Rudina Bleta*a,
Sébastien Noëla,
Ahmed Addadb,
Anne Ponchela and
Eric Monfliera
aUniv. Artois, CNRS, Centrale Lille, ENSCL, Univ. Lille, UMR 8181, Unité de Catalyse et Chimie du Solide (UCCS), F-62300 Lens, France. E-mail: rudina.bleta@univ-artois.fr
bUniv. Lille, CNRS, INRA, ENSCL, UMR 8207 – UMET – Unité Matériaux et Transformations, F-59000 Lille, France
First published on 27th January 2016
Mesoporous RuO2/TiO2 composites were prepared using a template-directed colloidal self-assembly approach combined with a cyclodextrin (CD)-assisted aqueous impregnation method. The supramolecular assemblies formed between the randomly methylated β-cyclodextrin (RaMeβ-CD) and the block copolymer P123 acted as a template for the formation of a highly porous TiO2 network over which uniform dispersion of ruthenium nanoparticles was achieved. By combining dynamic light scattering, X-ray diffraction, N2-adsorption, temperature-programmed reduction, field-emission scanning electron microscopy and high-resolution transmission electron microscopy, we show that CD-based assemblies provide a versatile and easily accessible toolbox with different functionalities for generating metal-supported catalysts with controlled pore architecture and uniform metal distribution. The performance of these supported catalysts was evaluated in the liquid phase hydrogenation of methyl oleate (MO, C18:1) to methyl stearate (MS, C18:0). Control of ruthenium dispersion into the large pores of RaMeβ-CD-P123-templated TiO2 material enhanced catalyst activity and selectivity for the hydrogenation of the internal C
C bond and permitted catalyst separation and reuse without loss of activity. Our findings highlight the pivotal role played by the CD-based assemblies on the performance of supported ruthenium catalysts.
Recently, our group has explored the possibility of using cyclodextrin (CD)-based supramolecular assemblies as template or structure directing agents for the elaboration of inorganic materials with a large variety of morphologies, porosities and crystal phase compositions.21–25 A particular feature of CDs is their ability to form, in association with polymers, supramolecular assemblies with many different kinds of architectures such as for instance, spherical or ellipsoidal micelles, vesicles, elongated polypseudorotaxanes and three-dimensional hydrogels.26–29 Interestingly, silica oligomers23 or colloidal nanoparticles prepared by sol–gel process21,22,25 may easily infiltrate within these assemblies and replicate their original structure. Moreover, CDs have also the unusual property to form adducts with a large number of metal salts enabling their uniform dispersion over solid supports.30–35 We aim to take advantage of the experience that our group has acquired on the elaboration of nanostructured titanium dioxide (TiO2) in order to use this material as support for uniform dispersion of ruthenium nanoparticles. Indeed, besides its interest as efficient photocatalyst for fundamentals and industrial applications,36–39 titania has also proved to be an important support in heterogeneous catalysis due to its high surface area, chemical and thermal stability, as well as ability to strongly interact with various metal nanoparticles.40–44 Moreover, ruthenium has been identified as a promising catalyst for applications in the hydrogenation of biomass-derived compounds such as levulinic acid,45 furanic molecules,46,47 arabinoic acid,48 xylose,44 and fatty esters49–51 under mild conditions.
