (rTiO2) Perylene imides (PI).

Research Progress of PCN in Denitrification

Tailoring the Nanostructure

Tailoring the nanostructure (modulating in‐plane layers and interlayers) of PCN is performed through regulating the polymerization process (e.g., precursors mass and types, calcination time and temperature), introducing different morphologies, porous characteristics, and engineering defects into the pristine PCN based on nano templating and nano casting approach.[ , , , , , , , , ] The controllable nanostructure design of PCN not only improves the surface area to encourage the mass transfer kinetics but also increases the active sites on the surface of the catalysts and optimizes the energy band structure (bandgap and band position) and optical absorption, significantly advancing the efficiency of PODN. For instance, Zhang et al. synthesized different PCN polymers by calcinating various precursors, showing the diverse activity of the PODN.[ ] The results showed that the best precursor for the preparation of PCN was melamine, assistant with the consideration of the synthetic cost, toxicity, and products yield of PCN. This work could provide new insights and enlightenment into the PCN synthesis (selection and optimization of precursors) and an in‐depth and comprehensive cognition of the microstructure–activity relationships of PCN. A porous PCN with N defective sites could be produced by thermal treatment with urea, which showed a high specific surface area and wide bandgap, thereby promoting PODN activity.[ ] The enhanced activity was revealed by the increased adsorption of NO molecules favored by N defective sites, the compensated electrons favored by the production of the final products, the enhanced generation of ROS favored by the high separation of charges, and more defective sites. Moreover, the mass of precursors, along with the overlooked factor for the synthesis of PCN, exerted an unexpected effect on the nanostructure design of PCN. The nanostructure and capability of PCN semiconductors could be well‐designed and well‐tailored by varying the weight of precursors. The PCN with thin layers and increased surface area favored reaction sites and mass transfer, with elevated CB position favored improved redox ability, with promoted PODN capability were triumphantly accomplished as declining the mass of thiourea.[ ] The regulation of the calcination temperature and time to produce PCN exhibited similar positive effects on PODN.[ ] Furthermore, a porous honeycomb structure for PCN could be achieved by adding a certain amount of water into precursors before calcination, which exhibited a highly enhanced NO removal ratio (48%) compared with the pristine PCN (30.6%).[ ] Adding further HCl to the prepared PCN precursors, the activity of PODN for the obtained porous PCN (80%) was enhanced.[ ] This positive effect was due to the changed modal of thermal condensation and the introduction of Cl–/NH4 + and large voids (donated or accepted electrons, Figure  ), which increased the surface area and eliminated part of the quantum confinement effect, thereby enhancing the PODN activity.
Figure 5

A) Schematic illustrations of a) blank C6N9H3 and b) the large voids padded by chloride ions of C6N9H3. Reproduced with permission.[ ] Copyright 2017, Elsevier. B) The possible formation mechanism of PCN nanosheets. C) Illustration of the electronic band structure and photocatalytic mechanism of PCNs samples. B,C) Reproduced with permission.[ ] Copyright 2018, Elsevier. D) Schematic formation mechanism of porous PCN. Reproduced with permission.[ ] Copyright 2019, Elsevier. E) Schematic mechanism of PODN on the PCN‐based photocatalysts. Reproduced with permission.[ ] Copyright 2016, American Chemical Society.

A) Schematic illustrations of a) blank C6N9H3 and b) the large voids padded by chloride ions of C6N9H3. Reproduced with permission.[ ] Copyright 2017, Elsevier. B) The possible formation mechanism of PCN nanosheets. C) Illustration of the electronic band structure and photocatalytic mechanism of PCNs samples. B,C) Reproduced with permission.[ ] Copyright 2018, Elsevier. D) Schematic formation mechanism of porous PCN. Reproduced with permission.[ ] Copyright 2019, Elsevier. E) Schematic mechanism of PODN on the PCN‐based photocatalysts. Reproduced with permission.[ ] Copyright 2016, American Chemical Society. In addition, porous PCN nanosheets could be obtained by thermal exfoliation, induced band structure variation and the quantum confinement effect favored by the reduced particle size associated with a decreased layer thickness.[ , ] For instance, Wu et al. obtained porous PCN nanosheets via a two‐step layer‐by‐layer thermal exfoliation, increased electrical conductivity and enlarged PCN bandgap (Figure 5B).[ ] The promoted kinetics of charges and oxidation capability could be achieved through the above structure optimization, thereby providing new chances for regulating the PCN synthesis and redox capability toward efficient PODN (Figure 5C). Organic molecules (glyoxal), as a soft template, could be introduced in the synthesis process of porous PCN nanosheets, which showed enhanced O2 activation and PODN activity (Figure 5D).[ ] The inorganic salt of (NH4)2SO4 and NH4HCO3 as bubble soft templates was also selected to design the porous structure of PCN.[ , ] These bubble soft templates endowed PCN with a porous structure and enhanced specific surface area favored gas diffusion and transfer, meanwhile, rendered up‐shifted CB position favored charge separation and transportation (Figure 5E).[ ] Given these benefits and advantages from the modifications of the thermal exfoliation and soft templates, the improved PCN with porous structure endows promoted performance toward PODN. In addition, the PCN with a mesoporous structure is also widely used for PODN reaction at the ppb level.[ ] The mesoporous/nanosphere SiO2 was a type of hard template, which modifies the morphology and texture of PCN by Dong et al. The significant enhancement of activity for mesoporous PCN was ascribed to the co‐contributions of boosted surface area and pore volume, enhanced optical‐capturing ability, increased redox capability, and inhibited recombination of charge carriers. The flower‐like PCN was assembled from holy nanosheets by the co‐production of N vacancies, demonstrating a much higher visible activity of oxidation denitrification (ODN) compared with the bare PCN.[ ] The improved PODN efficiency of flower‐like PCN was due to the broadened absorption capability of visible light and strengthened kinetics of solar‐induced charges favored by condensing the stacking of the π–π layer and breaking the interplanar hydrogen bonds. Powdery PCNs exhibit high activity in PODN reactions.[ ] However, its practical application is still limited, because the powdery catalyst can be facile blown away and lost, with time‐consuming filtration/separation.[ ] Therefore, the introduction of the supported technology can solve the key technical problem of the powdery photocatalyst from the test to the application stage, which provides the possibility for the powdery photocatalyst to create greater economic and environmental benefits in the actual production and application process. Firstly, the PCN was in situ immobilized on structured ceramic foam (Al2O3) by the chemical interaction, which was utilized to decomposed NO in the air under the irradiation of real indoor energy‐saving lamps.[ ] The photocatalytic NO removal ratio of immobilized PCN could reach up to 77.1% at a pyrolysis temperature of 600 °C, which showed superior reusability in PODN reaction. The immobilization of PCN on Al2O3 was confirmed and expected to realize practical application to remediate atmospheric environmental issues.

Introduction of Vacancies

The production of thin‐layered PCN in assistance with a porous structure can be achieved through the exfoliation of bulk PCN, including liquid‐phase and gas‐phase exfoliation.[ , , , , ] The superiority and advantages of the resultant thin‐layered PCN can be associated with the enlarged specific surface area (favored mass transportation kinetics and reactive sites) and improved electron and hole separation/transportability efficiency. In addition, the production of N defective sites in PCNs increases the adsorption of NO molecules, which leads to NO activation and conversion, thereby providing great potential for PODN.[ ] However, PCN materials synthesized by traditional thermal condensation usually exhibit a low density of defective and active sites, thereby leading to sluggish charge migration and PODN efficiency.[ , , ] Absorbing the reactants on the surface of the “perfect” semiconductor photocatalyst without any functional groups or defective sites is difficult, leading to the difficulty of photocatalytic reaction.[ , , ] Therefore, defect engineering on the surface of PCN materials (C/N vacancies produced on the periodic heptazine units) is considered and confirmed as an advanced modification toward efficient and stable PODN, because defects usually endow strong effects on optimizing the structure of semiconductors.[ , ] Moreover, the introduction of vacancies changes the surface or internal structure of the catalyst to generate new levels, regulates the photo‐electrochemical nature of the PCN catalyst, and provides enhanced reaction sites for the reactants, thereby improving the performance of the photocatalytic reaction.[ , ] Although vacancies as general defects exist in the semiconductors, the mediators' function of vacancies can offer new mechanisms and insights to modulate the electronic structure and charge kinetics of the photocatalysts.[ , , ] In general, vacancies can be generated after lattice atom escape and classified into anionic and cationic vacancies.[ , , , , ] The anionic vacancies are vital for multiphase catalysis because of the endowed optical‐absorbing capabilities, the function of specific adsorption/reaction sites for reactant molecules, and the capture sites for electrons.[ ] For example, the O vacancies as a representative anionic vacancy in metal oxides have been actively pursued in capturing electrons, activating O2, and utilizing solar light.[ , ] Based on the discovery linked to O‐vacancy inorganic materials, anionic vacancies produced from PCN could effectively adsorb/activate target air pollutants, harvest photogenerated electrons, and provide specific sites.[ , ] Current approaches developed for generating anionic vacancies into PCN primarily involve calcination under kinds of atmospheric conditions or at diverse temperatures.[ , ] The roles of anionic vacancies in spatially distributing charges, accelerating charge kinetics and activating target reactants (O2 and NO ) are investigated and expounded. For example, Wang et al. in situ synthesized a sort of N‐vacancy PCN with porous microtubes via soft‐chemical methods.[ ] The surface N vacancies as specific sites functioned as capturing solar‐induced electrons and activating O2 while enhancing the solar‐absorbing capability of PCN (Figure  ). Moreover, the reactants diffusion and directed charge transfer were facilitated by the porous and tubular architectures of the PCN microtubes. The prepared porous PCN microtubes with N vacancies exhibited advanced NO degradation in comparison with bulk PCN with visible light. The unique N3C vacancies in the amorphous PCN matrix were stable and highly efficient during the procedure of PODN, which were ascribed to the boosted ROS generation (1O2 and O2 ⋅−) and improved light absorption for complete NO removal (Figure 6B).[ ] The PCN with three coordinated (N3C) N vacancies could also be achieved by directly condensing the hybrid of N‐abundant precursors (azodicarbonamide and melamine).[ ] Different from the pristine PCN, the obtained PCN with N vacancies showed better PODN activity and stability because of the wide absorption range of visible light and the accelerated charge transmission. The N vacancies produced in PCN could serve as the reactive sites, which weakened the adsorption of intermediates/final products, strengthened the desorption of final products, facilitated the O2 activation and ROS conversion (Figure 6C), thereby contributing the enhanced PODN performance and the retained reusability. When the PCN was heated under an H2 atmosphere, N defects were introduced, and the accelerated NO+ intermediate was formed to improve the PODN efficiency (Figure 6D).[ ] The acidic groups (e.g., SO4 2− and PO4 3−) can intensify the adsorption of O2 and accelerate the separation of charge carrier and generation of ROS favored by hot electrons utilization, which is necessary for PODN.[ , ] When the NaBH4 is introduced into the PCN, the N defect and acidic group (borate) were simultaneously produced.[ ] The resultant defective borate‐decorated PCN showed high efficiency in the ppb‐level PODN reaction because of the promoted visible‐light absorbance, accelerated charge kinetics, and improved ROS generation.
Figure 6

A) Models of O2 adsorbed on: a) PCN and b) N‐deficient PCN after geometry optimization. The corresponding calculated EDD diagrams of O2 absorbed on c) PCN and d) N‐deficient PCN. Reproduced with permission.[ ] Copyright 2019, American Chemical Society. B) a,b) XRD patterns of the obtained CN and ACN3 samples, and c) the comparison of the FTIR spectra, and d) N 1s XPS spectra, e) ESR spectra, and f) the comparison of schematic atomic model of incomplete ACN constructed from melon units with three kinds of nitrogen labeled as N2C, N3C, and NH . Reproduced with permission.[ ] Copyright 2021, Wiley‐VCH. C) NO‐TPD spectra, electron localization function (ELF) and optimized NO adsorption of PCNs samples. Reproduced with permission.[ ] Copyright 2020, Elsevier. D) a) Structure of containing N‐defective PCN. b) Bader effective charge analysis. c) EPR spectra of samples. Reproduced with permission.[ ] Copyright 2020, Elsevier. E) The effect of the pre‐adsorption of NO on the EPR spectrum of PCN and Ns‐PCN. Reproduced with permission.[ ] Copyright 2017, Elsevier.

