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Article

2D Mesoporous Channels of PMO; a Platform for Cluster-Like Pt Synthesis and Catalytic Activity in Nitrophenol Reduction

1
International Center for Materials Nanoarchitechtonics (MANA), National Institute for Materials Science (NIMS), 1-1 Namiki, Tsukuba, Ibaraki 305-0044, Japan
2
Graduate School of Pure and Applied Sciences, University of Tsukuba, Tsukuba, Ibaraki 305-8573, Japan
3
Materials Science and Nanotechnology Department, Faculty of Postgraduate Studies for Advanced Sciences (PSAS), Beni-Suef University, 62511 Beni-Suef, Egypt
4
Organic and Nano Group (ONG), Department of Chemistry, University of Maragheh, 55181-83111 Maragheh, Iran
5
Department of Chemistry, School of Science and Technology, The University of Georgia, Tbilisi 0171, Georgia
*
Authors to whom correspondence should be addressed.
Catalysts 2020, 10(2), 167; https://doi.org/10.3390/catal10020167
Submission received: 28 December 2019 / Revised: 20 January 2020 / Accepted: 21 January 2020 / Published: 1 February 2020
(This article belongs to the Special Issue Catalysis for Two-Dimensional (2D) Materials)

Abstract

:
Thiourea-bridged organosiloxane is used to synthesize a periodic mesoporous organosilica (PMO). Since this PMO has an S-enriched surface, owing to thiourea functional groups, it exhibits strong coordination toward Pt ions, and it shows a high tunability in the Pt nanoparticles size. This hybrid mesoporous material is employed as a catalyst in the efficient reduction reaction of 4-nitrophenol to 4-aminophenol at room temperature in an aqueous media.

Graphical Abstract

1. Introduction

Rapid industrialization and the release of pollutants are an overwhelming threat for green spaces and sustainable nature [1,2,3,4,5,6]. Specifically, the release of organic pollutants from industry (e.g., dyes and drug wastewater) and agriculture (e.g., fertilizers and pesticides) to groundwater and rivers are huge sources of pollution in the ecosystem. One of the most common organic classes of pollutants in industrial wastewaters is nitroaromatics. These are assumed to be toxic materials since they can damage kidney and liver in humans [7,8,9]. These compounds are being widely investigated to solve this issue. However, the challenges in this area have not been fully solved yet. 4-nitrophenol (4-NP) is a typical nitroaromatic compound that is considered to be toxic. However, many processes have been developed for 4-NP removal by reducing it to amino form or degradation with strong (photo)catalytic degradation methods. Catalytic reduction of 4-NP to p-aminophenol (p-AP) is an effective removal approach of 4-NP. Interestingly, 4-AP is considered to be a valuable intermediate product to manufacture many analgesics and antipyretic drugs (paracetamol, phenacetin) [10,11,12,13,14,15].
Very recently, noble metal nanoparticles (MNP), e.g., Pt, Pd, and Au, have attracted wide attention due to their dominant (photo)catalytic activities in a variety of the reactions such as coupling, oxidation, reduction, and decomposition [16,17,18,19,20,21,22,23,24,25,26]. However, the high surface energy of MNPs results in easy agglomeration and consequent loss in catalytic activity which strongly discourages their application in the field of catalysis [12,15,25,27]. Therefore, the loading of MNPs on an appropriate nanostructure to harness the aggregation and stabilize the generated nanoparticles has been acknowledged as a favorable strategy to solve the current issue [8,13,26,28]. Besides, minimizing the size of MNPs toward a single atom is a newly emerging approach to maximize catalytic efficiency by direct involving the maximum number of atoms in the catalysis [29]. To achieve such accomplishments, the functional groups of the surface in support may play a crucial role in determining the fate of nanoparticles. Sulfur-based functional groups can be superior functional groups to accomplish this. Among MNPs, Pt with a relatively lower price and diverse catalytic activity have attracted a great attention and been extensively applied in different catalytic reactions [16,17,20,25,30,31].
In the recent decade, periodic mesoporous organosilica (PMO) materials with an ordered porous structure and wide variety of organic moiety, tunable architecture, and high surface area have been widely employed in the heterogeneous and green design of the catalysts [19,32,33,34,35,36,37]. Some of them might be promising candidates to generate and support sub-2 nm sized MNPs with uniform distribution, which is the key to attaining high catalytic performance [38,39,40,41]. We studied the tenability of organosiloxane precursors with TEOS in the rational synthesis of PMOs [41]. Very recently, we also synthesized 1,3-bis(3-(triethoxysilyl) propyl) thiourea (BTSPT) through a new approach and incorporated it to synthesize a new thiourea-bridged PMO (PMO-TU) with a perfect 2D hexagonal mesostructure (Scheme 1). This thiourea-bridged PMO was successfully incorporated for ultrasmall Pd nanoparticles with a high uniformity and stability which showed an excellent catalytic activity toward formic acid dehydrogenation and coupling reaction [19,40]. Here, we present the synthesis of ultra-small and uniform Pt nanoparticles, which is successfully deposited on the surface of the PMO-TU and employed in the catalytic reduction of 4-NP to 4-AP by Pt supported PMO-TU (Pt@PMO-TU).

