Transformations de l'isopropanol sur solides aluminiques : une approche mixte expérimentale / modélisation multi-échelle

The upgrading of lignocellulosic biomass into strategic molecules for the chemical industry requires the adaptation of refining procedures to the transformation of oxygenated species. In this context, the dehydration of alcohols has seen renewed interest over the last decade. The work presented here aims at unravelling the reactivity of a model alcohol (isopropanol) over aluminic catalysts at the molecular scale. To this purpose, a study combining experiments and modelling at the molecular scale (DFT) and at the reactor scale (kinetic modelling) has been set up. By combining infrared spectroscopic experiments, kinetic measurements and molecular modelling of the adsorption and reaction pathways of isopropanol on gamma alumina, it is shown that this reactivity is mainly governed by the (100) facets of alumina. The competing formation of propene (major product) and diisopropylether (minor product) involves a common alcoolate intermediate adsorbed on a Lewis acidic aluminium atom, either by direct elimination of a water molecule (E2 mechanism) or by condensation with a second alcohol molecule adsorbed in vicinity (SN2 mechanism).A micro-kinetic model involving this single reaction site and including the transformation of the ether into isopropanol and propene allows reproducing the experimental results, provided that the effect of co-adsorbed water and alcohol molecules in the environment of the active site is taken into account, as the formation of water – intermediate dimers and the stabilization of the second alcohol molecule both contribute to an adjustment of the ether/propene ratio.La valorisation de la biomasse lignocellulosique en molécules plateforme pour l'industrie chimique rend nécessaire l'adaptation des méthodes de raffinage à la transformation de composés organiques oxygénés. La déshydratation des alcools connaît dans ce contexte un fort regain d'intérêt. Les travaux de cette thèse s'attachent à comprendre à l'échelle moléculaire la réactivité d'un alcool modèle (isopropanol) sur catalyseurs aluminiques, au travers d'une étude mettant en jeu expériences et modélisation aux échelles moléculaire (DFT) et du réacteur (modélisation cinétique). En combinant expériences de spectroscopie infrarouge, mesures cinétiques et modélisation moléculaire appliquée à l'adsorption et aux chemins réactionnels de l'isopropanol sur l'alumine gamma, il est montré que la réactivité de cet alcool est principalement gouvernée par la facette (100) de l'alumine. Les formations compétitives de propène, majoritaire, et de diisopropyléther, minoritaire, impliquent un même intermédiaire alcoolate, adsorbé sur un atome d'aluminium acide de Lewis, qui évolue soit par élimination directe d'une molécule d'eau (mécanisme E2), soit par condensation avec une seconde molécule d'alcool adsorbée à proximité (mécanisme SN2). Un modèle microcinétique fondé sur ce site unique de réaction, incluant de surcroît la décomposition de l'éther en isopropanol et en propène, permet de reproduire les résultats expérimentaux à condition de prendre en compte l'effet de molécules d'eau et d'alcool co-adsorbées dans l'environnement du site actif, la formation de dimères eau - intermédiaire et la stabilisation de la seconde molécule d'alcool contribuant à l'ajustement du rapport éther/propène

Conversion of isopropanol on aluminic materials : a mixed experimental and multi-scale modeling approach

La valorisation de la biomasse lignocellulosique en molécules plateforme pour l'industrie chimique rend nécessaire l'adaptation des méthodes de raffinage à la transformation de composés organiques oxygénés. La déshydratation des alcools connaît dans ce contexte un fort regain d'intérêt. Les travaux de cette thèse s'attachent à comprendre à l'échelle moléculaire la réactivité d'un alcool modèle (isopropanol) sur catalyseurs aluminiques, au travers d'une étude mettant en jeu expériences et modélisation aux échelles moléculaire (DFT) et du réacteur (modélisation cinétique). En combinant expériences de spectroscopie infrarouge, mesures cinétiques et modélisation moléculaire appliquée à l'adsorption et aux chemins réactionnels de l'isopropanol sur l'alumine gamma, il est montré que la réactivité de cet alcool est principalement gouvernée par la facette (100) de l'alumine. Les formations compétitives de propène, majoritaire, et de diisopropyléther, minoritaire, impliquent un même intermédiaire alcoolate, adsorbé sur un atome d'aluminium acide de Lewis, qui évolue soit par élimination directe d'une molécule d'eau (mécanisme E2), soit par condensation avec une seconde molécule d'alcool adsorbée à proximité (mécanisme SN2). Un modèle microcinétique fondé sur ce site unique de réaction, incluant de surcroît la décomposition de l'éther en isopropanol et en propène, permet de reproduire les résultats expérimentaux à condition de prendre en compte l'effet de molécules d'eau et d'alcool co-adsorbées dans l'environnement du site actif, la formation de dimères eau - intermédiaire et la stabilisation de la seconde molécule d'alcool contribuant à l'ajustement du rapport éther/propène.The upgrading of lignocellulosic biomass into strategic molecules for the chemical industry requires the adaptation of refining procedures to the transformation of oxygenated species. In this context, the dehydration of alcohols has seen renewed interest over the last decade. The work presented here aims at unravelling the reactivity of a model alcohol (isopropanol) over aluminic catalysts at the molecular scale. To this purpose, a study combining experiments and modelling at the molecular scale (DFT) and at the reactor scale (kinetic modelling) has been set up. By combining infrared spectroscopic experiments, kinetic measurements and molecular modelling of the adsorption and reaction pathways of isopropanol on gamma alumina, it is shown that this reactivity is mainly governed by the (100) facets of alumina. The competing formation of propene (major product) and diisopropylether (minor product) involves a common alcoolate intermediate adsorbed on a Lewis acidic aluminium atom, either by direct elimination of a water molecule (E2 mechanism) or by condensation with a second alcohol molecule adsorbed in vicinity (SN2 mechanism).A micro-kinetic model involving this single reaction site and including the transformation of the ether into isopropanol and propene allows reproducing the experimental results, provided that the effect of co-adsorbed water and alcohol molecules in the environment of the active site is taken into account, as the formation of water – intermediate dimers and the stabilization of the second alcohol molecule both contribute to an adjustment of the ether/propene ratio