A) Models of O2 adsorbed on: a) PCN and b) N‐deficient PCN after geometry optimization. The corresponding calculated EDD diagrams of O2 absorbed on c) PCN and d) N‐deficient PCN. Reproduced with permission.[ ] Copyright 2019, American Chemical Society. B) a,b) XRD patterns of the obtained CN and ACN3 samples, and c) the comparison of the FTIR spectra, and d) N 1s XPS spectra, e) ESR spectra, and f) the comparison of schematic atomic model of incomplete ACN constructed from melon units with three kinds of nitrogen labeled as N2C, N3C, and NH . Reproduced with permission.[ ] Copyright 2021, Wiley‐VCH. C) NO‐TPD spectra, electron localization function (ELF) and optimized NO adsorption of PCNs samples. Reproduced with permission.[ ] Copyright 2020, Elsevier. D) a) Structure of containing N‐defective PCN. b) Bader effective charge analysis. c) EPR spectra of samples. Reproduced with permission.[ ] Copyright 2020, Elsevier. E) The effect of the pre‐adsorption of NO on the EPR spectrum of PCN and Ns‐PCN. Reproduced with permission.[ ] Copyright 2017, Elsevier. Moreover, PCN with carbon vacancy was investigated and applied in PODN, showing an extraordinarily NO removal rate in comparison with pristine PCN.[ ] This excellent activity was ascribed to the facilitated transfer of electrons favored by the negatively shifted potential of CB, increased adsorption/activation of O2 molecules favored by the superior surface area and boosted electrons. In particular, the ultrathin PCN layers with abundant surface C vacancies could be obtained through thermally condensing the hybrid of melamine and cyanuric acid, demonstrating higher efficiency and stability of PODN.[ ] Different from the above‐mentioned conversion and decomposition mechanism, the NO was reduced into the N2 for the ultrathin PCN with C vacancies. The ultrathin PCN structures possessed a unique surface structure (C vacancies) that could serve as traps of the electrons to localize the photogenerated charges and function as an adsorption site for NO through the binding of the PCN interface (Figure 6E). The direct transmission of electrons from the vacancy of PCN to the absorbed NO molecules resulted from the localization of the solar‐generated electron and NO molecule, thereby contributing to the NO reduction into N2. This work is important to current research work. In general, NO2 and NO3 – are the currently accepted products for PODN by the public, whereas the gaseous N2 as another clean and possible product can straightforwardly desorb from the reactive sites of PCN, thereby reducing the deactivation of photocatalysts and avoiding secondary environmental pollution.[ ] However, the green product of N2 cannot easily be observed and obtained from the NO conversion because of the high dissociation energy of the N≡O bond (632 kJ mol–1).[ ] Therefore, exploring novel photocatalysts that can be used in NO photoreduction is of great importance.

Regulating Molecular Structure

Regulating the electronic structure (energy‐band configuration and bandgap) has been proven to be an ideal and effective strategy to determine the optical absorption ability and redox capacities, contributing to the investigation and advance of visible‐light‐sensitive PCN with optimized performance.[ , , , ] Adjusting and perfecting the conventional systems and electronic structure of the PCN is necessary because of the insufficient absorption and utilization of sunlight.[ , ] Therefore, copolymerizing another similar aromatic structure with PCN precursors as a type of molecular doping strategy is viewed as a noteworthy step to extend the electrons of the aromatic system and modify the electronic band structure of PCN.[ , , ] Ho et al. developed a copolymerization method, in which the monomer of the 2,4,6‐triaminopyrimidine (TAP) was copolymerized into the matrix of PCN, and the tubular PCN was produced through rolling‐up the nanosheets (Figure  ).[ ] The π‐electron conjugated units of PCN were facilitated and enlarged by the introduction of the C4N2 ring from the TAP molecules into the PCN structure. Moreover, the resultant PCN photocatalysts displayed a tunable bandgap and efficient charge kinetics, which resulted in outstanding performance toward the removal of NO gas pollutants. Zhu et al. constructed a perfected π‐conjugated PCN by coordination among 3p orbits of Na (NaOH) and lone electron of N 2p of PCNs with melon structure.[ ] The improved π‐conjugated PCN structure enhanced the seizing capability of visible light, boosted the activation of O2 favored by several active sites, and promoted the directional transfer of charges, thereby demonstrating superior activity toward PODN reaction.
Figure 7

A) Incorporation of TAP into the Network of PCN. Reproduced with permission.[ ] Copyright 2015, American Chemical Society. B) a) Pristine PCN mode. b) Boron atom substitution doping at c) two inequivalent carbon sites or d) three inequivalent nitrogen sites. d) Interstitial doping at pore or interlayers. All samples underwent a subsequent geometry optimization. e) XRD patterns (the small inset represents the (002) peaks of all samples after enlargement) and f) FT‐IR spectra of CN, CNT, and BCNT. g) XPS high‐resolution spectra of B 1s for BCNT and CNT. Reproduced with permission.[ ] Copyright 2018, Elsevier. C) Calculated crystal structures of a) CN, b) CN‐K2, and c) CNNa2. d,e) Top views of the doped layer in (b) and (c), correspondingly. Reproduced with permission.[ ] Copyright 2016, American Chemical Society. D) DFT calculates the electron density distribution of various metals doped in PCN. E) a) NO‐TPD spectra and b) O2‐TPD spectra of PCN and c) M/PCN‐0.2, O2 physical adsorption of PCN, d) schematic diagram of possible adsorption sites for O2, e) O2 forming covalent bonds with functional groups, f) O2 forming hydrogen bonds with functional groups, g) 1H solid‐state nuclear magnetic resonance (NMR) spectra of PCN and M/PCN‐0.2, h) the H atoms in solid‐state NMR spectra, and i) O2 forming covalent bonds with the functional groups. Reproduced with permission.[ ] Copyright 2020, Elsevier.

A) Incorporation of TAP into the Network of PCN. Reproduced with permission.[ ] Copyright 2015, American Chemical Society. B) a) Pristine PCN mode. b) Boron atom substitution doping at c) two inequivalent carbon sites or d) three inequivalent nitrogen sites. d) Interstitial doping at pore or interlayers. All samples underwent a subsequent geometry optimization. e) XRD patterns (the small inset represents the (002) peaks of all samples after enlargement) and f) FT‐IR spectra of CN, CNT, and BCNT. g) XPS high‐resolution spectra of B 1s for BCNT and CNT. Reproduced with permission.[ ] Copyright 2018, Elsevier. C) Calculated crystal structures of a) CN, b) CN‐K2, and c) CNNa2. d,e) Top views of the doped layer in (b) and (c), correspondingly. Reproduced with permission.[ ] Copyright 2016, American Chemical Society. D) DFT calculates the electron density distribution of various metals doped in PCN. E) a) NO‐TPD spectra and b) O2‐TPD spectra of PCN and c) M/PCN‐0.2, O2 physical adsorption of PCN, d) schematic diagram of possible adsorption sites for O2, e) O2 forming covalent bonds with functional groups, f) O2 forming hydrogen bonds with functional groups, g) 1H solid‐state nuclear magnetic resonance (NMR) spectra of PCN and M/PCN‐0.2, h) the H atoms in solid‐state NMR spectra, and i) O2 forming covalent bonds with the functional groups. Reproduced with permission.[ ] Copyright 2020, Elsevier. Atomic doping is extensively proved and investigated to be another vital method in manipulating the electronic structure, primarily concentrating on incorporating external impurities into the photocatalysts.[ , , , ] Various atoms, including metal, nonmetal elements, and combinations, are incorporated into the matrix of PCN to achieve sufficient PODN performance.[ , , , ] For instance, phosphorus‐doped PCN (P/PCN) with a typical optical property and the down‐shifted VB‐edge of P/PCN‐5 exhibited stronger oxidation ability than that of the unmodified PCN, which ensured efficiently photocatalytic NO removal.[ ] The hollow B‐doped PCN tubes were produced by calcining the hybrid of the supramolecular self‐assembled precursors and boric acid, which widened the harvesting ability of visible light and advanced separation and transferability of light‐induced electron–hole pairs, thereby exhibiting the highest NO removal rate (30.4%) compared with the bulk PCN (20.8%) and PCN hollow tubes (22.9%, Figure 7B).[ ] Additionally, self‐doping is also developed to form some defects or vacancies by removing some elements of the photocatalyst and adjusting the energy‐band configuration and bandgap of semiconductor photocatalysts.[ , ] For instance, the carbon self‐doped PCN (substituted the bridging N atoms) could be produced by using a porous carbon foam template, which displayed enlarged surface area, extended near‐infrared light absorption and advanced electron–hole movement and transfer.[ ] The optimized carbon‐doped PCN demonstrated a remarkably high performance toward the PODN in air and exceeded other nonmetal‐doped inorganic materials including Ti‐based and Bi‐based semiconductors. Semiconductors loaded with metals (e.g., K, Cs, Mg, Ca, Sr, Ba, and Pd) by introducing the impurities into the PCN matrix can effectively lower the barrier of the rate‐determining step and mostly inhibit the production of the toxic intermediate (NO2), thereby decreasing the secondary environmental pollution and improving PODN activity.[ , , , ] For instance, Xiong et al. expounded the group IA elements (e.g., K and Na) by doping into the PCN under the sample conditions, investigated the electronic structure and PODN activity with the assistance of experimental and theoretical combination.[ ] Consequently, K‐intercalated PCN exhibited higher visible PODN performance than that of Na‐doped PCN. This variance was the intercalated types of K atoms (bridging interlayer) and Na atoms (introducing into the plane) doped PCN; thus, the K/PCN could provide a delivery channel via bridging the layers, and the Na/PCN increased the recombination of charges because of the promotion of in‐planar electron density (Figure 7C). The group IIA elements (e.g., Mg, Ca, Ba, and Sr) incorporated into the PCN matrix could also provide interlayer electron channels by the formation of coordinate bonds (connecting two adjacent layers with N atoms in the triazine rings of PCN), thereby distorting the PCN structure (Figure 7D,E).[ , , , , ] The surface electronic delocalization was destroyed by the distorted PCN structure, thereby suppressing surface charges recombination and improving the electron transport between two layers. In addition, the functional groups were enhanced by the distorted PCN structure, providing more chemisorption sites for O2. Given the above‐mentioned advantages, the PCN coupled with group IIA elements exhibited superior PODN efficiency compared with the pure PCN. The transition metal (e.g., Pd nanoparticles and Pd quantum dots (QDs)) doped in the PCN also showed a similar positive effect on visible PODN reaction.[ , ] Co‐doping can combine the advantages of single dopants, such as the delocalized electrons and the random transmission of charge in planes, thereby retarding a high charge‐recombination rate and probability.[ , , ] The interlayer energy barrier of PCN could be lowered by intercalating K+ and NO3 – into the interlayer to build a bidirectional electronic transmission channel.[ ] Abundant electrons could be offered to accelerate the O2 activation and ROS production to endow the K+ and NO3 – co‐doped PCN with great visible‐light performance of ODN. This positive result was also evidenced by Cui et al. and Chen et al., and double elements co‐functionalized PCN as an electronic trapping adjuster and mediator to encourage the astringent and localization of intralayer‐delocalized electrons, thereby facilitating the adsorption and activation of gas molecules, expediting the spatial charge kinetics, suppressing toxic NO2 generation.[ , ]

Constructing Composites

Engineering Schottky heterojunctions by incorporating plasmonic metal nanoparticles (e.g., Au, Ag, Cu, and Bi) in photocatalysts have been developed and proven to be a potential way to efficiently decrease the recombination of the light‐excited charges and advance the charge transmission, because of their viability and efficiency for the spatial separation of charges.[ , , ] For instance, Li et al. used NaBH4 as a reducing agent to fabricate monodisperse Au nanoparticle‐supported PCN, exhibiting an enhanced NO oxidation and NO2 inhibition ability.[ ] The promotion could be attributed to the enhanced adsorption/activation of gas molecules favored by the surface plasmon resonance (SPR) Au metal site, the improved separation efficiency of photogenerated charges, the lowered rate‐determining barrier favored by the unique electronic structure of Au/PCN, and the suppressed production of the toxic intermediate (NO2). The semimetal bismuth (Bi) can work as a potential substitute for noble SPR metals because of its low price, easy availability, and conductive properties.[ , , ] Bi can also work as an excellent and stable cocatalyst to lower the overpotential and advance the separation of the charge carriers.[ , ] When Bi, like nanospheres or nanoparticles, was introduced into the PCN nanosheets, the novel nanocomposites exhibited highly enhanced ODN activity and stability with visible light (Figure  ).[ , , ] This enhanced photocatalytic performance of Bi/PCN could be attributed to the co‐contributions of the enhanced optical absorption and the advanced kinetics of charge carriers because of the SPR effects of Bi‐metal and the Schottky heterojunctions production. The enhanced light‐driven e– could also reduce O2 to H2O2 and further convert into ⋅OH by trapping an electron, thereby further improving the NO photooxidation efficiency. Different from a one‐step‐modified PCN photocatalyst, Zhao et al. explored the PCN photocatalyst modified by copper through multistep modifications (Figure 8B).[ ] The obtained Cu/PCN photocatalysts could also improve NO removal activity by increasing electron transfer and ROS generation.
Figure 8

A) Proposed mechanism of the photocatalytic oxidation of NO for the 10% Bi/PCN composite. Reproduced with permission.[ ] Copyright 2017, Elsevier. B) Free energy of several possible modes of a) Cu2+ doping PCN, b) DOS of the PCN, and c) the schematic formation process of various Cu/PCN‐x samples. Reproduced with permission.[ ] Copyright 2019, American Chemical Society. C) The schematic production process to fabricate RGO/HPCNS. D) Schematic of the reaction mechanism for NO removal. C,D) Reproduced with permission.[ ] Copyright 2016, Royal Society of Chemistry.