2. Results and Discussion

We synthesized PMO-TU in the presence of a triblock copolymer, P123 (poly(ethylene glycol)-block-poly(propylene glycol)-block-poly(ethylene glycol)), and employed it as unique support for the synthesis of sub-2 nm Pt nanoparticles. Then, we characterized these materials using different instruments. To check whether the functional groups are created and preserved during the synthesis process of PMO, we checked the FTIR spectra of BTSPT, PMO-TU and Pt@PMO-TU (Figure 1a). A broad band at 3265 cm−1 is attributable to N–H stretching of the thiourea group. Two characteristic peaks at 2974 and 2928 cm−1 correspond to the asymmetric and symmetric stretching modes of aliphatic C–H bonds in propyl chain, respectively. A peak at 1553 cm−1 may refer to C=S bond stretching of the thiourea. Another peak at 1167 cm−1 corresponds to the stretching mode of C–N bond. Another two peaks at 1104 and 1080 cm−1 relate to the Si–O–Si linkage. Additionally, thermal gravimetric analysis (TGA) of Pt@PMO-TU confirms the existence of the organic thiourea (Figure 1b). The weight loss, starting from 200 °C to 500 °C can be related to the thiourea bridges of PMO-TU, which is approximately ~12 wt%. Based on the % of weight loss, the mol% of PMO and the organic moiety (TU) can be estimated as 1.5 mol% and 0.16 mol%, respectively.
The N2 adsorption-desorption isotherm of both PMO-TU and Pt/PMO-TU, as shown in Figure 1c,d, show a type IV behavior which is a representative of SBA-like mesoporous material [19,42]. The BET surface area for PMO-TU and Pt/PMO-TU was calculated to be 475 and 331.8 m2·g−1, respectively. Pt loading over the PMO support has caused less than 30% reduction in the value of the exposed surface area which confirms that the structure has not experienced a significant loss in the mesoporosity [19]. The total pore volume was calculated to be 1.19 cm3·g−1 for the PMO-TU support and decreased to 0.388 cm3·g−1 after Pt loading owing to the volume occupied by Pt nanoparticles deposited inside the pores. The average pore diameter has not changed significantly and was estimated to be 6.18 ± 0.61 nm and 6.9 ± 0.7 nm for the PMO-TU and Pt/PMO-TU composite, respectively.
Figure 2a shows a scanning electron micrograph for the PMO-TU support which has the morphology of entangled rod-like structures with an average diameter of 200 nm. The HRTEM micrograph (Figure 2b) reveals the ordered hexagonal symmetry of the PMO-TU substrate with a periodic honeycomb arrangement. Figure 2c shows the finely well-distributed Pt nanoparticles after deposition over the PMO-TU support. Figure 2d shows the morphology of the Pt/PMO-TU nanocomposite after being used as a catalyst for the reduction of 4-NP. It can be observed that the PMO still preserves its morphology without significant changes after being used as a catalyst, indicating its structural stability.
The loading of fine Pt nanoparticles in the PMO-TU support can be visualized by observing the sample using a high-angle annular dark-field scanning transmission electron microscope (HAADF-STEM), indicated in Figure 3a,b. HAADF-STEM images further show a uniform ultra-small distribution of Pt nanoparticles with good dispersion throughout the structure. For better understanding, two points from the Pt/PMO-TU sample were selected under STEM observation and investigated by using the energy-dispersive X-ray spectroscopy (EDS), shown in Figure 3c,d. Both EDS spectra (001 and 002 positions) show the corresponding peaks of Pt which confirm the existence of Pt located in the PMO-TU substrate.
The catalytic activity of the Pt/PMO-TU was tested for the reduction of 4-NP using NaBH4 as a reducing agent. As shown in Figure 4a, the PMO-TU substrate does not show any significant catalytic activity whereas the Pt/PMO-TU could reduce 4-NP totally in approximately 14 min. Figure 4b shows the time-dependent decrease in the absorption spectra of 4-NP leading to the formation of 4-AP (absorption peak at 293 nm). This absorption peak confirms that the decrease in the concentration of 4-NP is due to actual catalytic conversion to produce 4-AP and not due to simple adsorption over the surface of the nanocomposite. Additionally, we studied the starting time and finishing time of the reaction by HPLC analysis (Figure S1) and we found that the results are consistent with UV-Vis data in Figure 4b.
Figure 5a shows the effect of different reaction temperatures on the time-dependent decay of the 4-NP. The reaction was conducted at 25, 50 and 75 °C. As shown, increasing the reaction temperature leads to an increase in the reaction rate. The Arrhenius plot for such reaction is shown in Figure 5b where the activation energy calculated from the plot was equal to 18.327 KJ/mol. This value is the lowest reported so far (as far as the authors are aware) for the reduction of 4-NP over a Pt-based catalyst which indicated the catalytic superiority of the Pt/PMO-TU towards 4-NP reduction. The effect of changing the Pt/PMO-TU catalyst dose on the reaction rate was investigated and the results are shown in Figure 6a. It can be shown that increasing the catalyst dose to 20 mg leads to the complete reduction of 4-NP in approximately four minutes. The relation between the catalyst dose and the first-order reaction constant is shown in Figure 6b where a linear relation can be observed.
The initial concentration of NaBH4 was varied and the results are shown in Figure 5a. As shown, starting with an initial concentration of 250 mM lead to the complete reduction of 4-NP in less than 1 min. According to the authors’ best knowledge, the shortest conversion time reported for the reduction of 4-NP was two minutes using Pt-Pd nanocubes supported on nitrogen doped hollow carbon nanospheres [7]. Figure 7b indicates that increasing the NaBH4 concentration leads to a consequent increase in the value of the rate constant.
The stability of catalytic materials is a critical point. So, we evaluate the reusability of the Pt@PMO-TU catalyst by performing three cycles for 4-NP reduction. The results after each cycle showed high catalytic performance with efficient conversion (Figure 8), which points out the high stability and recyclability of our catalyst. Furthermore, we examined the reaction solution after three cycles by atomic adsorption spectroscopy (AAS) and the it shows that the leaching of Pt from PMO-TU is negligible.
To compare our results with the previous reports, we listed different types of catalysts in terms of time, conversion% and reaction conditions, as summarized in Table 1. Interestingly, it can be remarked that the catalytic activity obtained by our material is outstanding when compared with the previously reported catalysts.
Revisiting the mechanism of 4-NP reduction on noble metal surface through NaBH4 (as reductant) by Chen and Li [46], 4-NP first deprotonates to 4-aminophenolate, then, approaches to the surface of metal (here Pt) and accepts the electron and subsequently converts to the reduced form. The donated electron from metal is supplied by NaBH4. A plausible schematic for the reduction of 4-NP to 4-AP is presented in Scheme 2.

