Open Access

Structure and properties of molybdenum oxide nitrides as model systems for selective oxidation catalysts

  • Sven Kühn1,
  • Peter Schmidt-Zhang1,
  • Alexander HP Hahn1,
  • Manoup Huber1,
  • Martin Lerch1 and
  • Thorsten Ressler1Email author
Chemistry Central Journal20115:42

DOI: 10.1186/1752-153X-5-42

Received: 7 April 2011

Accepted: 15 July 2011

Published: 15 July 2011


Molybdenum oxide nitride (denoted as Mo(O,N)3) was obtained by ammonolysis of α-MoO3 with gaseous ammonia. Electronic and geometric structure, reducibility, and conductivity of Mo(O,N)3 were investigated by XRD, XAS, UV-Vis spectroscopy, and impedance measurements. Catalytic performance in selective propene oxidation was determined by online mass spectrometry und gas chromatography. Upon incorporation of nitrogen, Mo(O,N)3 maintained the characteristic layer structure of α-MoO3. XRD analysis showed an increased structural disorder in the layers while nitrogen is removed from the lattice of Mo(O,N)3 at temperatures above ~600 K. Compared to regular α-MoO3, Mo(O,N)3 exhibited a higher electronic and ionic conductivity and an onset of reduction in propene at lower temperatures. Surprisingly, α-MoO3 and Mo(O,N)3 exhibited no detectable differences in onset temperatures of propene oxidation and catalytic selectivity or activity. Apparently, the increased reducibility, oxygen mobility, and conductivity of Mo(O,N)3 compared to α-MoO3 had no effect on the catalytic behavior of the two catalysts. The results presented confirm the suitability of molybdenum oxide nitrides as model systems for studying bulk contributions to selective oxidation.


Molybdenum oxides are active heterogeneous catalysts for selective oxidation of light alkanes and alkenes [16]. In addition to catalytic activity and long-term stability, improved selectivity and efficient use of raw materials become of increasing importance in industrial applications. In spite of intensive research, structure-reactivity correlations and knowledge about the catalytically active species remain scarce. Hence, new catalysts are developed by "trial and error" methods. Although this approach has been successful, it becomes increasingly apparent that new ways need to be explored to further advance the design of improved functional materials. Therefore, a deeper understanding of the correlations between structure, activity, and selectivity will serve as the foundation for a knowledge-based development of new and enhanced catalysts.

Selective oxidation of alkenes using molybdenum oxide catalysts is commonly believed to proceed according to a reduction-oxidation-mechanism [1, 4]. In a first step the reactant partially reduces the metal oxide catalyst. Afterwards, the catalyst is re-oxidized by oxygen from the gas phase. Hence, lattice oxygen of the molybdenum oxide catalyst is suggested to selectively oxidize the alkene. Oxidation experiments using 18O have verified that lattice oxygen of α-MoO3 is involved in the catalytic process [7]. Accordingly, mobility of oxygen in the lattice of the oxide catalyst is expected to play an important role for catalyst activity and selectivity.

Conventional molybdenum based oxide catalysts consist of either binary molybdenum oxide system or mixed oxides with additional metal centers. Additional metals such as W, Nb, or V stabilize characteristic crystallographic structures which lead to oxidation catalysts with improved activity and selectivity [8, 9]. However, the influence of structural variety and chemical complexity in the mixed oxide systems on catalytic performance is difficult to distinguish. In order to reduce this inherent complexity of mixed oxide catalysts, suitable model systems are sought. In particular with respect to elucidating the effect of oxygen mobility on catalytic performance it appears counterproductive to vary chemical composition and oxide lattice structure simultaneously. Hence, instead of modifying the cation lattice to affect oxygen mobility it seems more promising to directly modify the anion lattice. Ideally however, this modification should have little influence on the long-range order crystallographic structure of the catalyst.

