Denis
Bernsmeier
a,
Erik
Ortel
a,
Jörg
Polte
b,
Björn
Eckhardt
a,
Sabrina
Nowag
c,
Rainer
Haag
c and
Ralph
Kraehnert
*a
aDepartment of Chemistry, Technische Universität Berlin, Straße des 17. Juni 124, 10623 Berlin, Germany. E-mail: ralph.kraehnert@tu-berlin.de
bDepartment of Chemistry, Humboldt-Universität zu Berlin, Brook-Taylor-Str. 2, 12489 Berlin, Germany
cDepartment of Chemistry, Freie Universität Berlin, Takustr. 3, 14195 Berlin, Germany
First published on 8th July 2014
Controlling the pore structure of metal oxide films and supported catalysts is an essential requirement for tuning their functionality and long-term stability. Typical synthesis concepts such as “Evaporation Induced Self Assembly” rely on micelle formation and self assembly. These processes are dynamic in nature and therefore strongly influenced by even slight variations in the synthesis conditions. Moreover, the synthesis of very small mesopores (2–5 nm) and independent control over the thickness of pore walls are very difficult to realize with micelle-based approaches. In this contribution, we present a novel approach for the synthesis of mesoporous metal oxide films and catalytic coatings with ordered porosity that decouples template formation and film deposition by use of hyperbranched core–multishell polymers as templates. The approach enables independent control of pore size, wall thickness and the content of catalytically active metal particles. Moreover, dual templating with a combination of hyperbranched core–multishell polymers and micelles provides facile access to hierarchical bimodal porosity. The developed approach is illustrated by synthesizing one of the most common metal oxides (TiO2) and a typical supported catalyst (PdNP/TiO2). Superior catalyst performance is shown for the gas-phase hydrogenation of butadiene. The concept provides a versatile and general platform for the rational optimization of catalysts based e.g. on computational prediction of optimal pore structures and catalyst compositions.
Several strategies for improved control over the nanostructure of metal oxide coatings and supported catalysts have been reported.8,9 So-called nanocasting provides access to tunable pore morphologies by replicating the nanostructure of a template material into an ordered pore system.10 Oxide coatings with ordered and well-connected mesopores can be formed by a strategy called evaporation-induced self assembly (EISA).11–13
Typical EISA-based syntheses employ micelles of amphiphilic block-copolymers as pore templates and a reactive metal precursor dissolved in volatile solvent(s). The volatile solvent evaporates during film deposition leading to increasing polymer concentration, assembly of the template molecules into micelles and finally formation of an ordered mesophase comprised of micelles and condensed precursor. Subsequent thermal treatments induce stiffening of the inorganic network, crystallization and removal of the template.9
EISA is a dynamic and delicate process. Due to the transient nature of solvent evaporation and polymer self-assembly it reacts very sensitive to the synthesis conditions and the thermodynamics of the employed block-copolymers. Mesoporous TiO2 films based on e.g. the template Pluronic P123 were reported to form either lamellar, hexagonal or cubic phases14 depending on the polymer concentration, pH, temperature as well as on relative humidity applied during and after film deposition.7
The strong sensitivity of EISA results in severe limitations of this synthesis approach. In the preparation of larger samples or thicker coatings local gradients in the evaporation conditions lead to inhomogeneities across the formed materials. Attempts to control pore size and wall thickness independently fail due to close interactions between template and precursor during self assembly.15 Moreover, the dynamic nature of micelles formed from amphiphilic block-copolymers typically makes the formation of well-ordered pore systems with small mesopores difficult to realize (see e.g.ref. 7 and 16 for TiO2).
Hyperbranched core–shell and core–multishell (“CMS”) polymers offer a potential solution. They typically consist of a core (e.g. hyperbranched glycerol) and one or more shells of a different polymer (e.g. an alkyl layer and outer poly(ethylene glycol) layer). Core–multishell polymers that feature a hydrophobic core or inner shell and a hydrophilic outer shell resemble somehow the structure of polymer micelles typically employed for EISA. However, the nature of the polymer bonds is covalent, hence no polymer assembly into micelles is needed anymore.
