Design of plasmonic Ag-TiO2/H3PW12O40 composite film with enhanced sunlight photocatalytic activity towards o-chlorophenol degradation

A series of plasmonic Ag-TiO2/H3PW12O40 composite films were fabricated and immobilized by validated preparation technique. The chemical composition and phase, optical, SPR effect and pore-structure properties together with the morphology of as-prepared composite film are well-characterized. The multi-synergies of as-prepared composite films were gained by combined action of electron-capture action via H3PW12O40, visible-response induced by Ag, and Schottky-junction formed between TiO2-Ag. Under simulated sunlight, the maximal K app of o-chlorophenol (o-CP) reached 0.0075 min−1 which was 3.95-fold larger than that of TiO2 film, while it was restrained obviously under acid condition. In the photocatalytic degradation process, ·OH and ·O2 − attacked preferentially ortho and para position of o-CP molecule, and accordingly the specific degradation pathways were speculated. The novel composite film exhibited an excellent applicability due to self-regeneration of H3PW12O40, well-protection of metal Ag° and favorable immobilization.

surface plasmon resonance (SPR) effect enables free carrier to transport and harvest visible light without a requirement of favorable band alignment 26,27 . Moreover, the Schottky barrier formed between semiconductor and noble metal significantly benefits the separation of electron-hole pairs [28][29][30] . As an especially attractive surface plasmon metal, Ag has been widely used to modify TiO 2 due to the properties of relatively low-cost, excellent conductivity, chemical stability, catalytic activity, and near-field enhancement [31][32][33][34][35][36][37] . Therefore, it is conceivable that introducing Ag into TiO 2 /H 3 PW 12 O 40 may enhance the visible-light catalytic activity.
Moreover, current studies on photocatalysis are mainly based on powder-type photocatalysts, which severely hinders their practical applications due to the post-treatment problems in these systems such as separation, recovery and reuse. To overcome these disadvantage, much attention has been paid to explore immobilized TiO 2 -based film materials 38,39 . Among various immobilized methods, the sol-gel method has been utilized extensively 40,41 . However, the occurrence of reunion and the required high temperature treatment exert a significantly adverse influence on the morphology and circulation of the immobilized materials 42,43 . In our previous study, a validated sol-gel-hydrothermal route followed by a spin-coating method was established, which exhibited a high catalytic stability and remarkable recyclability 11,12 . The hydrolysis rate was efficiently controlled by adding glacial acetic acid to avoid the reunion. Meanwhile, programmed temperature hydrothermal method with relatively low temperature was designed to ensure the crystallization of TiO 2 and Keggin structure of H 3 PW 12 O 40 in the high-pressure reactor.
Thus, a recoverable plasmonic Ag loaded TiO 2 /H 3 PW 12 O 40 composite film was designed in the current study and its photocatalytic activity was evaluated in terms of degrading o-chlorophenol (o-CP) under simulated sunlight. The morphology and structure of the composite film have been well-characterized; batch experiments were conducted to reveal the influence of Ag and H 3 PW 12 O 40 loading amount, initial concentration and pH value of o-CP on the photocatalytic performance to the target reaction; the photocatalytic mechanism and possible degradation pathways of o-CP were discussed deeply; finally, the recyclability of the composite films was tested by three times' o-CP degradation run.

Methods
The titanium tetraisopropoxide (TTIP, 98%) was purchased from Sigma-Aldrich Corporation. H 3 PW 12 O 40 (GR), isopropanol (AR), AgNO 3 (AR), o-CP (AR) were purchased from China Pharmaceutical Group. Other chemicals were of reagent grade and applied without further purification. Double distilled water was utilized throughout the experimental procedures.
Catalyst preparation. The preparation of TiO 2 /H 3 PW 12 O 40 film is described in the previous studies 11,12 .
On the basis, AgNO 3 was dropped gradually into isopropanol solution during the stirring according to certain proportion with TTIP or H 3 PW 12 O 40 , and the remaining steps were the same as the previous reported method. The obtained hydrogel was spin-coated onto quartz substrate (50 mm × 15 mm × 1 mm), and the as-prepared composite film was denoted as Ag(x%)-TiO 2 /H 3 PW 12 O 40 (y%), in which x and y represented the loading amount of Ag (wt%: 0.5%, 1% and 2%) and H 3 PW 12 O 40 (wt%: 5%, 10% and 15%), respectively. The unary TiO 2 and binary Ag-TiO 2 , TiO 2 /H 3 PW 12 O 40 films were also prepared with the above procedures.