A) Proposed mechanism of the photocatalytic oxidation of NO for the 10% Bi/PCN composite. Reproduced with permission.[ ] Copyright 2017, Elsevier. B) Free energy of several possible modes of a) Cu2+ doping PCN, b) DOS of the PCN, and c) the schematic formation process of various Cu/PCN‐x samples. Reproduced with permission.[ ] Copyright 2019, American Chemical Society. C) The schematic production process to fabricate RGO/HPCNS. D) Schematic of the reaction mechanism for NO removal. C,D) Reproduced with permission.[ ] Copyright 2016, Royal Society of Chemistry. The PCN‐based heterojunctions constructed with other semiconductors also exhibit accelerated kinetics of photogenerated charges, which improves carrier transfer across the junction favored by the differences in their band structures and provides the space charge separation/transport region favored by the band bending.[ , , , , , ] PCN coupled with graphene‐based materials (π‐conjugated structure and superior electric property) has been focused on improving its conductivity and catalytic performance by enhancing carrier separation/transfer and electron mobility.[ , , , ] The graphene/mesoporous PCN (G/MPCN) and graphene oxide/mesoporous PCN (GO/MPCN) nanocomposites endowed extremely boosted visible‐light‐driven ODN efficiency, which was caused by the enlarged surface nanostructure (accelerating the mass transfer kinetics), the improved the utilization of visible light, the boosted the reduction potential of electrons, and the encouraged the kinetics of charge carriers.[ ] The hollow porous PCN nanosphere (HPCNS) coupled with reduced GO (RGO/HPCNS) also exhibited a NO removal ratio of 64% (600 ppb level) and high stability because of the hollow porous morphology of HPCNS and the grafted RGO on the surface (Figure 8C,D).[ ] Except for the PCN heterojunction constructed from graphene‐based materials, heterojunctions constructed by other semiconductors can also advance the kinetics of charges in the spatial and built‐in electric field.[ , , , , , , ] Band alignment is one of the keys to construct a suitable and efficient heterojunction.[ , ] In general, the common heterojunction types can be primarily divided into the following types: type I heterojunction, type II heterojunction, p–n heterojunction, Z‐scheme heterojunction, and S‐scheme heterojunction based on the charge transfer among different energy bands (Figure  ).[ , , , ] For the type I heterojunction, the electrons and holes generated by light excitation migrate from a high‐potential semiconductor B to the same semiconductor A with relatively low potential. (Figure 9A).[ , , ] This type of migration causes a relatively suppressed separation of light‐excited carriers, but the charge kinetics of the type I heterojunction can be effectively regulated by adjusting the movement rates of charges. For instance, Dong et al. successfully and thermally treated the blended precursors of melamine and urea by in situ creating type I PCNM/PCNU metal‐free isotype heterostructures in view of staggered and aligned bands.[ ] The intrinsic shortcoming of charge kinetics of pristine PCN was decreased and overcome by the creation of type I PCNM/PCNU heterostructures, demonstrating excellent PODN activity and reusability at ppb‐level NO in comparison with PCN counterpart (Figure  ).
Figure 9

Schematic illustration of the separation of electron–hole pairs for A) type I heterojunction, B) type II heterojunction, C) p–n heterojunction. A‐C) Reproduced with permission.[ ] Copyright 2017, Wiley‐VCH. D) indirect Z‐scheme heterojunction, E) direct Z‐scheme heterojunction. D,E) Reproduced with permission.[ ] Copyright 2018, Elsevier. F) S‐scheme heterojunction. Reproduced with permission.[ ] Copyright 2020, Elsevier.

Figure 10

A) Illustration charge transfer of type I PCNM/PCNU heterostructures. Reproduced with permission.[ ] Copyright 2015, Royal Society of Chemistry. B) The proposed photocatalytic mechanism of LaCO3OH/PCN heterojunctions for NO degradation with visible light. Reproduced with permission.[ ] Copyright 2017, Royal Society of Chemistry. C) Photocatalytic mechanism of NO removal under visible‐light irradiation by NICO/PCN‐100: a) before contact, b) after contact, and c) the p–n heterojunction. Reproduced with permission.[ ] Copyright 2020, Elsevier. D) The proposed photocatalytic mechanism of (BiO)2CO3/PCN heterojunctions for NO degradation with visible light. Reproduced with permission.[ ] Copyright 2021, American Chemical Society. E) The mechanism of photocatalytic NO removal of Ag3PO4/Ag/PCN under visible light. Reproduced with permission.[ ] Copyright 2021, Elsevier. F) a) Type II heterojunction mechanism and b) Z‐scheme photocatalytic mechanism of NO removal under visible‐light irradiation by 30% BiOIO3/I–/PCN. Reproduced with permission.[ ] Copyright 2020, Elsevier. G) Photocatalytic mechanism of PI/PCN. Reproduced with permission.[ ] Copyright 2016, American Chemical Society. H) S‐scheme photocatalytic mechanism for Sb2WO6/PCN nanocomposite. Reproduced with permission.[ ] Copyright 2021, Elsevier.

Schematic illustration of the separation of electron–hole pairs for A) type I heterojunction, B) type II heterojunction, C) p–n heterojunction. A‐C) Reproduced with permission.[ ] Copyright 2017, Wiley‐VCH. D) indirect Z‐scheme heterojunction, E) direct Z‐scheme heterojunction. D,E) Reproduced with permission.[ ] Copyright 2018, Elsevier. F) S‐scheme heterojunction. Reproduced with permission.[ ] Copyright 2020, Elsevier. A) Illustration charge transfer of type I PCNM/PCNU heterostructures. Reproduced with permission.[ ] Copyright 2015, Royal Society of Chemistry. B) The proposed photocatalytic mechanism of LaCO3OH/PCN heterojunctions for NO degradation with visible light. Reproduced with permission.[ ] Copyright 2017, Royal Society of Chemistry. C) Photocatalytic mechanism of NO removal under visible‐light irradiation by NICO/PCN‐100: a) before contact, b) after contact, and c) the p–n heterojunction. Reproduced with permission.[ ] Copyright 2020, Elsevier. D) The proposed photocatalytic mechanism of (BiO)2CO3/PCN heterojunctions for NO degradation with visible light. Reproduced with permission.[ ] Copyright 2021, American Chemical Society. E) The mechanism of photocatalytic NO removal of Ag3PO4/Ag/PCN under visible light. Reproduced with permission.[ ] Copyright 2021, Elsevier. F) a) Type II heterojunction mechanism and b) Z‐scheme photocatalytic mechanism of NO removal under visible‐light irradiation by 30% BiOIO3/I–/PCN. Reproduced with permission.[ ] Copyright 2020, Elsevier. G) Photocatalytic mechanism of PI/PCN. Reproduced with permission.[ ] Copyright 2016, American Chemical Society. H) S‐scheme photocatalytic mechanism for Sb2WO6/PCN nanocomposite. Reproduced with permission.[ ] Copyright 2021, Elsevier. For type II heterojunctions, the high‐potential semiconductors A of photogenerated electrons that are excited by light migrate to the low‐potential semiconductors B, and the photogenerated holes are opposite, which is ascribed to the staggering energy levels between semiconductors (Figure 9B).[ , , , ] This type of migration as one of the potential strategies can improve photocatalytic activity by constructing a spatial and built‐in field, thereby effectively separating photogenerated carriers between semiconductors. For instance, Tian et al. in situ fabricated CeO2/PCN hybrid materials by a facile co‐pyrolysis of the precursors of Ce‐based and N‐abundant materials.[ ] The CeO2/PCN composite catalysts possessed brilliant PODN efficiency, which was resulted from the construction of CeO2/PCN type II heterojunction (endowing advanced charge kinetics across the intimate phase interfaces). Wang et al. controllably fabricated a novel heterostructure of hierarchical rouleaux triangle LaCO3OH/PCN nanocomposite by a hydrothermal strategy.[ ] During the hydrothermal process, the PCN served as a structural direct mediator and CO3 2– acted as source significantly affected the morphology manufacturing of LaCO3OH. The booming interfacial charge kinetics was one of the dominant factors for the improvement of LaCO3OH/PCN toward PODN reaction (Figure 10B). In current years, visible‐light‐responded Bi‐based catalysts with lone‐pair distortion of Bi 6s orbitals and hybridization of O 2p and Bi 6s orbitals shows the unique electronic structure, good chemical stability and controlled morphology, which have drawn increasing attention.[ , , ] For instance, the Bi2O2CO3/PCN and layered BiOBr/PCN heterojunctions, and (BiO)2CO3 nanosphere‐decorated PCN composite heterostructure demonstrated the promoted adsorption/activation of NO molecules and accelerated spatial charge separation (Figure 10C); the O2 molecule tended to adsorb on the electron‐rich areas and convert into O2 ⋅– radicals, thereby contributing to the efficient PODN of NO.[ , , ] The construction of PCN‐based p–n heterojunctions is also widely considered and proved to be one of the strategies to improve the dynamics of photogenerated carriers.[ , , ] As shown in Figure 9C, electrons (p‐type semiconductors) excited by light tend to migrate to the CB of n‐type semiconductors, while light‐excited holes are the opposite. This type of carrier migration generates an internal electric field (IEF) in the internal space, which accelerates the separation and migration of charges, resulting in higher dynamic efficiency than the type II heterojunction. For instance, Wang et al. successfully created a composite consisted of hollow Ni–Co bimetal oxide and layered PCN through the method of low‐temperature annealing.[ ] A spatial conductive trend caused by the creation of p–n heterojunction based on the Ni–Co bimetallic oxide and PCN advanced the charge dynamics; and the gas circulation was promoted by the pores of the hollow Ni–Co bimetallic oxide, thereby degrading the NO with visible light and showing predominant reusability (Figure 10D). In general, the above‐mentioned heterojunction can effectively separate light‐excited electrons and holes, thereby promoting PODN activity. However, the redox process that occurs in the above‐mentioned heterojunction is at a relatively low potential because of the specific charge transfer pathways, which sacrificed the partial redox ability of the semiconductors.[ , , ] In addressing this issue, Bard put forward the concept of the Z‐scheme heterojunction (direct/indirect (electron mediator‐assisted) Z‐scheme heterojunction) with a maximized redox potential.[ ] For the indirect Z‐scheme heterojunction, under the light excitation, the worthless electrons that generated at the low‐potential semiconductor (PSII) transferred and reacted with the holes on the high‐potential semiconductor (PSI) through the electron mediator (Pt and Au, Figure 9D).[ , , ] The remaining and effective holes on the PSII and the electrons on the PSI consume their accumulation through redox reactions, thereby achieving efficient separation of light‐generated charges. For instance, Li et al. designed and prepared a novel ternary Z‐scheme PCN/silver (Ag)/silver phosphate (Ag3PO4) photocatalyst using a two‐step method (Figure 10E).[ ] The optimal PCN/Ag/Ag3PO4 shows a 74% removal rate for NO , which was higher than that of the sole PCN and Ag3PO4. The superior performance was attributed to the improved thermodynamics and kinetics, which endowed promoted mass transfer, charge separation and transmission, optical capability, and physical/chemical properties. In addition, other nonmetal electron‐medicated indirect Z‐scheme heterojunction is also developed to improve the NO abatement efficiency driven by visible light. For instance, Wang et al. successfully prepared unique layered iodine (I)‐doped BiOIO3/PCN heterojunction by the method of exchange‐solvothermal (Figure 10F).[ ] The strong PODN activity of BiOIO3/I–/PCN at the ppb‐level was endowed by the close interfacial contact of the Z‐scheme heterojunction, namely, the promoted charge transport efficiency and wide optical range that improved the PODN efficiency was caused by the synergistic heterojunction. Different from the indirect Z‐scheme heterojunction, the charge transfer process of the direct Z‐scheme heterojunction does not need any electronic transmission mediator, and it can also form a built‐in electric field spatially to optimize the redox potential of the semiconductors.[ , , ] This type of charge transfer makes the preparation process of the indirect Z‐scheme heterojunction simpler than that of the direct Z‐scheme heterojunction. For example, Dong et al. constructed a direct Z‐scheme heterojunction consisting of PCN and perylene imides (PI) to address the issues (incomplete oxidation of NO and the photocatalyst deactivation).[ ] The Z‐scheme PI/PCN heterojunction exhibited significant PODN activity (compared with pristine PCN, Figure 10G). The improved PODN activity was attributed to the efficient charge separation of Z‐scheme PI/PCN heterojunctions, which provided stronger oxidized power for the holes and reduced power for electrons, thereby accelerating the ROS generation and NO conversion. The construction of the Z‐type heterojunction not only solves the problem that the photogenerated charge recombines easily in the single‐component semiconductor but also solves the problem of the reduced redox ability of the semiconductors due to the imperfect charge transfer pathway in the traditional heterojunction. Recently, a novel S‐scheme heterojunction is proposed to address the shortcomings of conventional type‐II heterojunction by Fu et al.[ ] The S‐type heterojunction is mainly composed of two n‐type semiconductors (reducing photocatalyst (RP) and oxidizing photocatalyst (OP)). Its band structure is similar to the traditional type II heterojunction, but the type of charge transfer is different. Due to the difference in work function and Fermi level between OP and RP, a built‐in electric field in space is formed. When the two n‐type semiconductors are in contact, their Fermi levels will be rearranged and cause their energy bands to bend. It will promote the recombination of meaningless light‐excited electrons and holes; and effective electrons and holes are retained to participate in following redox reactions, thereby encouraging the efficient separation of photogenerated carriers. For instance, Ren et al. fabricated a novel S‐scheme Sb2WO6/PCN nanocomposite by an ultrasound‐assisted method.[ ] The S‐scheme Sb2WO6/PCN nanocomposite exhibited excellent performance for PODN activity driven by visible light because of the boosted charge dynamics and improved ROS generation (Figure 10H). Therefore, PCN‐based heterojunctions have indeed made great achievements in PODN reaction; however, it is still in its infancy for practical application and commercialization.

