Reza Mirbagheria,
Dawood Elhamifar*a and
Shaaker Hajatiab
aDepartment of Chemistry, Yasouj University, Yasouj 75918-74831, Iran. E-mail: d.elhamifar@yu.ac.ir; dawood.elhamifar@gmail.com; Fax: +98-74-33223048; Tel: +98-74-33223048
bDepartment of Semiconductors, Materials and Energy Research Center (MERC), P.O. Box 31787-316, Tehran, Iran
First published on 10th March 2021
A novel method was used to prepare a magnetic phenylene-based periodic mesoporous organosilica nanocomposite with yolk–shell structure (Fe3O4@YSPMO). The Fe3O4@YSPMO nanomaterial was prepared by using easily accessible pluronic-P123 and cetyltrimethylammonium bromide (CTAB) surfactants under basic conditions. This material was employed for effective immobilization of potassium perruthenate to prepare an Fe3O4@YSPMO@Ru nanocatalyst for the aerobic oxidation of alcohols. The physiochemical properties of the designed Fe3O4@YSPMO@Ru nanocomposite were studied using PXRD, FT-IR, TGA, SEM, TEM, ICP, VSM and XPS analyses. Fe3O4@YSPMO@Ru was effectively employed as a highly recoverable nanocatalyst in the selective aerobic oxidation of alcohols.
Different methods have been used for the preparation of YS nanocomposites that can be divided into template-assisted and template-free approaches. The well-known template-less methods are Kirkendall14,15 and Ostwald ripening.16–19 Based on the type of surfactant, template-assisted methods are divided into hard20 and soft21 approaches. In the hard approach, the template is located between the core and shell. This template is selectively removed under special conditions to prepare the YS-structure. The disadvantage of tedious processing steps, makes the hard-template method inefficient. The soft-template assisted method has recently been employed as a simple and efficient strategy to prepare YS nanocomposites. To date, a few unusual and/or less-available surfactants have been used as a soft template to prepare YS materials.22–25 Some recently developed surfactants applied in this matter are SDBS and LSB,18 water/oil (W/O) microemulsions such as Igepal CO-520 (NP-5) and cyclohexane in water,26 FC4 with pluronic F-127 (ref. 24) and also FC4 with cetyltrimethylammonium bromide (CTAB).25
As mentioned above, most of these surfactants are expensive and commercially unavailable. Therefore, the preparation of novel yolk–shell nanocomposites using routine, low-cost and easily available soft-templates is a very important progress in this matter.
On the other hand, oxidation is a very important process in chemistry, due to its diverse industrial applications such as ground remediation with trichloroethylene (TCE) or tetrachloroethylene (PCE),27,28 pesticides removal,29 formaldehyde removal30–33 and elimination of chemical oxygen demand (COD) for industrial waste water,34 etc. Especially, the oxidation of alcohols to respective carbonyls is an important subject in organic synthesis. Various reagents and catalysts such as chromium oxide,35–39 manganese oxide,40–42 activated DMSO,43–46 hypervalent iodine,47–49 pyridine-SO3 (ref. 50) and NaOCl with TEMPO51–55 have been used for the oxidation of alcohols. Among different oxidants, molecular oxygen is of more interest due to its availability, low-cost and especially the production of water as only by-product. However, these homogeneous systems suffer from restrictions such as difficulty in catalyst and product separation and waste problems. Therefore, the use of heterogeneous catalysts has been highly developed in this matter. Some of recently developed catalytic systems are based on noble metals such as Pd56–64 and Ru.65–71 A number of reported studies in this matter are hydroxyapatite-supported palladium nanoclusters,72 methyl glycolate-supported gold,73 carbon-supported Pt, Pt–Ru and Pt3Sn,74 graphene-supported Pt and Pt–Ru,75 silica-supported TEMPO,76 PMO-IL@RuO4 (ref. 77) and ILNOS-Ti.78
In view of the above, herein, a novel soft-template assisted strategy has been developed for easy preparation of magnetic phenylene-based ordered mesoporous nanocomposite with yolk–shell structure (Fe3O4@YSPMO). Pleasingly, for the first time, the routine, easily available and low-cost surfactants (pluronic P123 and CTAB) were used as a template to prepare the Fe3O4@YSPMO nanomaterial (Scheme 1).
