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Abbreviation (ISO4): Prog Chem      Editor in chief: Jincai ZHAO

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Review

Millimeter-Sized Nanocomposites for Advanced Water Treatment: Preparation, Synergistic Effects and Applications

  • Wanyi Fu 1 ,
  • Yuhang Li 1 ,
  • Zhichao Yang 1 ,
  • Yanyang Zhang 1, 2 ,
  • Xiaolin Zhang 1, 2 ,
  • Ziyao Liu 1 ,
  • Bingcai Pan , 1, 2, *
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  • 1 State Key Laboratory of Pollution Control and Resource Reuse, School of Environment, Nanjing University,Nanjing 210023, China
  • 2 Research Center for Environmental Nanotechnology (RCENT), Nanjing University,Nanjing 210023, China
*Corresponding author e-mail:

Received date: 2023-05-11

  Revised date: 2023-06-10

  Online published: 2023-08-07

Supported by

National Key R&D Program(2022YFA1205601)

National Key R&D Program(2022YFA1205602)

National Natural Science Foundation of China(21925602)

National Natural Science Foundation of China(22236003)

Abstract

Nanomaterial features a high surface area-to-volume ratio and strong surface effects, offering excellent performance in water treatment and broad application prospects. Incorporating nanoparticles into millimeter-scale hosts to prepare millimeter-sized nanocomposite materials can couple the high reactivity of nanoparticles with the easy operability of millimeter-scale hosts. This is an important technical approach to overcome the engineering application bottlenecks of nanomaterials, such as their tendency to agglomerate, low stability, potential environmental risks, and difficult separation. This review summarizes the preparation methods, structural characteristics, and adsorptive and catalytic oxidative removal of pollutants from aqueous systems by millimeter-sized nanocomposites. It elaborates on the confinement effects from the perspectives of confined growth of nanoparticles, confined adsorption properties, and confined catalytic oxidation properties, as well as the synergistic purification effect between the hosts and nanoparticles. Finally, the scientific issues and practical challenges that urgently need to be addressed in the development of millimeter-sized nanocomposites are discussed. We believe this review will provide theoretical guidance and technical references for promoting the practical applications of nanomaterials.

Contents

1 Introduction

2 Common hosts and preparation methods of millimeter-sized nanocomposites

2.1 Polymeric hosts

2.2 Carbon-based hosts

2.3 Natural mineral based hosts

2.4 Ceramic-based hosts

3 Confinement effects and synergistic purification effects of millimeter-nanometer structure

3.1 Confined growth of nanoparticles in millimeter-sized hosts

3.2 Confined adsorption and regeneration of nanoparticles inside millimeter-sized hosts

3.3 Confined catalytic oxidation of nanoparticles inside millimeter-sized hosts

4 Practical applications of millimeter-sized nanocomposites in water treatment

4.1 Applications in adsorption

4.2 Applications in catalytic degradation

5 Conclusions and perspectives

5.1 Research gaps in scientific issues regarding nanoconfinement effects

5.2 Challenges to be addressed for practical applications of nanocomposite materials

Cite this article

Wanyi Fu , Yuhang Li , Zhichao Yang , Yanyang Zhang , Xiaolin Zhang , Ziyao Liu , Bingcai Pan . Millimeter-Sized Nanocomposites for Advanced Water Treatment: Preparation, Synergistic Effects and Applications[J]. Progress in Chemistry, 2023 , 35(10) : 1415 -1437 . DOI: 10.7536/PC230510

1 Introduction

Since the 21st century, the development demand in the field of water pollution control has gradually changed from curbing the deterioration of water environment quality to ensuring water quality safety and improving the ecological quality of water environment. Under this new development trend, the control requirements of many characteristic pollutants in water, such as heavy metals, phosphorus, arsenic, fluorine and new pollutants, are becoming more and more stringent, and the maximum allowable concentration of many target pollutants in water has been gradually reduced from mg/L to μg/L and ng/L. Traditional biochemical and physicochemical treatment technologies are often difficult to meet the needs of advanced water treatment, and the development of new materials and technologies for advanced water treatment has become the top priority in the field of water pollution control.
Nanomaterials have high specific surface area and strong surface effect, which are used more and more in adsorption, catalysis, membrane filtration and other fields, and have outstanding deep purification performance for heavy metals, phosphorus, fluorine, arsenic and organic pollutants. When nanoparticle materials are used in practical water treatment, they face engineering application bottlenecks such as agglomeration and deactivation, difficult separation, poor stability, and potential environmental risks. The preparation of millimeter-nanostructure composite materials by loading nanoparticles into millimeter-scale carriers can organically combine the high reactivity of nanoparticles with the good operability of carriers, which is one of the most important technical means to achieve its large-scale application. The millimeter-nanostructure composite material can not only highly disperse the nanoparticles with high reactivity through the porous structure of the millimeter-scale carrier, but also limit the nanoparticles by the nano-pore structure.That is, the nano-confinement effect, which affects the electron transfer process, changes the chemical characteristics of water, and induces the crystal growth orientation of nanoparticles, thus significantly affecting the decontamination process and efficiency of nanomaterials. At the same time, compared with the traditional nanoparticle dispersion system, the milli-nano structure composite material can effectively improve the stability of nanomaterials and reduce the dissolution and loss of materials.
In this paper, the preparation methods of millimeter-nanostructure composites are reviewed, the structural characteristics, applicable preparation ideas and effects of various millimeter-scale carrier materials are introduced, and the confinement effect of millimeter-nanostructure confinement space and the synergistic decontamination mechanism are described.The mechanism of confined space on adsorption process, regeneration performance, catalytic oxidation process and degradation performance was analyzed. Finally, the current situation and challenges of the application of milli-nano structured composites in water treatment were summarized, analyzed and prospected, in order to provide some theoretical guidance and technical reference for the development of the application of milli-nano structured composites in water treatment.

2 Common carrier and preparation method of milli-nano structure composite material

The millimeter-scale carrier materials used in the preparation of millimeter-nanostructure composites usually have porous structure and nano-pore channels.It mainly includes synthetic polymer materials (such as polystyrene resin and polyurethane sponge), natural polymers (such as cellulose and chitosan), carbon-based materials (such as activated carbon and biochar), natural minerals (such as zeolite and diatomite), and ceramic-based materials (e.g., alumina pellets and ceramic membranes) (Figure 1A). According to the structural characteristics (such as structural hardness, size and shape) and physicochemical properties (such as thermal expansion coefficient, water swelling, melting point, hydrophilicity and hydrophobicity, functional group structure) of millimeter-scale carrier materials,The applicable composite preparation methods are different, mainly including impregnation-in-situ growth method, flash freezing-in-situ growth method, swelling-in-situ deposition method, ion exchange-in-situ deposition method, and impregnation-calcination method (Fig. 1b-g). In this paper, the preparation methods and effects (such as nanoparticle dispersion, activity, stability, etc.) Of the corresponding millimeter-scale carriers are reviewed, and the advantages and disadvantages of various preparation methods are analyzed, which provides a technical reference for the preparation of millimeter-scale nanostructured composites.
图1 用于制备毫纳结构复合材料的(a)载体材料类别及(b~g)各类典型的制备方法[1,9,13,22,30,40]

Fig.1 (a) Categories of millimeter-scale host materials and (b~g) typical preparation methods for millimeter-sized nanocomposites[1,9,13,22,30,40]

2.1 Organic polymer carrier

Organic polymer materials are widely used as support materials because of their adjustable pore size, abundant functional groups and good stability. Organic polymer carriers mainly include synthetic polymers such as ion exchange resins and natural polymers (Table 1). Porous organic polymers can effectively control the size of metal nanoparticles through the spatial confinement of cooperative pores, immobilize metal species through the coordination or electrostatic interaction between organic functional groups and metal ions, and improve the pollutant purification efficiency through the interaction between carriers and target pollutants.
表1 以高分子聚合物为载体的毫纳结构复合材料应用于去除水中污染物的研究

Table 1 Studies on millimeter-sized nanocomposites with polymers as hosts applied in water decontamination