3. Materials and Methods

3.1. Synthesis of Pt@PMO-TU

PMO-TU was synthesized according to literature [19]. PtCl4 was first dissolved in a distilled water and then added to the dispersion of PMO-TU in ethanol while stirring. The dispersion was stirred for 1 h at room temperature and then, the solid was collected by centrifugation, washed with ethanol, and dried at 60 °C in an oven. The obtained solid in this step was redispersed in methanol and a methanolic solution of NaBH4/MeOH was added dropwise to the dispersion in stirring mode within 30 min at room temperature. Finally, the final product as a solid was centrifuged, washed, and dried at 60 °C and named Pt@PMO-TU. According to ICP-AES analysis, the wt% of Pt was ~1.5.

3.2. Characterization

FTIR spectra were collected using a Shimadzu IR-460 spectrometer. The morphology was observed with a HITACHI SU- 8230 microscope, operating at 10.0 kV. HRTEM images and EDX elemental maps were taken with a JEOL JEM-2100F microscope, operated at 200 kV. N2 adsorption–desorption isotherms were analyzed using a Quantachrome Autosorb at 77 K. The Pt loading amount was recorded by inductively coupled plasma atomic emission spectroscopy (ICP-AES) on a Perkin Elmer 2100DV. Thermogravimetric curves were performed using a Hitachi TG/DTA6200. UV−vis spectra were obtained with a UV-1800 biotech. HPLC chromatograph was determined using Shimadzu LC-20AD.

3.3. Catalytic Test

Pt@PMO-TU (10 mg) was dispersed in an aqueous solution of 4-NP (3 mM, 40 mL) and sonicated for 5 min. Then, NaBH4 (5 mmol, 190 mg) was added dropwise to the solution and stirred until the completing the reaction. During the reaction, sampling from reaction dispersion was performed by a syringe equipped with a syringe filter (for filtering the catalyst from the reaction media) and analyzed by UV-Vis spectrometer to monitor the reaction progress.

4. Conclusions

The synthesis of Pt nanoparticles with ultrasmall and uniform size in 2D mesochannels of thiourea-bridged periodic organosilica was confirmed by STEM technique. The catalytic activity of this PMO with Pt nanoparticles showed a high catalytic activity in the reduction of 4-nitrophenol. According to our study, the activation energy for this reaction in the presence of this catalyst was found to be 18.3 kJ. mol−1. All effective parameters on the catalytic activity of Pt@PMO-TU were studied and it was found that the catalyst is applicable at room temperature in aqueous media.

Supplementary Materials

The following are available online at https://www.mdpi.com/2073-4344/10/2/167/s1, Figure S1: HPLC chromatograph of 4-nitophenol (4-NP) and 4-aminophenol (4-AP).

Author Contributions

Conceptualization, E.D.; methodology, M.E. and H.M.; software, M.E. and H.M.; validation, M.E., Y.G. and E.D.; formal analysis, M.E. and H.M.; investigation, H.M., R.T.M. and R.T.; data curation, S.R., R.T.M. and S.K.; writing—original draft preparation, M.E. and Y.G; writing—review and editing, E.D.; supervision, S.R., N.F., S.K. and E.D.; project administration, S.R. and E.D. All authors have read and agreed to the published version of the manuscript.

Funding

This research received no external funding.

Conflicts of Interest

The authors declare no conflict of interest.