Catalyst characterization. The loading amounts of Ag and H 3 PW 12 O 40 in the composite films were determined by a Leeman Prodigy Spec inductively coupled plasma atomic emission spectrometer. X-ray diffraction (XRD) patterns were obtained on a Rigaku D/max-3c X-ray diffractometer (Cu Kα radiation, λ = 0.15405 nm). UV-Vis diffuse reflectance spectra (UV-Vis/DRS) were recorded on a Cary 500 UV-Vis-NIR spectrophotometer. X-ray photoelectron spectroscopy (XPS) was performed on a VG-ADES 400 instrument with Mg Kα-ADES source at a residual gas pressure lower than 10 −8 Pa. Raman scattering spectra were recorded on a Jobin-Yvon HR 800 instrument with an Ar + laser source of 488 nm wavelength in a macroscopic configuration. Field-emission scanning electron micrographs (FESEM) were obtained using a JEOL 6340 F scanning electron microscope. Nitrogen porosimetry was measured by a Micromeritics ASAP 2020. Surface areas were calculated by Brunauer-Emmett-Teller (BET) equation. Pore size distributions were calculated by BJH model based on the nitrogen desorption isotherm (samples were degassed for 1 h under vacuum at 363 K, and then for 12 h at 473 K). Transmission electron microscope (TEM) micrographs, high resolution TEM (HRTEM), and selected area electron diffraction (SAED) micrographs were recorded by a JEM-2100F HRTEM at an accelerating voltage of 200 kV.
Photocatalytic activity test. The photocatalytic degradation of o-CP was conducted in a home-made quartz photoreactor under the simulated sunlight provided by a PLS-SXE300 Xe lamp (300 W, Beijing Trustech Co. Ltd., China) placing ca. 15 cm above the reactor. The lamp was equipped with an IR cut filter to match the natural sunlight with the wavelength ranging from 320 to 780 nm and light intensity of 200 mW/cm 2 measured by a radiometer (OPHIR, Newport, USA). In the photocatalytic system, 2 pieces of the coated films (TiO 2 film, Ag-TiO 2 film, TiO 2 /H 3 PW 12 O 40 composite film, or Ag-TiO 2 /H 3 PW 12 O 40 composite film) with a weight of ca. 5.0 mg were submerged in the o-CP solution (100 ml). Prior to irradiation, the films were maintained in dark for 30 min to reach adsorption-desorption equilibrium of o-CP. After irradiation, a fixed amount of o-CP solution was sampled and analyzed at regular intervals. The degradation degree of o-CP solution was analyzed by HPLC equipped with Waters 2489 UV/visible detector and symmetry C18 (4.6 × 250 mm, particle size 5 μm), with a mobile phase of acetonitrile (40%) and H 2 O (60%, containing 0.1% acetic acid) at a flow rate of 0.7 ml·min −1 with a detection wavelength of 254 nm. The total organic carbon (TOC) was analyzed by a TOC-500 (Shimadzu). The intermediates during o-CP degradation were identified by a Waters Acquity UPLC/Quattro Premier XE LC/MS system. Besides, the concentrations of low molecular weight organic acids and Cl − were tested using a DX-300 ion chromatography equipped with AS4A-SC column and CDM-II conductivity detector.  Table 1. The results indicated that Keggin unit and metallic Ag were successfully loaded by the current methods and the saturation Keggin structure of H 3 PW 12 O 40 was retained integrally in the composite film with a P: W ratio of 1:12. Figure 1 shows that XPS spin-orbit lines of Ti 2p 3/2 (458.3 eV), Ti 2p 1/2 (464.0 eV), W 4f 7/2 (35.5 eV), W 4f 5/2 (37.2 eV), Ag 3d 5/2 (368.0 eV) and Ag 3d 3/2 (374.0 eV) were characteristic of Ti(IV) oxidation state, W(IV) oxidation state and metallic Ag in Ag-TiO 2 /H 3 PW 12 O 40 composite film, respectively [29][30][31] . O 1 s XPS line of Ag-TiO 2 /H 3 PW 12 O 40 composite film exhibited three peaks at 529.5 eV, 531.6 eV and 532.9 eV, originating from lattice