What Can We Learn from First Principles Multi-Scale Models in Catalysis? The Role of the Ni/Al 2 O 3 Interface in Water-Gas Shift and Dry Reforming as a Case Study

International audienceComputational first principles models based on density functional theory (DFT) have emerged as an important tool to address reaction mechanisms and active sites in metal nanoparticle catalysis. However, the common evaluation of potential energy surfaces for selected reaction steps contrasts with the complexity of reaction networks under operating conditions, where the interplay of adsorbate populations and competing routes at reaction conditions determine the most relevant states for catalyst activity and selectivity. Here, we discuss how the use of a multi-scale first principles approach combining DFT calculations at the atomistic level with kinetic models may be used to understand reactions catalyzed by metal nanoparticles. The potential of such an approach is illustrated for the case of Al 2 O 3-supported Ni nanoparticle catalysts in the water-gas shift and dry reforming reactions. In these systems, both Ni nanoparticle (metal) as well as metal/oxide interface sites are available and may play a role in catalysis, which depends not only on the energy for critical reaction steps, as captured by DFT, but also on the reaction temperature and adsorbate populations, as shown by microkinetic modelling and experiments

Origin of ligand-driven selectivity in alkyne semihydrogenation over silica-supported copper nanoparticles

ISSN:0021-9517ISSN:1090-269

CO2 hydrogenation on Cu-catalysts generated from ZnII single-sites: Enhanced CH3OH selectivity compared to Cu/ZnO/Al2O3

The hydrogenation of CO2 to CH3OH is mostly performed by a catalyst consisting mainly of copper and zinc (Cu/ZnO/Al2O3). Here, Cu-Zn based catalysts are generated using surface organometallic chemistry (SOMC) starting from a material consisting of isolated ZnII surface sites dispersed on SiO2 – ZnII@SiO2. Grafting of [Cu(OtBu)]4 on the surface silanols available on ZnII@SiO2 followed by reduction at 500 °C under H2 generates CuZnx alloy nanoparticles with remaining ZnII sites according to X-ray absorption spectroscopy (XAS). This Cu-Zn/SiO2 material displays high catalytic activity and methanol selectivity, in particular at higher conversion compared to benchmark Cu/ZnO/Al2O3 and most other catalysts. In situ XAS shows that CuZnx alloy is partially converted into Cu(0) and Zn(II) under reaction conditions, while ex situ solid state nuclear magnetic resonance and infrared spectroscopic studies only indicate the presence of methoxy species and no formate intermediates are detected, in contrast to most Cu-based catalysts. The absence of formate species is consistent with the higher methanol selectivity as recently found for the related Cu-Ga/SiO2.ISSN:0021-9517ISSN:1090-269

Metal(II) Formates (M = Fe, Co, Ni, and Cu) Stabilized by Tetramethylethylenediamine (tmeda): Convenient Molecular Precursors for the Synthesis of Supported Nanoparticles

ISSN:0018-019XISSN:1522-267

Zr(IV) surface sites determine CH3OH formation rate on Cu/ZrO2/SiO2 - CO2 hydrogenation catalysts

Cu/ZrO2/SiO2 are efficient catalysts for the selective hydrogenation of CO2 to CH3OH. In order to understand the role of ZrO2 in these mixed-oxides based catalysts, in situ X-ray absorption spectroscopy has been carried out on the Cu and Zr K-edge. Under reaction conditions, Cu remains metallic, while Zr is present in three types of coordination environment associated with 1) bulk ZrO2, 2) coordinatively saturated and 3) unsaturated Zr(IV) surface sites. The amount of coordinatively unsaturated Zr surface sites can be quantified by linear combination fit of reference X-Ray absorption near edge structure (XANES) spectra and its amount correlates with CH3OH formation rates, thus indicating the importance of Zr(IV) Lewis acid surface sites in driving the selectivity toward CH3OH. This finding is consistent with the proposed mechanism, where CO2 is hydrogenated at the interface between the Cu nanoparticles that split H2 and Zr(IV) surface sites that stabilizes reaction intermediates.ISSN:1872-206

Surface Sites in Cu-Nanoparticles: Chemical Reactivity or Microscopy?

Copper nanoparticles are widely used in catalysis and electrocatalysis, and the fundamental understanding of their activity requires reliable methods to assess the number of potentially reactive atoms exposed on the surface. Herein, we provide a molecular understanding of the difference observed in addressing surface site titration using prototypical methods: transmission electron micrscopy (TEM), H₂ chemisorption, and N₂O titration by a combination of experimental and theoretical study. We show in particular that microscopy does not allow assessing the amount of reactive surface sites, while H₂ and N₂O chemisorptions can, albeit with slightly different stoichiometries (1 O/2Cu_S and 1 H₂/2.2Cu_S), which can be rationalized by density functional theory calculations. High-resolution TEM shows that the origin of the observed difference between microscopy and titration methods is due to the strong metal support interaction experienced by small copper nanoparticles with the silica surface

Isolated Zr Surface Sites on Silica Promote Hydrogenation of CO2 to CH3OH in Supported Cu Catalysts

ISSN:0002-7863ISSN:1520-512