Along that line, metal oxide nitrides appear to be suitable model systems. In many cases nitrogen can be incorporated in the oxide lattice of a particular metal oxide without changing the crystallographic structure [10, 11]. Alternatively, metastable and previously not available oxide structures can be obtained without changing the cation composition [12, 13]. Both approaches may result in suitable model systems for selective oxidation catalysts. Zirconium oxide nitrides, for instance, have been shown to be active catalysts for ammonia decomposition [14]. It is suggested, however, that in these materials the nitrogen atoms not only affect anion mobility but also directly participate in the catalytic reaction.

In this work we have chosen molybdenum trioxide in the orthorhombic α-MoO3 modification as well-known model system for selective propene oxidation catalysts. α-MoO3 is transformed into the corresponding molybdenum oxide nitride by reaction with gaseous ammonia. Subsequently, the thus obtained model catalyst is used to reveal correlations between lattice oxygen availability, electrical properties, and catalytic activity and selectivity in selective propene oxidation.

Results and Discussion

Structural characterization of Mo(O,N)3

Geometric and electronic structure of Mo(O,N)3 and reference α-MoO3 were investigated by XRD, XAS, and DR-UV-Vis spectroscopy. The aim of these studies was to reveal significant differences in structural and electronic properties of the two materials to be used as model systems for oxidation catalysts. Interestingly, incorporation of nitrogen in α-MoO3 resulted in a pronounced color change of the material. In contrast to the light-grey color of α-MoO3, Mo(O,N)3 exhibited a dark-blue color. This color change, however, cannot be attributed to a significant reduction of MoO3 to MoO2 (< 5%).

XRD patterns and XAS spectra of α-MoO3 and Mo(O,N)3 are shown in Figure 1 and Figure 2, respectively. The XRD pattern and the XANES and EXAFS spectra of Mo(O,N)3 are similar to those of α-MoO3 without additional phases detectable. Crystallite size of α-MoO3 amounted to ~ 60 nm as calculated from the integral breadths of XRD peaks using the Scherrer equation [15]. Apparently, the long-range order and short-range order structure of α-MoO3 is preserved after incorporation of nitrogen. Despite the overall agreement, subtle differences can be seen in the XRD patterns and XAS data of α-MoO3 and Mo(O,N)3. An increased XRD peak broadening (Figure 1) and a reduced XAFS amplitude (Figure 2) indicate an increased formation of defects in the Mo(O,N)3 structure upon nitridation. It is suggested that nitrogen atoms substitute for oxygen in the layers of α-MoO3 leading to an increased strain and a corresponding peak broadening in the XRD pattern. Similarly, an increased distance distribution around the Mo centers in Mo(O,N)3 resulted in the XAFS amplitude reduction observed. Moreover, analysis of the Mo K edge shift revealed an average valence of +5.86 for Mo(O,N)3 and +5.96 for the α-MoO3 used as reference [16]. According to the simplified defect model assumed incorporation of nitrogen results in formation of vacancies in the anion lattice ( ). Therefore, the slight reduction in Mo average valence should not be related to the presence of nitrogen but rather originate from a slight reduction of α-MoO3 by gaseous ammonia during sample preparation. However, the corresponding 5% MoO2 were not detectable in the XRD or XAFS data of Mo(O,N)3.
Figure 1

XRD patterns (top) and DR-UV-Vis absorption spectra (bottom) of α- MoO 3 and Mo(O,N) 3 .

Figure 2

XANES spectra of α- MoO 3 and Mo(O,N) 3 at 298 K (top) and Fourier transformed χ(k) of α- MoO 3 and Mo(O,N) 3 (before and after catalysis) (bottom).

Absorption edge energies in the UV-Vis range as determined by DR-UV-Vis spectroscopy (Figure 1) amounted to 3.3 eV for α-MoO3 and 2.8 eV for Mo(O,N)3. Inter-valence transitions in the range from 1 - 3 eV in the UV-Vis spectrum of α-MoO3 corroborated the reduced average valence of 5.96 and the light-gray color of the reference α-MoO3 [17]. The dark-blue color of Mo(O,N)3 is suggested to originate from the formation of color centers accompanying the incorporation of nitrogen in the oxygen lattice. A similar effect has been described for intensely colored zirconium oxide nitrides compared to colorless ZrO2 [18].