The low-angle powder XRD pattern (Fig. 1) demonstrated a sharp d100 peak at 2θ of about 1° confirming the presence of periodicity in a shell with two-dimensional hexagonal structure for the catalyst. According to this peak, it can be concluded that none of the surfactants lonely exists in the outer layer and the final form of the shell is made through a combination of both surfactants.
Furthermore, the wide-angle PXRD was in agreement with Fe3O4 spinel structure and showed six peaks at 2θs of 30, 35, 43, 54, 57 and 64° corresponding, respectively, to the Miller indices (hkl) values of 220, 311, 400, 422, 440 and 511. The broad peak appeared at 2θ over 20–27 degree is also related to mesoporous silica shell (Fig. 2).
The FT-IR spectra of Fe3O4 NPs and also Fe3O4@YSPMO before and after the extraction of surfactants are shown in Fig. 3. These showed a peak at 573 cm−1 corresponding to Fe–O bond for all materials. The O–H bonds of material surface were appeared about 3400 cm−1. Interestingly, new bands were observed for Fe3O4@YSPMO, before and after the surfactant extraction (Fig. 3(B) and (C)). Before the surfactant extraction, the bands observed at 2922 and 2853 cm−1 are due to the aliphatic C–H bonds of P123 and CTAB surfactants (Fig. 3(B)). After the Soxhelet extraction, the latter signals were not seen confirming well removal of surfactants during extraction process (Fig. 3(C)). The peaks at 720–810 cm−1 are attributed to C–Si bonds. Moreover, the bands at 1096 and 932 cm−1 are due to symmetric and asymmetric vibrations of Si–O–Si bonds. The bands appeared around 3100 cm−1 are corresponded to aromatic C–H bonds of PMO shell. The CC bonds of phenylene rings were also observed at 1630 cm−1. These results confirm successful formation of phenylene-PMO-shell around magnetite NPs.
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Fig. 3 The FT-IR spectra of Fe3O4 (A), Fe3O4@YSPMO nanoparticles before (B), and after (C) surfactant extraction. |
Scanning electron microscopy (SEM) image is shown in Fig. 4(a). This image showed uniform spherical particles with an average size of 70 nm for the material. The transmission electron microscopy (TEM) image of Fe3O4@YSPMO is shown in Fig. 4(b). This also showed YS-structured spherical particles with a void space between black cores (Fe3O4 NPs) and gray shells (organosilicas) for the designed material.
Thermal stability of Fe3O4@YSPMO@Ru was studied by TGA (Fig. 5). A weight loss of about 6% below 120 °C is attributed to elimination of remained H2O, EtOH and MeOH from the synthetic process. The second weight loss (about 7%) was found at 121–300 °C corresponding to remained surfactants during extraction process. The main weight loss (27%) at 301–800 °C is due to removal of the phenylene moieties incorporated into material shell.
Immobilization of potassium perruthenate in the prepared material was investigated by using EDS and ICP analyses. The EDS pattern (Fig. 6) proved the presence of Ru, O, Si, Fe and C in the material. The exact amount of ruthenium was calculated by ICP (2.38 mol%). These data were found to be in good agreement with FT-IR and TGA results confirming well incorporation/immobilization of phenylene and perruthenate moieties into/onto material framework.
The VSM analysis was also performed to investigate the magnetic properties of the designed catalyst (Fig. 7). According to this, the saturation magnetization of Fe3O4@YSPMO@Ru nanocomposite was found to be about 14 emu g−1 confirming good magnetic properties of the catalyst.
