15 research outputs found
Dynamics of bound states of dihydrogen at Cu(I) and Cu(II) species coordinated near one and two zeolite framework aluminium atoms: A combined sorption, INS, IR and DFT study
Abstract Ambient conditions sorption isotherms of dihydrogen in a series of various levels of Cu-exchanged ZSM-5 zeolites, with two different Si/Al ratios, namely 11.5 and 25, show the presence of different amount of Cu centres able to strongly bind H2. Although the isosteric heats of adsorption derived from these isotherms are rather similar, of the order of 30 kJ/mol H2, Inelastic Neutron Scattering (INS) of adsorbed dihydrogen and Fourier-Transformed Infra-Red (FTIR) spectroscopy measurements of adsorbed CO and NO reveal that copper is encountered in two oxidation states. At least two types of Cu(I) ions are clearly detected as well as some heterogeneity of the Cu(II) species. The number of these Cu species is different in the two investigated ZSM-5 materials and depends on the Cu exchange level. With the aid of DFT model cluster calculations we find that under different coordination environments, determined by the Al distribution, both mono- and divalent Cu ions could bind H2 with a different strength. Unprecedentedly, we found that Cu-ions compensating two Al atoms, i.e. formally Cu(II) species, relatively far apart from each other, may behave very similarly to the monovalent Cu-species or alternatively viewed – as Cu(I) species that compensate for two framework Al-atoms. Such Cu-species also form stable η2 dihydrogen complexes
FTIR Evidence of Different Bonding of Methane to OH Groups on H–ZSM-5, HY, and SiO<sub>2</sub>
Low-temperature adsorption of CH<sub>4</sub> and <sup>15</sup>N<sub>2</sub> on H–ZSM-5, SiO<sub>2</sub>, and HY
is comparatively
studied. Partly and fully deuteroxylated samples were also investigated.
It was established that methane forms H bonds simultaneously with
oxygen and hydrogen from the Si–OH groups, which reflects in
enhanced shift of the OH modes to lower frequency as compared to the
case if methane was bound to the proton only. In contrast, methane
is attached to highly acidic hydroxyls forming a bond mainly with
the proton. At high methane equilibrium pressure, a second methane
molecule is bound to the same acidic OH group
Characterization of vanadium sites on vanadium-containing mesoporous silica catalysts and their catalytic behaviour in propane ODH
Parameters that affect the catalytic behaviour of vanadium-containing
mesoporous silicas in oxidative dehydrogenation reaction of propane are mainly
aggregation state of surface VOx species and reducibility of vanadium species.
Type and conditions of synthesis have big impact on the nature of vanadium
species and, therefore, influence significantly catalytic properties. Two vanadiumcontaining
mesoporous silica catalysts were synthesized by different techniques
(including direct synthesis from hydrogel containing vanadium precursor and wet
impregnation of SBA-15 mesoporous silica by vanadyl acetylacetonate) and their
physico-chemical and catalytic properties were studied and compared. Direct
synthesis of vanadosilicate led to catalysts with non-uniform mesoporosity, but
exhibiting better spreading of vanadium on the surface resulting in species with lower degree of polymerization compared to impregnated catalyst. It is reflected
in higher iso-conversional selectivity of directly synthesized catalyst towards
propene
Role of methods and conditions of preparation of vanadium species supported on lamellar zeolite MCM-36 in their catalytic behaviour in oxidative dehydrogenation of propane
In this work, we report successful preparation of hierarchical VOx-MCM-36
catalysts. Lamellar pillared zeolitic support (MCM-36) was prepared from layered
precursor of MCM-22P zeolite by swelling and pillaring. Vanadium was
introduced into MCM-36 support by different methods (including conventional
impregnation and ion exchange) by means of different precursors and synthesis
conditions. Textural properties of prepared catalysts were characterized by
nitrogen adsorption-desorption isotherms, the concentration of vanadium was determined by X-ray fluorescence and vanadium complex speciation was
investigated by diffuse reflectance UV-vis spectroscopy, hydrogen temperature
programmed reduction (H2 -TPR), electron paramagnetic resonance (EPR) and
Fourier transform infrared (FTIR) spectroscopy. Effect of synthesis method and
conditions on catalytic behaviour was tested in the oxidative dehydrogenation of
propane at 540 °C. The vanadium is present in oxidation state IV, instead of usual
oxidation state V, in the cases of the catalyst with low content of vanadium. The
best selectivity to propene with 13 % of conversion (43.9 %) was obtained when
the acid center was neutralized with potassium cations and the content of
vanadium was 2 wt %
OH/OD Isotopic Shift Factors of Isolated and H‑Bonded Surface Silanol Groups
The
OH/OD isotopic shift factors (<i>i = </i>ν<sub>OH</sub>/ν<sub>OD</sub>) of isolated silanols on SiO<sub>2</sub> and
[Si]BEA are between 1.3563 and 1.3568, values lower than the
theoretical shift of 1.3744. However, <i>i</i> of the harmonic
OH modes almost coincides with the theoretical value which indicates
that the experimental deviations in this case are mainly due to anharmonicity.
