α-alchilazione di aldeidi, via organocatalisi: un approccio sintetico e computazionale

During this internship, the α-alkylation of branched aldehydes was taken into consideration. An enantiopure Betti’s base derivative was used as catalyst, applying a new concept in catalysis: organocatalysis. The Betti’s base may be of particular interest for organic chemists working in the field of “reactions catalysed by enantiopure small organic molecules”, in particular for the ones interested in enantiopure primary amines. The potential of secondary amines as catalysts has certainly been known for years. It is indeed more innovative to conduct reactions using primary amine derivatives as catalyst. In this work, the efficacy of the primary amine was checked first. Then, the focus was set on finding optimal reaction conditions. Finally, to have a more complete picture of the structure of the compounds used in the project, experimental and computational IR spectra were compared, after the method was validated. Durante il periodo di tirocinio è stata presa in esame la reazione di α-alchilazione di aldeidi branched, utilizzando un derivato dell’ammina di Betti come catalizzatore enantiopuro ed applicando un nuovo tipo di catalisi: l’organocatalisi. Questi composti possono essere di particolare interesse per lavori in chimica organica, nel campo delle reazioni catalizzate da “piccole” molecole organiche, in particolare da ammine primarie a chiralità definita; la potenzialità delle ammine secondarie chirali come catalizzatori è certamente nota da anni, ma innovativo è condurre il tutto con l’impiego di un derivato amminico primario. Altri aspetti significativi sono gli apparenti e innumerevoli vantaggi, dal punto di vista economico ed ambientale, oltre che operativo e sintetico, derivanti dal nuovo tipo di catalisi. In un primo momento è stata verificata l’efficacia dell’ammina primaria sintetizzata nella reazione in progetto, quindi sono state individuate le condizioni di reazione ottimali. Infine, per un’analisi più completa di alcune molecole organiche e dopo un’opportuna validazione del metodo utilizzato, sono stati ottenuti a livello computazionale gli spettri IR delle molecole di sintesi prodotto e catalizzatore.

Design and optimization of turbo-expanders for organic rankine cycles

In a world focused on the need to produce energy for a growing population, while reducing atmospheric emissions of carbon dioxide, organic Rankine cycles represent a solution to fulfil this goal. This study focuses on the design and optimization of axial-flow turbines for organic Rankine cycles. From the turbine designer point of view, most of this fluids exhibit some peculiar characteristics, such as small enthalpy drop, low speed of sound, large expansion ratio. A computational model for the prediction of axial-flow turbine performance is developed and validated against experimental data. The model allows to calculate turbine performance within a range of accuracy of ±3%. The design procedure is coupled with an optimization process, performed using a genetic algorithm where the turbine total-to-static efficiency represents the objective function. The computational model is integrated in a wider analysis of thermodynamic cycle units, by providing the turbine optimal design. First, the calculation routine is applied in the context of the Draugen offshore platform, where three heat recovery systems are compared. The turbine performance is investigated for three competing bottoming cycles: organic Rankine cycle (operating cyclopentane), steam Rankine cycle and air bottoming cycle. Findings indicate the air turbine as the most efficient solution (total-to-static efficiency = 0.89), while the cyclopentane turbine results as the most flexible and compact technology (2.45 ton/MW and 0.63 m3/MW). Furthermore, the study shows that, for organic and steam Rankine cycles, the optimal design configurations for the expanders do not coincide with those of the thermodynamic cycles. This suggests the possibility to obtain a more accurate analysis by including the computational model in the simulations of the thermodynamic cycles. Afterwards, the performance analysis is carried out by comparing three organic fluids: cyclopentane, MDM and R245fa. Results suggest MDM as the most effective fluid from the turbine performance viewpoint (total-to-total efficiency = 0.89). On the other hand, cyclopentane guarantees a greater net power output of the organic Rankine cycle (P = 5.35 MW), while R245fa represents the most compact solution (1.63 ton/MW and 0.20 m3/MW). Finally, the influence of the composition of an isopentane/isobutane mixture on both the thermodynamic cycle performance and the expander isentropic efficiency is investigated. Findings show how the mixture composition affects the turbine efficiency and so the cycle performance. Moreover, the analysis demonstrates that the use of binary mixtures leads to an enhancement of the thermodynamic cycle performance.

Design of an indirectly fired gas turbine integrated with an organic rankine cycle unit for combined heat and power production

In the last years, the European countries have paid increasing attention to renewable sources and greenhouse emissions. The Council of the European Union and the European Parliament have established ambitious targets for the next years. In this scenario, biomass plays a prominent role since its life cycle produces a zero net carbon dioxide emission. Additionally, biomass can ensure plant operation continuity thanks to its availability and storage ability. Several conventional systems running on biomass are available at the moment. Most of them are performant either in the large-scale or in the small power range. The absence of an efficient system on the small-middle scale inspired this thesis project. The object is an innovative plant based on a wet indirectly fired gas turbine (WIFGT) integrated with an organic Rankine cycle (ORC) unit for combined heat and power production. The WIFGT is a performant system in the small-middle power range; the ORC cycle is capable of giving value to low-temperature heat sources. Their integration is investigated in this thesis with the aim of carrying out a preliminary design of the components. The targeted plant output is around 200 kW in order not to need a wide cultivation area and to avoid biomass shipping. Existing in-house simulation tools are used: They are adapted to this purpose. Firstly the WIFGT + ORC model is built; Zero-dimensional models of heat exchangers, compressor, turbines, furnace, dryer and pump are used. Different fluids are selected but toluene and benzene turn out to be the most suitable. In the indirectly fired gas turbine a pressure ratio around 4 leads to the highest efficiency. From the thermodynamic analysis the system shows an electric efficiency of 38%, outdoing other conventional plants in the same power range. The combined plant is designed to recover thermal energy: Water is used as coolant in the condenser. It is heated from 60°C up to 90°C, ensuring the possibility of space heating. Mono-dimensional models are used to design the heat exchange equipment. Different types of heat exchangers are chosen depending on the working temperature. A finned-plate heat exchanger is selected for the WIFGT heat transfer equipment due to the high temperature, oxidizing and corrosive environment. A once-through boiler with finned tubes is chosen to vaporize the organic fluid in the ORC. A plate heat exchanger is chosen for the condenser and recuperator. A quasi-monodimensional model for single-stage axial turbine is implemented to design both the WIFGT and the ORC turbine. The system simulation after the components design shows an electric efficiency around 34% with a decrease by 10% compared to the zero-dimensional analysis. The work exhibits the system potentiality compared to the existing plants from both technical and economic point of view.