PCN for Desulfurization

The emission of sulfur compounds accelerates the erosion of the historical building, destroys soil chemistry, and disturbs the pH of water bodies, thereby jeopardizing marine life.[ , , , ] Moreover, breathing in a toxic climate can result in numerous health concerns (e.g., asthma, heart disease, and respiratory syndrome).[ , , , ] Notably, the source of sulfur compounds emissions is primarily produced by the random and massive release of sulfur fuel oil combustion waste, subsequently causing air pollution, health concerns, acid rain, and global warming.[ , , , ] Considering the above‐mentioned negative and harmful influences of sulfide and the needs of social development, exploring an efficient desulfurization strategy to degrade the sulfur hazards and inhibit sulfide production is necessary. Sulfur‐removal technologies can be generally characterized into two categories: hydrodesulfurization (HDS) technology and non‐HDS technology (Figure  ).[ , , , , ] HDS is widely adapted and revised the desulfurization process in the industry. It can produce low‐sulfur oil; however, the toxic hydrogen sulfide and the reduced octane number in fuel oil are also produced. In addition, HDS is operated under harsh operating conditions, including reacting with H2 at high temperatures (200–450 °C) and pressures (3–6 MPa), and employing expensive catalysts, causing the inability of HDS to produce superlative desulfurization efficiencies.[ , , , , ] Given the limited efficiency and high cost of HDS, non‐HDS technology as an advancement of effective alternative deep desulfurization technologies has been considered, including physical desulfurization (PDS), biological desulfurization (BDS), and chemical desulfurization (CDS).[ , , , , , , , , ] PDS can be performed under mild conditions (low temperature and pressure); however, the adsorption capacity and adsorbent regeneration are rather limited; and it is confronted with a complex and high‐cost recovery of the extraction agent process.[ , ] The development of BDS still faces extreme problems regarding its practical application because of its requirement and limitation of complex reaction equipment/technology, high desulfurization cost, and inefficient biocatalyst.[ , ] The CDS technology exhibits the merits of high desulfurization efficiency and robust catalytic stability, but the high cost, large loss of catalyst, and secondary environmental pollution are identified during the desulfurization process.[ , ] Therefore, developing more efficient desulfurization technologies is necessary, which promotes the deep oxidation of the desulfurization process while reduces the process cost and energy consumption.
Figure 11

General features and development course of the removal of sulfur compounds. Reproduced with permission.[ ] Copyright 2021, Wiley‐VCH.

General features and development course of the removal of sulfur compounds. Reproduced with permission.[ ] Copyright 2021, Wiley‐VCH. Photocatalytic oxidation desulfurization (PODS) is essentially an advanced version of ODS, referring to efficient ROS generation and then react with the C–S–C bond of sulfur compounds, which has received considerable research interest because of its economic, sustainable, and reusable advantages.[ , , , , ] Under this process, sulfur compounds (e.g., BT: benzothiophene, RSH: n‐dodecanethiol, 4,6‐DMDBT: 4,6‐dimethyl dibenzothiophene, Th: thiophene, DBT, CH3SH, etc.) can be converted to SO4 2–, or matching sulfone, and then be absorbed and extracted by an alkaline solution/polar solvent.[ , , , ] To date, a significant development with kinds of photocatalysts is achieved for PODS reaction, which is primarily for inorganic substances (e.g., CeO2, Fe2O3, TiO2, and WO3) to metal‐free organic polymer (PCN).[ , , , , ] The PCN comprised of sp2‐hybridized carbon and nitrogen atoms has been considered as a suitable species with a particular electronic structure, good physicochemical stability, and facile synthesis.[ , , , ] For instance, in 2014, the TiO2/PCN composites that employed in photocatalytic oxidative desulfurization received a surprising activity, which was ascribed to the increased absorption of the optical region.[ ] This work implied the greatest potential of PCN utilization in PODS applications, attracting considerable attention from researchers. However, the PODS efficiency remains moderate because of the low specific surface area of the PCN. In 2015, Zhu et al. used PCN with enlarged surface area as the support of heteropoly acid, and the obtained catalyst displayed excellent reusability in the ODS process.[ ] In 2016, MPCN as a single heterogeneous photocatalyst was first introduced into the ODS reaction, which could oxidate DBT with visible light and reached 100% under optimal conditions for the desulfurization rate of model fuel.[ ] Given the suitable band position of the PCN, the photogenerated electrons of CB that were excited by the visible light exhibited an extraordinary capacity to reduce O2 and formed a strong oxidized O2 ⋅–. The intermediate products are mineralized and converted to SO4 2– and the corresponding sulfone after combining with the ROS or h+, and the specific conversion processes are shown in the following equations[ ] However, PCN still has limitations, which needs to be addressed, including insufficient optical absorption, inhibited charge dynamics, inadequate reaction sites, and agglomerate photocatalysts.[ , , , ] In addressing the above‐mentioned obstacles, nanostructure design, electronic structure modulation, and heterostructure construction based on PCN are used to achieve efficient PODS activity.[ , , ] Considering the limited amount of PODS reviews, we hypothesize that summarizing the recent development of PCN on PODS reaction is necessary. Some recently reported PCN‐based photocatalysts with various strategies used in POND are shown in Table  .
Table 2

Summary of recently reported PCN‐based photocatalysts utilized in desulfurization reaction

PhotocatalystsTypesExperimental conditionsLight sourceAnalyzerMain products and sulfur compounds removal ratioRefs.
Mesoporous PCNNanostructure design

Reactor: 100 mL

Cat. a) : 0.1 g

Conc. b) : 100 ppmw

Time c) : 100 min

S Source: DBT d) , 4,6‐DMDBT e) , and BT f)

Solvent: n‐octane

300 W Xe lamp (λ > 420 nm)WK‐2D

Products: DBTO2

η g) (S): 100% (4,6‐DMDBT: 30 min.; DBT and BT: 90 min)

[ 107 ]
Na/PCNElectronic structure regulation

Reactor: 20 mL

Cat.: 0.1 g

Conc.: 200 µg g−1

Time: 360 min

S Source: DBT Solvent: n‐octane

300 W Xe lamp (λ > 420 nm)Agilent GC h) ‐7890B

Products: SO4 2–

η(S): 66.1%

[ 300 ]
Ag/PCNElectronic structure regulation

Reactor: unmarked

Cat.: 0.1 g

Conc.: 5 ppm

Time: 180 min

S Source: CH3SH

Solvent: no

W‐type fluorescent lamps (λ > 420 nm)GC‐14B with FID i)

Products: SO4 2–

η(S): 93%

[ 116 ]
Ti3C2/PCNHeterostructure construction

Reactor: 20 mL

Cat.: 0.05 g

Conc.:140 µg g−1

Time: 180 min

S Source: Th j)

Solvent: n‐octane

300 W Xe lamp (λ > 420 nm)Agilent GC‐7890B

Products: SO4 2–

η(S): 72%

[ 66 ]
CeF3/PCNHeterostructure construction

Reactor: 200 mL

Cat.: 0.1 g

Conc.:140 µg g−1

Time: 180 min

S Source: DBT

Solvent: n‐octane

300 W Xe lamp (λ > 420 nm)UV fluorescence

Products: DBTO2

η(S): 84.2%

[ 301 ]
(Bmin)3PMo12O40/PCNHeterostructure construction

Reactor: 25 mL

Cat.: 0.05 g

Conc.:1000 ppm

Time: 240 min

S Source: DBT

Solvent: n‐octane

250 W high‐pressure sodium lampAgilent GC‐6890

Products: DBTO2

η(S):99.1% (DBT)

[ 302 ]
ZnTcPc/PCNHeterostructure construction

Reactor: 100 mL

Cat.: 0.02 g

Conc.: 800 μL L–1

Time: 240 min

S Source: Th

Solvent: n‐octane

400 W halogen lampAgilent GC‐6890

Products: SO4 2–

η(S): 72%

[ 303 ]
TiO2/PCNHeterostructure construction

Reactor: 20 mL

Cat.: 0.2 g

Conc.: 500/250 ppm

Time: 120 min

S Source: DBT, BT and RSH k)

Solvent: acetonitrile

250 W high pressure Hg lamp (UV light)Agilent GC‐7890A

Products: BTO2/DBTO2

η(S): 100% (DBT); ≈90% (BT/RSH)

[ 293 ]
CeO2/ATP l) /PCNHeterostructure construction

Reactor: 200 mL

Cat.: 0.1 g

Conc.:200 ppm

Time: 180 min

S Source: DBT

Solvent: n‐octane

300 W Xe lamp (λ > 420 nm)UV fluorescence (THA2000S)

Products: DBTO2

η(S): 98%

[ 129 ]
BiVO4/PCN/SiO2 Heterostructure construction

Reactor: unmarked

Cat.: 0.2 g

Conc.: 300 ppm

Time: 300 min

S Source: DBT Solvent: dodecane

Xe lamp (λ > 420 nm)GC/FID‐9790 m)

Products: DBTO2

η(S): 99%

[ 119 ]
CuO–ZnO/PCNHeterostructure construction

Reactor: 120 mL

Cat.: 0.05 g

Conc.: 150 ppm

Time: 30 min

S Source: DBT

Solvent: ethanol

200 W lamp (λ > 420 nm)Agilent GC 7890/MS n) −5975C

Products: DBTO2

η(S): 84.5%

[ 304 ]
ZnM‐LDHs/PCNHeterostructure construction

Reactor: 250 mL

Cat.: 0.18 g

Conc.: 150 ppm

Time: 180 min

S Source: DBT, 4,6‐DMDBT, and BT Solvent: acetonitrile

500 W mercury lamp (λ > 420 nm)KY3000‐SN

Products: DBTO2

η(S): 96.8%

[ 305 ]
BiOI/I3–/PCNHeterostructure construction

Reactor: 120 mL

Cat.: 0.05 g

Conc.: 70 ppm

Time: 30 min

S Source: CH3SH Solvent: ethanol

8 W LED belt (440–490 nm)Agilent GC‐7890A

Products: SO4 2–

η(S): 94.17%

[ 130 ]

The mass of the photocatalysts (Cat.)