Mesoporous powders of different metal oxides have been synthesized using CMS polymers as unimolecular pore templates. Yin et al. obtained a 2D mesoporous titania network employing amphiphilic core-double-shell polymers.17 Nowag et al. reported the synthesis of bimodal mesoporous Pt/SiO2 powders using a mixture of a CMS polymer and micelles of a PEO–PPO–PEO (Pluronic P123).18 However, the obtained silica showed separated domains of unordered CMS-templated pores (dporeca. 2 nm) and larger SBA-15-type mesopores (dporeca. 6 nm) cast by P123 micelles. The studied CMS polymer also stabilized the colloidal Pt nanoparticles employed in the synthesis,18,19 demonstrating bifunctionality as pore template as well as particle stabilizer. However, the potential of CMS polymers to generate oxide coatings and catalysts with small mesopores, ordered porosity, materials with tunable pore-wall thickness and hierarchical porosity via dual templating remains so far unexplored.
We present a new strategy for polymer-templated metal oxide films with small mesopores and tunable wall thickness. The strategy gives direct access to hierarchical pore systems as well as catalytic functionality. The synthesis combines the advantages of EISA and CMS polymer templates. CMS polymers, consisting of hyperbranched polyglycerol cores, hydrophobic inner alkyl layers and a hydrophilic outer layer of monomethylated poly(ethylene glycol), are shown to control the obtained pore size and to act as particle stabilizers. This novel approach enables for the first time (i) the synthesis of nanocrystalline metal oxide films with ordered pores and size control between 3 and 5 nm, (ii) independent control over the thickness of pore walls and the size of the mesopore by adjusting the content of CMS polymer in the dip-coating solution, (iii) metal oxide films with hierarchical bimodal mesoporosity obtained by combining CMS polymers with micelle-based templates, and (iv) catalytic coatings PdNP/TiO2 with small mesopores. The obtained catalysts show the highest activity reported so far in literature for selective gas-phase hydrogenation of 1,3-butadiene.
Two different polymers with core–multishell structure, called CMS5 and CMS10 hereafter, were employed as templates. CMS5 consisted of a hyperbranched polyglycerol core with a molar mass of approximately 5000 g mol−1, an intermediate shell of C18 alkyl chains and an outer shell of monomethylated poly(ethylene glycol) (mPEG750) with a total mass of the polymer of Mw = 93300 g mol−1.18 CMS10 consisted of a hyperbranched polyglycerol core with a molar mass of approximately 10
000 g mol−1, an intermediate shell of C12 alkyl chains and an outer shell of monomethylated poly(ethylene glycol) (mPEG750, Mw = 750 g mol−1) with a total mass of Mw = 56
500 g mol−1. The synthesis of the CMS polymers was realized by amide coupling of the shell molecules to the hyperbranched core as described by Keilitz et al.21 Amphiphilic block copolymers poly(ethylene oxide)-b-poly(butadiene)-b-poly(ethylene oxide) (PEO–PB–PEO containing 18
700 g mol−1 PEO and 10
000 g mol−1 PB) were obtained from Polymer Service Merseburg GmbH (see ref. 15 for details).
Dip-coating of all samples was performed with a withdrawal rate of 300 mm min−1 in a controlled atmosphere of RH = 40% at 25 °C. The films were subsequently dried at 80 °C for 4 h in a tube furnace under flowing air. To remove the templates the temperature was then raised in flowing air with 1 K min−1 to 300 °C, held constant for 1 h and followed by naturally cooling down to room temperature. To further crystallize the TiO2 framework, the obtained films were treated with a second calcination procedure ramping with 3 K min−1 to 450 °C and holding this temperature for 5 min followed by cooling to room temperature.
Lab scale SAXS analysis of dissolved CMS polymers in ethanol was performed using a SAXSess instrument (Anton Paar GmbH). Obtained scattering curves were analyzed with the assumptions of spherical shape, homogeneous electron density and a Schulz–Zimm size distribution.
2D-SAXS pattern with a beam incident angle of β = 13° or 90° in respect to the film surface were recorded at the HASYLAB B1 beamline at DESY Hamburg with a sample to detector distance of 1338 mm and a calibrated radiation energy of 16026 eV using a 2D PILATUS 1M detector. The SAXS data were processed employing the software FIT2D Version V12.077. The modulus of the scattering vector q is defined in terms of the scattering angle θ and the wavelength λ of the radiation used: thus q = 4π/λ
sin(θ/2). XRD was measured on a Bruker D8 Advance (Cu Kα radiation) with gracing incident beam (1°). Reflexes were assigned using PDFMaintEx library Version 9.0.133. The average crystallite size was calculated applying the Scherrer equation. Obtained data were analyzed with the Rietveld method using TOPAS V4.2 (Bruker AXS). Experimental settings were considered by the Fundamental Parameter approach incorporated in the program. Phases of anatase (I41/amd) and palladium (Fm3m) were refined using scale factor, lattice parameter and crystallite size. Influence of four background parameters and zero point error were taken into account. The crystallite sizes were calculated from peak broadening based on the volume-weighted column height.