The anharmonicity slightly decreases when the OH groups participate
in weak H-bonding with adsorbed CH<sub>4</sub> or CO which should
lead to an increase of <i>i</i>. However, contrary to these
expectations, <i>i</i> additionally decreases. This is attributed
to the lower acidity of the OD groups as compared to the respective
OHs. The value of <i>i</i> is also lower for H-bonded silanols
as compared to isolated SiOH groups. It is concluded that <i>i</i> depends on the extent of H-bonding which allows easy distinguishing
between isolated and H-bonded surface hydroxyls
Pt/CeO<sub><i>x</i></sub>/ZrO<sub><i>x</i></sub>/γ-Al<sub>2</sub>O<sub>3</sub> Ternary Mixed Oxide DeNO<sub><i>x</i></sub> Catalyst: Surface Chemistry and NO<sub><i>x</i></sub> Interactions
Surface
chemistry and the nature of the adsorbed NO<sub><i>x</i></sub> species on a Pt/CeO<sub>2</sub>–ZrO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub> catalyst were investigated by IR spectroscopy,
X-ray diffraction, H<sub>2</sub>-temperature programmed reduction,
and NO<sub><i>x</i></sub>-temperature programmed desorption.
Parallel studies were also carried out with benchmark samples such
as CeO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub>, ZrO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub>, CeO<sub>2</sub>–ZrO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub> and Pt-supported versions of these materials.
All samples were studied in their reduced and nonreduced forms. The
use of CO as a probe molecule revealed that during the synthesis of
the mixed-metal oxide systems, deposited zirconia preferentially interacted
with the alumina hydroxyls, while deposited ceria was preferentially
located at the Lewis acid sites. Despite the limited extent of Zr<sup>4+</sup> ions incorporated into the CeO<sub>2</sub> lattice, the
reduction of ceria was promoted and occurred at lower temperatures
in the presence of zirconia. When deposited on ZrO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub>, platinum formed relatively big particles and
existed in metallic state even in the nonreduced samples. The presence
of ceria hindered platinum reduction during calcination and yielded
a high platinum dispersion. Subsequent reduction with H<sub>2</sub> led to the production of metallic Pt particles. Consequently, NO
adsorption on nonreduced Pt-containing materials was negligible but
was enhanced on the reduced samples because of Pt<sup>0</sup>-promoted
NO disproportionation. The nature of the nitrogen-oxo species produced
after NO and O<sub>2</sub> coadsorption on different samples was similar.
Despite the high thermal stability of the NO<sub><i>x</i></sub> adsorbed species on the ceria and zirconia adsorption sites,
the NO<sub><i>x</i></sub> reduction in the presence of H<sub>2</sub> was much more facile over Pt/CeO<sub>2</sub>–ZrO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub>. Thus, the main differences in
the NO<sub><i>x</i></sub> reduction functionalities of the
investigated materials could be related to the ability of the catalysts
to activate hydrogen at relatively lower temperatures
Surprising Coordination Chemistry of Cu<sup>+</sup> Cations in Zeolites: FTIR Study of Adsorption and Coadsorption of CO, NO, N<sub>2</sub>, and H<sub>2</sub>O on Cu–ZSM‑5
Cations
exchanged in zeolites are generally characterized by a
low coordination number and can thus attach simultaneously more than
one small guest molecule. For instance, Cu<sup>+</sup> ions in ZSM-5
can accept, at low temperature, up to three CO and up to two NO molecules.