Herein, the TiO2 support is synthesized using the recently developed RaMeβ-CD-P123 directed colloidal self-assembly approach24,25 while the native β-CD is employed as dispersing agent to improve dispersion of metal nanoparticles over the solid support. Since the efficiency of the final catalyst depends on various factors including the characteristics of the support,52 the size and composition of individual metal nanoparticles53,54 as well as the metal–support interactions,1,13,14 control of the preparation process is essential. For this purpose, we have undertaken a detailed investigation of the effect of both the supramolecular template (RaMeβ-CD-P123 assemblies) and the dispersing agent (native β-CD) on the characteristics of the heterogeneous Ru/TiO2 catalysts. Finally, the efficiency of these latter was evaluated in the liquid phase hydrogenation of methyl oleate (MO, C18:1) to methyl stearate (MS, C18:0) under mild conditions (50 °C, 40 bar H2).55–57
cos
θ), where K is the shape factor (taken as 0.9 in this study considering that the particles are spherical), λ is the X-ray radiation wavelength (1.54056 Å for Cu Kα), β is the full width at half-maximum (fwhm) and θ is the Bragg angle. Nitrogen adsorption–desorption isotherms were collected at −196 °C using an adsorption analyser Micromeritics Tristar 3020. Prior to analysis, 200–400 mg samples were outgassed at 320 °C overnight to remove the species adsorbed on the surface. From N2 adsorption isotherms, specific surface areas were determined by the BET method61 and pore size distributions were calculated using the NLDFT (nonlocal density functional theory) model62 assuming a cylindrical pore structure. The relative errors were estimated to be the following: SBET, 5%; pore volume (pv) (DFT), 5%; pore size (ps) (DFT), 20%. Temperature programmed reduction (TPR) measurements were performed using a Micromeritics AutoChem 2920 chemisorption analyser equipped with a thermal conductivity detector (TCD) for monitoring the H2 consumption. Prior to analysis, 30–40 mg samples were placed in a U-tube quartz reactor and outgassed under argon flow at 120 °C for 2 h. After cooling to 25 °C, the sample was reheated at 500 °C with a heating rate of 10 °C min−1 and the RuO2 reduction was performed in a 5% H2/Ar (v/v) flow with a flow rate of 10 mL min−1. Field emission scanning electron microscopy (FE-SEM) observations were performed to examine the morphology of the support materials using a FEG Hitachi S-4700 field-emission microscope operating at 5 kV. Before imaging, samples were covered with a thin layer of carbon to reduce the accumulation of charges at high magnification. High resolution transmission electron microscopy (HR-TEM) observations were performed on a Tecnai microscope operating at an accelerating voltage of 200 kV. The RuO2/TiO2 powder was deposited directly on the surface of a carbon coated copper grid.
CH(CH2)7CO2CH3, C18:1) to methyl stearate (CH3(CH2)16CO2CH3, C18:0).56,57 Before catalytic testing, the RuO2/TiO2 composite was introduced in a U-tube quartz reactor and reduced at 400 °C for 4 h under H2 atmosphere with a heating rate of 2 °C min−1 and a flow rate of 30 mL min−1. The catalytic tests were carried out using a 50 mL cylindrical stainless steel autoclave reactor equipped with a magnetic drive stirring and a thermostatic bath for the temperature control. In a typical experiment, 80.8 mg supported catalyst (0.02 mmol Ru) was introduced to a solution containing 593 mg methyl oleate (MO/Ru molar ratio = 100) dissolved in 10 mL of heptane. The mixture was purged three times with nitrogen at room temperature and then, pressurized with H2 (40 bar). The reactions were run at a constant temperature of 50 °C for 2 h using a stirring speed of 750 rpm. Finally, the reaction products were analysed using a Varian 3900 gas chromatograph (GC) equipped with a CP-Sil-5B column (15 m × 0.25 mm × 0.25 μm) and a flame ionisation detector (FID). The injector and detector temperatures were 250 °C. Conversion and selectivity were quantified based on the relative GC-areas referred to an external standard (dodecane) calibrated to the corresponding pure compounds. Each catalytic run was performed in duplicate and the values reported are the averages between two runs, with an uncertainty equal or less than 5%. For the recycling tests, the catalyst was recovered after each run by filtration, washed with heptane three times, dried at 70 °C for 2 h and reduced under H2 flow at 400 °C for another 4 h.
We first examined the impact of RaMeβ-CD-P123 assemblies on the structural and textural characteristics of the support material. The sol–gel TiO2 material (TiO2-sg, no template used) (Fig. 2A) presents very low pore volume and surface area (0.03 cm3 g−1 and 21 m2 g−1 respectively, Table 1) due to the small size of the crystallites in the titania sol and their high level of aggregation which facilitates the contact between neighbouring grains, thus resulting in a very rapid conversion to rutile (XRD Fig. 2B) and a drastic decrease of the pore volume.25 The isotherm and pore size distribution of nanostructured RaMeβ-CD-P123-templated TiO2 (TiO2-ns) (Fig. 2A) indicate that the supramolecular assemblies remarkably improve the textural characteristics of the support material. Indeed, a dramatic increase in the pore size (from 5.3 to 16.3 nm) and pore volume (from 0.03 to 0.36 cm3 g−1) is noticed together with a strong increase in the specific surface area (from 21 to 80 m2 g−1) (Table 1). Moreover, from the XRD patterns shown in Fig. 2B, it can be seen that the RaMeβ-CD-based assemblies make the titania material more stable against the anatase-to-rutile and brookite-to-rutile phase transformation, as evidenced by the strong decrease in the intensity of the (110) peak at 2θ = 27.4° assigned to the rutile phase (R) (JCPDS card no. 00-034-0180).25 Finally, from the representative FE-SEM images, it is clear that the RaMeβ-CD-based assemblies also play a key role in restructuring the titania framework. Thus, while the TiO2-sg material is made up predominantly of shapeless and aggregated particles (Fig. 2C), the RaMeβ-CD-P123-templated material (TiO2-ns) is mainly comprised of fine and rounded grains randomly packed into a highly porous framework (Fig. 2D).
