Fine chemicals are highly pure substances that are commercially produced by chemical reactions for highly specialized applications. In most cases, however, these reactions involve stoichiometric and highly polluting steps. A possible solution is the development of processes using enzymatic, homogeneous or heterogeneous catalysts. In this review, selected examples of clean heterogeneously-catalyzed reactions applied to the synthesis of fine chemicals are reported for the purpose of highlighting the growing need for more sustainable industrial processes, i.e., processes that produce minimal waste and avoid as much as possible the use of toxic and/or hazardous reagents and solvents. A thorough knowledge of catalyst properties, reaction conditions and interactions with the reacting substrate are essential for optimizing the synthesis, thus making it possible to move on from laboratory to industrial production.

The combined steam/dry reforming (S/DR) technology was used to produce syngas from clean biogas. In the reaction conditions proposed, the catalytic bed can produce, without deactivation, a syngas with a H₂/CO ratio of ≈2 directly processable for methanol or Fischer–Tropsch syntheses. Starting from the laboratory data obtained in the industrial conditions, mass and energy balances for the overall process were obtained from Aspen HYSYS simulations. The environmental evaluation was performed by applying the life cycle assessment (LCA) methodology, comparing different scenarios to the current industrial route to produce syngas (autothermal reforming or ATR of natural gas). The analysis showed that clean biogas-to-syngas technology using reforming processes has the potential to reduce the anthropogenic impact on the environment. The ReCiPe method showed that when the combined S/DR process is conducted using clean biogas also as a heat source, the CO₂ balance turns negative, ensuring that the whole process has excellent potential as carbon capture and utilization (CCU) technology providing the lowest damage in all categories. Its improvement would make it possible to further reduce the environmental burden of the overall process, which is essential for achieving sustainable development.

Over the past decade, a great deal of effort has been devoted to developing reductive processes in the field of biomass valorisation for the sustainable production of bio-fuel additives and chemicals. Catalytic transfer hydrogenation, which uses alcohol as the hydrogen source, is an interesting approach that avoids the use of both high H₂ pressure and precious metal catalysts. In this work, the vapour-phase production of 2-methylfuran from biomass-derived furfural (FU), using methanol as the H-transfer agent and FeVO₄ catalyst, was studied. At a temperature of 320 °C it was possible to achieve 80% yield of 2-methylfuran, with small amounts of 2,5-dimethylfuran and 2-vinylfuran as by-products. Catalyst characterization highlighted that FeVO₄ reduction took place under the studied conditions, leading to the in situ development of a true active phase. The study of the reaction network permitted us to infer on the relative contribution of H-transfer and hydrogenation, the latter from the in situ generated formaldehyde and H₂, to 2-methylfuran, formation. The reported results indicate the potential application of H-transfer with FeVO₄ catalysts as an efficient process for the selective de-oxygenation of biomass-derived molecules.