oxygen species of TiO 2 , Keggin unit and adsorbed oxygen, respectively 44,45 . Thus, it can be concluded that (1)  (3) the introduction of metallic Ag was confirmed by a spin energy separation of 6.0 eV 47 , since under heating parent AgNO 3 was decomposed gradually into metallic Ag that tended to aggregate to form nanocrystals, as the following reactions 48 :        The surface-enhanced Raman scattering (SERS) signals indicated a strong SPR effect was generated in all the Ag-deposited films in spite of such a low Ag deposition amount. Compared with no Ag-deposited film, SPR excited by visible light would lead to an enhanced electromagnetic field around the nanoparticle, which could significantly promote the generation of "hot electron" at the interface of metal particle Ag and semiconductor TiO 2 . Furthermore, a potential energy difference (E SPR -ϕ b ) between potential energy (E SPR ) and Schottky barrier (ϕb) was also established at the interface according to the energy band structure feature of Ag and TiO 2 crystal, which could facilitate the transfer of "hot electrons" from Ag to the conduction band (CB) of TiO 2 and hinder the reverse transfer at the same time. While the shift of Raman peaks may be owing to the alterations of electronic density induced by electrons transfer among TiO 2 , H 3 PW 12 O 40 and Ag, which may improve the activity of catalyst. It was also agreed with other reports 56,57 .
SEM. As shown by FESEM (Fig. 7), the as-prepared TiO 2 , Ag-TiO 2 , TiO 2 /H 3 PW 12 O 40 , and Ag-TiO 2 /H 3 PW 12 O 40 film varied considerably in morphology. TiO 2 particles illustrated a regular rice shape with a size of ca. 80 nm; Ag-TiO 2 particles were composed with spheres of TiO 2 (2-4 μm) and Ag (ca. 500 nm); TiO 2 /H 3 PW 12 O 40 particles displayed as spheres with diameters ranging between 80-100 nm covered by packed humps; whereas the surface of Ag-TiO 2 /H 3 PW 12 O 40 particles became smoother than that of TiO 2 /H 3 PW 12 O 40 due to the deposition of Ag into the pore structures of TiO 2 /H 3 PW 12 O 40 . Ti, P, W, and Ag were observed to distribute homogeneously in Ag-TiO 2 / H 3 PW 12 O 40 film by EDS analysis (Fig. 8).
BET and BJH. Figure 9 exhibits the adsorbed nitrogen amounts increased rapidly at p/p 0 < 0.1 and H3 hysteresis loop excited at p/p 0 = 0.4-0.8, indicating the presence of microporosity (<2 nm) and mesoporosity (2-50 nm) in the prepared photocatalysts (TiO 2 , Ag-TiO 2 , TiO 2 /H 3 PW 12 O 40 and Ag-TiO 2 /H 3 PW 12 O 40 ). BET surface area and pore volume of each prepared photocatalyst are summarized in Table 2. These results were consistent with BJH desorption pore distribution curves and pore diameters calculated by BJH method (Fig. 10). BET surface area (169.9 m 2 ·g −1 ) and pore volume (0.4390 cm 3 Figure 11 illustrates the photocatalytic degradation of o-CP (5 mg·L −1 , 100 ml, pH = 6.3)     12,13 . Additionally, loading of Ag could not only enhance the quantum efficiency via generating Schottky junction at the interface between Ag and TiO 2 (Fig. 5), but also increase the absorption of visible-light due to SPR effect, which has been confirmed by the above characterization (Fig. 2). In order to clarify the enhancement of SPR effect, o-CP photocatalytic degradation was carried out under visible light (The lamp was equipped with the filter to cut UV light with 200-400 nm wavelength). After introducing Ag into TiO 2 and TiO 2 /H 3 PW 12 O 40 film, the degradation efficiency towards o-CP increased from 5.55% (TiO 2 ) to 21.80% (Ag-TiO 2 ), and from 13.75% (TiO 2 /H 3 PW 12 O 40 ) to 26.60% (Ag-TiO 2 /H 3 PW 12 O 40 ) (Fig. 11), which was attributed to the loading of plasmonic metal.
