Structure and reactivity of single site Ti catalysts for propylene epoxidation
Introduction
Propylene epoxidation using molecular oxygen is a promising, alternative route to synthesize propylene oxide (PO), a chemical of great industrial importance [1], [2], [3], [4], [5]. Since Haruta first discovered that supported gold nanoparticles on TiO2 are active and selective for the direct epoxidation of propylene in the presence of molecular oxygen and hydrogen, it had been gradually realized that the reactivity, PO selectivity and hydrogen efficiency could benefit from synergic effects of small nano-sized gold particles and the neighboring TiO2 [6] . Studies suggest that highly dispersed isolated Ti sites serve as the preferential sites to adsorb propylene, while the gold nanoparticles are responsible for the formation of the OOH* species from oxygen and hydrogen [7], [8], [9]. The OOH* species then migrate toward nearby Ti sites to produce PO from propylene. The isolation of Ti sites was found to increase the PO selectivity with less byproduct formation. The adjacent Ti sites were found to favor bidentate adsorption of propylene, leading to the formation of undesired byproducts. Understanding the TiO2 structure is of great importance for designing highly efficient Au
TiO2 based catalysts for propylene epoxidation.
To establish the Ti structure and performance relationship, Haruta and coworkers deposited TiO2 on non-porous silica using incipient wetness impregnation (IWI) and subsequently calcined the support up to 1000 °C [10]. The PO yield and selectivity improved by increasing the calcination temperature. The improved PO yield and selectivity were ascribed to the formation of the site-isolated tetrahedral TiO2 in the SiO2 framework with the presence of Ti
O
Si. However, as TiO2 prepared by IWI tends to initially form clusters and nanoparticles on the SiO2 support, it could be difficult to drive all of the TiO2 to form single-site Ti in SiO2 framework using high temperature calcination. Another potential concern is the possible loss of surface area due to the collapse of pores during high temperature calcination. Other efforts have been used to synthesize single-site catalysts for propylene epoxidation. To generate single-site Ti, Nijhuis and co-workers used a Ti-grafted silica method prepare Ti-doped SiO2 for propylene epoxidation with H2 and O2, and achieved promising activity with 2.7% propylene conversion and PO selectivity at 89.4% [11]. A sol-gel method was used to prepare site-isolated Fe in the SiO2 framework for propylene epoxidation with O2, and showed good activity without the use of Au [12], however, the catalysts showed 33.6% PO selectivity at 5.5% conversion.
The establishment of the Ti structure and performance relationship can benefit from the use of uniformly dispersed single-site Ti on the SiO2 support. In this study, we investigated the isolated TiO2 single-site initially deposited on porous SiO2 by atomic layer deposition (ALD), a method that has been used to prepare single-site catalysts [13], [14], [15]. Advanced catalyst synthesis is advancing from obtaining understandings of the catalytic active sites [16] to assemble catalytic active architecture [17]. ALD represents a promising technique to construct catalytic active architecture in a “bottom-up” manner to achieve high activity, selectivity, and stability [18], [19]. It is a thin film deposition technique that uses organometallic compounds as precursors. It enables conformal coatings because the deposition conditions are optimized to ensure the surface self-limiting reaction between the organometallic precursors and the reaction sites on the substrates. Under surface self-limiting reaction conditions, the gaseous organometallic precursor molecules, e.g., titanium isopropoxide or TTIP, preferentially react with the surface reaction sites, e.g., surface hydroxyl groups, forming stable intermediates on the substrate [20], [21]. These stable, chemisorbed intermediates will not decompose to form TiO2 until a co-reactant is dosed, e.g., H2O. The steric hindrance effect from the bulky TTIP ligands ensures that the intermediates distance from each other and prevent the possible formation of Ti
O
Ti bonds, and the chemisorption nature of the intermediates allows the facile formation of Ti
O
Si bonds. In a previous study, we have prepared site-isolated Ti for Au-based catalysts using TiO2 ALD for propylene epoxidation with H2 and O2 at 100 °C [22]. The catalysts showed 90% selectivity at 100 °C, however the PO formation rate was relatively low, about 1–2 gPO h−1 kg−1cat. A substantial gain in PO formation rate and propylene conversion could be obtained by carrying out the reaction at higher reaction temperature. To maintain high PO selectivity at high temperature, it is necessary to optimize the catalyst structure that favors the PO formation pathway. In this work, we used ALD to generate single-site Ti, followed by a post-ALD calcination to alter the coordination of Ti, and connect the Ti
O structure and its performance in propylene epoxidation with H2 and O2. Using ultraviolet–visible (UV–vis) diffuse reflectance spectroscopy and X-ray absorption spectroscopy (XAS), we investigated the structure of single-site Ti in the SiO2 framework as a function of calcination temperature. The PO selectivity shows a linear correlation to the Ti
O coordination number and bond distance, and DFT calculations predict a linear scaling of the partial charge of the Ti site as a function of the coordination number and bond distance.