Millimeter-scale hosts Appearance
size of
hosts (mm)
Embedded
nanoparticles
Size of
nano-
particles
(nm)
Preparation methods Target pollutants Removal mechanism Adsorption capacity (mg/g) Removal efficiency Treated water matrix Experimental scale Operation duration ref
Macroporous ion exchange resins
D201a 0.7~0.9 HZO N.A.b Impregnation-precipitation Phosphate Adsorption 21.3 N.A Effluent from
municipal WWTPe
Fixed-bed column 1800 BV 2
D201 0.6~0.7 HZO 20~40 Impregnation-precipitation As(V) Adsorption 70.53 N.A. Acidic mining effluent Fixed-bed column 2900 BV 3
D201 0.4~1.0 HLO 3.56~
67.23
Impregnation-precipitation Phosphate Adsorption N.A. 91.23% River water Pilot-scale fixed-bed 8 months,
10 m3/d
5
D201 0.9~1.1 nZVI 2~11 Impregnation-precipitation Cu(Ⅱ)-
EDTA
Adsorption N.A. 88.3% Synthetic solution Fixed-bed column 500 BV 6
D201 0.4~0.8 HFO N.A. Impregnation-precipitation Selenite Adsorption ~37 N.A. Simulated wastewater Fixed-bed column ~1200 BV 107
D201 0.6~1.0 HFO N.A. Iron exchange-
precipitation
Phosphate Adsorption 17.8 N.A. Industrial effluent from a pesticide plant Fixed-bed column ~930 BV 10
D201 N.A. Li/Al LDHsc 5~20 Iron exchange-
precipitation
Fluoride Adsorption 32.6 N.A. Fluoride contaminated groundwater Fixed-bed column ~155 BV 84
D201 0.7~0.9 CeO2 2.5~4.2 Iron exchange-
precipitation
As(Ⅲ) Oxidation-adsorption 9.96 99.6% Simulated wastewater Fixed-bed column ~6500 BV 108
D201 0.6~0.8 nZVI 10~30 Iron exchange-reduction Se(Ⅵ) Adsorption N.A. >99% Simulated wastewater Fixed-bed column ~1240 BV 109
D201 (chloride type) 0.6~1.0 HFO 12.3 Iron exchange-
precipitation
Phosphate Adsorption N.A. <0.5 mg/L Biochemical effluent
from municipal WWTP
Field fixed-bed 3500~4000 BV 79
Cation exchanger D001 ~1 HFO N.A. Impregnation-precipitation Cu(Ⅱ)-
citrate
Adsorption/
Oxidation
N.A. 81.6% Simulated wastewater Fixed-bed column 1300 BV 110
Strongly basic anion
exchanger HAIX
0.5~0.7 HFO N.A. Iron exchange-
precipitation (commercial ArsenXnp)
As Adsorption N.A. <50 μg/L Arsenic well water Field fixed-bed 29 000 BV 7
Strongly basic anion
exchanger HAIX
0.3~1.2 HFO 3~5 Iron exchange-
precipitation (commercial
ArsenXnp)
As(V) Adsorption N.A. <10 μg/L Arsenic drinking water Field fixed-bed 91~120 days 86
Anion exchanger IRA-900 N.A. HFO N.A. Iron exchange-
precipitation
Phosphate Adsorption N.A. <10 μg/L Secondary effluent
from municipal WWTP
Fixed-bed column 1500 BV 111
Anion exchanger
DOWEXTM M4195
0.3~0.8 HFO N.A. Impregnation-
precipitation
Phosphate Adsorption N.A. <10 μg/L Simulated wastewater Fixed-bed column ~320 BV 112
Cross-linked ion exchange resins
Highly cross-linked
anion exchanger of
polystyrene matrix
0.6~0.7 HZO N.A. Impregnation-precipitation Fluoride Adsorption 20.9 <1.5 mg/L Simulated fluoride-
containing groundwater
Fixed-bed column ~80 BV 82
Cross-linked anion
exchanger
0.45~
0.55
HFO 11.6 Impregnation-precipitation As(V) Adsorption 31.6 <10 μg/L Simulated wastewater Fixed-bed column 2950 BV 12
Strongly basic anion
exchanger of poly-
styrene matrix
0.7~1.0 HMO 5.0~7.0 Impregnation-precipitation Phosphate Adsorption N.A. <0.5 mg/L Simulated wastewater Fixed-bed column 460 BV 54
Gel type ion exchange resins
Gel anion exchanger IRA-900 N.A. HFO N.A. Swelling-precipitation As(V) Adsorption N.A. >90% Simulated wastewater Fixed-bed column 10,000 BV 64
Gel cation exchanger C-100 0.3~0.5 HFO 20~100 Coprecipitation Pb(Ⅱ) Adsorption N.A. <0.2 mg/L Lead-acid battery
wastewater
Field fixed-bed 6500 BV 88
Gel strongly basic anion exchanger 201 × 4 N.A. HFO N.A. Iron exchange-
precipitation
As(V) Adsorption N.A. <10 μg/L Simulated wastewater Fixed-bed column 3900 BV 22
Synthetic polymers
Polystyrene bead 2 FeOOH 2.0~7.3 Flash freezing-in situ growth As(V) Adsorption 140~190 N.A. Single contaminant
solution
Laboratory beaker N.A. 13
Polystyrene bead 2 α-Fe2O3 3 Flash freezing-in situ growth As(V) Adsorption 32.0 <10 μg/L Simulated wastewater Fixed-bed column ~2900 BV 55
PDMS sponged 9 TiO2-Au 3~15 Sugar-template method RhB Photocatalysis N.A. ~96% in
3 h
Single contaminant
solution
Laboratory beaker N.A. 113
Polyurethane sponge N.A. Iron oxide N.A. Hydrothermal growth
method
As(Ⅲ),
As(V)
Adsorption As(Ⅲ): 4.2
As(V): 4.6
<50 μg/L Simulated wastewater Fixed-bed column As(Ⅲ): 123 BV
As(V): 144 BV
23
Natural polymers
Chitosan N.A. Iron oxide N.A. Impregnation-deposition Phosphate Adsorption N.A. 52.3% Stream water Pilot-scale adsorption tower 33 days 81
Bead cellulose 0.3~0.9 Fe(OH)3 200~300 Impregnation-deposition As(Ⅲ),
As(V)
Adsorption As(Ⅲ): 99.6
As(V): 33.2
<10 μg/L Simulated fluoride-
containing groundwater
Fixed-bed column As(Ⅲ): 2200 BV
As(V): 5000 BV
24

Note: a. Macroporous strongly basic anion exchanger of polystyrene matrix D201; b. Not available or Not applicable; c. Li/Al Layered double hydroxides; d. Polydimethylsiloxane sponge; e. Wastewater treatment plant

(1) macroporous ion exchange resin
Ion exchange resin is a kind of polymer material with crosslinked network structure, which is usually modified by suspension copolymerization of styrene and divinylbenzene, followed by sulfonation, chloromethylation, amination and other chemical reactions. Macroporous ion exchange resins with good macroporous network structure, high mechanical strength and certain specific surface area can be obtained by adding pore-forming agents in the copolymerization reaction, which have been widely used in many industrial fields. Ion exchange resin is an ideal carrier for the preparation of nanostructured composites because it can immobilize nanoparticles through the mesh confinement effect and has a pre-concentration effect on charged pollutants through the Donnan membrane effect.
The milli-nanostructured composite materials with macroporous resin as the carrier are usually prepared by the "dipping-in situ growth method" (also known as "precursor introduction-nano-mesh confined nucleation"), in which the precursor of nanoparticles (such as metal ions or metal complex molecules) is introduced into the resin by ion exchange, evaporation and concentration, etc.Then, the precursor is promoted to grow into the target nanoparticle material in the nano-mesh by heat treatment, alkali treatment, redox reaction, etc., to prepare the macroporous resin-based milli-nano structure composite material (Figure 1b). Pan Bingcai et al. Used this method to load nano-hydrated zirconia (HZO), hydrated lanthanum oxide (HLO), hydrated iron oxide (HFO) and nano-zero-valent iron (nZVI) on macroporous strongly basic anion exchange resin D201.A series of milli-nano structured composite materials are prepared, which show fast adsorption kinetics and high adsorption selectivity for inorganic pollutants in water, such As phosphate, heavy metal complexes, As (V), etc., and can be efficiently desorbed and regenerated[1][2,3][4,5][1][6]. Caspian University and Bangladesh University of Engineering and Science have developed a commercial adsorbent ArsenXnp for arsenic removal, which is composed of macroporous anion exchange resin loaded with HFO nanoparticles. The apparent diameter of the adsorbent is 0. 3 ~ 1. 2 mm, and the loading of HFO on the resin is 150 mg Fe/G. The material has high mechanical strength and good stability, and is suitable for fixed-bed reactors[7,8].
In addition, milli-nanostructured composites suitable for macroporous ion exchange resin supports can also be prepared by the "ion exchange-in situ deposition" method (Figure 1 C). The method utilizes quaternary ammonium groups uniformly distributed on a polystyrene skeleton to introduce a precursor into resin pore channels through ion exchange, and then uniformly loaded nanoparticles are prepared through an in-situ deposition method[9]. For example, Pan et al. Used F e C l 4 - as HFO precursor to prepare macroporous anion exchange resin-based nano-HFO composite (HFO-201) by ion exchange-in situ deposition method, which has good adsorption and removal capacity for phosphate[10].
However, the pore structure of macroporous resin support is often disordered and the pore size distribution is wide (10 ~ 200 nm), which leads to the size of nanoparticles growing in the pores varies from several to tens of nanometers, and it is difficult to achieve size uniformity[4,11]. The formed nanoparticles are easy to block the pore channels of the carrier and reduce the availability of the active sites. For example, the in situ growth method encapsulating nano-iron oxide in porous polystyrene and mesoporous silicate caused severe pore blockage, which inhibited the diffusion of pollutants to the surface of Nanoparticles (NPs) and led to a 35% reduction in the density of active sites[12~14][15]. Another preparation method, in which the polymer precursor is mixed with NPs followed by a phase change, results in a composite with a lower porosity[16]. The phase separation of the polymer matrix from NPs at the solid-liquid interface leads to severe agglomeration of NPs, such that the number of active sites accessible to contaminants is reduced[17,18]. In addition, the content of nanoparticles loaded in the carrier also has a great influence on the adsorption performance of the composite. Some scholars have found that when HFO is encapsulated in the carrier, the increase of Fe content leads to pore blockage, which leads to the decrease of adsorption site density and adsorption capacity[19,20]. In one study, α-Fe2O3 and Fe3O4 nanoparticles were encapsulated in macroporous polymer gel, and the adsorption capacity for As (Ⅲ) was found to be reduced by 30%[21]. At present, it is still a challenge to prepare resin materials with uniform pore size distribution and control the size and uniformity of confined nanoparticles.
(2) gel-type resin
Because the preparation of the gel type resin does not need to add a pore-forming agent, the production cost of the gel type resin is obviously reduced compared with that of the macroporous resin. However, the chemical structure of gel-type resin is not permanent, and only after full swelling in water, it produces a pore structure with a diameter of 0. 5 ~ 5.0 nm, and the overall porosity is small. The method for preparing the milli-nano structure composite material by using the characteristic that the non-porous gel swells to form pores when meeting water is mainly a "swelling-in-situ deposition" method (fig. 1e), that is, the non-porous gel and a nanomaterial precursor solution are stirred to be uniformly distributed in the pores of the gel,The nano-particles are deposited in situ in the gel pores with a spatial grid structure by adding an alkali solution and the like, and after vacuum drying and dehydration treatment, the pores generated by swelling disappear, and the nano-particles in the pores are extruded by a crosslinking skeleton to realize a confined structure, so that the milli-nano structure composite material is obtained. For example, Liu Yan et al. Used the commercial gel-type strong base anion exchange resin 201 × 4 as the matrix to prepare the composite material loaded with nano-HFO by the "swelling-in situ deposition" method, and found that the HFO particles played a supporting role in the gel resin skeleton, which made it have obvious physical pore structure and significantly improved the mechanical strength[22]. The HFO nanoparticles are mainly needle-like and have a large specific surface area, and the available active site density is increased by about 67% compared with the macroporous composite material. Due to the lack of rigid pores, the swelling rate of gel resin in water is large, the mechanical strength is low, and it is easy to break in the process of repeated regeneration and swelling, which affects its long-term application performance.
(3) Homopolymeric hypercrosslinked resin
At present, the commonly used polystyrene resin is mainly prepared by suspension copolymerization, and then the pore structure is regulated by controlling the degree of post-crosslinking reaction. Compared with macroporous resin, hypercrosslinked resin has a certain uniformity of pore size distribution, and has the characteristics of high pore volume and strong mechanical strength. Li et al. Prepared milli-nanostructured composite HFO-NS by "ion exchange-in situ deposition" method in three cross-linked anion exchange resins (NS) with different pore size distributions to study the effects of confined space size on HFO crystal form, particle size, surface chemical properties and As (V) adsorption kinetics[12]. The results showed that the average particle size of confined HFO NPs decreased from 31. 4 nm to 11. 6 nm with the decrease of the average pore size of the anion exchange resin from 38. 7 nm to 9. 2 nm, and the density of surface active sites increased due to the size effect, and the adsorption capacity of As (V) increased significantly.
(4) Other synthetic polymers
Polystyrene beads and sponges are the main synthetic polymers used as supports for milli-nano structured composites. The porous structure can be used to infiltrate the precursor solution of the nanomaterial into the pores of the porous material by means of vacuumizing or soaking, and then the milli-nano structure composite material can be prepared by drying, baking and other processes.
Zhang et al. Developed a sub-10nm iron oxide composite preparation method based on the "flash freezing-in situ growth" technique (Fig. 1 d)[13]. In this method, the microphase separation between polymer molecules and solvent molecules is initiated by rapid cooling, and the pore-forming effect is produced by the micro-nano crystallization of solvent molecules to form a rich and ordered mesoporous structure, and then the sub-10 nm iron oxide is formed in the nanopore by the "in-situ growth method". The prepared nanostructured nanocomposites have a uniform size of about 1 mm, and the iron oxide nanoparticles in the nanostructured nanocomposites have a narrow particle size distribution (2. 0-7. 3 nm), which is adjustable and well dispersed, and can avoid the blockage of the pore structure of the carrier while obtaining a higher loading, thus ensuring the high availability of the active sites on the surface of the nanoparticles. Compared with the rod-like iron oxide (18 nm × 60 nm), the as-prepared nanostructured composites have a 10 ~ 15 times higher standardized treatment capacity for arsenic, showing significant size effect and surface effect.
Sponge is a kind of porous polymer with high specific surface area, such as polyurethane sponge, which is widely used. It has chemical inertness and good mechanical properties, and its pore structure composed of organic framework can load functional nanomaterials. In previous studies, nano-functional materials were loaded on the polyurethane skeleton by hydrothermal growth method, that is, polyurethane sponge was placed in metal ion solution, and nanoparticles were attached to the surface of the skeleton under high temperature and high pressure. In order to prevent the polyurethane sponge from dissolving, the water temperature used should be lower than 180 ℃. For example, Nguyen et al. Used the hydrothermal growth method to load iron oxide particles into polyurethane sponge to obtain polyurethane sponge composite, which was applied to the adsorption of As (Ⅲ) and As (V) in water. For the solution containing As (V) with an initial concentration of 1000 μg/L, the adsorption column after 28 days of continuous operation can achieve a stable removal of the effluent concentration of less than 50 μg/L[23].
The synthetic polymer materials mentioned above (such as polystyrene resin and polyurethane sponge) have rich pore structure and high specific surface area, and can be reused many times after elution, but most of them are not easy to biodegrade, so secondary treatment after waste should be considered. For example, the polystyrene matrix is easy to embrittle, the low temperature impact resistance is poor, and the heat deformation temperature is relatively low, so there may be a potential risk of microplastics in the long-term use process. Therefore, the structural stability of organic polymer-based nanocomposites still needs to be further improved.
(5) Natural polymer materials
Synthetic polymer materials are relatively expensive, while natural polymer materials, such as chitosan and cellulose, have the advantages of wide source, low cost, environmental friendliness and good biodegradability. Among them, cellulose is a macromolecular polysaccharide composed of glucose units, which mainly exists in plant cell walls and is the most widely available in natural polymer materials. At present, researchers use cellulose loaded functional nanomaterials to achieve selective removal of pollutants in water. Among them, the representative metal oxides used for nanocellulose-based composite adsorption materials are iron oxide (β-FeOOH), zinc oxide (ZnO) and titanium dioxide (TiO2), etc[24][25][26]. Metal oxide nanoparticles and cellulose are adsorbed on the surface of nanocellulose through van der Waals force and electrostatic attraction to form a composite material, which is directly used for pollutant removal. For example, Alipour et al. Modified Fe3O4 and ZnO magnetic nanoparticles by thiourea and coated them on the surface of cellulose to obtain a composite material, which had a maximum adsorption capacity of 554.4 mg/G for Pb2+[25].