Thermal stability of Mo(O,N)3

After confirming that the long-range structure of α-MoO3 persisted after incorporation of nitrogen, thermal stability of Mo(O,N)3 was studied prior to aiming at correlations between oxygen mobility and catalytic properties. Therefore, in situ XRD patterns of Mo(O,N)3 were measured under oxidative reaction conditions (5% O2 in He). Figure 3 shows the evolution of XRD patterns of Mo(O,N)3 in the temperature range from 473 K to 773 K. The XRD patterns of Mo(O,N)3 exhibited an increasing peak intensity and decreasing peak-broadening with increasing reaction temperature. Conversely, the XRD patterns of α-MoO3 showed no significant changes during thermal treatment in oxygen. For a more detailed analysis, evolution of the integral breadth determined from the 110, 101, and 020 reflections of α-MoO3 and Mo(O,N)3 is shown in Figure 3. Only minor changes were detectable for α-MoO3. Conversely, above ~623 K the integral breadth determined for Mo(O,N)3 changed dramatically while the effect decreased going from 020 to 110 and 101. Variations in integral breadth can be attributed to changes in crystallite size, strain, or disorder. Because of the characteristic evolution of integral breadth with temperature as depicted in Figure 3 the changes observed were interpreted in terms of varying disorder in the crystallites of Mo(O,N)3. Apparently, at temperatures above ~623 K nitrogen was removed from the molybdenum oxide lattice. This was accompanied by a reduced defect density in the layers of Mo(O,N)3 which corresponds to the more pronounced change in peak-width of the 020 peak compared to 110 or 101 (Figure 3). Above 700 K the integral breadths of thermally treated Mo(O,N)3 became similar to those of α-MoO3. This indicates the largely reversible incorporation and removal of nitrogen from the oxide layer structure of α-MoO3. Furthermore, evolution of DR-UV-Vis spectra of Mo(O,N)3 during thermal treatment in oxygen revealed an increase of the absorption edge energy above ~623 K. Again the final edge energy above 700 K corresponded to that of α-MoO3. Eventually, Mo(O,N)3 samples subjected to thermal treatment at 673 K in various in situ experiments exhibited a remaining nitrogen content of about 25% of the original amount. Hence, it was concluded that Mo(O,N)3 constitutes a suitable model system for correlating structural and functional properties of an anion-lattice modified Mo oxide catalyst at temperatures below 673 K.
Figure 3

Evolution of XRD patterns during thermal treatment of Mo(O,N) 3 (473 - 773 K, 5% O 2 in He) and integral breadth calculated for reflections 020 (rectangles), 110 (circles), and 101 (triangles) of α- MoO 3 and Mo(O,N) 3 .

Reducibility of α-MoO 3 and Mo(O,N) 3

According to the redox mechanism for selective oxidation reactions, availability of lattice oxygen to the gaseous reactants appears to be an important parameter for activity and selectivity of oxidation catalysts. Hence, temperature-programmed reduction is a common method to investigate and compare metal oxide catalysts. Here, the reduction behavior of α-MoO3 and Mo(O,N)3 was studied in situ by XRD, XAS, and DR-UV-Vis spectroscopy. As reported previously, α-MoO3 is readily reduced to MoO2 in 5% propene at temperatures above ~ 650 K [16, 1921]. Besides the formation of shear-structural defects in the α-MoO3 layers, no ordered intermediate phases are detectable during reduction. Similar to these previous reports reduction of both Mo(O,N)3 and α-MoO3 to MoO2 was observed by in situ XRD and XAS. However, analysis of Mo K edge position and evolution of gaseous products revealed a much improved reducibility of Mo(O,N)3 (Figure 4). Apparently, the presence of nitrogen in the α-MoO3 layers resulted in an onset temperature of ~ 660 K for Mo(O,N)3 compared to ~ 700 K for α-MoO3. Given the nearly identical long-range order structures, crystallite sizes, and morphologies of α-MoO3 and Mo(O,N)3, the better reducibility of Mo(O,N)3 has to be attributed to an increased oxygen mobility in the defect-rich layers of Mo(O,N)3. The higher oxygen mobility of Mo(O,N)3 compared to α-MoO3 may be caused by oxygen vacancies formed during incorporation of nitrogen in α-MoO3 according to . Eventually, the treatment of Mo(O,N)3 at temperatures above 750 K resulted in the removal of nitrogen from the oxide layers. Upon re-oxidation to MoO3 both materials exhibited the same reduction behavior.
Figure 4