The Pd concentration was determined using inductively coupled plasma-optical emission spectroscopy (ICP-OES) using a 715-ES-inductively coupled plasma (ICP) analysis system (Varian).
Kr adsorption was measured at 77 K using the Autosorb-1-C automated gas adsorption station from Quantachrome. The surface area was calculated via Brunauer–Emmett–Teller (BET) method. Before adsorption measurement the samples were degassed at 150 °C for 2 h in vacuum. To determine the coating mass, the mass depth of each film was calculated by STRATAGem film analysis software (v 4.3) based on WDX spectrums analyzed with the Cameca “Camebax-microbeam” electron microprobe at ZELMI (TU-Berlin). In this study, BET surface area values are related either to the coating mass (m2 g−1) or to the geometric film volume (m2 cm−3).
The 2D SAXS pattern recorded perpendicular to the substrates surface (β = 90°, Fig. 1B) features an isotropic ring, which confirms the ordered pore structure. The corresponding d-spacing in x-direction dx ≈ 8.4 nm (qx ≈ 0.75 nm−1) corresponds well with the periodicity of 9 nm observed by SEM on the film surface. The pattern recorded at a smaller angle (β = 13°, Fig. 1C) shows an ellipsoidal shape. Such patterns are typically attributed to an ordered mesostructure after isotropic shrinkage in the direction normal to the substrate.23,24 A comparison of dx with the d-spacing in z-direction (qz ≈ 1.93 nm−1; dz ≈ 3.3 nm) suggests an anisotropic shrinkage of approximately 61%. XRD analysis of the sample (Fig. 1G) does not show distinct reflections that could be assigned to a crystalline titania phase.
The observed film properties are consistent with data reported for mesoporous EISA-based TiO2 films synthesized from block-copolymer templates, except for the smaller pore size and d-spacing. Anisotropic shrinkage of about 60% was reported for TiO2 films templated by micelles of F127,24ca. 70% for PEO–PB–PEO polymers.15 The circular (β = 90°) and elliptical scattering features (β = 13°) are similar to scattering patterns previously assigned to a distorted cubic arrangement of micelle-templated mesopores.23 However, the pore ordering in films templated by CMS polymers appears to be less pronounced than reported for many titania films templated by micelles of e.g. F127,24 P123,14 Brij 58.16,25 The lower degree of pore ordering could be related to the polydispersity of the employed CMS polymer which have a polydispersity index of approximately 1.5. Also the low crystallinity is typical for micelle-templated TiO2 films calcined at 300 °C.26
The surface area (Kr sorption) of the CMS10-templated films amounts to 182 m2 g−1 or 703 m2 cm−3 (Tcalc = 300 °C) and 59 m2 g−1 or 236 m2 cm−3 (Tcalc = 450 °C), respectively. In comparison, micelle-templated anatase films (PEO213–PB184–PEO213, TiCl4) calcined at 475 °C offer a surface area of 85 m2 g−1.15 113 m2 g−1 were reported by Yu et al. for TiO2 anatase films synthesized from titanium tetraisopropoxide/Pluronic P123 after calcination at 400 °C.28 Hence, the surface area of CMS10-templated TiO2 is in the same order of magnitude as observed for micelle-templated TiO2. The high surface area of the CMS-templated films implies that mesopores are interconnected and accessible to krypton gas.
The combined data confirms that hyperbranched core–multishell polymers can template ordered mesopores of about 4–5 nm size in TiO2 films. Pore sizes are smaller than typically obtained with micelles of amphiphilic block-copolymers. Additional tests on the influence of relative humidity during dip-coating (see ESI Fig. S2‡) prove that the synthesis is also more robust than typical EISA syntheses. In contrast to Pluronic-templated films,29 the pore morphology of CMS-templated TiO2 did not change for relative humidities between 12 and 80%.