2.2 Carbon-based material carrier

(1) granular activated carbon
Activated carbon is a kind of carbon-based material obtained by carbonization and activation of carbon-rich materials, which has many advantages, such as large specific surface area, rich surface chemical groups, developed pore structure system and so on, and has been widely used in practical water treatment projects. Activated carbon adsorption is one of the important process units in water treatment plants. The preparation of nanocomposites by loading nanoparticles on granular activated carbon carriers with abundant pores can fully combine the high selectivity and adsorption activity of nanomaterials with the operational flexibility of the carriers themselves. The preparation method of granular activated carbon matrix composite is mainly impregnation-calcination method, that is, the precursor solution of nanomaterials is infiltrated into the pores of porous materials by means of vacuumizing or soaking, and the composite is prepared by drying and calcination after impregnation and equilibration (Fig. 1f). For example, Mullick and Neogi prepared activated carbon-zirconium dioxide nanocomposite by loading zirconium dioxide on activated carbon, and the study showed that the specific surface area of activated carbon-zirconium dioxide was 1103 m2/g.Zirconium dioxide particles were uniform in size (about 52. 3 nm) and stably and effectively dispersed and immobilized on activated carbon, showing good fluoride removal adsorption performance and less interference from coexisting anions in water[27]. However, the encapsulation of nanoparticles in activated carbon may lead to a decrease in the surface area of nanoparticles and may also block the pore size of activated carbon[28]. For example, in one study, even if the proportion of Fe in the HFO-loaded composite was increased to 79%, the adsorption capacity of arsenic was only 0.024 mg/G[29]. In addition, the equilibrium time for the adsorption of arsenic in water by the composite adsorption material with activated carbon carrier is longer, and the adsorption performance is greatly affected by pH. In addition, the mechanical strength of activated carbon materials under high fluid resistance is also facing a certain test, and the crushing and loss of carrier materials inevitably lead to the loss of active nanoparticles.
(2) Biochar
Biochar is often obtained by pyrolysis and carbonization of straw, sawdust, fruit peel, fruit shell, sludge and other biomass under anaerobic or anoxic conditions, which is extremely rich in raw materials, with high specific surface area, rich pore structure and stable chemical properties, and has significant economic and environmental benefits. The preparation of milli-nano structure composite material with biochar as carrier is mainly to mix and impregnate biomass or biochar with metal salt precursor or nanoparticle solution, and then generate biochar through different thermochemical processes (such as slow pyrolysis and hydrothermal carbonization) to obtain functional composite material. For example, Sun et al. used a carbonization-activation two-step method (Fig. 1G) to grow FeNi nanoparticles in corncob-derived carbon (CCAC) in a confined manner. The porous structure and high specific surface area of CCAC effectively dispersed the FeNi nanoparticles, which significantly enhanced the photo-Fenton catalytic performance of the composite, and its catalytic degradation efficiency for rhodamine was 2.3 times that of the unconfined FeNi nanoparticles[30]. Wang et al. Loaded nanoscale zero-valent iron (nZVI) on the surface of konjac glucomannan derived carbon by impregnation-pyrolysis reduction method, and the nZVI was uniformly coated in the carbon carrier, which effectively slowed down the oxidation and agglomeration of nZVI[31]. The composite material showed a uranium enrichment rate of up to 90.1% within 60 min, and the enrichment capacity was 720.8 mg/G. However, most of the current studies on biochar adsorption of pollutants are laboratory studies, lacking long-term pilot studies and large-scale application reports, and there are few studies on the regeneration and reuse of materials, so far there is a lack of common standards for biochar preparation methods and application processes. At the same time, large-scale production is also a key factor limiting the large-scale commercial application of biochar[32,33].

2.3 Natural mineral carrier

Natural mineral materials are a class of environmentally friendly materials in nature, which are abundant and have no potential secondary pollution, and have become one of the key directions of functional materials for water treatment. The main minerals used to prepare functional materials for water treatment are zeolite, diatomite, bentonite, etc. (Table 2). Due to the stable physical pore structure of these natural mineral materials, the preparation method of milli-nanostructured composites based on these materials is mainly the "impregnation-calcination" method (Fig. 1 f).
表2 以碳基材料和天然矿物为载体的毫纳结构复合材料应用于水处理的研究

Table 2 Studies on millimeter-sized nanocomposites with carbon-based materials and natural minerals as hosts applied in water decontamination

Millimeter-scale hosts Appearance size of hosts (mm) Nanoparticles Size of na-
noparticles (nm)
Preparation methods Target pollutants Removal mecha-nism Adsorption capacity (mg/g) Removal efficiency Treated water matrix Experimental scale Operation duration ref
Carbon-based material
Activated carbon 0.25~0.5 HFO 2 Impregnation-calcination As(V) Adsorption 5 N.A.a Single contaminant solution Laboratory conical flask N.A. 28
Straw biochar 5~10 Ce 2~5 Impregnation-precipitation- pyrolysis Phosphate Adsorption 77.7 N.A. Single contaminant solution Laboratory batch
adsorption experiments
N.A. 114
Corncob biochar N.A. FeNi 880 Carbonization-activation RhB Photo-Fenton catalysis N.A. 97% in
90 min
Single contaminant solution Laboratory photo-reactor N.A. 30
Biochar aerogel N.A. nZVI 50~100 Impregnation-Pyrolysis
reduction
U (Ⅵ) Adsorption-reduction 720.8 90.1% in
80 min
Single contaminant solution Laboratory conical flask N.A. 31
Coffee ground
biochar
N.A. Pd 2~11 Impregnation-calcination 4-nitrophenol and meth-
ylene blue
Catalytic reduction N.A. N.A. Single contaminant solution Laboratory beaker N.A. 115
Natural minerals
Zeolite N.A. nZVI 37~110 Impregnation-reduction As(V) Adsorption 47.3 59% in
180 min
Single contaminant solution Laboratory batch
adsorption experiments
N.A. 116
Zeolite 0.8~1.2 HAlO N.A. Impregnation-ion exchange Phosphate Adsorption 7.0 N.A. Simulated wastewater Fixed-bed column 137 BV 117
Zeolite N.A. La N.A. Hydrothermal method Phosphate Adsorption N.A. >95% Primary and secondary
effluent from wastewater
treatment plant
Laboratory batch
adsorption experiments
N.A. 118
Zeolite 0.18~0.25 Mg-Al-La ternary hy-droxides 82.1 Coprecipitation Phosphate Adsorption 80.8 <0.5 mg/L Single contaminant solution Fixed-bed column ~4800
BV
119
Diatomite N.A. HFO N.A. Impregnation-calcination As Adsorption 20.5 < 50 μg/L Groundwater containing high
concentrations of arsenic
Fixed-bed column 937 BV, 44 d 120
Diatomite N.A. Magnetite 15 Hydrosol method Cr(Ⅵ) Adsorption 69.2 N.A. Single contaminant solution Laboratory batch
adsorption experiments
N.A. 121
Diatomite 0.15 nZVI 10 Hydrothermal reduction method Phosphate Adsorption 37.0 N.A. Single contaminant solution Laboratory batch
adsorption experiments
N.A. 122
Diatomite 0.05 nZVI 20~60 Impregnation-reduction Simazine Catalytic reduction 0.97 N.A. Single contaminant solution Laboratory beaker N.A. 123
(1) Zeolite
Natural zeolite is a kind of porous hydrous aluminosilicate with wide distribution, low price and skeleton structure, which has the ability of ion exchange and adsorption. Natural zeolites have been used in engineering applications such as ammonia nitrogen adsorption, heavy metal and radioactive element fixation. In recent years, researchers have used natural zeolite as a carrier to improve its adsorption capacity and selectivity by loading functional nanoparticles (such as Fe, Mg, La oxides). For example, Zeng Qi et al. First loaded silica on natural zeolite, and then loaded lanthanum hydroxide nanoparticles with high adsorption activity for F-, which significantly increased the specific surface area of natural zeolite and significantly improved its adsorption performance for F-, with the maximum adsorption capacity of 14. 2 mg/G[34]. Jiang Yinshan et al. Used natural zeolite as carrier and TiCl4 as titanium source to load anatase TiO2 on zeolite without high temperature treatment in aqueous system, which combined firmly and had excellent and stable catalytic performance.The decomposition and decolorization rate of methyl orange and methylene blue under sunlight is nearly 100%, and the catalyst can be reused, which not only improves the adsorption capacity of pollutants on the catalyst, but also solves the problem that the TiO2 powder is not easy to recycle[35].
(2) Diatomite
Diatomite is a biochemical sedimentary stone formed by the siliceous wall of diatoms. Its main chemical composition is silicon dioxide. It has high porosity, uniform pore size distribution and high chemical stability. The nano-sized TiO2 composite photocatalyst prepared with diatomite as carrier can efficiently treat rhodamine B dye wastewater with a decolorization rate of more than 90%[36]. In addition, the diatomite supported BiOCl/TiO2 composite prepared by precipitation calcination method can be used to degrade formaldehyde under visible light by using the unique photoelectric properties of BiOCl with layered crystal structure[37]. When the mass ratio of TiO2 to BiOCl is 55 ∶ 45, the sintering temperature is 600 ℃, and the pH value of the solution is 6, the degradation rate of formaldehyde by BiOCl/TiO2 composite is as high as 84. 1%. However, granular diatomaceous earth is fragile when disturbed, which will lead to an increase in water turbidity.
Natural minerals have excellent chemical stability, high specific surface area, porous structure and a variety of functional groups, which are pollution-free when used in ecological restoration and conform to the concept of green ecology. However, the active sites of natural minerals are limited, and the specific adsorption capacity of pollutants is low. The adsorption capacity of natural minerals can be improved by loading functional nanomaterials. At the same time, the natural mineral carrier can fix nanoparticles, combined with the adsorption and ion exchange characteristics of mineral pores, to further enhance the decontamination efficiency of natural mineral-based composites. However, in the past decade, there have been few studies on milli-nano structured composites supported by natural minerals, and the existing literature mainly focuses on the fields of fluoride removal and photocatalysis[38]. In addition, when natural minerals are used as functional materials for water treatment, it is often necessary to pretreat the organic impurities existing in the natural minerals themselves. Bentonite is sticky and easy to expand when it meets water, so it is necessary to heat treat the raw material of bentonite. If it is directly used in the dynamic water treatment system, it is easy to cause pipeline blockage. At the same time, there are few studies on the recycling of functional materials with natural minerals as carriers, most of which are disposable, resulting in high cost. China is rich in non-metallic mineral resources, including diatomite, zeolite, bentonite and other porous minerals, and the research on making full use of natural minerals to develop high-performance functional materials for water treatment needs to be further strengthened.