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Scheme 1. Procedures for the synthesis of the bis-thiourea linker.
Scheme 1. Procedures for the synthesis of the bis-thiourea linker.
Catalysts 10 00167 sch001
Figure 1. (a) FT-IR for 1,3-bis(3-(triethoxysilyl)propyl) thiourea (BTSPT), thiourea-bridged periodic mesoporous organosilica (PMO-TU) and Pt@PMO-TU, (b) thermal gravimetric analysis (TGA) of Pt@PMO-TU and (c,d), respectively, Nitrogen adsorption–desorption isotherms and corresponding pore-size distribution curves of both PMO-TU and Pt/PMO-TU.
Figure 1. (a) FT-IR for 1,3-bis(3-(triethoxysilyl)propyl) thiourea (BTSPT), thiourea-bridged periodic mesoporous organosilica (PMO-TU) and Pt@PMO-TU, (b) thermal gravimetric analysis (TGA) of Pt@PMO-TU and (c,d), respectively, Nitrogen adsorption–desorption isotherms and corresponding pore-size distribution curves of both PMO-TU and Pt/PMO-TU.
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Figure 2. (a,b) SEM micrograph of thiourea-bridged periodic mesoporous organosilica (PMO-TU) support, (b) SEM micrograph of Pt/PMO-TU nanocomposite, (c) HRTEM micrograph of PMO-TU support (yellow arrows show the supported Pt nanoparticles), and (d) HRTEM micrograph of the Pt/PMO-TU nanocomposite.
Figure 2. (a,b) SEM micrograph of thiourea-bridged periodic mesoporous organosilica (PMO-TU) support, (b) SEM micrograph of Pt/PMO-TU nanocomposite, (c) HRTEM micrograph of PMO-TU support (yellow arrows show the supported Pt nanoparticles), and (d) HRTEM micrograph of the Pt/PMO-TU nanocomposite.
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Figure 3. (a,b) high-angle annular dark-field scanning transmission electron microscope (HAADF-STEM) images of Pt@PMO-TU (yellow arrows show supported Pt nanoparticles), (c,d) energy-dispersive X-ray spectroscopy (EDS) spectra of Pt/PMO-TU nanocomposite.
Figure 3. (a,b) high-angle annular dark-field scanning transmission electron microscope (HAADF-STEM) images of Pt@PMO-TU (yellow arrows show supported Pt nanoparticles), (c,d) energy-dispersive X-ray spectroscopy (EDS) spectra of Pt/PMO-TU nanocomposite.
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Figure 4. (a) Time-dependences of the absorbances at 400 nm for the reduction of 4-NP with NaBH4 in the presence of PMO-TU and Pt/PMOTU and (b) absorption spectra for the reduction of 4-nitrophenol, Conditions: [4-PN] = 3 mM, [NaBH4] = 125 mM, [Catalyst] = 10 mg, T = 25 °C.
Figure 4. (a) Time-dependences of the absorbances at 400 nm for the reduction of 4-NP with NaBH4 in the presence of PMO-TU and Pt/PMOTU and (b) absorption spectra for the reduction of 4-nitrophenol, Conditions: [4-PN] = 3 mM, [NaBH4] = 125 mM, [Catalyst] = 10 mg, T = 25 °C.
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Figure 5. (a) Time-dependences of the absorbances at 400 nm for the reduction of 4-NP with NaBH4 in the presence Pt/PMO-TU and (b) Arrhenius plot (ln k versus 1/T) Conditions: [4-PN] = 3 mM, [NaBH4] = 125 mM, [Catalyst] = 10 mg, T = 25, 50, 75 °C..