The concentration of Sulfur compounds (Conc.)

Irradiation time (Time)

Dibenzothiophene (DBT)

4,6‐Dimethyl dibenzothiophene (4,6‐DMDBT)

Benzothiophene (BT)

The removal efficiency η (%) of pollutant was calculated as: η (%) = (1 − C/C 0) × 100%

Gas chromatograph (GC)

Flame ionized detector (FID)

Thiophene (Th)

n‐Dodecanethiol (RSH)

Attapulgite (ATP)

GC/FID‐9790, Fuli, Hangzhou, China (GC/FID‐9790)

Mass spectrometer (MS).

Summary of recently reported PCN‐based photocatalysts utilized in desulfurization reaction Reactor: 100 mL Cat. : 0.1 g Conc. : 100 ppmw Time : 100 min S Source: DBT , 4,6‐DMDBT , and BT Solvent: n‐octane Products: DBTO2 η (S): 100% (4,6‐DMDBT: 30 min.; DBT and BT: 90 min) Reactor: 20 mL Cat.: 0.1 g Conc.: 200 µg g−1 Time: 360 min S Source: DBT Solvent: n‐octane Products: SO4 2–‐ η(S): 66.1% Reactor: unmarked Cat.: 0.1 g Conc.: 5 ppm Time: 180 min S Source: CH3SH Solvent: no Products: SO4 2–‐ η(S): 93% Reactor: 20 mL Cat.: 0.05 g Conc.:140 µg g−1 Time: 180 min S Source: Th Solvent: n‐octane Products: SO4 2–‐ η(S): 72% Reactor: 200 mL Cat.: 0.1 g Conc.:140 µg g−1 Time: 180 min S Source: DBT Solvent: n‐octane Products: DBTO2‐ η(S): 84.2% Reactor: 25 mL Cat.: 0.05 g Conc.:1000 ppm Time: 240 min S Source: DBT Solvent: n‐octane Products: DBTO2 η(S):99.1% (DBT) Reactor: 100 mL Cat.: 0.02 g Conc.: 800 μL L–1 Time: 240 min S Source: Th Solvent: n‐octane Products: SO4 2–‐ η(S): 72% Reactor: 20 mL Cat.: 0.2 g Conc.: 500/250 ppm Time: 120 min S Source: DBT, BT and RSH Solvent: acetonitrile Products: BTO2/DBTO2 η(S): 100% (DBT); ≈90% (BT/RSH) Reactor: 200 mL Cat.: 0.1 g Conc.:200 ppm Time: 180 min S Source: DBT Solvent: n‐octane Products: DBTO2 η(S): 98% Reactor: unmarked Cat.: 0.2 g Conc.: 300 ppm Time: 300 min S Source: DBT Solvent: dodecane Products: DBTO2 η(S): 99% Reactor: 120 mL Cat.: 0.05 g Conc.: 150 ppm Time: 30 min S Source: DBT Solvent: ethanol Products: DBTO2 η(S): 84.5% Reactor: 250 mL Cat.: 0.18 g Conc.: 150 ppm Time: 180 min S Source: DBT, 4,6‐DMDBT, and BT Solvent: acetonitrile Products: DBTO2 η(S): 96.8% Reactor: 120 mL Cat.: 0.05 g Conc.: 70 ppm Time: 30 min S Source: CH3SH Solvent: ethanol Products: SO4 2– η(S): 94.17% The mass of the photocatalysts (Cat.) The concentration of Sulfur compounds (Conc.) Irradiation time (Time) Dibenzothiophene (DBT) 4,6‐Dimethyl dibenzothiophene (4,6‐DMDBT) Benzothiophene (BT) The removal efficiency η (%) of pollutant was calculated as: η (%) = (1 − C/C 0) × 100% Gas chromatograph (GC) Flame ionized detector (FID) Thiophene (Th) n‐Dodecanethiol (RSH) Attapulgite (ATP) GC/FID‐9790, Fuli, Hangzhou, China (GC/FID‐9790) Mass spectrometer (MS).

Research Progress of PCN for Desulfurization

In general, heteroatom doping is considered to be an effective and recommendable strategy to alter the electronic structures of the PCN.[ , , , ] This modification will endow PCN with unoccupied molecular orbitals. This promotes the charge separation capability, hindering the recombination of solar‐excited electron–hole pairs, and contributes toward visible‐light responsivity. For instance, Zhang et al. reported the NaCl‐assisted uniform doping of Na in PCN matrix via a method of mixed‐calcination.[ ] The synthetic method resulted in the production of a porous and highly dispersed structure, thereby improving the surface energy, increasing the optical‐harvesting capability, and retarding the recombination of solar‐excited electron–hole pairs. During the whole PODS process, a promotion effect was produced by ROS generation from the reaction of electron and O2. Consequently, the as‐synthesized photocatalysts revealed excellent Th desulfurization performance. MXenes as layered materials have been reported and participated in various fields.[ , ] A composition of semiconductors and MXene may be used to produce a Schottky heterostructure to enhance the performance of photocatalytic reaction by primarily facilitating the dynamics of photoinduced electrons and holes.[ , , ] A Ti3C2 (typical MXene) as an efficient and low‐cost co‐catalyst was chosen to couple with PCN and then applied in the PODS reaction by Li et al.[ ] Constructing a Schottky barrier composed of Ti3C2 and PCN could effectively improve the kinetic efficiency of photogenerated charges, provide an ideal electronic storage library, and promote the generation of ROS to accelerate the transformation of the final product. In addition, PCN nanosheets that dispersed on mesoporous silica and then hybridized with visible‐light‐responsive BiVO4 exhibited as high as 99% conversion of DBT. Heterojunction photocatalysts construction based on coupling two semiconductors depend on the band potential of the CB/VB and band alignment from a thermodynamic point of view.[ , , , , ] In addition, heterojunction photocatalysts can solve the drawbacks and limits of single‐component catalysts endowed with weak redox capability, inefficient catalytic efficiency, and inappropriate CB and VB positions. The CeF3 photocatalyst has aroused much attention and is regarded as an optical component because of the contribution of charge, optical, and ionic conductivity response.[ ] The introduction of CeF3 into the PCN by constructing a heterojunction is viewed as a potential photocatalyst to increase the activity and stability. For instance, Lu et al. utilized CeF3 nanoparticles to decorate the PCN nanosheets and fabricate CeF3/PCN nanocomposites with well band alignment by the method of microwave hydrothermal (Figure 12A).[ ] The well‐defined CeF3/PCN heterojunction could be endowed with the effective separation of photogenerated electrons and holes, and the synergistic effect of the CeF3/PCN type II nanocomposite exhibited the superior degradation rate of DBT with visible light. Similar and positive results could be achieved from type II zinc phthalocyanine/PCN (ZnTcPc/PCN) composites by Zhang et al.[ ] In addition, the ternary CeO2/attapulgite (ATP)/PCN noncompounds were created by a facile self‐assembly method, which effectively produced an enlarged surface area (enhanced adsorption and reaction sites) and prevented the generation of restacked PCN.[ ] The extended adsorption edge of the optical and the facilitated kinetics of charges was also achieved by the synergetic effect of CeO2/PCN type II heterojunctions, thereby converting 98% of DBT and exhibiting excellent recyclability (Figure  ).
Figure 12

A) Schematic illustration of the photocatalytic mechanism of the CeF3/PCN composite. Reproduced with permission.[ ] Copyright 2020, Elsevier. B) Photocatalytic desulfurization mechanism of CeO2/ATP/PCN ternary nanocomposite. Reproduced with permission.[ ] Copyright 2017, Elsevier. C) Conversation pathway of adsorption and photocatalytic oxidation of CH3SH. Reproduced with permission.[ ] Copyright 2018, American Chemical Society. D) Z‐scheme heterostructure of the photocatalytic oxidation of ZnM‐LDHs/PCN (M = Al, Cr). Reproduced with permission.[ ] Copyright 2020, American Chemical Society.

A) Schematic illustration of the photocatalytic mechanism of the CeF3/PCN composite. Reproduced with permission.[ ] Copyright 2020, Elsevier. B) Photocatalytic desulfurization mechanism of CeO2/ATP/PCN ternary nanocomposite. Reproduced with permission.[ ] Copyright 2017, Elsevier. C) Conversation pathway of adsorption and photocatalytic oxidation of CH3SH. Reproduced with permission.[ ] Copyright 2018, American Chemical Society. D) Z‐scheme heterostructure of the photocatalytic oxidation of ZnM‐LDHs/PCN (M = Al, Cr). Reproduced with permission.[ ] Copyright 2020, American Chemical Society. Different from the type II heterojunctions, the Z‐scheme heterojunctions maximize the redox ability of the semiconductor component through a zigzag charge transfer mechanism and provide an IEF to promote the separation/transmission dynamics of the electron–hole pairs.[ , , , ] For instance, Hu et al. synthesized a self‐stabilized Z‐scheme heterojunction photocatalyst of I3–‐containing BiOI ultrathin nanosheets/porous PCN (BiOI/I3–/PCN) by a facile solvothermal method (Figure 12C).[ ] The indirect BiOI/I3–/PCN heterojunction presented a dramatically PODS efficiency toward CH3SH removal in comparison with pure BiOI and PCN because of the promoted separation dynamics and redox potential of light‐excited charge. The pathway of photocatalytic CH3SH removal suggested the partial oxidization of the adsorbed CH3SH and the cleaved C–S bond, which was primarily endowed by the active N atoms (PCN) and Bi‐metal (BiOI), thereby facilitating the formation and oxidation capacity of ROS. Huang et al. successfully synthesized direct Z‐scheme photocatalysts of ZnM‐LDHs/PCN (M = Al, Cr) by electrostatic self‐assembly (Figure 12D).[ ] Photocatalytic desulfurization of ZnAl‐LDHs/PCN and ZnCr‐LDHs/PCN could reach above 95%, which was primarily ascribed to the improved carrier transfer, the suppressed electron–hole recombination, and the improved redox potential. A triplex CuO–ZnO/PCN dual Z‐scheme heterojunction was achieved via a multistep ultrasound‐assisted hydrothermal procedure, showing a 99.1% desulfurization rate and excellent stability under visible‐light‐irradiation.[ ] The outstanding photocatalytic performance was originated from the improved specific surface area and charge kinetics favored by the production of dual Z‐scheme CuO‐ZnO/PCN nanocomposites.