The adsorption capacity of all the photocatalysts (Fig. S1 of Supporting Information) was limited (TiO 2 : 6.67%; Ag-TiO 2 : 12.38%; TiO 2 /H 3 PW 12 O 40 : 9.94%; Ag-TiO 2 /H 3 PW 12 O 40 : 5.89%) even though they possessed large BET surface area, which could be attributed to the low amount of the catalyst (ca. 5.0 mg) in the current system. Compared with other related researches, the as-prepared Ag-TiO 2 /H 3 PW 12 O 40 composite film represented a more excellent property on the light utilization with a comparable catalyst amount 58 .   films did not alter the adsorption capability of o-CP (5 mg·L −1 , 100 ml, pH = 6.3) significantly (Fig. S3). The degradation efficiency of o-CP (82.40%) peaked with a Ag loading amount of 1% in Ag-TiO 2 /H 3 PW 12 O 40 film (Fig. 13). It implied that a great majority of transferred electrons were trapped due to the strong electron accepting ability of metallic Ag, resulting in an effective separation of the electrons and holes. However, excessive Ag nanoparticle not only acted as an electron-hole recombination center, but also blocked partial UV-light that could reach the surface of TiO 2 59,60 , which further decreased its photocatalytic activity. Thus, Ag(1%)-TiO 2 /H 3 PW 12 O 40 (10%) represented the maximum photoactivity, and was selected in subsequent photocatalytic experiments. Fig. S4, the direct photolysis rate of o-CP (100 ml, pH = 6.3) was 5.11%, 3.83% and 1.83% with initial concentrations of 5 mg·L −1 , 10 mg·L −1 , and 20 mg·L −1 , the photocatalytic degradation rate was 82.40%, 76.60% and 63.70%, respectively (Fig. 14). Thus, both the direct photolysis and photocatalytic degradation rate decreased gradually with the raise of initial concentration of o-CP by reason of the restraint on light transmittance and light utilization of catalyst. Additionally, with a fixed catalyst dosage, the more o-CP molecules adsorbed and accumulated on the film surface (Fig. S5), the less contact between the reactive oxygen species and catalyst 61 . Herein, the minimum initial concentration (5 mg·L −1 ) was the optimal condition for photocatalytic degradation. Fig. 15, at the alkaline conditions, the degradation rate was 79.70% at pH = 9.2 and 73.80% at pH = 12.1, which was significantly higher than that at the acid condition (46.80% at pH = 3.1). The contact of o-CP molecules with the catalyst or sunlight irradiation was intercepted under the acid condition (Figs S6 and S7), resulting in a low degradation efficiency. Under the alkaline condition, the adsorption process was hindered by the electrostatic repulsion between the electronegative composite film (both Ag and H 3 PW 12 O 40 are fairly strong electron acceptors) and negatively charged o-CP. Whereas, the direct photodegradation rate elevated rapidly with increase of pH values, since high pH value was in favor of generation of hydroxyl ions 62 , which would subsequently enhance the photodegradation efficiency via forming hydroxyl radicals with holes.  The photocatalytic degradation rate achieved the maximum value (82.40%) at pH = 6.3 due to the largest adsorption amount of o-CP. In addition, photocatalytic activity of TiO 2 peaked at pH pzc (pH = 6.25), which was close to the initial pH value of o-CP solution (pH = 6.3). Hence, pH = 6.3 was optimal initial pH value for the photodegradation of o-CP 63,64 . Photocatalytic kinetics. The kinetics of photocatalytic reactions under different conditions are summarized in Table 3. The results indicated the kinetics could be well described by simplified Langmuir-Hinshelhood (L-H) Model:

Effect of initial pH. As illustrated in
in which K app is the apparent constant as the basic kinetic parameter when the initial concentration is low; c is the initial concentration of the target compound. Under the optimal condition, K app of o-CP photocatalytic degradation reaction achieved 0.0075 min −1 by Ag(1%)-TiO 2 /H 3 PW 12 O 40 (10%) film, which was 1.63-fold, 3.26-fold and 3.95-fold larger than that of Ag-TiO 2 , TiO 2 /H 3 PW 12 O 40 film and TiO 2 film, respectively. K app fluctuated largely along with the variation of H 3 PW 12 O 40 loading amount and initial pH value, which suggested both of the factors exerted an essential influence on the kinetics of o-CP degradation.