Increasing concentrations of the CMS10-template result in films with similar morphologies (Fig. 2A–F). The resulting film thicknesses range from 70 nm to 95 nm. Templated mesopores with about 4 nm diameter can be observed for all concentrations. FFTs for all images indicate the preserved pore ordering. However, the pore spacing systematically changes as indicated by the changing diameter of the ring seen in the FFTs. The periodic spacing decreases monotonously from 10 nm to 6 nm with increasing polymer content, which indicates a decrease in the wall thickness of the templated pores. Hence, the developed synthesis enables for the first time for pore diameter smaller 5 nm the control of the pore-wall thickness independent of the templated mesopore size.
Fig. 3 (left column, 1:
0) displays SEM (a and b) and FFT (c) images of a TiO2 film templated with CMS5 polymer. The films morphology strongly resembles that of CMS10 templated TiO2 (Fig. 1A) showing an abundance of locally ordered mesopores. However, pore diameter (3 nm) and periodic distance (7.5 nm) are apparently smaller than for the films templated with CMS10 (4–5 nm and 9 nm, respectively). The smaller structural features produced by CMS5 agree well with the observation that CMS5 forms also smaller polymer entities already in solution (SAXS: 6.6 nm) than CMS10 (SAXS: ca. 8.3 nm, see ESI S1‡). Hence, the size of templated mesopores can be controlled by the size of the dissolved polymer template, which can be related to the molar weight of its hyperbranched core.
Fig. 3 presents SEM images in low (A) and high (B) magnification and corresponding FFTs (C) of calcined titania films templated with either CMS5 (“1:
0”), with different mixtures of CMS5 and PEO–PB–PEO (mass ratio 1
:
1, 1
:
3, 1
:
6), and with PEO–PB–PEO only (“0
:
1”). The mass ratio between CMS5 and PEO–PB–PEO increases from left to right in Fig. 3. This was realized by varying the amount of CMS5 in the employed dip-coating solutions. The film thicknesses range from 70 nm to 100 nm.
SEMs image of the film templated with CMS5 polymer (Fig. 3, 1:
0) show mesopores on the outer film surface with a pore diameter of ca. 3 nm. The periodic distance from FFT amounts to 7.5 nm. Templating with micelles of PEO–PB–PEO in the absence of CMS templates produces TiO2 structures with large mesopores of about 20 nm diameter and a periodic distance of 29.3 nm (Fig. 3, ratio 0
:
1) (see ref. 15 for more details). For all films synthesized with the template mixtures (Fig. 3, 1
:
1, 1
:
3, 1
:
6) a bimodal porosity can be clearly recognized. All systems show mesopores with the desired pore diameters of about 3 nm originating from CMS5 and 20 nm from PEO–PB–EPO micelles, respectively. However, the films differ in the local distribution of the differently templated pores. At a mass ratio CMS5 to PEO–PB–PEO of 1
:
1 separated pore domains for each template are formed (Fig. 3, 1
:
1). FFT images show therefore two distinct rings with periodic distances of 7.0 nm and 28.0 nm corresponding to individual domains of the respective polymer template.
The size of the individual domains decreases with increasing PEO–PB–PEO content as indicated by SEM and FFT (Fig. 3, 1:
3). The individual domains of PEO–PB–PEO finally disappear at a ratio CMS5 to PEO–PB–PEO of 1
:
6. Large 20 nm pores are homogeneously distributed across the whole film, with smaller CMS5-templated pores located in all the walls of the larger mesopores (Fig. 3, 1
:
6). The respective FFT shows one clear ring which corresponds to the periodic distances of the PEO–PB–PEO-templated pore structure and a broad halo originating from the smaller pore spacings. Hence, the combined data suggest that a hierarchically organized bimodal porosity is obtained.
It should be noted that also the available surface area changes significantly with the introduction of hierarchical porosity. The BET surface area of a CMS5-templated film amounts to 1050 m2 cm−3, whereas a film prepared with a CMS5 to PEO–PB–PEO ratio of 1:
3 shows about 160 m2 cm−3. The decrease in surface area originates from the effect that additional larger mesopores are introduced at the expense of smaller ones.
In conclusion, hyperbranched CMS polymers act as unimolecular template species and enable in combination with PEO–PB–PEO polymers a simple one-pot synthesis of metal oxides with hierarchically organized bimodal mesoporosity. Both desired pore sizes can be controlled individually by the size of each respective template.