PCN for VOC Removal

VOC (formaldehyde (HCHO), benzene, toluene, ethylbenzene, and xylene (BTEX)) are primarily produced by exhaust gas from fuel combustion and chemicals from indoor decoration materials, which are ubiquitous in the atmospheric environment, posing great harm to human health.[ , , , , , , ] A variety of approaches are identified for controlling VOC in indoor environments such as source control, ventilation, and air cleaning.[ , , , , ] Large equipment (e.g., a light source, plasma equipment, or heating equipment) is necessary for the emission source control and ventilation, making this process complicated and increasing footprint costs.[ , , ] At present, air purification gradually remains to be a potential method because of the restraint in the secondary environmental pollution production, which involves diverse control techniques, for example, physical adsorption, biological treatment and chemical oxidation.[ , , , , , , ] Compared with physical adsorption and biological treatment, the photocatalytic decomposition of VOC is considered to be a potential and sustainable chemical oxidation method due to the contribution of its high efficiency and reusability, simple operation, and nonpolluting characteristics.[ , ] It can degrade VOC to low‐toxicity products (carbon dioxide (CO2) and water (H2O)) without generating other harmful by‐products at ambient temperature, which promotes long‐term environmental protection.[ , ] In the past decades, several kinds of research have been conducted and investigated in the photocatalytic decomposition of VOC, which address indoor pollution issues.[ , ] TiO2 as a dominant photocatalyst is extensively studied and carried out in the VOC decomposition because of the advantages of the suitable oxidative capability, superior anticorrosion and reusability.[ ] However, the response of the TiO2 to UV light (≈4% of solar energy) seriously limits its practical application. The metal‐free and visible‐light‐responsive PCN catalysts have gained increasing interest, which is ascribed to the enlarged specific surface area for mass transfer and reactive sites supply, suitable and adjustable electronic structure for ROS generation, abundant functional groups/defects for coupling other useful species.[ , , ] These characteristics lead to boosted chemical stability, optical absorption, and adsorption capacity for the gas molecules, showing great potential for photocatalytic VOC removal. For the first time, Yu et al. created a direct TiO2/PCN Z‐scheme noncompounds through a facile calcination route.[ ] The introduced PCN‐based Z‐scheme noncompounds showed a great influence on the photocatalytic decomposition of HCHO in the air because of the efficient spatial separation kinetics of light‐induced charge carriers. In general, the formation processes of the intermediates during the photooxidation of HCHO are shown in the following equations[ ] However, the efficiency of PCN photocatalysts on removing VOC is still moderate because of the limited utilization of the visible light, sluggish charge kinetics and severe aggregations of photocatalysts. The electronic structure regulation and heterostructure construction on PCN are rapidly developed to enlarge the exploitation of PCN photocatalysts on VOC removal, showing the importance and development of this field.[ , , , ] Here, we reviewed the catalyst preparation/synthesis, measurements of catalytic activity, and discussion/understanding of the activity enhancement and catalytic mechanism in the VOC photooxidation. Some recently reported PCN‐based photocatalysts with various strategies used in VOC removal are shown in Table  .
Table 3

Summary of recently reported PCN‐based photocatalysts utilized in VOC removal

PhotocatalystsTypesExperimental conditionsLight sourceAnalyzerMain products and VOC removal ratioRefs.
Porous PCN nanosheetsNanostructure design

Reactor: 1.5 L

Cat. a) : 0.5 g

Conc. b) : 20 L

VOC: HCHO

Time c) : 6 h

Yellow LED light (λ = 585 nm)Spectrophotometer

Products: CO2, H2O

η d) (HCHO): 56.32%

[ 327 ]
K/PCNElectronic structure regulation

Reactor: 6 L

Cat.: 0.1 g

Conc.: 300 ppm

VOC: HCHO

Time: 24 min

350 W Xe lamp (λ > 420 nm)Innova 1412 e)

Products: CO2, H2O

η(HCHO): 90%

[ 118 ]
Ag/PCNElectronic structure regulation

Reactor: 1 L

Cat.: 4 mg

Conc.: 700 ppmv

VOC: toluene

Time: 6–8 h

6 W LED lamps (λ = 400 nm)

Agilent GC

6890

Products: CO2, H2O

η(HCHO): 95%

[ 328 ]
Sb/PCNElectronic structure regulation

Reactor: 6 L

Cat.: 0.4 mg cm−2

Conc.: 1 L

VOC: acetone, styrene, and cumene

Time: 180 min

6 W daylight lamps (λ > 390 nm)GC‐2010 Plus

Products: CO2, H2O

η(acetone/ cumene): ≈80%

[ 329 ]
C/PCNElectronic structure regulation

Reactor: 20 L

Cat.: 1 g

Conc.: 50 ppm

VOC: HCHO

Time: 300 min

250 W HPML f) (λ > 420 nm)TU‐1901 g)

Products: CO2, H2O

η(HCHO): 84.63%

[ 325 ]
C/O co‐doped PCNComposite construction

Reactor: 20 L

Cat.: 50 mg

Conc.: 1 mL

VOC: toluene

Time: 180 min

300 W Xe lamp (λ > 420 nm)GC‐2010

Products: BZH

η(HCHO): 1.02%

[ 330 ]
Bi12TiO20 /PCNComposite construction

Reactor: 600 mL

Cat.: 0.5 g

Conc.:160 ppm

VOC: HCHO

Time: 420 min

300 W Dy lamp (λ ≥ 400 nm)Innova 1412

Products: CO2

η(HCHO): 75%

[ 331 ]
Ag3PO4/PCNComposite construction

Reactor: 42 mL

Cat.: 0.05 g

Conc.: 0.5 mg m–3

VOC: HCHO

Time: 600 min.

420 nm monochrome LEDPOV‐18 h)

Products: CO2

η(HCHO): 22.4%

[ 332 ]
Ag‐ZnO/PCNComposite construction

Reactor: 40 L

Cat.: 0.2 g

Conc.:1.7 ppm

VOC: HCHO

Time: 180 min

350 W Xe lampGAS Tiger 2000‐CH2O‐L i)

Products: CO2

η(HCHO): 81.2%

[ 138 ]
TiO2/PCN/waste zeolitesComposite construction

Reactor: 40 L

Cat.: 0.15 g

Conc.:1.2 ppm

VOC: HCHO

Time: 180 min

300 W Xe lamp (λ >420 nm)C‐XP‐308B j)

Products: CO2

η(HCHO): 81.2%

[ 333 ]
Bi2MoO6/Bi/PCNComposite construction

Reactor: 2.2 L

Cat.: 0.015 g

Conc.:1600 ppm

VOC: HCHO

Time: 600 min

300 W Xe lamp (λ > 420 nm)Online gas infrared detector and GC k) detector

Products: CO2, H2O

η(HCHO): 98.80%

[ 135 ]
AgFeO2/PCNComposite construction

Reactor: 100 mL

Cat.: 0.5 g

Conc.: 20 mg L−1

VOC: HCHO

Time: 180 min

300 W Dy lamp (λ > 400 nm)UV1750 l)

Products: CO2

η(HCHO): 94%

[ 334 ]
TiO2/PCNComposite construction

Reactor: 15 L

Cat.: 0.3 g

Conc.: 170 ppm

VOC: HCHO

Time: 50 min

365 nm UV lampModel UV‐A m)

Products: CO2, H2O

η(HCHO): ≈90%

[ 106 ]
STO/TN/N‐PCNComposite construction

Reactor: unmarked

Cat.: 0.2 g

Conc.: 1000 ppm

VOC: toluene

Time: 360 min

300W Xe lamp (λ > 420 nm)GC

Products: CO2

η(toluene): ≈93%

[ 335 ]
BiVO4/PCNComposite construction

Reactor: unmarked

Cat.: 0.1 g

Conc.: 25 ppm

VOC: toluene

Time: 480 min

300 W Xe lamp (λ > 400 nm)GC/FID 9790 n)

Products: CO2

η(toluene): 68.2%

[ 336 ]
WO3/PCNComposite construction

Reactor: unmarked

Cat.: unmarked

Conc.: 2000 ppm

VOC: toluene

Time: 48 h

LED lamp (435 nm)GC‐8A o)

Products: CO2

η(toluene): 80%

[ 63 ]
PCN nanosheets/textileNanostructure design

Reactor: 10 L

Cat. a) : 0.5 g

Conc. b) : 100 ppm

VOC: HCHO

Time c) : 20 min

300 W Xe lamp (λ > 420 nm)GC‐2014C

Products: CO2, H2O

η e) (HCHO): 100%

[ 337 ]
Ag‐BTiO2/PCNComposite construction

Reactor: 83.2 mL

Cat.: 0.5 g

Conc.: 1 ppm

VOC: m‐xylene

Time: 300 min

8 W lamp (λ = 400‒720 nm)GC‐MS

Products: CO2

η(m‐xylene): 79%

[ 338 ]
H3PW12O40/PCNComposite construction

Reactor: 300 mL

Cat.: 135 mg

Conc.: 500 L

VOC: m‐xylene

Time: 120 min

300 W Xe lampsAgilent 1200 HPLC

Products: BZH, CO2

η(m‐xylene): 90.1%

[ 313 ]
V2O5/PCNComposite construction

Reactor: 53 mL

Cat.: 30 mg

Conc.: 0.1 ppm

VOC: p‐xylene

Time: unmarked

150 W Xe lampGC‐MS

Products: CO2

η(p‐xylene): 97%

[ 339 ]
Bi2MoO6/PCNComposite construction

Reactor: 25 mL

Cat.: 40 mg

Conc.: 0.1 ppm

VOC: toluene

Time: 180 min

300 W Xe lamp (λ > 400 nm)GCMS‐QP2010

Products: BZH

η(toluene): ≈90%

[ 340 ]
MnO x /PCNComposite construction

Reactor: unmarked

Cat.: 0.4 mg cm–2

Conc.: 700 ppmv

VOC: toluene

Time: 6–10 h

6 W sunlight‐type lampsAgilent GC 6890

Products: BZH, CO2

η(toluene): ≈85%

[ 341 ]
TiO2/PCNComposite construction

Reactor: unmarked

Cat.: 0.4 mg cm−2

Conc.: 100–200 ppmv

VOC: toluene

Time: 4 h

6 W Fluorescent UVAgilent GC 6890

Products: BZH, CO2

η(toluene): 96.4%

[ 342 ]
CeO2–TiO2/PCNComposite construction

Reactor: unmarked

Cat.: 40 mg

Conc.: 700 ppmv

VOC: toluene

Time: 6–10 h

6 W Fluorescent UVAgilent GC 6890

Products: BZH, CO2

η(toluene): 95%

[ 343 ]
ZnO/NiMoO4/PCNComposite construction

Reactor: 1.9 L

Cat.: unmarked

Conc.: 4000 μmol L–1

VOC: toluene

Time: 120 min

8 W ultraviolet lampAgilent 7890A

Products: BZH, CO2

η(toluene): 95%

[ 344 ]
BiPO4/PCNComposite construction

Reactor: 120 mL

Cat.: 0.1 g

Conc.: 120 ppm

VOC: toluene

Time: 240 min

500 W Xe lamp (λ > 400 nm)Agilent GC 7890A

Products: BZH, CO2

η(toluene): 82%

[ 345 ]
In2S3/PCNComposite construction

Reactor: unmarked

Cat.: 50 mg

Conc.: unmarked

VOC: toluene

Time: 180 min

500 W Xe lamp (λ >400 nm)GC‐MS

Products: BZH, CO2

η(toluene): 89.7%

[ 346 ]
ZSM‐4/Mn‐PCNComposite construction

Reactor: unmarked

Cat.: 1 g

Conc.: 25 ppm

VOC: toluene

Time: 90 min

4 W VUV lampsGC‐MS

Products: BZH, CO2

η(toluene): 90%

[ 347 ]
TiO2/PCN/cotton fabricsComposite construction

Reactor: 350 mL

Cat.: 0.58 g

Conc.: 0.2 µL

VOC: toluene

Time: 50 min

4 W VUV lampsGC‐MS

Products: BZH, CO2

η(toluene): 93.64%

[ 348 ]
BiVO4/PCNComposite construction

Reactor: 10 mL

Cat.: 100 mg

Conc.: 25 ppm

VOC: toluene

Time: 8 h

300 W Xe lamps (λ > 400 nm)GC/FID‐9790

Products: BZH, CO2

η(toluene): 68.2%

[ 336 ]
Cs x WO3/PCNComposite construction

Reactor: 10 mL

Cat.: 50 mg

Conc.: 200 ppm

VOC: HCHO

Time: 240 min

300 W Xe lamps (λ > 400 nm)Model 1412

Products: BZH,

CO2

η(HCHO): 100%

[ 312 ]
NiWO4/PCNComposite construction

Reactor: 1 L

Cat.: 0.5 g

Conc.: 1000 ppm

VOC: toluene

Time: 240 min

100 W lamps (λ > 400 nm)GC‐FID

Products: BZH,

CO2

η(toluene): 100%

[ 349 ]
Ag3PO4/PCN/PVAComposite construction

Reactor: 143 mL

Cat.: 0.5 g

Conc.: 440 ppmv

VOC: toluene

Time: 80 min

Xe lamps (λ > 420 nm)Techcomp 7900

Products: BZH,

CO2

η(toluene): 20.79%

[ 133 ]
CdS/PCNComposite construction

Reactor: 143 mL

Cat.: 100 mg

Conc.:10 mmol

VOC: toluene

Time: 180 min

Xe lamps (λ > 420 nm)GCMS‐QP2010

Products: BZH, CO2

η(toluene): 83%

[ 350 ]
α‐Fe2O3/Ag/PCNComposite construction

Reactor: 17 mL

Cat.: 0.25 g

Conc.:20 ppm

VOC: ethylbenzene

Time: 180 min

50 W white LED lamps (λ > 420 nm)Spectroradiometer

Products: CO2

η(ethylbenzene): 25%

[ 351 ]
α‐Fe2O3/Cu/PCNComposite construction

Reactor: 4.536 mL

Cat.: 0.25 g

Conc.:20 ppm

VOC: ethylbenzene

Time: unmarked

50 W white LED lamps (λ > 420 nm)GC‐MS

Products: CO2

η(ethylbenzene): 37.5%

[ 352 ]

The mass of the photocatalysts (Cat.)