| Sample | SBETa (m2 g−1) | Vcumb (cm3 g−1) | PSc (nm) | RuO2 sized (nm) |
|---|---|---|---|---|
| a Specific surface area determined in the relative pressure range 0.1–0.25.b Cumulative pore volume.c Average pore size resulting from NLDFT calculations.d RuO2 crystallite size determined using the Scherrer equation. | ||||
| TiO2 supports | ||||
| TiO2-sg | 21 ± 1 | 0.030 ± 0.002 | 5.3 ± 1.1 | — |
| TiO2-ns | 80 ± 5 | 0.360 ± 0.018 | 16.3 ± 3.3 | — |
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| RuO2-TiO2 catalysts | ||||
| Ru2.5TiO2-sg | 8 ± 0 | 0.015 ± 0.001 | 6.2 ± 1.2 | 15.8 ± 1.6 |
| Ru2.5β-CDTiO2-sg | 16 ± 1 | 0.045 ± 0.002 | 5.9 ± 1.2 | 11.5 ± 1.2 |
| Ru2.5TiO2-ns | 51 ± 3 | 0.265 ± 0.012 | 16.5 ± 3.3 | 9.8 ± 1.0 |
| Ru2.5β-CDTiO2-ns | 75 ± 4 | 0.314 ± 0.016 | 16.8 ± 3.3 | 9.2 ± 0.9 |
Then, the interactions between Ru(III) nitrosyl nitrate and native β-CD were investigated using dynamic light scattering (DLS) combined with X-ray diffraction (XRD) measurements. Fig. 3A displays the DLS plots of native β-CD (0.016 M) before (a) and after equimolar addition of ruthenium salt (Ru/β-CD molar ratio = 1) (b). As expected, β-CD presents a bimodal size distribution plot with two populations centred at 70 and 380 nm associated with the formation of aggregates. Interestingly, after addition of ruthenium nitrosyl nitrate, these aggregates undergo partial disintegration, as evidenced by the shift of the hydrodynamic radius to 22 and 130 nm respectively. Further evidence for such interaction was provided from XRD measurements performed on β-CD and Ru/β-CD assemblies dried at 60 °C (Fig. 3B). Thus, the numerous diffraction lines characteristic of the cage-type crystalline microstructure of β-CD disappear upon addition of ruthenium nitrosyl nitrate indicating disruption of the β-CD microstructure. In analogy with the experiment described above, DLS measurements were also performed on the β-CD/TiO2 suspensions (Fig. 3C). From the size distribution plots of the TiO2 sols (0.5 M) prepared without and with the native β-CD (β-CD/Ti molar ratio = 0.032), the decrease in the apparent hydrodynamic radius from 110 to 85 nm suggests rupture of TiO2 aggregates due to the adsorption of the cyclic molecule onto the TiO2 surface.24 Moreover, the disappearance of the most intense XRD reflections (at 9.0° and 12.5°) of the corresponding TiO2 and β-CD/TiO2 xerogels dried at 60 °C confirms the breakdown of the cage-type structure of β-CD after interaction with titania surface (Fig. 3D).
Taken together, our results provide evidence of the fact that β-CD presents a strong affinity for both the mesoporous TiO2 support and the Ru(III) nitrosyl nitrate. Such behaviour is likely to alter the degree of dispersion of the ruthenium nanoparticles over the support and, by consequence, affect the performance of the final catalyst.
On the bases of the results obtained above, we focused the continuation of our study on the preparation and characterization of a series of Ru/TiO2 catalysts using both conventional sol–gel TiO2 (TiO2-sg) and nanostructured RaMeβ-CD-P123-templated TiO2 (TiO2-ns) supports. The ruthenium nitrosyl nitrate impregnating solution was prepared without or with assistance of the native β-CD (Ru/β-CD = 11).