2.4 Ceramic-based carrier

UNK 1 porous pellet
As a high-performance catalyst support material, alumina has excellent characteristics such as high specific surface area, pore volume and thermal stability, and is often used as a support to prepare Mn, Ti and Mg composite catalytic ozonation catalysts (Table 3). The particle size of the active γ-Al2O3 pellet is 3 – 5 mm, and it has excellent mechanical strength, so it is a carrier material suitable for practical application, and its service life can reach 3 – 5 years in a fixed-bed reactor, so it has broad prospects for industrialization[39]. Wang et al. Used Fe(NO3)3·9H2O as the metal precursor and citric acid-modified Al2O3 beads as the porous support to prepare a composite with highly uniformly dispersed Fe species by the "impregnation-calcination" method, in which the Fe species existed in the structure of Al-O-FeIII[40]. Compared with the Fe2O3/Al2O3 catalyst, the prepared material has higher specific surface area, the Lewis acid sites on the surface of the catalyst are significantly increased, and the prepared material shows higher catalytic ozonation activity and organic matter degradation performance. Qiao et al. Prepared metal composite catalyst Mn-Ti-Mg/Al2O3 by impregnation method and applied it to the advanced treatment of coal chemical wastewater by catalytic ozonation[41]. The results showed that the organic pollutants in the wastewater were well degraded by the Mn-Ti-Mg/Al2O3 catalytic ozonation process.
表3 以陶瓷基为载体的毫纳结构复合材料应用于/降解去除水中污染物的研究

Table 3 Studies on millimeter-sized nanocomposites with ceramic-based materials as hosts applied in water decontamination

Millimeter-scale
hosts
Appearance size
of hosts
Nanoparticles Size of
nanoparticles
Preparation methods Target pollutants Removal mecha-
nism
Adsorption capacity
(mg/g)
Treated water
matrix
Experimental scale Operation duration ref
Al2O3 spheres
Al2O3 sphere 3-5 mm Cu-Co
bi-mental
N.A.a Impregnation- carbothermal reduction COD of coal-gasification wastewater Catalytic ozonation 58.8% Coal-gasification wastewater Pilot-scale fixed-
bed, 5 m3/d
30 days 39
Al2O3 sphere 3-5 mm Fe N.A. Impregnation-calcination P-nitrophenol Catalytic ozonation TOC: 68.1% Single contaminant
solution
Laboratory fixed bed reactor 45 min 40
Al2O3 sphere 10.3 mm Fe2O3 N.A. Impregnation-calcination COD and color of distillery wastewater Catalytic ozonation COD: ~78%
Color: ~90%
Distillery wastewater Laboratory ozone
reaction column
30 min 124
γ-Al2O3 sphere 3-5 mm MnxCe1-xO2 ≤25nm Impregnation-calcination COD of coking wastewater Catalytic ozonation COD: >45.6% Bio-treated coking
wastewater
Full-scale applica-
tion, 100 m3/h
885 days 104
γ-Al2O3 sphere N.A. Mn-CeOx N.A. Impregnation-calcination Bromaminic acid Catalytic ozonation TOC: 64.7% Chemical industry
wastewater
Pilot-scale ozone
oxidation tower
22 days 106
γ-Al2O3 sphere 2 mm Cu-Mn oxides 5~10nm High-gravity-assisted im-pregnation Nitrobenzene Catalytic ozonation TOC: 81.7% Single contaminant
solution
Laboratory high-
gravity rotating
packed bed
60 min 125
γ-Al2O3 sphere 2 mm Ce-MnOx N.A. High-gravity-assisted im-pregnation Nitrobenzene Catalytic ozonation TOC: 98.3% Single contaminant
solution
Fixed-bed column 100 min 126
Ceramic membranes
ZrO2/TiO2 flat
ceramic mem-brane
Diameter 47 mm, thickness 2.5 mm FeOCl N.A. Impregnation-calcination Bisphenol A Fenton-like >82% Simulated wastewater Laboratory mem-
brane filtration
120 h 75
α-Al2O3 flat ceramic
membrane
Length 1046 mm, width 280 mm Mn oxides N.A. Impregnation-calcination DOC, PPCPs, EDCs Ozonation-ceramic membrane filtra-tion-biologically active carbon filtra-tion DOC:47.5%
PPCPs:98.5%
EDCs:99.8%
Secondary effluent
from WWTP
Pilot-scale,
20 m3/d
48 days 46
α-Al2O3 flat ceramic mem-brane Diameter 22 mm, thickness 2 mm Co3O4 N.A. Impregnation-calcination Sulfamethoxazole PMS fenton-like 59% Single contaminant
solution
Laboratory mem-
brane filtration
100 min 44
α-Al2O3 flat ceramic
membrane
Diameter 38 mm, thickness 2.5 mm Ti-Mn/TiO2 100nm Dip coating- calcination Dye Red-3BS and Aniline Catalytic ozonation CODCr:52.1% Simulated wastewater Laboratory mem-
brane filtration
6 h 93
Al2O3 spheres
α-Al2O3 tubular
ceramic membrane
Length 1016 mm, diameter 30 mm Ti-Mn/TiO2 20nm Dip coating- calcination Aquaculture wastewater Catalytic ozonation-membrane filtration CODMn: 38.0%
Color: 93.1%
Aquaculture wastewater Pilot-scale 240 min 45
α-Al2O3 tubular
ceramic membrane
Length 250 mm, outer diameter 10 mm, inner diam-eter 7 mm Ce/TiOx 8.3nm Sol-impregnation-calcination Diethyltoluamide Catalytic ozonation- membrane filtration 40% Single contaminant solution Laboratory mem-
brane filtration
30 min 47
Tubular ceramic
membrane
Length 1000 mm, diameter 30 mm TiO2 200~
500nm
Impregnation-calcination COD of
dyestuff wastewater
Membrane filtration- catalytic ozonation CODCr: >90% Secondary effluent
from dyestuff
WWTP
Pilot-scale, 10 t/d 30 days 43
AAO template Diameter 24 mm, thickness 0.06 mm Fe3O4 N.A. Solvothermal
method
Para-chlorobenzoic acid Heterogeneous Fenton N.A. Single contaminant
solution
Laboratory con-
tinuous flow-through
experiment
N.A. 66
(2) ceramic membrane
Ceramic membrane is a kind of inorganic membrane separation material, which is mainly made of γ-Al2O3, ZrO2 and TiO2. Compared with polymer membrane, ceramic membrane has the advantages of high temperature resistance, chemical corrosion resistance, high mechanical strength and long service life. However, the traditional ceramic membrane separation process only has a single physical separation function, and there is a problem of membrane fouling in operation, which makes it difficult to intercept dissolved organic matter and refractory organic matter in water. The coupling of ceramic membrane and advanced oxidation technology has the functions of separation and catalytic degradation, which can not only improve the effluent quality by catalytic degradation of pollutants, but also effectively alleviate membrane fouling, and overcome the shortcomings of difficult catalyst recovery in advanced oxidation technology alone, so it has attracted wide attention in water treatment[42]. The ceramic membrane has a porous structure and is an ideal carrier for loading nanoparticles (Table 3). Therefore, the preparation of catalytic ceramic membranes loaded with metal oxides or multimetallic compounds catalysts has become an important basis for promoting the popularization and application of membrane filtration and catalytic coupling technology. Researchers have prepared catalytic separation ceramic membranes by loading catalyst nanoparticles in ceramic membranes, and developed a series of coupling technologies of membrane separation and advanced oxidation, including photocatalysis, persulfate (PMS) activation, catalytic ozonation, heterogeneous Fenton, etc. Zhang et al. Prepared a tubular ceramic membrane loaded with Mn-TiO2 by impregnation-calcination method, and designed a pilot-scale study of catalytic ozonation coupled membrane separation process for dye wastewater treatment; the water treatment capacity of the process was 10 t/d at an average permeate flux of 110 L/(m2·h), and the effluent CODCr concentration was always less than 10 mg/L[43]. Bao et al. Prepared a porous functional ceramic membrane (CoCM) loaded with Co3O4 for activated PMS degradation of sulfamethoxazole (SMX), and the removal rate of SMX increased by 34% compared with the original ceramic membrane[44]. In addition, the contact angle of CoCM is smaller, the permeability of pure water is higher, and the formation of Co — O — Al bond effectively inhibits the leaching of cobalt during membrane filtration. Chen et al. Supported TiO2 and Ti-Mn oxide successively in a tubular ceramic membrane, and Ti-Mn oxide particles with a size of about 20 nm were uniformly distributed on the surface and in the internal pores of the TiO2 ceramic membrane[45]; Furthermore, a pilot plant of membrane separation coupled with catalytic ozonation process was designed to study the treatment of aquaculture wastewater.Compared with the TiO2 ceramic membrane, the Ti-Mn-TiO2 ceramic membrane showed higher catalytic ozonation ability (the removal rate of organic matter was up to 52. 1%) and membrane anti-fouling ability. Chen et al. Prepared a flat ceramic membrane loaded with Mn oxide, and carried out a pilot study on the advanced treatment of secondary effluent from municipal wastewater treatment plant by coupling with in-situ ozone oxidation process[46]. The results showed that the ceramic membrane loaded with Mn oxide had stronger ozone catalytic activity than the traditional alumina ceramic membrane, and the system operated stably for 48 days at a higher membrane water flux (Dissolved organic carbon)) and a lower ozone dose (5 mg/L), and the effluent Dissolved organic carbon (DOC) concentration was always lower than 5 mg/L. Lee et al. Prepared the Ce-TiOx modified catalytic ceramic membrane with hierarchical porous structure by sol-dip-calcination method, and the Ce nanoparticles with the size of about 8.3 nm were uniformly distributed on the TiOx layer[47]. In the process of DEET degradation by membrane filtration coupled with catalytic ozonation, the mineralization rate of pollutants is as high as 35%.
From the above study, it can be seen that the confinement space of the millimeter-scale carrier can significantly improve the dispersion and stability of nanoparticles, and has a significant regulatory effect on the particle size of nanoparticles. At the same time, the confined space can also control the crystal form and crystal orientation of nanoparticles, thereby affecting their reactivity. The confinement space of milli-nanostructured composites not only affects the structure of the prepared materials, but also affects the reaction process, decontamination mechanism, water phase characteristics and so on. These are attributed to the confinement effect of milli-nanostructured composites, which will be described in detail in the next section.