XRD analysis (Fig. 4I) reveals broad reflections at 2 Theta angles of 25°, 36–39° and 47° that can be assigned to crystalline TiO2 anatase (PDF 21-1272). At 2 theta of 40° another weak reflection is observed. The reflection can be assigned to a metallic Pd phase (PDF 46-1043). Other phases, e.g. PdO (PDF 46-1211), were not detected. The average crystallite size (derived from Rietveld refinement) amounted to 11.8 nm for anatase and 5.3 nm for Pd. The values are consistent with crystallite and particle sizes extracted from TEM. Compositional analysis of the PdNP/TiO2 catalyst with ICP-OES indicates a content ratio of Pd to TiO2 of approximately 2.4 wt%. This value matches closely with the 2.5 wt% Pd expected from the composition of the dip-coating solution.
Activity and selectivity of the PdNP/TiO2 catalyst in the gas phase hydrogenation of 1,3-butadiene are illustrated in Fig. 5 showing (A) the influence of temperature on 1,3-butadiene conversion and (B) selectivity to 1-butene and to selectivity to all butenes (sum of S1-butene, Strans-2-butene and Scis-2-butene) vs. butadiene conversion. Both graphs contain corresponding benchmark data for a previously synthesized 0.5 wt% PdNP/TiO2 catalyst with a similar PdNP size as reported in ref. 4. The benchmark catalyst was synthesized with F127 as mesopore template, titanium(IV) bis(ammonium lactato)dihydroxide (TALH) as TiO2 precursor and colloidal PdNP.4 Note that a loading of size-controlled PdNP higher than 0.5 wt% could not be obtained in this previous study due to the fact that the particle stabilizer (PVP) degraded the micelle-templated pore structure.
Both catalysts are active and selective. Butadiene conversion increases with increasing temperature for both catalysts (Fig. 5A). The butadiene conversion at 70 °C amounted to 26% for PdNP/CMS10/TiCl4 and to 5.6% for PdNP/F127/TALH, respectively. Thus, the CMS10-templated catalyst shows a ca. five times higher activity than the TALH-based reference catalyst. This five times higher activity correlates well with the five times higher Pd loading (2.5 wt%) that could be achieved only with the new CMS-based catalyst.
Almost identical product selectivities to 1-butene, trans-2-butene, cis-2-butene and small amounts of n-butane were observed for both catalysts (Fig. 5B). At butadiene conversions up to about 50% the selectivity for 1-butene is 55% which is in line with values reported in literature for other Pd-based catalysts.22 Moreover, the Arrhenius plots constructed for both catalysts in the interval 50 to 80 °C were fitted by straight lines and yielded the same activation energy for both catalyst of about 62 kJ mol−1. The equivalent trends in selectivity and activation energy indicate that both catalysts possess the same intrinsic behavior.
Generally, variations of the pore system (pore size, bimodal porosity) can be used to influence the catalytic performance in cases when pore diffusion is limiting. For very small pores the reactant transport in the pore system of the catalyst can be limited by Knudsen diffusion. However, all data presented here were recorded in the kinetic regime. Hence, the data characterize the materials intrinsic catalytic properties, not the effects of pore diffusion.
The space time yield (STY) calculated at 50 °C for the new mesoporous PdNP/CMS10/TiO2 catalyst corresponds to 0.122 mol s−1 kg−1. Hence, the developed catalytic coating shows in the kinetic regime and under comparable conditions space-time-yields for butenes that are at least two to six times higher than values reported in literature (e.g. 0.016 mol s−1 kg−1,31 0.019 mol s−1 kg−1,4 0.061 mol s−1 kg−1 (ref. 32)).
Extending the synthesis approach to use CMS polymers as bifunctional NP stabilizer and porogen produces PdNP/TiO2 catalytic coatings with controlled mesoporosity, a high accessible surface area and high Pd loading. No detrimental effects of the synthesis on the properties of the catalyst support (film integrity, pore templating, pore ordering) or the active PdNP (particle size, activity and selectivity in butadiene hydrogenation) were observed.
Catalytic activity and pore diffusion within the support can be easily tuned with the presented approach. The concept thus provides a versatile and general platform for the rational optimization of catalysts based e.g. on computational prediction of optimal pore structures.33 The synthesis also paves the way to model-type catalysts with well-defined pore structure, particle size and high metal loading for the investigation of structure–activity relationships as well as practical applications.
Footnotes |
† Dedicated to the occasion of the 80th birthday of Prof. Dr. Manfred Baerns |
‡ Electronic supplementary information (ESI) available. See DOI: 10.1039/c4ta01842g |
This journal is © The Royal Society of Chemistry 2014 |