Abstract

We have made high surface area catalysts for the selective oxidation of methanol to formaldehyde. This is done in two ways - (i) by doping haematite with Al ions, to increase the surface area of the material, but which itself is unselective and (ii) by surface coating with Mo which induces high selectivity. Temperature programmed desorption (TPD) of methanol shows little difference in surface chemistry of the doped haematite from the undoped material, with the main products being CO2 and CO, but shifted to somewhat higher desorption temperature. However, when Mo is dosed onto the haematite surface, the chemistry changes completely to show mainly the selective product, formaldehyde, with no CO2 production, and this is little changed up to 10% Al loading. But at 15 wt% Al, the chemistry changes to indicate the presence of a strongly acidic function at the surface, with additional dimethyl ether and CO/CO2 production characteristic of the presence of alumina. Structurally, X-ray diffraction (XRD) shows little change over the range 0-20% Al doping, except for some small lattice contraction, while the surface area increases from around 20 to 100 m2 g-1. Using X-ray absorption spectroscopy (XAS) it is clear that, at 5% loading, the Al is incorporated into the Fe2O3 corundum lattice, which has the same structure as α-alumina. By 10% loading then it appears that the alumina starts to nano-crystallise within the haematite lattice into the γ form. At higher loadings, there is evidence of phase separation into separate Al-doped haematite and γ-alumina. If we add 1 monolayer equivalent of Mo to the surface there is already high selectivity to formaldehyde, but little change in structure, because that monolayer is isolated at the surface. However, when three monolayers equivalent of Mo is added, we then see aluminium molybdate type signatures in the XANES spectra at 5% Al loading and above. These appear to be in a sub-surface layer with Fe molybdate, which we interpret as due to Al substitution into ferric molybdate layers immediately beneath the topmost surface layer of molybdena. It seems like the separate γ-alumina phase is not covered by molybdena and is responsible for the appearance of the acid function products in the TPD.

Highlights

  • We have made high surface area catalysts for the selective oxidation of methanol to formaldehyde

  • In particular we have utilised the soft X-ray capabilities of the Phoenix beamline at the Swiss Light Source (SLS) to carry out Al X-ray absorption near edge structure (XANES) and extended X-ray absorption fine structure (EXAFS) in order to assess the changes in local structure as Al loading increases

  • Since Al-doping boosts the surface area of these materials, we label Al-doped samples of Fe2O3 as high surface area (HSA) Fe2O3: the weight proportion of Al in a sample is denoted in percentage terms, so 5 wt% Al-doped Fe2O3 is labelled 5% HSA Fe2O3

Read more

Summary

Introduction

We have made high surface area catalysts for the selective oxidation of methanol to formaldehyde. Initial studies of Al-doped haematite have been conducted as support materials in shell-core selective oxidation catalysts.[6] It was found that the incorporation of 5 wt% Al into Fe2O3 doubled the surface area of the post-calcination material, while essentially retaining the corundum structure.

Objectives
Results
Conclusion
Full Text
Paper version not known

Talk to us

Join us for a 30 min session where you can share your feedback and ask us any queries you have

Schedule a call

Disclaimer: All third-party content on this website/platform is and will remain the property of their respective owners and is provided on "as is" basis without any warranties, express or implied. Use of third-party content does not indicate any affiliation, sponsorship with or endorsement by them. Any references to third-party content is to identify the corresponding services and shall be considered fair use under The CopyrightLaw.