Figure 5. (a) Time-dependences of the absorbances at 400 nm for the reduction of 4-NP with NaBH4 in the presence Pt/PMO-TU and (b) Arrhenius plot (ln k versus 1/T) Conditions: [4-PN] = 3 mM, [NaBH4] = 125 mM, [Catalyst] = 10 mg, T = 25, 50, 75 °C..
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Figure 6. (a) Time-dependences of the absorbances at 400 nm for the reduction of p-NP with NaBH4 in the presence different dosage of Pt/PMO-TU and (b) plot of rate constant (k) versus catalyst dose. Conditions: [4-PN] = 3 mM, [NaBH4] = 125 mM, [Catalyst] = 5, 10 and 20 mg, T = 25 °C.
Figure 6. (a) Time-dependences of the absorbances at 400 nm for the reduction of p-NP with NaBH4 in the presence different dosage of Pt/PMO-TU and (b) plot of rate constant (k) versus catalyst dose. Conditions: [4-PN] = 3 mM, [NaBH4] = 125 mM, [Catalyst] = 5, 10 and 20 mg, T = 25 °C.
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Figure 7. (a) Time-dependences of the absorbances at 400 nm for the reduction of p-NP with different initial concentrations of NaBH4 in the presence Pt/PMO-TU and (b) plot of rate constant (k) versus catalyst dose initial concentrations of NaBH4. Conditions: [4-PN] = 3mM, [NaBH4] = 65, 125 and 250 mM, [Catalyst] = 10 mg, T = 25 °C.
Figure 7. (a) Time-dependences of the absorbances at 400 nm for the reduction of p-NP with different initial concentrations of NaBH4 in the presence Pt/PMO-TU and (b) plot of rate constant (k) versus catalyst dose initial concentrations of NaBH4. Conditions: [4-PN] = 3mM, [NaBH4] = 65, 125 and 250 mM, [Catalyst] = 10 mg, T = 25 °C.
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Figure 8. Reusability study of the Pt@PMU-TU catalyst.
Figure 8. Reusability study of the Pt@PMU-TU catalyst.
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Scheme 2. The mechanism of 4-nitrophenol reduction (the ratio of Pt: 4-Nitrophenol:NaBH4 is 1:0.024:1.54 × 10−4, respectively).
Scheme 2. The mechanism of 4-nitrophenol reduction (the ratio of Pt: 4-Nitrophenol:NaBH4 is 1:0.024:1.54 × 10−4, respectively).
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Table 1. Comparison of the activity of our catalyst with those previously reported.
Table 1. Comparison of the activity of our catalyst with those previously reported.
CatalystConv. (%)t (min)Reaction ConditionsRef.
AgPd NCs/rGO95.6%3NaBH4 (5 mM); p-NP (0.7 mM); catalyst (0.05 mg); rt[8]
Pd-PBL98.3%32NaBH4 (1 × 10−4 mmol); p-NP (1 × 10−3 mmol); catalyst (1 mol %); rt[43]
Au/Fe3O4100%10NaBH4 (0.1 M); p-NP (10 mM); catalyst (2 mg); rt[44]
Au/CNTs membrane100%15NaBH4 (50 mM); p-NP (0.2 mM); catalyst (0.25 mM); rt[28]
Ag–OMS-C96%2.5NaBH4 (0.5 M); p-NP (0.1 mM); catalyst (10 mg); rt[15]
ZVI NCs100%1NaBH4 (3.2 mM); p-NP (0.14 mM); catalyst (0.44 mM); rt[45]
PtPd@N-HCS100%2NaBH4 (0.1 M); p-NP (0.25 mM); catalyst (2 mg); rt[7]
Pt/PMO-TU100%<1NaBH4 (250 mM); p-NP (3 mM); catalyst (10 mg); rtThis work
ZVI: zero-valent iron; NCs: Nanoclusters; rGO: reduced graphene oxide; PBL: Phenylene-Bridged Bis(thione) Ligands; CNTs: carbon nanotubes; OMS-C: ordered mesoporous silica cubic; N-HCS: nanocube-hollow carbon nanosphere; rt: room temperature.