The XPS survey spectrum (Fig. 8) of the nanocomposite was taken and analyzed to investigate its chemical composition. Before the XPS analysis, Savitzky–Golay filtering was implemented on the XPS spectra to reduce their noise level.81,82 All signals were calibrated to have C 1s at BE of 284.9 eV. As shown in Fig. 8, Si 2p3/2 is observed at 103.27 eV, which confirms its contribution in the PMO part of the material as SiO2. The peak of Ru 3p3/2 appeared at binding energy of 463.5 eV confirming the presence of Ru as Ru (4+). It was also found that the oxygen contributes in the material as SiO2 (533 eV) and RuO2 (530.2 eV). Iron and potassium were not found in XPS spectra though they were shown to be present in the material by using EDS. As known, EDS is a characterization technique for analyzing bulk materials and thus it was able to detect Fe from Fe3O4 as core material. Despite EDS, XPS is a surface sensitive technique with sampling depth of three times of inelastic scattering mean free path of electrons (IMFP) with a given kinetic energy within a given overlayer. For instance, the IMFPs of Fe 2p electrons with kinetic energy of about 543 eV within the overlayers of SiO2 and RuO2 are calculated from Tanuma–Powell–Penn (TPP) formula to be 1.85 and 1.11 nm, respectively. In other words, the escape depth of such electrons within SiO2 and RuO2 are about 5.55 and 3.33 nm. This indicates that the thickness of the RuO2/PMO shell enveloping the core Fe3O4 is larger than the escape depth of Fe 2p electrons. The relative sensitivity factor for Ru 3p is much higher than that of other elements in the prepared core shell that should result in a Ru 3p signal of high intensity. In spite of this, it is of low intensity, which indicates that to the amount of RuO2 is very low. Therefore, the disappearance of Fe signal is mainly attributed to the thick PMO layer.
The interaction of aromatic compounds and metal complexes is an important subject because of its importance in the fields of nucleic acids,83,84 proteins,85,86 crystal engineering,87 material science88 and drug design. Especially in ruthenium–arene complexes, an important interaction is between π-electrons of aromatic rings and the Ru cationic sites with high oxidation states.89,90 This kind interaction leads to both immobilization and reduction of Ru species. In the present study, we used potassium perruthenate with the oxidation state of +7 for Ru. However, the XPS analysis showed that the oxidation state of supported Ru is +4 in the designed nanocomposite. This is an evidence of successful immobilization of ruthenium species on the organosilica shell that can be achieved via coordination of aromatic π-electrons with the Ru-centers followed by the reduction of the oxidation state of Ru from +7 to +4.
After the successful preparation and characterization, the Fe3O4@YSPMO@Ru was used as an effective and recoverable catalyst for aerobic oxidation of alcohols. To obtain the best conditions, the oxidation of 1-phenylethanol was selected as a test model. As shown in Table 1, the reaction progress is greatly influenced by the amount of catalyst, solvent and temperature. Accordingly, the best result was obtained using 0.3 mol% of Fe3O4@YSPMO@Ru catalyst in trifluorotoluene (TFT) at 90 °C. In the next study, the catalytic activity of our designed Fe3O4@YSPMO@Ru nanocatalysts was compared with Fe3O4@YSPMO@Pd and Fe3O4@YSPMO@Au nanomaterials (Table 1, entry 7 versus entries 9 and 10). The result showed that the best result is delivered in the presence of Fe3O4@YSPMO@Ru.
Entry | Catalyst (mol%) | Solvent | Temperature (°C) | Time (h) | Yieldb (%) |
---|---|---|---|---|---|
a Conditions: 1-phenylethanol (1 mmol), O2 (1 atm).b GC yield.c The Fe3O4@YSPMO@Pd was used as catalyst.d The Fe3O4@YSPMO@Au was used as catalyst. | |||||
1 | 0.1 | — | R.t. | 12 | — |
2 | 0.1 | Toluene | R.t. | 12 | 10 |
3 | 0.1 | Toluene | 60 | 12 | 55 |
4 | 0.1 | Toluene | 90 | 12 | 67 |
5 | 0.2 | Toluene | 90 | 12 | 80 |
6 | 0.2 | TFT | 90 | 12 | 96 |
7 | 0.3 | TFT | 90 | 6 | 96 |
8 | 0.3 | TFT | 75 | 6 | 78 |
9c | 0.3 | TFT | 90 | 6 | 94 |
10d | 0.3 | TFT | 90 | 6 | 68 |
After that, the applicability of this conditions for other alcohols was examined (Table 2). As shown, different alcohols are effectively converted to their corresponding carbonyls (Table 2, entries 1–8). It is noteworthy that this process was very selective for oxidation of primary benzylic alcohols to aldehydes without the formation of appreciable amounts of carboxylic acids (Table 2, entries 1–3). Moreover, 1-phenylpropanol, 1-phenylethanol and benzhydrol also delivered corresponding ketones in high yields (Table 2, entries 4–6). Interestingly, the Fe3O4@YSPMO@Ru was also effective in the selective oxidation of cinnamyl alcohol and the corresponding α,β-unsaturated carbonyl was produced in a good yield (Table 2, entry 7). The primary and secondary aliphatic alcohols (both acyclic and cyclic) were also reactive in the presence of designed catalytic system and converted to the corresponding carbonyls in good yield and selectivity (Table 2, entries 8–10). These results confirm the high ability of Fe3O4@YSPMO@Ru for selective aerobic oxidation of a broad range of aliphatic and aromatic alcohols.