Section snippets
Catalyst synthesis
TiO2 surface self-limiting reaction was performed in a low vacuum (∼1 Torr) atomic layer deposition (ALD) reactor (Gemstar-6, Arradiance). Ultrahigh purity N2 (Airgas, 99.999%) was used as the carrier gas and further purified using a Supelco gas purifier (Sigma-Aldrich) before entering the reactor. In a typical preparation, 0.5 g of SiO2 (Silicycle S10040M) was uniformly spread onto a stainless steel tray held at 200 °C. Titanium isopropoxide (TTIP) was used as the precursor and contained in a
Experimental analysis
The SiO2 gel support (Silicycle S10040M) used in this work has a specific surface area of 93.3 m2/g. Assuming a growth rate of 0.3 Å/cycle and TiO2 density of 4.23 g/cm3 [22], the volume of TiO2 deposited on 1 g of the support after one ALD cycle equals to 93.3 m2 times 0.3 Å. Thus, the expected weight gain on 0.5 g of SiO2 after one ALD cycle of TiO2 is ∼1.3 wt%. Weight gain measurements were performed to establish the appropriate exposure conditions to saturate the SiO2 surface and ensure
Conclusions
In conclusion, the results presented here show that the selectivity to propylene oxide is linearly correlated to the coordination number of Ti
O in the Ti
SiO2 support in propylene epoxidation on Au-based catalysts. The single-site, 4-fold coordinated Ti sits favors high PO selectivity and improving hydrogen efficiency, while the single-site, 6-fold coordinated Ti sites prefers the formation of undesired byproducts such as propanal and CO2. The DFT calculations corroborate the experimental trends
Acknowledgements
This work is sponsored by the National Science Foundation (Grant # CBET-1511820 and CBET-1510485). Z. G. gratefully acknowledged the fellowship from the Alabama State funded Graduate Research Scholars Program (GRSP). This research used resources of the Advanced Photon Source, a U.S. Department of Energy (DOE) Office of Science User Facility operated for the DOE Office of Science by Argonne National Laboratory under Contract No. DE-AC02-06CH11357. Computer resources are provided by the Alabama
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2022, Chemical Engineering ScienceCitation Excerpt :For further interpretation of the catalytic performance, characterizations were carried out to study the deactivation mechanism of the catalysts. Various research (Lee et al., 2019; Feng et al., 2018; Feng et al., 2017; Lu et al., 2018; Ren et al., 2020; Lin et al., 2020; Ishida et al., 2020; Lu et al., 2019; Feng et al., 2018) had shown that the deactivation is caused either by the agglomeration of the Au nanoparticles or by carbon deposition. HRTEM was employed first to characterize the structure of the catalyst before and after the deactivation (Fig. 8).
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2022, FuelCitation Excerpt :The broad peak located at 2θ = 23° in the fresh catalyst spectra typically represents amorphous SiO2. Notably, the anatase TiO2 peak at 2θ = 25° was absent in the spectra, which indicates the lack of crystalline TiO2 on the surfaces of the supports [17,33]. Moreover, the peaks ascribed to the anatase phase were absent in the XRD patterns of the deactivated and regenerated catalysts.