3 Confinement Effect and Synergistic Decontamination Mechanism of Milli-Nano Structure

The development of millimeter-nanostructured composites can break through the application bottlenecks of nanoparticle materials, such as poor stability and difficult operation. At the same time, the nanoparticle-carrier interaction mechanism generated by the combination of millimeter-scale carriers and nanoparticle materials can improve the utilization and activity of nano-effects. The results show that the confinement space structure of the carrier can produce confinement effect on the decontamination performance of nanoparticles, induce the crystal growth process, change the water chemical characteristics, and affect the electron transfer process, thus significantly affecting the decontamination process and efficiency of nanoparticles.

3.1 Confined Growth Characteristics of Nanoparticles in Millimeter-scale Carrier

Previous studies on confined crystallization and other related directions have shown that nanoconfinement can affect the nucleation and growth of nanoparticles from multiple levels, including crystal stability, growth orientation and crystal face exposure. First of all, the spatial confinement may change the growth of nanoparticles from thermodynamically dominated to kinetically dominated, which affects the stability of the crystal form, that is, it is conducive to the formation and stable existence of metastable nanocrystals. Kinetically dominated metastable structures are first formed in the nucleation and growth of crystals. Due to the limitation of space size, the metastable structures in the nanoconfined system are difficult to effectively distort or undergo Ostwald ripening, so that the metastable structures can exist and be maintained[48]. For example, zirconium phosphate crystals mostly exist in the thermodynamically stable α phase in the open system, while a mixture of α phase and metastable γ phase is formed in the confined space of 7. 9 nm. Compared with α-zirconium phosphate nanoparticles, the P — O bond length of confined zirconium phosphate is shorter, the bond energy is larger, the O 1s electron binding energy is increased by about 1. 0 eV, and the adsorption performance for target metal ions is improved by 10 ~ 90 times. The study shows that there is a significant difference in the adsorption mechanism of zirconium phosphate on heavy metals between the confined system and the open system. The former is mainly the internal sphere coordination with strong selectivity, while the latter is the non-specific electrostatic interaction (Fig. 2)[49].
图2 纳米限域与开放体系中磷酸锆的生长行为及吸附机制[49]

Fig.2 Growth behavior and adsorption mechanism of confined and bulk zirconium phosphate[49]

Secondly, the type of confined space also affects the orientation of crystal growth and the exposure of dominant crystal planes. With the decrease of the confinement size, the influence of the carrier on the nanoparticles increases, and the shape, crystal growth orientation and dominant crystal plane of the nanoparticles may be significantly different. For example, the growth orientation of hydroxyapatite in the columnar pores of etched membranes and anodic aluminum oxide (AAO) membranes is quite different from that in the open system. In the confined system, hydroxyapatite grows mainly along the [001] crystal axis, forming a dominant orientation along the long axis of the columnar nanopores[50]. At the same time, the physical and chemical properties of the support can also affect the nucleation and growth of nanoparticles. Due to the influence of the hydrophilic and hydrophobic properties of the support and the functional groups, the nanopore wall can exert obvious interfacial tension and electrostatic interaction on the crystal nucleus, thus changing the volume free energy and surface free energy of crystal nucleus growth, and further affecting the critical size of crystal nucleation, the shape of crystal nucleus and the growth orientation. For example, Bi nanorods grow along the (202) crystal plane parallel to the film plane in the pores of the AAO film etched by phosphoric acid, while there are two main crystal planes of (012) or (202) in the AAO film etched by sulfuric acid[51]. Completely different from the Fe3O4 nanoparticles with the main exposed crystal face (111) in the open system, the Fe3O4 nanoparticles grown in the 3D graphene nanoconfined space preferentially expose the (400) crystal face, and the adsorption capacity of roxarsone is as high as 454. 48 mg/G, which is nearly 2. 8 times higher than that of the former[52]. Similarly, the confined growth of ZnFe2O4 nanocrystals in the graphene lattice exhibited a high proportion of exposure of (311) facets, which led to a substantial enhancement in the photocatalytic degradation rate of methylene blue, about 20 times higher than that of the previously reported ZnFe2O4 spinel materials[53]. From the above study, it can be seen that nanoconfinement can be used as a means of crystal plane control to control nanoparticles with highly active crystal plane exposure, thereby improving the decontamination performance of materials. However, there is a lack of in-depth research on the confined growth characteristics of nanoparticles in milli-nano structured materials for water treatment, and it is urgent to systematically explore the influence of the size, shape and surface chemical properties of the confined space on the crystal structure of nanoparticles and the means of regulation.

3.2 Confined Adsorption and Regeneration Characteristics of Nanoparticles in Millimeter-sized Carrier

The confined space can not only change the crystal growth behavior of the immobilized nanoparticles, but also change the adsorption performance of nanomaterials to pollutants by changing the solution properties of the confined phase and the acid-base properties of the interface, regulating the internalization process of pollutants, and improving the anti-pollution performance.
The surface physicochemical properties of confined nanoparticles are often significantly different from those of bulk materials. For example, the point of zero charge of hydrated manganese oxide in nanoporous polystyrene confined system increases from about 6.2 in open system to about 10.5 in confined system, and the surface charge reverses from negative charge to positive charge under nearly neutral conditions, resulting in a nearly 10-fold increase in phosphate adsorption capacity[54]. In the open system, the point of zero charge of nano-goethite is about 9. 2, which rises to about 10. 5 in the nanopore of 7. 9 ~ 26.2 nm, and the saturation adsorption capacity of As (V) is increased by 7 ~ 10 times[13,55]. With the decrease of the average pore size from 38. 7 nm to 9. 2 nm, the surface net charge of ferrihydrite loaded in the pore increases gradually, and the adsorption performance of As (III/V) increases significantly[12]. By fitting the surface complexation model, it was found that the adsorption affinity of confined ferrihydrite for H+ was weaker than that of the open system, and accordingly, the adsorption affinity of confined ferrihydrite for metal cations such as Cu2+ was weakened, while the adsorption affinity for anions such as A s O 4 3 - was significantly enhanced[15].
In addition, the properties of the aqueous phase in the nanoconfined system also change significantly. Water phase is the working environment for the purification of pollutants by nanomaterials, and the properties of water phase have an important influence on the interfacial process and mechanism of pollutant purification. For example, the dielectric coefficient of water in low-dimensional nanopores decreases sharply, which makes it easy for pollutants to form electrically neutral ion pairs with ions of different charges through association, thus changing the Coulomb interaction between nanomaterials and pollutants[56]. In addition, the decrease of the dielectric constant of confined water reduces the hydration number of ions, which in turn affects the interaction between ions and adsorption sites and the adsorption mechanism[57]. For example, zeolites and other materials have nanopore structures, and ions larger than the size of the pore structure need to be partially dehydrated before entering the pore channel. The adsorption mechanism of the dehydrated ions in the nanopore changes from surface ion exchange to inner sphere complexation, thus increasing the adsorption capacity and selectivity[58]. At the same time, many studies have observed that the pH of the solution in the nanoconfined space is significantly lower than that in the open system, and the adsorption process of heavy metals, arsenic, phosphate and other pollutants on iron oxides is very sensitive to pH, which can be dominated by monodentate mononuclear coordination, bidentate binuclear coordination, outer ring coordination or surface precipitation at different pH[59,60][61,62].
In addition to changing the adsorption mode of phosphorus, arsenic, fluorine and other pollutants on nanoparticles, confinement can also promote the reversible internalization of target pollutants in nano-metal oxides under certain conditions. The so-called internalization refers to the process in which pollutants are adsorbed by solid phase materials and then enter their crystal lattices to form new crystal structures. For example, the main mechanism of phosphate removal by hydrous lanthanum oxide (HLO) is inner sphere complexation, whereas the HLO nanoparticles confined in the crosslinked polystyrene support immobilize phosphate through the formation of LaPO4·xH2O nanocrystals, and the regeneration efficiency can be increased to about 95%[4]. For another example, nanoconfinement changes the adsorption of phosphate on La(OH)3 from surface coordination to lattice internalization, which can be transformed into LaPO4 crystals in only about 1 day (Figure 3A). This may be due to the fact that the nanoconfinement makes the La(OH)3 in a metastable state, and phosphate can quickly enter the lattice to achieve internalization[63]. At the same time, the LaPO4 formed by internalization is also in a thermodynamic metastable state, and the OH- can quickly enter the crystal lattice during regeneration to promote the transformation of the LaPO4 crystal into a La(OH)3,O as to realize the reversible interconversion between the crystal forms of the LaPO4 and the La(OH)3 and successfully break through the bottleneck that the La(OH)3 is difficult to regenerate and recycle after adsorbing and dephosphorizing[4].
图3 限域体系中纳米颗粒对污染物的吸附特性:(a)La(OH)3吸附磷酸根的晶型变化[63];(b)离子交换树脂的Donnan膜效应对污染物的富集及离子交换作用[11];(c)限域驱动磷酸钙分区结晶并提升抗污染能力[65]