The concentration of Sulfur compounds (Conc.)

Irradiation time (Time)

The removal efficiency η (%) of pollutant was calculated as: η (%) = (1 − C/C 0) × 100%

Photoacoustic IR multi‐gas monitor, INNOVA Air Tech 95 Instruments Model 1412 (Innova 1412)

High‐pressure mercury lamp (HPML)

TU‐1901 UV–vis spectrophotometer (TU‐1901)

POV‐18 volatile organic degradation instrument, SUNCAT, China (POV‐18)

GAS Tiger 2000‐CH2O‐L, Shenzhen Wanandi Technology Co., Ltd. (GAS Tiger 2000‐CH2O‐L)

Shin Kosumosu Denki Form‐tector, C‐XP‐308B (C‐XP‐308B)

Gas chromatograph (GC)

UV–vis spectrophotometer, UV1750, Shimadzu Corporation, Japan (UV1750)

UV radiometer, Model UV‐A, made in the Photoelectric Instrument Factory of Beijing Normal University (Model UV‐A)

GC/FID‐9790, Fuli, Hangzhou, China (GC/FID‐9790)

Shimadzu GC‐8A, FID detector (GC‐8A).

Summary of recently reported PCN‐based photocatalysts utilized in VOC removal Reactor: 1.5 L Cat. : 0.5 g Conc. : 20 L VOC: HCHO Time : 6 h Products: CO2, H2O η (HCHO): 56.32% Reactor: 6 L Cat.: 0.1 g Conc.: 300 ppm VOC: HCHO Time: 24 min Products: CO2, H2O η(HCHO): 90% Reactor: 1 L Cat.: 4 mg Conc.: 700 ppmv VOC: toluene Time: 6–8 h Agilent GC 6890 Products: CO2, H2O η(HCHO): 95% Reactor: 6 L Cat.: 0.4 mg cm−2 Conc.: 1 L VOC: acetone, styrene, and cumene Time: 180 min Products: CO2, H2O η(acetone/ cumene): ≈80% Reactor: 20 L Cat.: 1 g Conc.: 50 ppm VOC: HCHO Time: 300 min Products: CO2, H2O η(HCHO): 84.63% Reactor: 20 L Cat.: 50 mg Conc.: 1 mL VOC: toluene Time: 180 min Products: BZH η(HCHO): 1.02% Reactor: 600 mL Cat.: 0.5 g Conc.:160 ppm VOC: HCHO Time: 420 min Products: CO2 η(HCHO): 75% Reactor: 42 mL Cat.: 0.05 g Conc.: 0.5 mg m–3 VOC: HCHO Time: 600 min. Products: CO2 η(HCHO): 22.4% Reactor: 40 L Cat.: 0.2 g Conc.:1.7 ppm VOC: HCHO Time: 180 min Products: CO2 η(HCHO): 81.2% Reactor: 40 L Cat.: 0.15 g Conc.:1.2 ppm VOC: HCHO Time: 180 min Products: CO2 η(HCHO): 81.2% Reactor: 2.2 L Cat.: 0.015 g Conc.:1600 ppm VOC: HCHO Time: 600 min Products: CO2, H2O η(HCHO): 98.80% Reactor: 100 mL Cat.: 0.5 g Conc.: 20 mg L−1 VOC: HCHO Time: 180 min Products: CO2 η(HCHO): 94% Reactor: 15 L Cat.: 0.3 g Conc.: 170 ppm VOC: HCHO Time: 50 min Products: CO2, H2O η(HCHO): ≈90% Reactor: unmarked Cat.: 0.2 g Conc.: 1000 ppm VOC: toluene Time: 360 min Products: CO2 η(toluene): ≈93% Reactor: unmarked Cat.: 0.1 g Conc.: 25 ppm VOC: toluene Time: 480 min Products: CO2 η(toluene): 68.2% Reactor: unmarked Cat.: unmarked Conc.: 2000 ppm VOC: toluene Time: 48 h Products: CO2 η(toluene): 80% Reactor: 10 L Cat. : 0.5 g Conc. : 100 ppm VOC: HCHO Time : 20 min Products: CO2, H2O η (HCHO): 100% Reactor: 83.2 mL Cat.: 0.5 g Conc.: 1 ppm VOC: m‐xylene Time: 300 min Products: CO2 η(m‐xylene): 79% Reactor: 300 mL Cat.: 135 mg Conc.: 500 L VOC: m‐xylene Time: 120 min Products: BZH, CO2 η(m‐xylene): 90.1% Reactor: 53 mL Cat.: 30 mg Conc.: 0.1 ppm VOC: p‐xylene Time: unmarked Products: CO2 η(p‐xylene): 97% Reactor: 25 mL Cat.: 40 mg Conc.: 0.1 ppm VOC: toluene Time: 180 min Products: BZH η(toluene): ≈90% Reactor: unmarked Cat.: 0.4 mg cm–2 Conc.: 700 ppmv VOC: toluene Time: 6–10 h Products: BZH, CO2 η(toluene): ≈85% Reactor: unmarked Cat.: 0.4 mg cm−2 Conc.: 100–200 ppmv VOC: toluene Time: 4 h Products: BZH, CO2 η(toluene): 96.4% Reactor: unmarked Cat.: 40 mg Conc.: 700 ppmv VOC: toluene Time: 6–10 h Products: BZH, CO2 η(toluene): 95% Reactor: 1.9 L Cat.: unmarked Conc.: 4000 μmol L–1 VOC: toluene Time: 120 min Products: BZH, CO2 η(toluene): 95% Reactor: 120 mL Cat.: 0.1 g Conc.: 120 ppm VOC: toluene Time: 240 min Products: BZH, CO2 η(toluene): 82% Reactor: unmarked Cat.: 50 mg Conc.: unmarked VOC: toluene Time: 180 min Products: BZH, CO2 η(toluene): 89.7% Reactor: unmarked Cat.: 1 g Conc.: 25 ppm VOC: toluene Time: 90 min Products: BZH, CO2 η(toluene): 90% Reactor: 350 mL Cat.: 0.58 g Conc.: 0.2 µL VOC: toluene Time: 50 min Products: BZH, CO2 η(toluene): 93.64% Reactor: 10 mL Cat.: 100 mg Conc.: 25 ppm VOC: toluene Time: 8 h Products: BZH, CO2 η(toluene): 68.2% Reactor: 10 mL Cat.: 50 mg Conc.: 200 ppm VOC: HCHO Time: 240 min Products: BZH, CO2 η(HCHO): 100% Reactor: 1 L Cat.: 0.5 g Conc.: 1000 ppm VOC: toluene Time: 240 min Products: BZH, CO2 η(toluene): 100% Reactor: 143 mL Cat.: 0.5 g Conc.: 440 ppmv VOC: toluene Time: 80 min Products: BZH, CO2 η(toluene): 20.79% Reactor: 143 mL Cat.: 100 mg Conc.:10 mmol VOC: toluene Time: 180 min Products: BZH, CO2 η(toluene): 83% Reactor: 17 mL Cat.: 0.25 g Conc.:20 ppm VOC: ethylbenzene Time: 180 min Products: CO2 η(ethylbenzene): 25% Reactor: 4.536 mL Cat.: 0.25 g Conc.:20 ppm VOC: ethylbenzene Time: unmarked Products: CO2 η(ethylbenzene): 37.5% The mass of the photocatalysts (Cat.) The concentration of Sulfur compounds (Conc.) Irradiation time (Time) The removal efficiency η (%) of pollutant was calculated as: η (%) = (1 − C/C 0) × 100% Photoacoustic IR multi‐gas monitor, INNOVA Air Tech 95 Instruments Model 1412 (Innova 1412) High‐pressure mercury lamp (HPML) TU‐1901 UV–vis spectrophotometer (TU‐1901) POV‐18 volatile organic degradation instrument, SUNCAT, China (POV‐18) GAS Tiger 2000‐CH2O‐L, Shenzhen Wanandi Technology Co., Ltd. (GAS Tiger 2000‐CH2O‐L) Shin Kosumosu Denki Form‐tector, C‐XP‐308B (C‐XP‐308B) Gas chromatograph (GC) UV–vis spectrophotometer, UV1750, Shimadzu Corporation, Japan (UV1750) UV radiometer, Model UV‐A, made in the Photoelectric Instrument Factory of Beijing Normal University (Model UV‐A) GC/FID‐9790, Fuli, Hangzhou, China (GC/FID‐9790) Shimadzu GC‐8A, FID detector (GC‐8A).

Research Progress of PCN for VOC Removal

The porous PCN nanosheets with enhanced surface area for VOC adsorption, shortened charge transfer distance for dynamics promotion, and improved active sites for reactants in comparison with pristine PCN counterparts, have attracted attention and interest in VOC decomposition through green strategy.[ ] For example, Kong et al. designed and synthesized porous PCN nanosheets by treating the MA with citric acid and then thermal condensing under an N2 atmosphere.[ ] The obtained PCN nanosheets improved significantly in HCHO decomposition with LED light, which is contributed to the reduced diffusion distance of charges, improved reactive sites for HCHO (Figure  ). This work opens the avenue for PCN in the application of VOC degradation under solar irradiation.
Figure 13

A) Schematic degradation mechanism of porous PCN nanosheet. Reproduced with permission.[ ] Copyright 2021, Elsevier. B) Schematic diagram of charge separation and formaldehyde photodegradation on biochar/PCN composite under visible light irradiation. Reproduced with permission.[ ] Copyright 2019, Elsevier. C) A schematic illustration of the facet coupled effect and electron–hole pair separation of the composite. Reproduced with permission.[ ] Copyright 2016, Elsevier. D) Schematic diagram of the photocatalytic oxidation of HCHO in Bi2MoO6/Bi/PCN under visible light. Reproduced with permission.[ ] Copyright 2020, American Chemical Society. E) TEM images of BiVO4/PCN samples. Reproduced with permission.[ ] Copyright 2017, Elsevier. F) Diagram for the band levels and the proposed electron–hole pair separation of a) STO/TN and b) STO/TN/N‐PCN heterojunctions. Reproduced with permission.[ ] Copyright 2017, American Chemical Society.