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Esmat, M.; Mohtasham, H.; GadelHak, Y.; Mehrebani, R.T.; Tahawy, R.; Rostamnia, S.; Fukata, N.; Khaksar, S.; Doustkhah, E. 2D Mesoporous Channels of PMO; a Platform for Cluster-Like Pt Synthesis and Catalytic Activity in Nitrophenol Reduction. Catalysts 2020, 10, 167. https://doi.org/10.3390/catal10020167

AMA Style

Esmat M, Mohtasham H, GadelHak Y, Mehrebani RT, Tahawy R, Rostamnia S, Fukata N, Khaksar S, Doustkhah E. 2D Mesoporous Channels of PMO; a Platform for Cluster-Like Pt Synthesis and Catalytic Activity in Nitrophenol Reduction. Catalysts. 2020; 10(2):167. https://doi.org/10.3390/catal10020167

Chicago/Turabian Style

Esmat, Mohamed, Hamed Mohtasham, Yasser GadelHak, Reza Tarbiat Mehrebani, Rafat Tahawy, Sadegh Rostamnia, Naoki Fukata, Samad Khaksar, and Esmail Doustkhah. 2020. "2D Mesoporous Channels of PMO; a Platform for Cluster-Like Pt Synthesis and Catalytic Activity in Nitrophenol Reduction" Catalysts 10, no. 2: 167. https://doi.org/10.3390/catal10020167

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