XRD patterns of the different catalysts are presented in Fig. 4. Similarly to the undoped TiO2-ns support (Fig. 2B), Ru2.5TiO2-ns and Ru2.5β-CDTiO2-ns catalysts contain only anatase and brookite implying that no anatase-to-rutile or brookite-to-rutile phase transformation occurs during the second calcination at 400 °C. On the other hand, three distinct crystalline phases (anatase, brookite and rutile) are clearly observed for the Ru2.5TiO2-sg and Ru2.5β-CDTiO2-sg catalysts. Furthermore, for all catalysts, in addition to the peaks of the support material, other reflexion lines are clearly identified at 2θ = 27.8° and 34.9° which could be indexed to the (110) and (101) planes respectively of the tetragonal RuO2 (JCPDS 00-043-1027). Note that for the TiO2-sg supported catalysts, the (110) and (101) planes of RuO2 and rutile-TiO2 overlap due to the lattice matching between these two phases both of which adopt a tetragonal structure. It is also worthy to mention that both the support and the dispersing agent affect the size of RuO2 crystallites. Thus, for the Ru2.5 and Ru2.5β-CD catalysts deposited over TiO2-ns, the crystallite sizes determined from the line broadening of the (110) diffraction peak are 9.8 nm and 9.2 nm respectively, while the average sizes obtained for the catalysts deposited over TiO2-sg are beyond 10 nm (Table 1).
To further investigate the impact of RuO2 nanoparticles on the textural characteristics of the catalysts, N2-adsorption analyses were carried out. From the adsorption isotherms (Fig. 5A) and corresponding pore size distributions (Fig. 5B), it can be noticed that, whatever the type of the support (TiO2-sg or TiO2-ns), the textural characteristic are only slightly modified after deposition of RuO2 nanoparticles, indicating that no pore blocking occurs. For instance, the surface area, pore volume and pore size of the Ru2.5β-CDTiO2-ns catalyst (75 m2 g−1, 0.31 cm3 g−1 and 16.8 nm respectively) are very close to those of the undoped TiO2-ns support (80 m2 g−1, 0.36 cm3 g−1 and 16.3 nm respectively) (Table 1). In a somewhat different way, the Ru2.5β-CDTiO2-sg catalyst presents a higher pore volume compared to the TiO2-sg support (0.045 cm3 g−1 vs. 0.030 cm3 g−1) as well as a second population of mesopores centred at 14.8 nm. This is an indication that the native β-CD has also a beneficial effect in restructuring the titania framework during the impregnation step due to the ability of this cyclic molecule to adsorb onto the surface of the oxide nanoparticles, as mentioned earlier.
To probe the reducibility of mesoporous RuO2/TiO2 composites, temperature programmed reduction (TPR) measurements were also carried out. The TPR profiles of the different supported catalysts are shown in Fig. 6.
As expected, the non-doped TiO2 material shows a very weak signal and no reduction peak indicating that the support alone can hardly react with H2. In contrast, the Ru2.5TiO2-sg catalyst displays a very broad peak centred at ∼320 °C assigned to the reduction of Ru4+ to metallic Ru0.63 Such a high reduction temperature may result from the formation of RuO2 aggregates which interact strongly with the rutile phase (major polymorph in the TiO2-sg support) and which are difficult to reduce. On the other hand, the Ru2.5β-CDTiO2-sg catalyst displays two detached peaks at ∼320 °C and ∼210 °C suggesting that, at least, two different ruthenium species coexist in this sample. Thus, the higher temperature may be attributed to the reduction of RuO2 aggregates, in strong interaction with the TiO2-sg support, which exist also in the Ru2.5TiO2-sg catalyst, while the lower one may be assigned to the reduction of small and more easily reducible RuO2 species in weak interaction with the support and formed only in the presence of β-CD. This result suggests that, by locating at the metal–support interface, the cyclodextrin should reduce the contact points between TiO2 and RuO2 particles, thus preventing the incorporation of these latter into the titania support during the calcination process. Note that the catalysts supported over TiO2-ns globally display lower reduction temperatures, i.e. in the range of 180–230 °C, compared to those supported over TiO2-sg materials (210–320 °C). This is an indication that the RaMeβ-CD-P123-templated support promotes the formation of small and readily reducible RuO2 nanoparticles. Moreover, as RuO2 has different lattice parameters from TiO2-anatase and TiO2-brookite (the major polymorphs in the TiO2-ns support), the metal–support interactions in these catalysts should be weaker compared to those between RuO2 and TiO2-sg support. Taken together, our results provide evidence of the fact that small nano-sized and well-dispersed RuO2 particles could be obtained using nanostructured TiO2 prepared by template-directed colloidal self-assembly as support and native β-CD as dispersing agent.
