Kinetics and Mechanism of Formic Acid Decomposition in Aqueous Solution using Ruthenium Pre-catalysts with Hydrophilic Phosphine Ligands

Hydrogen holds the potential to be an alternative to replace fossil fuels in the future. The tremendous research effort dedicated to the issue of hydrogen storage has led to considerable advancements in the development of both adsorption materials and chemical storage. Still, for many of these systems the gap between current state of research and industrial application is considerable. When it comes to systems for the reversible storage of hydrogen, the HCOOH/CO2 cycle currently shows the most promises. Its physical-chemical properties make formic acid an ideal system for hydrogen storage. Herein, a series of homogeneous catalytic systems have been developed for hydrogen generation from formic acid in aqueous solution. These catalysts are formed from commercially available RuCl3 with a variety of water-soluble phosphine ligands. These ligands vary in the type, number and position of their hydrophilic substituents. Most of them allow the efficient decomposition of formic acid under mild conditions for a large number of catalytic cycles. Especially a new series of cationic phosphine ligands provide the catalytic systems with high activity. Due to the observed high initial reaction rate of many catalytic systems, mechanistic studies have also been undertaken with important intermediates and a catalytic cycle being proposed. Accordingly, the heterogeneous catalysts have also been developed based on the immobilization of homogeneous ruthenium complexes. The immobilized catalysts also afford hydrogen with high purity and allow easy catalyst separation, overcoming the previous limitations in the use of homogeneous catalysts, particularly for mobile/portable applications. The research undertaken in this thesis is presented in three main parts: (i) the development and optimization of homogeneous catalytic systems; (ii) the development and optimization of heterogeneous/immobilized catalytic systems; (iii) the mechanistic studies on the initial fast catalytic cycle of homogeneous catalysts.

Homogeneous catalytic decomposition of formic acid for high pressure hydrogen generation

Céline Fellay

The main obstacles in the widespread use of hydrogen as energetic alternative to fossil fuels are storage problems intrinsically linked to its extremely light and explosive nature. Since no ideal storage systems currently exist, reversible fixation of hydrogen is a very active field of research. Formic acid has previously been proposed as hydrogen storage material using heterogeneous catalysts to decompose it. These systems, however, lose activity over time and/or have low selectivity. Formic acid decomposition has been revisited during the course of this thesis in attempt to provide a catalytic system that efficiently and selectively decomposes formic acid into H2 and CO2. Accordingly, a homogeneous catalytic system to decompose formic acid in aqueous phase has been developed. The catalytically active species are formed in situ from [Ru(H2O)6]2+ or RuCl3, and sulfonated phosphine ligands. The decomposition takes place under mild conditions, over a large range of temperatures (25-170°C) and pressures (1-750 bar, at least). The robustness of the catalytic systems allows a very large number of catalytic runs to be performed without any deactivation, hence, continuous hydrogen production could be achieved. Mechanistic investigations allowed the characterisation of several intermediates and a catalytic cycle has been proposed. The selective catalytic process developed affords hydrogen essentially free of CO, at desired rates and pressures, overcoming previous limitations in the use of formic acid as a hydrogen storage material. The research undertaken in this thesis is presented in three parts: (i) development and optimisation of the catalytic system in batch mode, (ii) mechanistic investigations on the optimised catalysts, and (iii) development of a continuous hydrogen production system.