Evolution of Mo K edge shift during reduction of α- MoO 3 (solid line) and Mo(O,N) 3 (dashed line) (300 K - 773 K, 5% propene in He) and corresponding ion currents of water and acrolein.

Electrical properties of Mo(O,N)3

Incorporation of nitrogen in the layer structure of α-MoO3 should have a pronounced effect on the electrical properties of Mo(O,N)3 (i.e. both electronic and ionic conductivity). Conductivity of α-MoO3 and Mo(O,N)3 was studied by impedance spectroscopy. At 300 K the conductivity of Mo(O,N)3 exceeded that of α-MoO3 by a factor of 500. Unfortunately, the set-up used did not permit to distinguish between electronic and ionic conductivity in a mixed conductor such as α-MoO3. Hence, the dominating conduction process at a given temperature was concluded from the corresponding activation energy obtained from temperature-dependent impedance measurements. As an example, Figure 5 shows the Nyquist presentation of impedance measurements of α-MoO3 in the temperature range from 524 K to 834 K. The decreasing diameter of the semi-circles corresponds to a decreasing resistance with increasing temperature. Evolution of the resistance of Mo(O,N)3 during thermal treatment in air is shown in Figure 5. Above 600 K Mo(O,N)3 exhibited an increasing resistance. Eventually, at temperatures above 700 K the thermally treated Mo(O,N)3 showed the same resistance as α-MoO3. This temperature range coincides with the onset of oxygen mobility above 600 K and the removal of nitrogen from Mo(O,N)3 between 600 K and 700 K followed by formation of regular α-MoO3. Hence, the evolution of electrical properties of Mo(O,N)3 is in good agreement with the structural changes occurring between 600 K and 700 K (Figure 3).
Figure 5

Nyquist presentation of impedance measurements of α-MoO 3 (top) at selected temperatures between 524 K and 659 K and evolution of resistances of α- MoO 3 and Mo(O,N) 3 with increasing temperature (bottom).

From an Arrhenius type presentation of the conductivity as a function of temperature, the activation energies of the corresponding dominating processes can be obtained. α-MoO3 showed two different extrinsic conduction processes with activation energies of 0.22 eV and 0.77 eV below 773 K (Figure 6). These values agree with previous reports [22] and have been assigned to electronic and structural defects in α-MoO3 (0.22 eV) and oxygen mobility at temperatures above 639 K (0.77 eV). Above 773 K an activation energy of 1.56 eV was found. With respect to the band gap energy of α-MoO3 of 3.3 eV, this activation energy is assigned to intrinsic conduction of MoO3. At temperatures below 500 K Mo(O,N)3 showed two activation energies of different extrinsic conduction processes (Figure 6). Because of the beginning and rather continuous reaction of Mo(O,N)3 to α-MoO3 at temperatures above 500 K, no reliable activation energies could be obtained in this temperature range.
Figure 6

Arrhenius type presentation of conductivity of α- MoO 3 (top) and Mo(O,N) 3 (bottom). Activation energies of various conduction processes are indicated.