However, only one N<sub>2</sub> molecule can be coordinated to such
sites. Although mixed aqua-carbonyl and aqua-dinitrogen complexes
are formed, no mixed carbonyl-nitrosyl, carbonyl-dinitrogen, or nitrosyl-dinitrogen
species can be produced. Thus, adsorption of NO on CO precovered sample
results in segregation of the CO adsorption layer according to the
reaction: 2Cu<sup>+</sup>–CO + 2NO → Cu<sup>+</sup>(CO)<sub>2</sub> + Cu<sup>+</sup>(NO)<sub>2</sub>. Adsorption of N<sub>2</sub> on NO precovered sample leads to a similar process: 2Cu<sup>+</sup>–NO + N<sub>2</sub> → Cu<sup>+</sup>(NO)<sub>2</sub> + Cu<sup>+</sup>–N<sub>2</sub>. No carbonyl-dinitrogen complexes
are produced during CO–N<sub>2</sub> coadsorption. The role
of the ligand and the nature of the bond in the formation of geminal
and mixed-ligand complexes are discussed
Purification of Hydrogen from CO with Cu/ZSM-5 Adsorbents
The transition to a hydrogen economy requires the development of cost-effective methods for purifying hydrogen from CO. In this study, we explore the possibilities of Cu/ZSM-5 as an adsorbent for this purpose. Samples obtained by cation exchange from aqueous solution (AE) and solid-state exchange with CuCl (SE) were characterized by in situ EPR and FTIR, H2-TPR, CO-TPD, etc. The AE samples possess mainly isolated Cu2+ cations not adsorbing CO. Reduction generates Cu+ sites demonstrating different affinity to CO, with the strongest centres desorbing CO at about 350 °C. The SE samples have about twice higher Cu/Al ratios, as one H+ is exchanged with one Cu+ cation. Although some of the introduced Cu+ sites are oxidized to Cu2+ upon contact with air, they easily recover their original oxidation state after thermal treatment in vacuum or under inert gas stream. In addition, these Cu+ centres regenerate at relatively low temperatures. It is important that water does not block the CO adsorption sites because of the formation of Cu+(CO)(H2O)x complexes. Dynamic adsorption studies show that Cu/ZSM-5 selectively adsorbs CO in the presence of hydrogen. The results indicate that the SE samples are very perspective materials for purification of H2 from CO
Low-Temperature Adsorption of H<sub>2</sub> and D<sub>2</sub> on Dehydrated and Water Precovered CPO-27-Ni
Metal–organic frameworks (MOFs)
possessing open metal sites
(e.g., from the CPO-27 series) are a promising class of materials
for hydrogen storage. However, there is still no consensus on the
vibrational signatures of H<sub>2</sub> adsorbed on different sites.
In this work we report results of a combined Fourier transform infrared
(FTIR) spectroscopy and density functional theory (DFT) study on H<sub>2</sub> adsorption on dehydrated and D<sub>2</sub>O-precovered CPO-27-Ni.
For unambiguous interpretation of the results adsorption of CO was
also studied. Low-temperature CO adsorption on dehydrated CPO-27-Ni
results in formation of Ni<sup>2+</sup>–CO adducts stabilized
by π-back-donation and characterized by a CO stretching frequency
at 2182 cm<sup>–1</sup> (low coverage). With D<sub>2</sub>O-precovered
a sample CO replaces part of the preadsorbed D<sub>2</sub>O molecules,
and in this case the ν(CO) is significantly lowered (2172 cm<sup>–1</sup>). When H<sub>2</sub> is adsorbed at 100 K on dehydrated
sample, complexes involving Ni<sup>2+</sup> sites are formed and characterized
by a ν(H–H) band at 4031 cm<sup>–1</sup>. A satellite
band (Q<sub>trans</sub> mode) is detected at 4249 cm<sup>–1</sup>. Similar results were obtained after D<sub>2</sub> adsorption. However,
D<sub>2</sub> was more strongly adsorbed than H<sub>2</sub> and the
Q<sub>trans</sub> mode was of lower relative intensity. Only at high
H<sub>2</sub>/D<sub>2</sub> equilibrium pressures (≥50 mbar)
occupation of secondary sites was clearly detected by a ν(H–H)
band at 4118 cm<sup>–1</sup> or ν(D–D) band at
2964 cm<sup>–1</sup>. No significant differences in the strength
of adsorption of H<sub>2</sub> and D<sub>2</sub> were detected in
this case, suggesting the mode of adsorption is different from that
realized for the complexes involving Ni<sup>2+</sup> sites. Progressive
filling of the Ni<sup>2+</sup> sites by D<sub>2</sub>O leads to a
strong decrease in intensity of the H<sub>2</sub>/D<sub>2</sub> bands
associated with Ni<sup>2+</sup> sites and red shift of their frequencies
indicating a decrease of the interaction strength. On the contrary,
the bands due to H<sub>2</sub>/D<sub>2</sub> interaction with secondary
sites appear with enhanced intensities and are blue-shifted, which
suggests an increase of the interaction strength. These results were
confirmed by DFT calculations showing an increase of the H<sub>2</sub> adsorption enthalpy on secondary sites (identified as framework
oxygen atoms) in the presence of water due to attractive interaction
of H<sub>2</sub> with the nearby water molecule. Spectral evidence
of direct interaction of adsorbed H<sub>2</sub>/D<sub>2</sub> with
adsorbed water was also found. Our results allow confirming that H<sub>2</sub> adsorbed on open Ni<sup>2+</sup> sites is characterized by
a stretching frequency lower than 4100 cm<sup>–1</sup> and
some proposed values of M<sup><i>n</i>+</sup>–H<sub>2</sub> adducts above 4100 cm<sup>–1</sup> are in fact due
to H<sub>2</sub> interacting with secondary sites affected by H<sub>2</sub>O located in the vicinity