Fig.3 Confined adsorption properties of milli-sized nanocomposites. (a) Changes in crystal phase of La(OH)3 for phosphate adsorption[63]; (b) The Donnan membrane effect of ion exchange resin for the enrichment and ion exchange of pollutants[11]; (c) The confinement-driven calcium phosphate partitioning crystallization and improved anti-pollution ability[65]

In addition, the carrier space structure of the milli-nano structure composite material can improve the enrichment, adsorption selectivity and anti-coexisting matrix interference performance of the material to the target pollutant through the Donnan film effect. For example, when ion exchange resin is used as a millimeter-scale carrier, its positively charged quaternary ammonium functional groups exclude cations (such as Ca2+, Mg2+, and K+) in water through the Donnan membrane effect, while enhancing mass transfer and pre-enrichment of inorganic anionic pollutants (such as arsenic, fluorine, and phosphate), which can be removed by adsorption of immobilized nanoparticles (such as HFO and HZO) (Figure 3B)[2,11,12,64].
Nano-confinement can also significantly improve the anti-pollution ability of nanoparticles. Ca2+, Mg2+ and silicate, which coexist widely in water, are easily adsorbed by nano-hydrated iron oxide (HFO) and polymerized on the surface to form scale, resulting in a significant decline in the deep decontamination performance of the material. Although some studies have been carried out to alleviate the adverse effects of coexisting substances on advanced water treatment by adding scale inhibitors, coagulation and membrane separation, it is difficult to fundamentally overcome the problems that the scale content is much higher than the target pollutant and the nano-HFO is seriously polluted by scale. Zhang et al. Found that the scaling behavior of Ca2+ and Mg2+ plasma in confined nano-iron oxide composites was quite different from that in open systems, which changed from mainly scaling on the surface of nano-HFO to zonal independent crystallization.The coexisting ions such as Ca2+ and Mg2+ not only do not affect the adsorption activity of confined HFO, but also provide additional adsorption sites through the formation of phosphate precipitates, which greatly improves the adsorption performance of pollutants such as phosphate (Figure 3C)[65].

3.3 Confined Catalytic Oxidation Characteristics of Nanoparticles in Millimeter-sized Carrier

Nano-confined catalysts have been widely used in the study of catalytic oxidation of organic pollutants in water, and the confinement effect has led to significant enhancement of the activity and stability of many catalysts. Among them, the development of some nano-confined catalysts is mainly used to explore the performance and mechanism of confinement effect, such as carbon nanotubes, graphene, metal organic frameworks and other materials as carriers, which are still easy to agglomerate and difficult to recycle, and are difficult to be applied to large-scale water treatment. The following will focus on the catalytic oxidation characteristics of confined catalysts with milli-nano structure, such as composite materials with alumina templates, alumina spheres and ceramic membranes as carriers.
Firstly, the nanoconfined space can effectively shorten the mass transfer distance from free radicals to pollutants, and solve the problem of low utilization efficiency of hydroxyl radicals (HO ·) caused by mass transfer limitation in heterogeneous Fenton reaction, thus rapidly degrading pollutants. For example, when the Fe3O4 nanoparticles grown in the nanopores of the alumina template are used as Fenton-like catalysts, the efficient degradation of methylene blue can be achieved in a very short residence time (14 s), which is far better than the catalytic reaction of unconfined Fe3O4 nanoparticles under the same conditions (≥ 3 H)[66]. The study suggests that within the critical confinement scale of 20 nm, the catalytic reaction can achieve high-intensity and intensive space utilization of HO · (Figure 4A).
图4 膜孔的限域催化氧化特性:(a)限域空间内HO·高强度、集约化的高效利用[66];(b)膜孔对大分子有机物的尺寸排阻效应及对小分子有机物限域氧化[75]

Fig.4 Confined catalytic oxidation in membrane pores. (a) Intensive utilization of HO· in confined space[66]; (b) Size exclusion effect of membrane pores on large molecular organic compounds and confined oxidation of small molecular organic compounds[75]

Secondly, nanoconfinement can improve the activity of the catalyst by regulating the solution properties in the microenvironment. The active sites on the surface of iron oxides are easily competed by hydroxyl ions, which leads to the sensitivity of catalytic Fenton-like reaction activity to the pH of the solution. The unique hydrogen bond network structure of water molecules in the nanoconfined space, the interaction of the "pore wall-nanoparticle" surface electric double layer, and the functional groups of the carrier can all lead to the change of the pH of the solution in the microdomain[67][68,69]. For example, when the pore size of AAO is below 58 nm, the pH of the solution in the confined space is lower than that in the open system, and decreases with the decrease of the pore size of the membrane, which leads to the degradation rate of phenols, aniline and other pollutants by Mn3O4 formed in AAO nanopores (3 ~ 5 nm) is three orders of magnitude higher than that in the open system[70,71][72]. Similarly, the pore size of mesoporous silicon decreases from 1000 nm to 1 nm, and the difference between the pH of the solution in the pore and the bulk increases from nearly 0 to nearly 2 units[73]. At the same time, some studies have proposed that nanoconfinement can adjust the microenvironment of catalytic sites, thereby changing the Fenton-like reaction path and kinetic process[74]. However, at present, there is a lack of characterization means and computational methods to deeply analyze the micro-mechanism and micro-environment.
In addition, nanoconfinement can also provide new ideas for improving the oxidation selectivity of advanced oxidation reactions. For example, the active species produced by Fenton reaction is generally HO ·, which is easily quenched by dissolved organic matter widely existing in water, and the oxidation selectivity of target pollutants is insufficient. Zhang et al. Used FeOCl nanocatalyst grown in situ in the pores of ultrafiltration ceramic membrane to carry out confined catalytic Fenton-like reaction (Fig. 4B), and found that nanoconfinement could inhibit organic matter with larger molecular size from entering the pores through steric hindrance effect.At the same time, the high-intensity limited oxidation of small molecular organic matter is carried out in the nano-pores, so as to realize the selective oxidation of small molecular organic pollutants such as p-chlorobenzoic acid and other new pollutants[75].
In recent years, the research of catalytic separation membrane is increasing. The functional coupling of advanced oxidation and membrane separation not only promotes the large-scale application of advanced oxidation technology, but also realizes seamless docking with existing common processes. Membrane pore filtration can solve the problem of mass transfer limitation relying on diffusion in traditional sequencing batch reactor, and enhance the mass transfer effect. At the same time, the nano-membrane pores are equivalent to numerous nano-reactors, and the confined space can not only improve the free radical generation efficiency of advanced oxidation and the degradation efficiency of pollutants, but also inhibit membrane fouling and achieve the self-cleaning effect of the separation membrane. For example, Chen et al. Prepared a catalytic ceramic membrane doped with manganese oxide in the membrane pores, and coupled it with in-situ ozone and biological activated carbon, and applied it to the pilot study of reclaimed water treatment and reuse, revealing the synergistic effect of the coupling process[46]. Among them, the manganese oxide ceramic membrane can significantly catalyze ozone oxidation, greatly improve the generation rate of hydroxyl free radicals, effectively remove dissolved organic matter, polysaccharides and proteins in reclaimed water, improve the removal rate of biopolymers and humic-acid-like substances, and greatly reduce the resistance of filter cake layer and gel layer, effectively alleviate the pollution of ceramic membrane.

4 Practical application of milli-nanostructured composite in water treatment

4.1 Practical Application of Milli-Nano Structure Composite Material in the Field of Adsorption, Separation and Purification

The milli-nano structural composite material is convenient to use and operate, and can realize continuous flow, large-scale production and engineering application. In the practice of adsorption decontamination engineering, adsorption separation technology is mainly applied through fixed bed/adsorption column. The milli-nano structural composite material is filled into a fixed bed, and the treatment effect of the milli-nano structural composite material on actual water body under the condition of continuous long-term operation is tested, so as to verify the stability of large-scale production and the practical application potential. At present, there are few pilot studies on the application of composite nanomaterials in the field of adsorption and decontamination, and there are even fewer commercial and engineering applications. Relevant research teams at home and abroad, such as Pan Bingcai of Nanjing University, Lee of Seoul University in Korea and SenGupta of Caspian University in the United States, have carried out continuous exploration and research in this direction, and some milli-nano structural composites have achieved large-scale production and engineering application. Based on the types of target pollutants (phosphorus, fluorine, arsenic, heavy metals, etc.), the practical application of milli-nano structure composite materials in the field of adsorption and separation will be introduced below.

4.1.1 Dephosphorization

Pan Bingcai and others have long been committed to the development of millimeter-nanostructure composite materials and the research on the technology and principle of advanced water treatment, and have developed a series of resin-based millimeter-nanostructure composite materials suitable for selective adsorption of phosphate, including Fe-based composite nanomaterials HFO @ D201, Mn-based composite nanomaterials HMO @ NS, Zr-based composite nanomaterials HZO @ D201 and La-based composite nanomaterial La-201[10,76][54][2][4]. The above materials have shown the advantages of high selectivity for phosphorus removal, easy regeneration and resistance to coexisting matrix interference in the laboratory research process. Some milli-nano structural composite materials have achieved large-scale production and engineering application (Figure 5), and have carried out 10 ~ 1000 t/d deep phosphorus removal pilot technical verification in Jiangsu, Guangdong, Hong Kong and Canada[5,77 ~79]. Among them, Zhang et al. Used La-series composite nanomaterial La-201 to conduct a pilot study on deep phosphorus removal with a treatment scale of 10 m3/d and a duration of 8 months for river water in Hong Kong (influent total phosphorus concentration of 0.09 mg/L), which could reduce the effluent phosphorus concentration below the eutrophication limit (0.02 mg/L), and showed a good removal effect on orthophosphate (91.23%) and total phosphorus (78.51%), indicating that the adsorption system had strong robustness[5]. Hua et al. Applied the iron composite nanomaterial HFO-201 to a sewage treatment plant in Yixing City, Jiangsu Province, which adopted the membrane bioreactor (MBR) process, and carried out the scale-up verification of the phosphorus removal technology for biochemical effluent (the filling amount of the material was 2.6 L). The effective treatment capacity of the material for the actual phosphorus-containing wastewater (TP = 1.0 ~ 2.0 mg/L) was as high as 4000 BV (the penetration point was TP = 0.5 mg/L), and the adsorption capacity was 4.4 ~ 4.8 mg P[79]. HFO-201 can be regenerated efficiently (regeneration rate > 95%) by using NaOH-NaCl mixed solution after penetration, which preliminarily verifies the adaptability of the deep phosphorus removal technology of composite nanomaterials to municipal wastewater treatment plants, and shows a certain prospect of popularization and application. In recent years, they have further realized the ton-level production of a variety of phosphorus removal milli-nano structural composite materials (such as iron series material HFO-201, zirconium series material HZO-201 and lanthanide series material La-201) and the trial production of skid-mounted integrated system (with a treatment capacity of 60 t/d), and carried out a 180-day continuous field pilot study on the deep phosphorus removal of municipal sewage biochemical tail water[80]. The fixed bed column test with the actual biochemical tail water as the treatment object showed that the macro-prepared milli-nano structure composite material could maintain a stable long-term deep phosphorus removal (effluent TP < 0.1 mg/L) and organic matter synergistic pollution reduction effect under the real water quality conditions. Their work provides technical reference for the preparation of new phosphorus removal materials, the development of phosphorus removal technology and equipment suitable for municipal sewage plants, and the engineering application of nanotechnology in water treatment. Lee et al. Of Seoul National University used chitosan-based nano-iron oxide composite to conduct a 33-day field pilot test on natural water (total phosphorus concentration of 0.020 ~ 0.046 mg/L) in Suwon City, South Korea, and the total phosphorus removal rate reached 52.3%, and the working capacity of the material was 0.059 mg P/G[81].
图5 潘丙才等开发的毫纳结构复合材料。(a)不同复合材料的外观;(b)材料样品;(c)规模化量产的毫纳结构复合材料和(d)固定床水处理工程装置。