Functional and structural characterization of Mo(O,N)3under catalytic conditions

Functional characterization of Mo(O,N)3 and α-MoO3 in selective propene oxidation was conducted simultaneously with in situ structural UV-Vis and XAS measurements. For a sufficient time-resolution, the gas phase composition was qualitatively analyzed by a non-calibrated mass spectrometer. Time-resolved measurements were required because of the ongoing nitrogen removal from Mo(O,N)3 at temperatures above 600 K. Prolonged experiments under steady-state conditions may have been prone to missing minor differences in the performance of the catalysts. Repeated quantitative measurements of the gas phase composition under selective oxidation reaction conditions were performed by gas chromatography at selected temperatures.

Evolution of Mo K edge Fourier transformed χ(k) of α-MoO3 and Mo(O,N)3 measured during thermal treatment in 5% propene and 5% oxygen in the temperature range from 300 K to 723 K is depicted in Figure 7. In the first run, besides minor differences in the spectra of the starting materials, α-MoO3 and Mo(O,N)3 exhibited a similar evolution. The reduction in amplitude was mainly caused by the increasing reaction temperature. During a second thermal treatment under reaction conditions and, hence, after removal of nitrogen above 600 K, both samples showed the same structural evolution. Moreover, the Mo K edge position of α-MoO3 showed no significant change during treatment in propene and oxygen. Conversely, above ~600 K the Mo K edge position of Mo(O,N)3 continuously shifted to higher energies with increasing temperature. This behavior is again correlated to the removal of nitrogen at temperatures above ~ 600 K. During the second run the edge position remained at a constant value, similar to that of α-MoO3. Hence, evolution of the local geometric and electronic structure revealed that removal of nitrogen from Mo(O,N)3 under propene oxidation conditions resulted in regular α-MoO3 exhibiting the same structural and electronic properties as the starting α-MoO3 material. This is in good agreement with the in situ XRD measurements described above (Figure 3).
Figure 7

Evolution of Fourier transformed χ(k) of α- MoO 3 (top) and Mo(O,N) 3 (bottom) during treatment in 5% propene and 5% oxygen in the temperature range from 300 K to 723 K.

As to the catalytic properties of α-MoO3 and Mo(O,N)3, evolution of propene oxidation products acrolein and CO2 during two consecutive treatments is depicted in Figure 8. Apparently, under propene oxidation conditions both materials exhibited a very similar behavior already during the first treatment. Thus, no significant differences in onset temperature or product evolution were detectable. In spite of their significantly different structural and electronic characteristics (reducibility and conductivity) both sample showed a nearly identical catalytic performance.
Figure 8

Ion currents (CO 2 and acrolein) measured during in situ XAFS studies on α- MoO 3 (red) and Mo(O,N) 3 (black) (Figure 7) in 5% propene and 5% oxygen in the temperature range from 300 K to 723 K.

In situ DR-UV-Vis experiments under propene oxidation conditions were performed in a temperature range from 298 K to 700 K during two consecutive runs. Evolution of DR-UV-Vis spectra of α-MoO3 and Mo(O,N)3 is depicted in Figure 9. Above 4 eV the two series exhibited a very similar behavior. This corresponded to only minor structural changes in both MoO3 type materials under catalytic reaction conditions. Conversely, below the absorption edge at about 3.5 eV Mo(O,N)3 showed a more pronounced change in the DR-UV-Vis spectra with temperature. This change corresponded to the removal of nitrogen at temperatures above ~600 K and the accompanying modification of the electronic structure of Mo(O,N)3. Accordingly, the UV-Vis spectrum of Mo(O,N)3 after thermal treatment became more similar to that of regular α-MoO3. The apparent differences between the spectra of both catalysts after thermal treatment can be ascribed to a residual amount of nitrogen in the oxygen lattice of Mo(O,N)3. Overall, the structural changes observed in the evolution of UV-Vis spectra (Figure 9) were similar to the results of in situ XAS or XRD experiments as described above (Figure 3 and Figure 7). Apparently, in situ bulk structural studies on Mo(O,N)3 and α-MoO3 resulted in nearly the same short-range to medium-range structure after catalysis experiments. Conversely, UV-Vis spectroscopy proved to be more sensitive to minor electronic effects of nitrogen residuals in Mo(O,N)3 after thermal treatment.
Figure 9

In situ DR-UV-Vis absorption spectra of α- MoO 3 and Mo(O,N) 3 measured during two consecutive treatments in 5% propene and 5% O 2 in the temperature range from 300 K to 700 K.