Further evidence for the key role of RaMeβ-CD-based assemblies on the dispersion of RuO2 nanoparticles was provided by high resolution transmission electron microscopy (HR-TEM) combined with high angle annular dark-field scanning transmission electron microscopy (HAADF-STEM). Observations were performed on two selected catalysts, i.e. Ru2.5β-CDTiO2-ns and Ru2.5β-CDTiO2-sg.
From the TEM image shown in Fig. 7a, it can be noticed that the surface of the RaMeβ-CD-P123-templated TiO2 support is decorated with RuO2 nanoparticles which can be directly visualised by the bright spots resulting from the difference in Z-contrast between the two oxides (Fig. 7b). Moreover, EDS elemental mapping on different regions of the TEM micrograph (Fig. 7c–f) allows to further differentiate the two phases, i.e. TiO2 (white regions) and RuO2 nanoparticles (dark regions).
TiO2 nanoparticles in this sample are identified as a mixture of tetragonal anatase (∼15 nm) and orthorhombic brookite (∼10 nm) (Fig. 7g and h). Interestingly, mesopores of 15–20 nm diameter, resulting from the self-assembly of these nanoparticles around the supramolecular template, can also be clearly visualised in this micrograph (pink circles), in agreement with N2-adsorption analyses. On the other hand, RuO2 nanoparticles are more or less spherical and approximately 10–12 nm in size (Fig. 7i), in agreement with XRD results. Conversely, the Ru2.5β-CDTiO2-sg catalyst shows mainly a dense and less porous network (Fig. 7j) made-up of anatase (∼35%), brookite (∼26%) and rutile (∼39%) and over which RuO2 particles tend to form elongated heterogeneous structures (Fig. 7k–n). Such unusual epitaxial growth of RuO2 nanoparticles over rutile-TiO2 was also observed by Xiang et al.64 in a previous study and was suggested to result from the structural matching between these two phases which actually share the same type of lattice symmetry (tetragonal) and have very similar lattice parameters (a = 4.59 Å, c = 2.96 Å for rutile-TiO2 and a = 4.49 Å, c = 3.10 Å for RuO2).
C bond without affecting the carbonyl C
O bond. In the present study, we evaluated the performance of the different supported Ru/TiO2 catalysts in the liquid phase hydrogenation of methyl oleate to methyl stearate.
Prior to catalytic tests, RuO2/TiO2 composites were pre-treated under hydrogen flow at 400 °C for 4 h to reduce the RuO2 in metallic Ru. TEM analyses confirmed that Ru(0)/TiO2-sg was made-up predominantly of aggregated particles dispersed in a dense and less porous network (TiO2-sg), while Ru(0)/TiO2-ns catalyst was mainly comprised of small and well-dispersed nanoparticles dispersed in a porous and nanostructured network (TiO2-ns) (Fig. S1, ESI†). This is in agreement with what was observed on non-reduced RuO2/TiO2-sg and RuO2/TiO2-ns composites (Fig. 7).
The results obtained in catalysis after 2 h of reaction (40 bar H2, 50 °C) with the four catalysts, prepared using either conventional sol–gel or nanostructured TiO2 supports, with the assistance or not of the native β-CD (Ru/β-CD = 11), are shown in Fig. 8. The results obtained with the non-doped supports (TiO2-sg and TiO2-ns) as well as with the Ru2.5 catalyst supported over commercial TiO2 (Ru2.5TiO2-A and Ru2.5TiO2-P25) are added for comparison. Depending on the preparation method, clear differences can be observed in both the catalytic activity (Fig. 8a) and selectivity (Fig. 8b). The control TiO2-sg and TiO2-ns supports show almost no activity in the hydrogenation of methyl oleate. On the other hand, all supported Ru/TiO2 catalysts are selective in the hydrogenation of the olefinic C
C bond producing the fully saturated ester, i.e. methyl stearate (C18:0) as the main product and the methyl elaïdate (C18:1, trans-9) as the only byproduct. Moreover, it is worth noting that the catalytic performance strongly differs depending on the type of the support (TiO2-sg or TiO2-ns) and the impregnation method (with or without assistance of native β-CD). Thus, when Ru is deposited over nanostructured RaMeβ-CD-P123-templated TiO2, the catalytic activity increases sharply from 36% (Ru2.5/TiO2-sg) to 82% (Ru2.5/TiO2-ns). Interestingly, further improvement in the conversion efficiency is noticed when the native β-CD is used as dispersing agent. Thus, the conversion rate increases by ∼14% (from 36% to 50%) for the Ru2.5 catalyst deposited over TiO2-sg and by ∼12% (from 82% to 94%) for the same catalyst deposited over TiO2-ns support. Note that among the four supported catalysts prepared using colloidal self-assembly approach, Ru2.5β-CDTiO2-ns is the fastest one, achieving almost full MO conversion (∼94%) in 2 h. Moreover, it is interesting to notice that the activity of this catalyst is almost 3-fold higher than that of ruthenium deposited over commercial anatase-TiO2 (Ru2.5TiO2-A) and P25-TiO2 (Ru2.5TiO2-P25).