Fig.5 Millimeter-sized nanocomposites developed by Prof. Bingcai Pan’s research group. (a) Appearance of different composite materials; (b) Material samples; (c) Large-scale production of nanoscale composite materials; and (d) Fixed-bed water treatment engineering equipment

4.1.2 Defluorination

Aiming at the problem of advanced treatment of fluoride in industrial wastewater, Pan Bingcai et al. Developed zirconium-based milli-nano structure composite materials, which can selectively and deeply remove fluorine in water through inner sphere coordination, and realize the large-scale production of related materials[11,82,83]. A demonstration project (≥1000 m3/d) of advanced fluoride removal was built in an integrated circuit wastewater treatment plant in Nanjing. The effluent (fluoride concentration of 4 ~ 5 mg/L) from the secondary sedimentation tank of the wastewater treatment plant was treated. The project has been running stably for three months, and the fluoride concentration in the effluent is less than 1.0 mg/L (less than 0.6 mg/L in most of the time).The results met the Class III standard of the Environmental Quality Standard for Surface Water (GB 3838-2002), and a pilot study on deep fluoride removal from groundwater was carried out. During 150 days of continuous operation, the fluoride concentration in the effluent was stably controlled below 1. 0 mg/L by the fluoride removal unit consisting of five stages of adsorption columns in series[83]. The structure and defluorination performance of the zirconium composite nano-adsorption material after repeated recycling are stable, and the long-term working performance is excellent, which proves the practical application potential of the zirconium composite nano-structure composite material. In recent years, Pan Bingcai et Al. Developed a new milli-nano structure composite material (LALDH-201) using anion exchange resin D201 loaded with Li/Al layered double hydroxide (LALDH), and designed a fixed bed device, which was applied to the treatment of fluorine-containing groundwater somewhere in Yunnan, with good regeneration effect and no reduction in working capacity after five cycles[84]. Liu Jinhuai et al. developed a "natural mineral nanocomposite defluorination agent drinking water defluorination technology", that is, using the pores of natural zeolite to fix defluoridation nanomaterials. At present, defluoridation projects have been established in high-fluorine areas such as Sanyi Town, Mengcheng County, Anhui Province, with a daily treatment capacity of 2400 tons of high-fluorine water, and the effluent quality meets the national drinking water standard (GB 5749-2006)[85]. At the same time, the waste after defluorination can be used as building materials to achieve harmless treatment.

4.1.3 Arsenic removal

The commercial arsenic removal adsorbent ArsenXnp developed by Caspian University and Bangladesh University of Engineering and Science is to load Fe2O3 nanoparticles in macroporous anion exchange resin with an apparent size of 0.3 – 1.2 mm,It has high stability and has been successfully used for the treatment of arsenic-containing groundwater in remote villages in western Bangladesh, India, with efficient arsenic removal (effluent arsenic concentration less than 50 μg/L) at a treatment capacity of more than 20 000 BV[7]. Sylverster et al. Used ArsenXnp to conduct field tests in New Mexico and Arizona in the United States for 91 days and 122 days, respectively, and showed high selective adsorption of arsenic, with the concentration of arsenic in the effluent less than 10 μg/L[86]. The field test found that the ArsenXnp has a good anti-interference ability for common anions in water, such as nitrate, sulfate, chloride and so on, but the interference of silicate and phosphate ions still exists. Pan Bingcai et al. Prepared resin-based hydrous zirconia (HZO-201) milli-nano structure composite material, and applied it to remove As (V) in actual acid mining and metallurgical wastewater. On the premise of ensuring that the concentration of As (V) in the effluent is less than 50 μg/L, the single batch treatment capacity reaches 2900 BV[3]. They have solved the problem of large-scale production of resin-based zirconium milli-nano structural composites and successfully achieved ton production[87].

4.1.4 Heavy metal removal

Pranudta et al. Used gel-type cation exchange resin loaded with HFO (C100-Fe) to prepare a new adsorbent used as a fixed bed filler and used to remove Pb2+ in industrial acidic wastewater from battery production plants[88]. After 30 days of continuous operation, the pilot-scale field study showed that C100-Fe could selectively adsorb Pb2+ and achieve efficient selective removal of Pb2+ (effluent Pb2+ concentration was less than 0. 2 mg/L) at nearly 6500 BV treatment capacity. Pan Bingcai et al. Invented a variety of new environmental nanocomposites and realized large-scale production by using the unique network aggregation confinement effect and Donnan enhanced diffusion effect of crosslinked polystyrene materials, which have been widely used in the advanced treatment of heavy metal wastewater in electronic electroplating, tanning, mining and metallurgical industries in Taihu Lake, Huaihe River and Three Gorges Reservoir areas.Heavy metals such as Pb, Cr, Cu and Ni in wastewater are selectively and deeply removed, and 12 demonstration projects have been built. The treated effluent can meet the latest requirements of upgrading and emission reduction, and can realize the recycling of about 400 tons of heavy metals such as Cr and Ni every year[89].

4.2 Practical Application of Milli-Nano Structure Composites in the Field of Catalytic Degradation and Pollution Purification

Advanced oxidation technologies (such as ozonation, Fenton/Fenton-like, electrocatalysis, photocatalysis) can effectively degrade new pollutants, such as pharmaceuticals and personal care products (PPCPs) and endocrine disrupting chemicals (EDCs), by producing reactive species with strong oxidizing properties. However, a large number of advanced oxidation technology research is still in the laboratory stage, and the practical application is affected by many factors, such as the suitability of catalyst and process equipment, operation cost and so on. The development of milli-nano composite catalyst provides a good platform for the practical application and promotion of advanced oxidation technology.It not only overcomes the problems of easy agglomeration of catalyst particles, difficult separation and recovery, and difficult realization of continuous flow in the traditional sequencing batch advanced oxidation process, but also improves the removal efficiency of pollutants and alleviates pore blockage and pollution by using the confinement effect of nanopores. However, there are few reports on other practical applications of AOPs processes in academic research, such as Fenton, photocatalysis, electrocatalysis, etc., except for traditional Fenton technology[90]. The reason is that Fenton or Fenton-like reaction processes such as H2O2 or persulfate often require a large amount of oxidant, and the transportation and storage of oxidant is a challenge for large-scale wastewater treatment. Electrochemical oxidation technology is difficult to be applied to large-scale treatment projects because of its limited treatment scale and high electrode cost. Photocatalytic oxidation requires high uniformity of light, and the suspended solids and high chroma in wastewater are not conducive to the transmission of light, which limits the efficiency of photocatalytic technology and the feasibility of engineering. Relatively speaking, the preparation method and generator equipment of ozone are relatively mature, which can provide stable oxidant supply for large-scale wastewater treatment. The addition of ozone is similar to air aeration, which can scour the membrane surface and catalyst, and enhance the mass transfer effect. Therefore, the practical application of AOPs process based on catalytic ozonation is relatively more, and the milli-nano structural composite materials used mainly include catalytic separation membranes and functional alumina pellets.
At present, Quan Xie of Dalian University of Technology, Zhang Xihui of Tsinghua University, Masten of Michigan State University, Wang Jianbing of China University of Mining and Technology (Beijing) and Zhang Guoquan of Dalian University of Technology are mainly committed to the development of heterogeneous catalytic ozonation technology and its application in the pilot test and engineering application of actual water bodies at home and abroad. The following is a brief introduction to the characteristics and practical applications of the milli-nano structural composites of these research groups.

4.2.1 Ozonation/catalytic membrane filtration coupling technology

Inorganic membranes have the advantages of strong chemical stability, pollution resistance, strong hydrophilicity and long service life, while organic polymer membranes are easily degraded and aged when exposed to various free radicals produced by AOPs for a long time. Therefore, the application of ceramic membranes in water treatment has increased rapidly in recent years, and the coupling of ceramic membranes with catalytic properties and AOPs has broad application prospects.
Focusing on the development and preparation of new ozone catalytic ceramic membranes, Quan Xie et al. carried out a series of research work and prepared different types of catalytic tubular ceramic membranes (such as Ce-Ti composite catalytic ceramic ultrafiltration membrane and mesoporous Ti-Mn catalyst modified catalytic ceramic ultrafiltration membrane with multi-stage pore structure).To explore the removal efficiency of pollutants in water and the effect of membrane fouling control by catalytic ozonation-ceramic membrane separation coupling process[43,45,91 ~94]. They designed and assembled the pilot test equipment of catalytic ceramic membrane and ozone oxidation coupling system (Fig. 6) with reservoir source water (about 15 t/d), biochemical effluent from municipal sewage treatment plant (10 t/d), aquaculture wastewater (220 L/H) and pigment production wastewater (10 t/H) as treatment objects, and all of them achieved good organic pollutant removal effect and anti-pollution performance[94][91][45,92][43].
图6 全燮教授等研发的(a)管式陶瓷膜、(b)膜组件、(c)中试装置流程示意图及(d)现场照片[91,92]

Fig.6 Catalytic ceramic membranes developed by Professor Xie Quan’s research group. (a) Tubular ceramic membranes; (b) membrane components; (c) flow diagrams and (d) on-site photos of pilot-scale equipment[91,92]