The corresponding evolution of MS ion currents of acrolein and CO2 measured during treatment of α-MoO3 and Mo(O,N)3 in propene and oxygen from 300 K to 700 K is depicted in Figure 10. Apparently, during two consecutive treatments both catalysts exhibited the same onset of catalytic activity and the same qualitative evolution of catalytic performance. As stated above, no effect of the pronounced geometric and electronic differences between α-MoO3 and Mo(O,N)3 was detectable in the evolution of gaseous oxidation products during catalytic testing. The presence of nitrogen in Mo(O,N)3 and the removal of a large fraction of nitrogen from Mo(O,N)3 during treatment at temperatures above ~600 K did not result in detectable differences in catalytic behavior.
Figure 10

Ion currents (CO 2 and acrolein) measured during two consecutive treatments of α- MoO 3 (red) and Mo(O,N) 3 (black) (Figure 9) in 5% propene and 5% oxygen in the temperature range from 300 K to 700 K.

In addition to time-resolved MS measurement during catalytic testing, the gas phase composition at selected temperatures was quantitatively analyzed by gas chromatography. Conversion of propene and product selectivity to acrolein, CO2, and CO at 655 K and 700 K of α-MoO3 and Mo(O,N)3 are shown in Figure 11. Under the reaction conditions chosen, α-MoO3 and Mo(O,N)3 exhibited an average propene conversion of 1.1% or 2.2%, and 1.1% or 2.5%, respectively. Additionally, α-MoO3 and Mo(O,N)3 exhibited nearly the same product selectivities at the reaction temperatures used. As already observed in the time-resolved measurements, also under steady-state conditions the presence of nitrogen in Mo(O,N)3 did not result in significant differences in catalytic behavior compared to α-MoO3.
Figure 11

Propene conversion and selectivity of α- MoO 3 (top) und Mo(O,N) 3 (bottom) in 5% propene and 5% oxygen at 655 K (measurements 1-5) and 700 K (measurements 6-10).


Eventually, structure function correlations of Mo(O,N)3 can be concluded from the described investigations. Characterization of electronic and geometric structure as well as reducibility of Mo(O,N)3 resulted in a pronounced influence of the incorporation of nitrogen in the layer structure of α-MoO3 (Figure 1 - Figure 4). Compared to regular α-MoO3, Mo(O,N)3 exhibited a much increased electronic and ionic conductivity (Figure 5). The latter afforded a lowering of the onset of reduction of Mo(O,N)3 by about 40 K (Figure 4). Structural studies at elevated temperatures showed that nitrogen is removed from the oxide lattice of Mo(O,N)3 above ~600 K. The thus obtained MoO3 exhibited again the same short-range and long-range structural characteristics as the parent α-MoO3 material (Figure 3 and Figure 7). Nevertheless, in spite of these characteristic differences between the α-MoO3 and Mo(O,N)3 used, both materials exhibited no detectable differences in their catalytic behavior. Neither studying onset temperatures by time-resolved methods (Figure 8 and Figure 10) nor measuring conversion or selectivity under steady-state conditions (Figure 11) revealed a pronounced influence of the incorporation of nitrogen in the oxide lattice on catalytic properties.