A) Schematic degradation mechanism of porous PCN nanosheet. Reproduced with permission.[ ] Copyright 2021, Elsevier. B) Schematic diagram of charge separation and formaldehyde photodegradation on biochar/PCN composite under visible light irradiation. Reproduced with permission.[ ] Copyright 2019, Elsevier. C) A schematic illustration of the facet coupled effect and electron–hole pair separation of the composite. Reproduced with permission.[ ] Copyright 2016, Elsevier. D) Schematic diagram of the photocatalytic oxidation of HCHO in Bi2MoO6/Bi/PCN under visible light. Reproduced with permission.[ ] Copyright 2020, American Chemical Society. E) TEM images of BiVO4/PCN samples. Reproduced with permission.[ ] Copyright 2017, Elsevier. F) Diagram for the band levels and the proposed electron–hole pair separation of a) STO/TN and b) STO/TN/N‐PCN heterojunctions. Reproduced with permission.[ ] Copyright 2017, American Chemical Society. The introduction of alkali metals of K into the lattice structure of PCN can rearrange the structure, lessen the lattice structure defects, and enhance basicity, which is ascribed to the formed static coulomb in the unoccupied 3d/4p orbital of K and π‐conjugated C–N P .[ , , , , ] The increased basicity of K‐doped PCN can easily accelerate HCHO adsorption/activation/dissociation, meanwhile enhancing basicity, optical, and electrical properties, thereby showing great potential in HCHO removal.[ ] Therefore, the solid‐based PCN and potassium (K) were constructed and investigated in decomposing HCHO with solar light, which exhibited strengthened and reinforced performance. This investigation would shed a new way and insight for designing an advanced solid‐based PCN photocatalyst with a promoted π‐conjugated structure for the VOC decomposition. In addition, the activated carbon and porous materials can physically adsorb the gaseous HCHO to reduce the concentration of the indoor/outdoor HCHO.[ , , , , ] However, its application is inadequate and limited because of the capability and the adsorption/desorption rate, and the lifetime of light‐excited charges. To address the above shortcomings of the activated carbon, the combination of PCN photocatalysts and activated carbon was used to improve the efficiency of the HCHO removal. The intimate interface that existed in the activated carbon and PCN endowed a prolonged lifetime and accelerated transfer kinetics of charges, thereby exhibiting outstanding HCHO decomposition with visible light.[ ] For instance, a novel compound (C/PCN) consisted of a biochar skeleton, and “chrysanthemum” PCN was created by the method of co‐condensed treatment.[ ] “Chrysanthemum” PCN increased the reaction sites and charge separation kinetics, and the biochar skeleton increased the optical absorption range and the HCHO aggregation; thus, their visible‐light removal efficiency of HCHO was 84.63%, which was higher than that of the pure PCN (Figure 13B). However, the relatively weak oxidizing ability of PCN would restrict its applications in nondegradable VOC.[ ] According to previous reports, the introduction of O into the PCN matrix can promote ROS generation (H2O2 production) and reduce the width of the bandgap.[ ] Given the above advantage, Jing et al. successfully fabricated a C, O co‐doped PCN by a facile one‐step thermal condensation.[ ] This photocatalyst demonstrated excellent performance in selective oxidation of toluene with visible light, which is own to the promoted ROS generation and the suppressed recombination rate of photocarriers and electronic resistance. In 2019, Yao et al. used PCN nanosheets (exposing abundant hydroxyl and amino groups through the alkali treatment) to combine with the textiles through the strong hydrogen bonding interconnection, which showed efficiently decompose gaseous HCHO.[ ] The superior efficiency and stabilities of the PCN nanosheets could be ascribed to the ultrathin layer properties and enhanced light absorption. Rao et al. synthesized a series of Ag3PO4/PCN type II heterojunctions by introducing a certain amount of Ag3PO4 in PCN, which were used as photocatalysts in decomposing HCHO in a continuous flow.[ ] The formation of Ag3PO4/PCN nanocomposites increased the specific surface area for mass transfer, the separation/transfer dynamics of light‐excited electron–hole pairs, and the optical‐harvesting capability, thereby performing a high HCHO degradation ratio and reusability. The increased solar‐induced electrons on the CB were trapped by O2 and then reduced into ROS, whereas holes on the VB directly oxidized OH– and/or water to produce ROS, and the HCHO was further oxidized to nontoxic CO2 and H2O. In 2016, Sun et al. created a series of Bi12TiO20/PCN composites via a simple method of the hydrothermal‐ultrasonic route.[ ] The Bi12TiO20/PCN presented higher photocatalytic activity for the HCHO degradation than that of pure PCN and Bi12TiO20 because of the active facets ({111} facets of Bi12TiO20), low index surfaces, the matched band alignment endowed promoted charge kinetics (Figure 13C). As the above‐mentioned, the Z‐scheme heterojunction can maximize the redox ability of the semiconductor component through a zigzag charge transfer mechanism.[ , , ] The superfine Bi nanoparticles as a low‐cost alternative of charge transfer medium are usually used in the construction of indirect Z‐scheme nanojunctions because of the good conductivity and SPR properties.[ , ] In addition, Bi‐based inorganic materials show great potential in HCHO oxidization because of the band position and high‐energy orbital of Bi 6s. For instance, Wu et al. successfully constructed a solid indirect Z‐scheme nanojunction of Bi2MoO6/Bi/PCN through in situ reductions to yield Bi NPs (Figure 13D).[ ] This assembled nanojunction presented a commendable activity in degrading gaseous HCHO (96.15%) and robust CO2 selectivity (99.79%), which was primarily contributed to the small impedance endowed the decreased migration resistance of the charges, the vacancies on the surface of PCN endowed the promoted adsorption of HCHO, and the uniform distribution of Bi NPs endowed the boosted transmission of useless electrons. Tang et al. created a direct AgFeO2/PCN Z‐scheme composite by a simple precipitation method.[ ] The even loading of AgFeO2 particles on the surface of the layered PCN and the band alignment of Z‐scheme heterostructure endowed superior absorption in the visible‐light range, effective electron–hole separation, and maximized redox potential, thereby deeply degrading the HCHO into CO2 with visible light. Except for PCN applied in the photocatalytic HCHO removal, the progress of PCN has also been made in the removal of other parts of VOC. For instance, Sun et al. synthesized a direct coral‐like Z‐scheme BiVO4/PCN heterojunction by a simple calcination method, which showed great improvement in the photocatalytic oxidation of toluene (Figure 13E).[ ] The enhancement of the efficiency was due to the kinetics of the accelerated charge favored by the Z‐scheme heterojunction, which was favorable for ROS and active site generation. Similar positive effects could be achieved by direct Z‐scheme WO3/PCN heterojunctions utilized in acetaldehyde decomposition with visible light. Kong et al. firstly developed a titania nanotube‐supported SrTiO3 heterostructure (STO/TN), followed by introducing N‐doped PCN as the sensitizer (STO/TN/N‐PCN, Figure 13F).[ ] This compound showed enhanced optical absorption and facilitated the charge kinetics and transfer of pollutant species, which improved visible‐light‐driven mineralization of toluene.

Conclusions and Outlook

The removal of atmospheric pollutants, including NO , sulfur compounds, and VOC, through solar‐driven catalysis, is considered a potential solution to eliminate severe damages (human health and environment).[ , , , , ] Photocatalysts based on layered PCNs have demonstrated impressive performance of air pollution abatement because its layered structure favored the gas adsorption/activation/reaction, and defective structures favored the engineering and anchoring functional groups to improve charge kinetics and suitable band positions favored the ROS generation.[ , , , , , ] The Lewis basic sites of PCN can provide electrons to the adsorbed air pollutants and then break the bond order of N–O/C–S–C/C–H, thereby facilitating the conversion of air pollutants.[ , , , ] In addition, the visible‐light‐response PCN provides great potential and value for commercialization, which is different from the traditional TiO2 photocatalysts.[ , , ] This review explains the strategies to optimize and improve the efficiency of PCN‐based photocatalytic denitrification, desulfurization, and VOC removal through nanostructure design/electronic structure engineering/heterostructure manufacturing. Firstly, nanostructured PCN‐based composites prepared by exfoliation/templating/solvothermal technologies, and other methods show an excellent catalytic degradation efficiency of air pollutants compared with the pristine PCN counterpart with visible light. The morphological regulation, vacancy/defect engineering, and catalytic immobilization can modulate the surface/internal structure and photo/electrochemical characters to reduce the charges transfer distance, promote mass diffusion, enhance its reactants adsorption/activation, and products desorption, separate the powdery photocatalysts, and decrease photocatalytic loss. Secondly, reforming the electronic structure of PCN‐based photocatalysts through atomic and molecular doping can introduce extra impurities, adjust the redox potentials of charge carriers and optical absorption capability, and extend the delocalization of the π electrons, thereby promoting the efficiency of multiphase catalysis for the elimination of air pollutants. Finally, the heterostructure photocatalysts by combining PCN and other functional materials based on matching band and band alignment are found to be efficacious, which can improve the kinetics of light‐induced charge carriers and exhibit outstanding heterogeneous catalysis for the decomposition of air pollutants. In addition, the above‐mentioned solutions can also improve the air molecules activation and the ROS generation, further advancing the denitrification, desulfurization, and VOC removal. Thus, the photocatalytic efficiency of PCNs would be significantly enhanced more rationally with the structure design of PCN through different strategies. The potential results discussed and analyzed in this review can inspire scientists to develop more effective PCN‐based photocatalytic composites to reduce and degrade the air pollutants concentration. Although many advances have been achieved, the PCN‐based materials still cannot be commercially applied because of the issues of uncertain generation/conversion routes of by‐products, low performance with red‐light, nonuniform universal evaluation standards, limited/complicated simulation tools/technologies, inefficient durability, and reusability of photocatalysts, and photocatalytic regeneration. Therefore, establishing a complete evaluation system and conducting a basic exploration and research work is necessary to resolve these technical problems and challenges and accelerate the progress of commercialization. In our opinion, priority research soon should concentrate on the development of PCN‐based photocatalysts with the following demonstrated properties. 1) Lack of universal evaluation standards: Determining the actual efficiency of the photocatalysts is difficult to evaluate because of the diverse test systems. 2) Unsatisfactory and moderate photocatalytic activity: Although various PCN‐based photocatalysts have been reported and investigated in removing the air pollution, the actual efficiency is still too unsatisfactory and low to realize the practical needs. 3) Lack of infrared region utilization: The infrared region utilization of PCN should be developed to achieve greater improvement in solar energy efficiency. 4) Poor product selectivity: Considering a multilevel reaction of removing air pollutants takes place on PCN photocatalysts, a variety of toxic and harmful by‐products appear during the reaction. Therefore, reducing the production of toxic by‐products and deep oxidation to remove air pollutants is an essential step. 5) Poor and inadequate operational stability: Operational stability is one of the first prerequisites for the industrial application of catalysts. However, the current research on the operational stability of PCN photocatalysts still has many limitations, and the research is not yet in‐depth. 6) Lack of catalytic immobilization carrier and technology: Recycling and reusing PCNs during photocatalytic air abatement are difficult. Since the powdered photocatalyst is easily blown away under the continuous gas during the practical application, it causes loss of catalyst; and it also requires a time‐consuming and complicated filtration process during the recycling process, which increases the process cost. 7) Lack of in‐depth mechanism research: To substantially improve the reaction efficiency of photocatalytic removal of air pollutants, the reaction process needs to be identified through various advanced in situ detection technologies and theoretical calculations. More in‐depth researches are needed to break the current bottleneck in the next decades. Moreover, to further realize the large‐scale application of PCN‐based photocatalysts, its preparation process, cost and output are also major factors that still need to be considered. Thus, more efforts are still needed to devote to designing and producing low‐cost PCN‐based nano‐photocatalysts with superior activity, selectivity, and reusability and achieve the maximization of the above properties. A few further optimizations can be considered with regard to PCNs as follows. 1) Establishment of a standard test and judge system: The standard and the publicly recognized testing system can be built by internationally recognized experts to further improve the catalytic system and efficiency. 2) Crystal structure modulation: The crystallinity and defects modification of PCN can be devised to increase the kinetics of the charge and provide enhanced adsorption sites for reactants.[ , ] 3) Morphological modification: The PCN aerogels, mesoporous PCN, and ultrathin/single‐layer PCN nanosheets can be designed to promote the mass transfer and shorten the transmission distance of the photogenerated charges.[ , , , , , , , , ] 4) Immobilization base and process regulation: The increased stability and extended life of PCNs can be achieved by selecting suitable immobilization bases and improving the fixing process. 5) Atomic utilization promotion: The single‐atom‐based PCN photocatalytic systems can be designed and constructed to maximize atomic utilization.[ , , ] In addition to finding and designing suitable component materials to combine with PCN, its synthesis techniques and processes are also indispensable for the photocatalytic performance improvement and commercial development of its surface modification. Through the development of nanotechnology, solar‐driven engineering, and theoretical/model research fields, its photocatalytic performance can be significantly improved and large‐scale industrialization and commercial application of these materials can be realized. Given such optimizations, improving the efficiency of air purification based on PCN‐based photocatalysts and other solar‐related applications would be recommended.

Conflict of Interest

The authors declare no conflict of interest.
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Review 9.  Biocatalytic desulfurization (BDS) of petrodiesel fuels.

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