Photocatalytic Mechanism. In general, the photocatalytic degradation can be regarded as a process of generation, transfer, and consumption of the photogenerated carriers 65 . The photocatalyst absorbed the incident photons with energy above the semiconductor's band gap, generating the same number of electrons and holes, in which the hole abstracted electrons from absorbed pollutants or reacted with H 2 O to generate ·OH; while the conduction band electrons reduced the absorbed oxygen to produce ·O 2 − that further generated ·OH via chain reactions. In order to reveal the mechanism of enhanced photocatalytic activity of the plasmonic Ag-TiO 2 /H 3 PW 12 O 40 photocatalyst in depth, the active species generated during the process of photocatalyzed o-CP degradation were identified by free radicals and holes trapping experiments in the current study. Na 2 -EDTA (0.0037 g) 66 , isopropanol (0.1 ml) 67 , and benzoquinone (0.0108 g) 68 were employed to scavenge the holes (h + ), hydroxyl radicals (·OH), and superoxide radicals (·O 2 − ), respectively. After adding Na 2 -EDTA, the degradation efficiency did not alter significantly, implying    Table 3. The kinetics of o-CP photocatalytic reaction. the holes played a minor role in either oxidization or generation of ·OH during the o-CP degradation process. Whereas, the presence of isopropanol and benzoquinone decreased the degradation rate markedly to 38.4% and 51.5%, respectively, indicating both ·OH and ·O 2 − acted as a major role during the process (Fig. 16). The detailed photocatalytic mechanism of Ag-TiO 2 /H 3 PW 12 O 40 towards o-CP degradation under the simulated sunlight (320 nm < λ < 780 nm) is illustrated in Fig. 17. Under the UV-light (320 nm < λ < 400 nm), the electrons were firstly promoted from the valence band to the conduction band of TiO 2 , left the holes in the valence band of TiO 2 . Whereafter, the photogenerated electrons were transported constantly to metallic Ag and accumulated on its surface, forming the Schottky junction between Ag and TiO 2 . Furthermore, H 3 Figure 19(a) shows that the concentrations of acetic acid and butanedioic acid peaked within 4-6 h during the degradation process, while the formic acid concentration achieved the maximum value within 4-8 h, suggesting the ring-opening reaction occurred during the o-CP degradation. The releasing rate of Cl − was low before 6 h and increased greatly after 6 h, due to the occurrence of C-Cl bond cleavage. The results implied a possibility that the ring-opening reaction of o-CP molecule mainly occurred in the early stage during the degradation process, while most of C-Cl bond were broken subsequently. At 12 h, the concentration of Cl − reached 1.58 mg·L −1 , while the concentrations of low molecular weight organic acids decreased to 0.007 mg·L −1 , 0.002 mg·L −1 and 0.013 mg·L −1 for acetic acid, butanedioic acid and formic acid, respectively, which could be further mineralized to CO 2 and H 2 O. Moreover, as shown in Fig. 19(b), the releasing of Cl − and formation of low molecular weight organic acids could decrease pH value during the process, which would impede the progress of photocatalytic degradation, as confirmed previously (Fig. 15). Therefore, the decrease of pH value during the degradation process may explain why o-CP cannot be decomposed and mineralized completely.  Table 4). The mass fragment peaks were identified as o-chlorophenol (126.8 m/z), 2-chlorohydroquinone or 3-chlorocatechol (142.8 m/z), and 2-chlorobenzoquinone (144.8 m/z). Accordingly, the possible photocatalytic degradation pathways of o-CP were as follows (Fig. 20). As the key role in the photocatalytic degradation, ·OH and ·O 2 − attacked preferentially the ortho and para position of o-CP molecule 69 . The ortho position (Path 1) was attacked by ·OH generating 3-chlorocatechol followed by H-abstraction, and then 5-chloropentanol was generated and further decomposed to formic acid, butanedioic acid and Cl − after ring-opening reaction; The para position (Path 2) was attacked by both ·OH and ·O 2 − producing 2-chlorohydroquinone and 2-chlorobenzoquinone simultaneously, hereafter, butanediol and butanedioic acid were formed via ring-opening reaction, together with chloroethylene as another intermediate product that further produced acetic acid by dechlorinating processes. Finally, o-CP can be mineralized into Cl − , CO 2 and H 2 O. Recyclability of the catalyst. From viewpoint of practical applications, the recyclability is an essential aspect for the composite film photocatalyst, which can not only greatly reduce the cost but also avoid secondary pollution. In the current study, Ag(1%)-TiO 2 /H 3 PW 12 O 40 (10%) film was selected to conduct the recycling experiment under the optimum condition for three times, the composite film was dipped in ethanol to remove the absorbed o-CP molecules after each catalytic run, then washed by distilled water and dried at room temperature. The results showed that even after 3 times recycle, the composite film could still degrade more than 80.00% of o-CP (Fig. 21), and only 0.13% H 3 PW 12 O 40 and 0.05% Ag dropped from the film.