In the conventional reduction-oxidation mechanism for selective oxidation reactions the reactant is oxidized by nucleophilic lattice oxygen. This way, oxygen vacancies in the oxide lattice are generated at the surface of the catalyst. Subsequently, these vacancies are supposed to be re-filled by diffusion of oxygen from the bulk of the oxide catalyst to its surface. Desorption of products terminates the catalytic cycle and frees the active site for the next reactant molecule. Eventually, the catalyst needs to be re-oxidized by gas phase oxygen to prevent deep-reduction and deactivation. However, if in fact diffusion of oxygen was required to replenish the oxygen reservoir at the catalyst surface, influencing the mobility of oxygen in the catalyst bulk structure should have a distinct influence on its catalytic properties. The results presented here suggest that at least for α-MoO3 in propene oxidation this is not the case. Apparently, varying oxygen mobility has no detectable effect on the catalytic performance of α-MoO3. This implies that if oxygen vacancies are generated at the surface of the catalyst by reaction with propene, these vacancies will be directly filled by gas phase reaction without requiring diffusion of oxygen from the bulk. Hence, the similar catalytic behavior of α-MoO3 and Mo(O,N)3 may be attributed to similar surface structures forming on both materials under reaction conditions. This may underline the importance of the particular structure and composition of the surface rather than optimized bulk properties of selective oxidation catalysts. However, the bulk structural characterization techniques employed here do not permit further conclusions as to the surface structures of the materials. Moreover, whether activation and oxidation of propene, and activation of gas phase oxygen occur simultaneously or in consecutive steps can only be speculated. However, it appears that a conventional Langmuir-Hinshelwood type mechanism may sufficiently describe propene oxidation on α-MoO3 without requiring a particular contribution from the catalyst bulk.

In summary, the results presented here confirm the suitability of molybdenum oxide nitrides as model systems for studying bulk contributions to selective alkene oxidation. With regular α-MoO3, incorporation of nitrogen permits to significantly and reversibly modify electronic properties and bulk oxygen mobility. Nitrogen can be conveniently removed from the oxide lattice by thermal treatment resulting in the original starting material. Hence, catalytic properties of the materials with and without nitrogen in the oxide lattice can readily be probed by consecutive experiments. Future studies on mixed molybdenum oxide nitrides will be employed to confirm both their applicability as model systems and our conclusions regarding correlations between catalytic performance and electrical properties of oxide catalysts.


Preparation of molybdenum oxide nitride

Molybdenum oxide nitride (in the following denoted as Mo(O,N)3) was prepared by reaction of gaseous ammonia with commercial α-MoO3 (Chempur). Ammonolysis was performed in a conventional tube furnace using a silica tube and direct gas supply[23]. After drying at 383 K in air, α-MoO3 was reacted to Mo(O,N)3 at 548 K with an NH3 flow of 10 l/h for 10 h. These particular conditions had been optimized in respect to a maximum concentration of incorporated nitrogen in MoO3 without a detectable amount of rutile-type MoO2 or Mo(O,N)2. Increasing the temperature, the presence of such phases was clearly detected using X-ray powder diffraction. With decreasing temperature the nitrogen content of the MoO3 phase strongly decreased. Quantitative nitrogen/oxygen analysis was carried out using the well-established hot gas extraction method (LECO TC-300/EF-300 N/O analyzer). At this procedure the samples were heated under flowing helium in a graphite crucible up to about 2700 °C. Oxygen was determined as CO2 by IR spectroscopy, the amount of nitrogen as N2 gas by heat conductivity measurements of the nitrogen/helium gas. Such measurements resulted in a nitrogen content of 0.41 (± 0.01) wt-% for the sample used in this work. Hot gas extraction, however, does not permit to study the nitrogen content of the material in situ under catalysis or oxidation-reduction conditions.

Diffuse reflectance UV-Vis spectroscopy

A JASCO V-670 double beam spectrometer was used for DR-UV-Vis measurements. Ex situ spectra were recorded in a BaSO4 coated integration sphere in a wavelength range from 200 to 2000 nm and a scanning speed of 40 nm/min. In situ measurements used a "Praying Mantis" set-up (Harrick) at a scanning speed of 200 nm/min in a range from 220 to 900 nm under catalytic (5% propene and 5% O2 in He) or reducing (5% propene in He) reaction conditions.