EPFL2008

Direct Carbon Dioxide Hydrogenation into Formic Acid in Acidic Media

Séverine Joëlle Moret

A major challenge in the face of increasing global energy demand is the development of alternative environmentally friendly and renewable energy resources. Hydrogen is an excellent energy carrier, but has drawbacks in storage density and is dangerous to handle. An alternative approach involves controlled release of hydrogen from suitable materials, and an excellent candidate for this is formic acid. Because hydrogen production from formic acid is more convenient in acidic aqueous solutions, development of direct carbon dioxide hydrogenation has to be carried out under the same acidic conditions that provides a direct reversible hydrogen storage system. As current sources of formic acid are derived from fossil fuels, emphasis must be placed on conversion of renewable carbon sources to this materials. This thesis examines the direct hydrogenation of carbon dioxide to formic acid using homogeneous catalysts. Importantly, this reaction was achieved in base and additive-free conditions. Direct formic acid synthesis, without any additives has several advantages, including simpler isolation of the product. In addition, formic acid can also be used as a feedstock chemical and thus contributing to decrease the released CO2 to the atmosphere and consequently to the possible reduction of the greenhouse effect. A homogeneous catalytic system based on a [RuCl2(PTA)4] pre-catalyst active for carbon dioxide hydrogenation without the need for additives was developed. While unprecedented conversions were achieved in aqueous mixtures, a remarkable solvent effect was discovered for dimethyl sulfoxide. Furthermore, both catalytic systems are air stable and highly robust allowing for multiple recycling runs. Studies on the activity of the ruthenium pre-catalyst in the reverse reaction of hydrogen delivery in dimethyl sulfoxide have been undertaken and revealed promising results to achieve a CO2 neutral catalytic cycles. Mechanistic studies were carried out using NMR spectroscopy and provide valuable insights into the reasons for the high activities for the catalyst. After a general introduction on current hydrogen storage technologies, the research undertaken in this thesis will be presented in three main parts: (1) Optimization of the high pressure sapphire NMR techniques used for the study of systems under pressure; (2) Development of homogeneous ruthenium catalytic systems for the direct hydrogenation of carbon dioxide to formic acid; (3) Mechanistic studies on the direct carbon dioxide hydrogenation using the [RuCl2(PTA)4] pre-catalyst

EPFL2014

Carbon dioxide for hydrogen storage via formic acid derivatives and methanol

Katerina Stefania Sordakis

Securing our energy future while minimizing the associated environmental impacts is a challenging endeavor and the fundamental aspect of sustainable development. The choice of energy resource and the reduction of greenhouse gas emissions, primarily carbon dioxide (CO2), are key parameters in this process. Hydrogen gas (H2) is an energy carrier with the potential of "green" production and utilization, in addition to having attractive inherent fuel properties. However, complications during its storage arise from its intrinsically light nature. Chemical H2 fixation within liquid formic acid (FA) and its derivatives is therefore a promising approach. In the present dissertation, reversible H2 storage cycles based on homogeneous FA/formate dehydrogenation and CO2/bicarbonate hydrogenation, as well as the related CO2 transformation to methanol are investigated. The first chapter provides an overview of challenges underlying energy sustainability, prospects for integration of H2 with our energy infrastructure, the employment of FA as a liquid organic hydrogen carrier and state of the art homogeneous catalysts for selective FA dehydrogenation and CO2 hydrogenation. The combination of these reactions to form a closed CO2 loop is the basic concept behind a reversible H2 storage system as it is envisaged by our group. In the second chapter, FA dehydrogenation/formation in the presence of triethylamine is discussed. The results are summarized as equilibrium positions within this couple, which can be controlled by adjustment of the operating pressure and temperature. The basic additive promotes H2 fixation but also allows for on-demand H2 release from a triethylammonium formate substrate. The third chapter addresses H2 storage in basic media, i.e. aqueous bicarbonate hydrogenation, with a Ru(III) catalyst precursor and a number of water-soluble phosphine ligands. The latter are introduced to tailor the exhibited activity by affecting the steric and electronic parameters of the catalyst. All phosphines provide high bicarbonate conversions, albeit with low reaction rates. Chapter four summarizes the optimization and mechanistic studies of the reversible formate dehydrogenation reaction, in the presence of a Ru(II)-mTPPTS catalyst. Cesium is chosen as the cation for the formate/bicarbonate salts because it leads to their high solubility in the aqueous solvent and therefore an increase in the hydrogen storage capacity. The involved equilibria are determined and a reaction mechanism for the formate dehydrogenation step is proposed, based on NMR studies. Advantages of the presented approach include the utilization of water as the solvent, the absence of CO2 throughout the reactions and the successful in situ recycling of the environmentally benign hydrogen carrier. In Chapter five the feasibility of producing both FA and methanol directly from CO2, at room temperature, in a "one-pot" reaction using aqueous solvent is demonstrated. Formic acid formation occurs in water without additives or organic solvents with a homogeneous iridium catalyst. Formic acid also undergoes disproportionation into methanol, with the same complex. Under optimized conditions, FA conversions of 98% and methanol selectivities of 96% are achieved in the disproportionation reaction. These reactions are relevant to the field of sustainable H2 storage, but might also provide an alternative approach to the commercial fossil-fuel-dependent production of formic acid and methanol.