Entry | Alcohol | Time (h) | Yieldb (%) | TONc | TOFd (h−1) |
---|---|---|---|---|---|
a Conditions: alcohol (1 mmol), O2 (1 atm), catalyst (0.3 mol%) in TFT at 90 °C.b GC yields.c TON: defined as [mmol of product/mmol of catalyst].d TOF: defined as [TON/time].e Conditions: alcohol (1 mmol), O2 (1 atm), catalyst (0.5 mol%) in TFT at 90 °C. | |||||
1 | Benzyl alcohol | 5 | 98 | 326.7 | 65.3 |
2 | 4-Chlorobenzyl alcohol | 6.5 | 94 | 313.3 | 48.2 |
3 | 4-Methoxybenzyl alcohol | 4.5 | 98 | 326.7 | 72.6 |
4 | 1-Phenylethanol | 6 | 96 | 320 | 53.3 |
5 | 1-Phenylpropanol | 6 | 95 | 316.7 | 52.8 |
6 | Benzhydrol | 12 | 92 | 306.7 | 25.6 |
7 | Cinnamyl alcohol | 24 | 68 | 226.7 | 9.4 |
8e | 2-Octanol | 24 | 68 | 136 | 5.7 |
9e | Cycloheptanol | 24 | 73 | 146 | 6.1 |
10e | 3-Phenyl-1-propanol | 16 | 56 | 112 | 7 |
Next, the recoverability and reusability of Fe3O4@YSPMO@Ru in 1-phenylethanol oxidation were studied. To do this, after the completion of oxidation process, the catalyst was removed and it was dried and reused in conditions the same as the first run. The result showed that the Fe3O4@YSPMO@Ru can be recovered at least five times with no considerable decrease in performance (Fig. 9).
A hot filtration test was also performed on the above-mentioned reaction as a test model. This experiment was performed to make it clear whether the active catalytic species are leaching during the reaction process or not. To this end, after the completion of about 50% of the oxidation process, the catalyst was removed and the reaction progress of residue was monitored. Interestingly, after 10 h, no considerable conversion of alcohol was observed (Fig. 10). Moreover, the atomic absorption analysis also showed no leaching of ruthenium in the filtrate mixture. These results confirm effective immobilization and high stability of active Ru-species during the applied conditions.
Finally, the efficiency of Fe3O4@YSPMO@Ru was compared with some of recently reported ruthenium based heterogeneous catalysts in the oxidation of 1-phenylethanol (Table 3). As shown, the amount of applied catalyst in our study is much lower than previous studies. Moreover, the recovery times for Fe3O4@YSPMO@Ru is more than the former catalysts. These observations clearly confirm high catalytic efficiency and also high durability of the Fe3O4@YSPMO@Ru in comparison to reported catalysts.
Entry | Catalyst | Conditions | Time (h) | Recovery times | Ref. |
---|---|---|---|---|---|
1 | Ru(OH)x/Fe3O4 | Toluene, cat. (3.8 mol%) O2 (1 atm), 105 °C | 2 | 1 | 91 |
2 | Fe3O4@SiO2/Ru(OH)x | Toluene, cat. (12.6 mol%) O2 (10 atm), 80 °C | 7 | 2 | 92 |
3 | RuO4@MCM-41 | Toluene, cat. (1.3 mol%) O2 (10 atm), 80 °C | 24 | 1 | 93 |
4 | Ru@PMO-IL | TFT, cat. (2.5 mol%) O2 (1 atm), 70 °C | 5.5 | 4 | 77 |
5 | Fe3O4@YSPMO@Ru | TFT, cat. (0.3 mol%) O2 (1 atm), 90 °C | 6 | 5 | This work |
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