On-line gas phase analysis

Quantitative catalysis measurements were performed using an online gas chromatography system (Varian CP-3800) and a non-calibrated mass spectrometer (Pfeiffer Omnistar). Hydrocarbons and oxygenated reaction products were analyzed using a Deans switch consisting of a carbowax capillary column connected to a AL2O3/MAPD column or a fused silica restriction (25 m*0.32 mm each), and flame ionization detectors. Reactant gas flow rates of oxygen, propene, and Helium were adjusted with separate mass flow controllers to a total flow of 40 ml/min. A mixture of 5% propene and 5% oxygen in helium was used for catalytic testing in the temperature range from 300 K to 748 K. All lines and valves were preheated to 473 K.

Powder X-ray diffraction

Ex situ XRD measurements were conducted on an X'Pert PRO MPD diffractometer (Panalytical, θ-θ geometry) using Cu Kα radiation and a solid-state multiple-channel detector. Wide angle XRD scans were collected in reflection mode using a silicon sample holder. In situ XRD experiments were performed in θ-θ geometry on a STOE diffractometer (Cu Kα-radiation) equipped with a PARR reaction chamber. Temperature-programmed experiments were conducted in a range from 473 K to 773 K in steps of 25 K and an effective heating rate of 0.32 K/min (2θ range from 10° to 42°). Measuring time per XRD scan amounted to about 2 hours. The gas-phase composition at the cell outlet was analyzed online with a mass spectrometer (Pfeiffer Omnistar).

X-ray absorption spectroscopy (XAS)

In situ transmission XAS spectra were measured at the Mo K edge (20.0 keV) at beamline X1 at the Hamburg Synchrotron Radiation Laboratory, HASYLAB, using a suitable in situ cell [21]. Samples were pressed to pellets with a diameter of 5 mm (7 mg with 30 mg boron nitride). EXAFS spectra at the Mo K edge in the k space up to 14 Å-1 were collected in ~ 4 min. Temperature-programmed reduction was conducted in 5% propene and He (total flow of 40 ml/min) in a temperature range from 293 K to 773 K at a heating rate of 5 K/min. Reaction tests were performed in 5% propene and 5% O2 in He in the temperature range from 293 K to 723 K (5 K/min, total flow 40 ml/min). The gas atmosphere was analyzed using a non-calibrated mass spectrometer in a multiple ion detection mode (Pfeiffer Omnistar).

X-ray absorption fine structure (XAFS) analysis was performed using the software package WinXAS v3.2 [24]. Linear polynomials and 3rd degree polynomials were fitted to the pre-edge and post-edge region of an absorption spectrum for background subtraction and normalization, respectively. The extended X-ray absorption fine structure (EXAFS) χ(k) was extracted by using cubic splines to obtain a smooth atomic background μ 0 (k). The FT(χ(k)*k3), often referred to as pseudo radial distribution function, was calculated by Fourier transforming the k3 weighted experimental χ(k) function, multiplied by a Bessel window, into the R space.

Impedance spectroscopy

Impedance of molybdenum oxides and oxide nitrides was obtained by measuring the magnitude |Z| and the phase φ of an alternating current as a response of an applied alternating potential (impedance analyzer N4L: IAI+PSM1735). From that the real part Z' and imaginary part Z'' of the complex impedance was calculated. The impedance was measured as a function of frequency (200 kHz - 0.1 Hz) and temperature (α-MoO3: 527 K - 848 K, Mo(O,N)3: 306 K- 449 K). Oxides and oxide nitride samples were pressed to pellets with a diameter of 15 mm (1.5 g initial weight, 7.5 kPa pressure) and placed between two Pt disc electrodes for impedance measurements.



The Hamburg Synchrotron Radiation Laboratory, HASYLAB, is acknowledged for providing beamtime for this work. A. Stys and A. Walter are acknowledged for contributing to the materials characterization. The authors are grateful to the Deutsche Forschungsgemeinschaft, DFG (Cluster of Excellence "Unifying Concepts in Catalysis") for financial support.

Authors’ Affiliations

Institut für Chemie, Technische Universität Berlin


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