Similarly to the catalytic activity, clear differences can be observed also in the selectivity of the supported catalysts. Thus, the increase in the methyl oleate conversion when moving from Ru2.5TiO2-sg to Ru2.5TiO2-ns leads also to a dramatic increase in the selectivity for the methyl stearate (from 47% to 80%). However, although a beneficial effect of β-CD is noticed for the Ru2.5TiO2-sg catalyst (MS selectivity increases from 47% to 67%), no clear difference exists between the Ru2.5TiO2-ns catalysts prepared without or with assistance of β-CD (MS selectivity is the same ∼80%).
Over the investigated mesoporous Ru/TiO2 catalysts, the catalytic performance agrees well with the textural characteristics of the support and the degree of dispersion of the ruthenium species. Indeed, the highest performance of the Ru2.5β-CDTiO2-ns catalyst may result from a combined effect of improved textural characteristics of the support and uniform dispersion of ruthenium nanoparticles. Thus, the high surface area of the RaMeβ-CD-P123-templated TiO2 material (80 m2 g−1) should provide a high level of dispersion of ruthenium nanoparticles, facilitating the contact of methyl oleate with the catalyst surface during the hydrogenation reaction. On the other hand, the high pore volume (0.36 cm3 g−1) should allow for more reactant molecules to be adsorbed to the internal surface of the pores, thus improving the diffusion of reactants and products toward the active phase during the catalytic process. Finally, the use of native β-CD as dispersing agent may allow for reducing the interparticle aggregation thanks to the ability of this cyclodextrin to interact with both RuNO(NO3)3 and TiO2 nanoparticles.30,32,33 Overall, our results reveal a dual role played by the CD-based assemblies: an enhancement of the porosity and surface area of the TiO2 material and an improvement of the dispersion of Ru nanoparticles over the support, parameters that appear to be essential for enhancing the efficacy of the catalyst in the liquid phase hydrogenation of methyl oleate.
Moreover, as leaching and deactivation are common phenomena encountered in any liquid phase hydrogenation reaction, the ease of recovery and reusability of the catalyst are important features that need to be considered. For this purpose, we have investigated the recyclability of the most efficient catalyst, i.e. Ru2.5β-CDTiO2-ns, in three successive runs. Interestingly, no loss of activity and selectivity was observed during the consecutive cycles, indicating that the supported catalyst exhibits high stability under the employed reaction conditions (Fig. 9).
We expect that the high surface area and large pore volume generated by the template-directed self-assembly of titania colloids should allow for a good dispersion of nanosized ruthenium particles and, therefore, effectively prevent aggregation while improving the chemical stability of the catalyst. Moreover, the thermal treatment at 400 °C should allow for a stable fixation of ruthenium species over the TiO2 material, preventing leaching from the matrix to the reaction media during the catalytic process. Hence, the high efficacy of this catalyst combined with ease of recovery and reuse without loss of conversion and selectivity makes the template-directed colloidal self-assembly a simple and versatile approach for the synthesis of supported catalysts with high performance in liquid phase hydrogenation of methyl oleate.
Overall, our results revealed that the CD-based assemblies provide a versatile and easily accessible toolbox with different functionalities for generating metal-supported catalysts with controlled pore architecture and uniform metal distribution. The approach combining the use of two different cyclodextrins with different functionalities is versatile and may be generalised to other monometallic or bimetallic catalysts supported over simple or mixed oxides prepared by sol–gel process.
Footnote |
| † Electronic supplementary information (ESI) available. See DOI: 10.1039/c5ra27161d |
| This journal is © The Royal Society of Chemistry 2016 |