The electrochemical impedance spectroscopy (EIS) of TiO 2 , Ag-TiO 2 , TiO 2 /H 3 PW 12 O 4 , and Ag-TiO 2 / H 3 PW 12 O 40 film was implemented to quest their charge transport capability. It is well-known that the smaller arc radius is, the higher separation efficiency of electrons-holes becomes. As displayed in Fig. 22 Fig. 23 with the cycles of light-on and light-off. Distinctly, Ag-TiO 2 /H 3 PW 12 O 4 and Ag-TiO 2 film represented a higher photocurrent intensity during the cycles of on-off intermittent irradiation, reconfirming that the introduction of Ag into the catalyst was feasible to increase both the quantum efficiency and separation efficiency of photogenerated electron-hole pairs, which was corresponding to the results of EIS. However, the stability of Ag-TiO 2 film was not the same as Ag-TiO 2 /H 3 PW 12 O 4 and its photocurrent intensity decreased after  Table 4. The chemical formulas of o-CP and the main intermediate products.
every cycle of light-on and light-off, which further induced the decreasing of photocatalytic activity. This can be attributed to the fact that metal Ag can be easily oxidized after depositing on the surface of TiO 2 particles, if the cover was absent.
Overall, an excellent photocatalytic activity, stability and reproducibility of Ag-TiO 2 /H 3 PW 12 O 4 composite film was attained from the following approaches: (1) the excellent photocatalytic activity was attributed to a large quantity of holes and electrons produced by adsorbing simulated sunlight irradiation induced by SPR effect; (2) the enhanced quantum efficiency was owing to the strong electron-accepting capability of H 3 PW 12 O 40 and the formation of Schottky junction via the modification with metallic Ag; (3) the excellent recyclability was due to the preferably preparation method, the self-regeneration of H 3 PW 12 O 40 as well as loading of Ag 0 into the TiO 2 / H 3 PW 12 O 40 framework.

Conclusions
An efficient plasmonic Ag-TiO 2 /H 3 PW 12 O 40 composite film with enhanced sunlight photocatalytic activity was prepared by modified sol-gel-hydrothermal method combined with spin coating technique. It has been revealed  that the composite film was an excellent photocatalytic activity towards o-CP degradation, mainly due to the extra active electrons and holes generated by SPR effect as well as Schottky junction via the modification with metallic Ag. ·OH and ·O 2 − were confirmed to play an essential role in photocatalytic degradation of o-CP, and the possible o-CP photodegradation pathways were put forward according to the identified intermediate products.
The mineralization testified the strong oxidation ability of Ag-TiO 2 /H 3 PW 12 O 40 catalyst, which could decompose the contaminants into CO 2 and H 2 O. It also showed a remarkably excellent stability and recyclability of the composite film in degrading o-CP, which may greatly limit the economic cost and secondary pollution. The studies in this work provide important information on o-CP degradation, which will promote the technical development for its removal. The plasmonic composite film could be used further for the decomposition of persistent organic pollutants with low concentration in practical water and wastewater treatment.