Zhang Xihui and others have been committed to the research and development of nano-flat ceramic membrane and its application in advanced water treatment for a long time, and have realized the large-scale production and engineering application of ceramic membrane (Fig. 7). Ceramic membrane coupled ozonation technology has been applied to the pilot study of micro-polluted source water, reclaimed water, industrial park sewage, petrochemical wastewater, sludge water and so on, and has achieved good results, and has realized the efficient integration with the existing water treatment process. For example, they used ozone/ceramic membrane integrated process to treat secondary effluent and reuse reclaimed water in the wastewater treatment plant of Baoshan Industrial Park in Hebi, Henan Province, with a treatment scale of 30,000 m3/d. In recent years, Zhang Xihui et al. Prepared a catalytic ceramic membrane doped with manganese oxide in the pores of the membrane, constructed an in situ ozone/ceramic membrane-Biological activated carbon (BAC) coupling process, realized the integration of the membrane and catalytic oxidation process, applied it to the indirect potable reuse of reclaimed water in a reclaimed water plant in Beijing, and conducted a 24-day pilot-scale study (Biological activated carbon)[95]. The in-situ ozone/manganese oxide ceramic membrane-biological activated carbon coupling process can efficiently remove conventional pollutants and emerging trace organic compounds, and the effluent quality DOC is less than or equal to 2 mg/L.It can meet the requirements of "Water Quality Standard for Groundwater Recharge of Urban Sewage Reclamation and Reuse" (GB/T 19772-2005), and the coupling process significantly improves the biological stability of reclaimed water, and its operation cost per ton of water is estimated to be 0. 324 yuan, which has good economy.
图7 张锡辉等研发的(a)平板陶瓷膜、(b)膜组件、(c)臭氧氧化-陶瓷膜过滤-BAC中试实验现场装置图及(d)流程示意图[95]

Fig.7 Flat ceramic membrane developed by Prof. Xihui Zhang’s research group. (a) flat ceramic membrane sheet; (b) ceramic membrane modules; (c) on-site photos and (d) process flow diagram of the pilot-scale ozone-ceramic membrane-BAC experimental equipment[95]

Masten of Michigan State University in the United States has conducted a series of research on ozone/ceramic membrane coupling process, including the effect and mechanism of ceramic membrane catalytic ozone in controlling membrane fouling and degrading pollutants, as well as the development of various ceramic membrane materials with catalytic oxidation functions[96~100][101]. The ozone/catalytic ceramic membrane coupling process has been applied to the treatment of surface water such as real river water and eutrophic lake water, showing excellent pollutant removal effect and anti-pollution performance[102].

4.2.2 Functional γ-Al2O3 pellet

Wang Jianbing et al. Of China University of Mining and Technology (Beijing) developed a practical millimeter-scale spherical MnxCe1-xO2/γ-Al2O3 ozone catalyst, and assembled a nano-bubble enhanced ozone absorption-catalytic oxidation superposition reaction system.The engineering application research on the secondary biochemical effluent of actual coking wastewater was carried out for 885 days, and the long-term stable and efficient operation effect was achieved, and the effluent quality met the requirements of the Discharge Standard of Pollutants for Coking Chemical Industry (GB 16171-2012)[103][104]. At the same time, they revealed that the main mechanism of catalyst deactivation during long-term operation is that the active sites on the catalyst surface are occupied by inorganic salts/crystals, which limits the interaction between ozone and active sites. Based on this, an in-situ alternate backwash regeneration process was developed and applied to the advanced treatment of biochemical effluent from high-salinity wastewater. The engineering application for more than two years has verified the high efficiency and stability of the process system[105].
In addition, Zhang Guoquan et al. Of Dalian University of Technology developed a γ-Al2O3-based milli-nano structure ozone catalyst loaded with Mn-CeOx, and designed a two-stage ozone reaction tower (Fig. 8), which was applied to the treatment of pharmaceutical wastewater and chemical wastewater by catalytic ozonation process[106]. In the pilot-scale continuous operation, the catalyst showed stable and efficient treatment effect.
图8 大连理工大学张国权等研发的Mn-CeOx/γ-Al2O3臭氧催化剂、量产照片及中试现场装置图[106]

Fig.8 Mn-CeOx/γ-Al2O3 ozone catalysts developed by Professor Guoquan Zhang’s research group at Dalian University of Technology, with production photos and pilot-scale plant equipment diagram[106]

5 Conclusion and prospect

Since the 21st century, scholars at home and abroad have made some progress in the creation and application of composite nanomaterials for water treatment, and have realized the cross-scale assembly of nanoparticles (< 10 ~ 100 nm) and millimeter-scale carriers. The preparation of milli-nanostructured composites not only overcomes the application bottleneck of easy agglomeration and difficult separation and recovery of nanoparticles, but also endows the materials with unique confinement effect, which improves the decontamination performance, selectivity and anti-interference performance. From the above pilot test and engineering application cases, it can be seen that the design of milli-nano structure promotes the practical application of nanomaterials. Although milli-nanostructured composites have broad application prospects, the current understanding of the confinement effect mechanism is obviously insufficient, which affects the precise regulation of high-performance milli-nanostructured composites. Most composite nanomaterials lack application testing in real scenarios and analysis of technical economy and safety, which affects the technological transformation of nanomaterials from laboratory to practical application. Some typical scientific issues and technical challenges are described below.

5.1 The research on scientific issues related to nano-confinement effect is obviously insufficient.

1) The mechanism of carrier-nanoparticle interaction is unknown. Nanoconfinement can significantly change the structure of nanomaterials, but there are few reports on the regulation and mechanism of carrier-nanoparticle interaction on the structure and activity of nanoparticles, which is still in the stage of passive discovery and appearance observation. From the point of view of development, the growth mechanism of metal oxide crystals in confined space can be combined with classical nucleation theory.The effects of confinement size and surface properties on the surface energy, critical size of nucleation and supersaturation during the crystal growth of nanoparticles were systematically analyzed, so as to master the control methods of directional exposure of crystal faces of metal oxides and realize the preparation of high-performance composites. In addition, the mechanism of the effect of confined space on the regeneration process of nanomaterials is not clear and needs to be further explored.
2) The understanding of carrier-nanoparticle coupling/synergy is not deep. Although the improvement mechanism of the decontamination performance of nano-functional materials has been recognized by the limited carrier at present, it is still not deep and comprehensive enough, and it stays on the superficial analysis of the treatment effect. For example, the synergistic and coupling effects of carriers and nanoparticles in the decontamination process are seriously neglected, and the adsorption and transformation characteristics of target pollutants on the surface and interface of composite nanomaterials and their process mechanisms are in the black box or gray box stage, which urgently need to be discussed in depth from multiple dimensions by combining theoretical calculations and characterization techniques with high spatial and temporal resolution.
3) Lack of in-situ characterization of decontamination characteristics and processes. At present, there is a lack of research on the pattern recognition of milli-nanostructured composite decontamination, the form and transformation process of pollutants in confined environment, and the reaction process and characterization of nanoparticles, and the information revealed by the existing ex-situ characterization methods such as electron spectroscopy is insufficient, so it is urgent to build an in-situ, high spatio-temporal resolution characterization method. For example, in the process of phosphorus removal, the formation of phosphorus-containing nanocrystals is the key way to improve the capacity and selectivity of phosphorus removal, but the mechanism of in-situ formation and reverse transformation (regeneration) of phosphorus-containing nanocrystals in the confined structure is not clear, which restricts the regulation and enhancement of the structure and process of phosphorous-containing nanocrystals.

5.2 Practical application challenges of nanocomposites

1) It is necessary to construct a systematic method for the preparation and structural regulation of milli-nano structural composites. The size of nanoparticles in the existing milli-nano structure composite materials is generally too large, and the nano-effect has not been fully utilized. The results show that when the size of nanoparticles is reduced to less than 10 nm, the proportion of highly reactive edge atoms on the surface of materials increases sharply, resulting in significant size and surface effects. In addition, the adsorption reaction usually occurs only on the surface of the material, while the ions in the solution may produce lattice substitution and solid diffusion with the internal crystal structure of the sub-10 nm particles, thus changing the nature of the adsorption process. Therefore, the development of millimeter-sized composites with sub-10 nm structure is the key to improve the deep removal performance of pollutants. At present, there are two main methods for the preparation of milli-nanostructured composites: confined growth method and embedding assembly method, but they face the problems of uneven distribution, agglomeration and overgrowth of nanoparticles caused by the difficulty of low-dimensional pore diffusion and the high surface energy of small nanoparticles. These problems have brought great challenges to the preparation and mass production of milli-nano structural composites with high stability and high activity. It is still a challenge to realize the macro-scale preparation of milli-nanostructured composites with confined sub-10 nm particles. The innovation of preparation methods depends on further revealing the interaction mechanism between carriers and nanoparticles and clarifying the influence of carriers on the stability and activity of nanoparticles.
2) It is necessary to consider the application and adaptability in real scenarios. It has always been a good vision for researchers to effectively connect scientific discoveries and technological innovations at the molecular or micro level to provide scientific basis and technical support for the synergy of pollution reduction and carbon reduction. Despite the excellent pollutant removal efficiency of milli-nano structured composites with nano-effects, most of the current research work is in the laboratory, and the efficiency test tends to be carried out with simulated sewage and wastewater. Especially for the advanced oxidation technology using nano-confined catalysts, the related research focuses on the research and development of new materials, but few studies focus on its practical application value. It is worth noting that in real scenarios, temperature, dissolved oxygen and coexisting substrates will synergistically affect the purification effect, material stability and regeneration process. For example, shedding, leaching, and regeneration of nanomaterials are issues of high concern for practical applications. In addition, for the development of composite nanomaterial treatment unit process, it is necessary to consider the organic connection and efficient integration with the existing water treatment process. Furthermore, selective adsorption and catalytic oxidation are expected to achieve high-purity enrichment and directional transformation of high-value pollutants in sewage and wastewater, thus building resource recovery strategies and approaches. However, there is an obvious lack of relevant research in this direction, and relevant technological innovation and application are urgently needed.
3) The economy and safety of new nanomaterials need to be systematically evaluated. At present, the preparation steps of composite nanomaterials are generally complicated and the material and energy consumption are high, so it is particularly important to develop an efficient, low-cost, green and mass production process of nanomaterials for practical application. In recent years, scholars have begun to consider the safety of nanomaterials from the perspective of the whole life cycle, taking into account the environmental impact of solvents, energy consumption and waste used in the preparation process.It also includes by-products, microplastics and metal ion dissolution produced in the process of removing pollutants in the application stage of nanomaterials, as well as reagent consumption and energy consumption in the process of regeneration or cleaning, and disposal of waste materials. At present, the safety assessment of nanomaterials mostly focuses on the chemical safety risk of the material itself, ignoring the overall environmental impact caused by the complex interaction with other coexisting substrates, natural environment and equipment used in the long-term operation of actual water treatment.
To sum up, this paper reviews the research status of milli-nanostructured composites in the field of water treatment from the aspects of preparation methods, structural properties, confined growth characteristics of nanoparticles, adsorption characteristics, catalytic oxidation characteristics and practical applications.The research deficiencies and application challenges of related directions are put forward, in order to provide theoretical basis and technical reference for promoting the practical application of nanomaterials.
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