Membrane-based separation processes are acquiring, in the last years, an increasing importance because of their intrinsic energetic and environmental sustainability: some types of polymeric materials, showing adequate perm-selectivity features, appear rather suitable for these applications, because of their relatively low cost and easy processability. In this work have been studied two different types of polymeric membranes, in view of possible applications to the gas separation processes, i.e. Mixed Matrix Membranes (MMMs) and high free volume glassy polymers. Since the early 90’s, it has been understood that the performances of polymeric materials in the field of gas separations show an upper bound in terms of permeability and selectivity: in particular, an increase of permeability is often accompanied by a decrease of selectivity and vice-versa, while several inorganic materials, like zeolites or silica derivates, can overcome this limitation. As a consequence, it has been developed the idea of dispersing inorganic particles in polymeric matrices, in order to obtain membranes with improved perm-selectivity features. In particular, dispersing fumed silica nanoparticles in high free volume glassy polymers improves in all the cases gases and vapours permeability, while the selectivity may either increase or decrease, depending upon material and gas mixture: that effect is due to the capacity of nanoparticles to disrupt the local chain packing, increasing the dimensions of excess free volume elements trapped in the polymer matrix. In this work different kinds of MMMs were fabricated using amorphous Teflon® AF or PTMSP and fumed silica: in all the cases, a considerable increase of solubility, diffusivity and permeability of gases and vapours (n-alkanes, CO2, methanol) was observed, while the selectivity shows a non-monotonous trend with filler fraction. Moreover, the classical models for composites are not able to capture the increase of transport properties due to the silica addition, so it has been necessary to develop and validate an appropriate thermodynamic model that allows to predict correctly the mass transport features of MMMs. In this work, another material, called poly-trimethylsilyl-norbornene (PTMSN) was examined: it is a new generation high free volume glassy polymer that, like PTMSP, shows unusual high permeability and selectivity levels to the more condensable vapours. These two polymer differ each other because PTMSN shows a more pronounced chemical stability, due to its structure double-bond free. For this polymer, a set of Lattice Fluid parameters was estimated, making possible a comparison between experimental and theoretical solubility isotherms for hydrocarbons and alcoholic vapours: the successfully modelling task, based on application of NELF model, offers a reliable alternative to direct sorption measurement, which is extremely time-consuming due to the relevant relaxation phenomena showed by each sorption step. For this material also dilation experiments were performed, in order to quantify its dimensional stability in presence of large size, swelling vapours.

Questa tesi affronta lo studio di una tipologia di vibrazione autoeccitata, nota come chatter, che si manifesta nei processi di lavorazione ad asportazione di truciolo ed in particolare nelle lavorazioni di fresatura. La tesi discute inoltre lo sviluppo di una tecnica di monitoraggio e diagnostica del chatter basato sul rilievo di vibrazioni. Il fenomeno del chatter è caratterizzato da violente oscillazioni tra utensile e pezzo in lavorazione ed elevate emissioni acustiche. Il chatter, se non controllato, causa uno scadimento qualitativo della finitura superficiale e delle tolleranze dimensionali del lavorato, una riduzione della vita degli utensili e dei componenti della macchina. Questa vibrazione affligge negativamente la produttività e la qualità del processo di lavorazione e pregiudica l’interazione uomo-macchina-ambiente. Per una data combinazione di macchina, utensile e pezzo lavorato, i fattori che controllano la velocità di asportazione del materiale sono gli stessi che controllano l’insorgenza del chatter: la velocità di rotazione del mandrino, la profondità assiale di passata e la velocità di avanzamento dell’utensile. Per studiare il fenomeno di chatter, con l’obbiettivo di individuare possibili soluzioni per limitarne o controllarne l’insorgenza, vengono proposti in questa tesi alcuni modelli del processo di fresatura. Tali modelli comprendono il modello viscoelastico della macchina fresatrice e il modello delle azioni di taglio. Per le azioni di taglio è stato utilizzato un modello presente in letteratura, mentre per la macchina fresatrice sono stati utilizzato modelli a parametri concentrati e modelli modali analitico-sperimentali. Questi ultimi sono stati ottenuti accoppiando un modello modale sperimentale del telaio, completo di mandrino, della macchina fresatrice con un modello analitico, basato sulla teoria delle travi, dell’utensile. Le equazioni del moto, associate al processo di fresatura, risultano essere equazioni differenziali con ritardo a coefficienti periodici o PDDE (Periodic Delay Diefferential Equations). È stata implementata una procedura numerica per mappare, nello spazio dei parametri di taglio, la stabilità e le caratteristiche spettrali (frequenze caratteristiche della vibrazione di chatter) delle equazioni del moto associate ai modelli del processo di fresatura proposti. Per testare i modelli e le procedure numeriche proposte, una macchina fresatrice CNC 4 assi, di proprietà del Dipartimento di Ingegneria delle Costruzioni Meccaniche Nucleari e Metallurgiche (DIEM) dell’Università di Bologna, è stata strumentata con accelerometri, con una tavola dinamometrica per la misura delle forze di taglio e con un adeguato sistema di acquisizione. Eseguendo varie prove di lavorazione sono stati identificati i coefficienti di pressione di taglio contenuti nel modello delle forze di taglio. Sono stati condotti, a macchina ferma, rilievi di FRFs (Funzioni Risposta in Frequenza) per identificare, tramite tecniche di analisi modale sperimentale, i modelli del solo telaio e della macchina fresatrice completa di utensile. I segnali acquisiti durante le numerose prove di lavorazione eseguite, al variare dei parametri di taglio, sono stati analizzati per valutare la stabilità di ciascun punto di lavoro e le caratteristiche spettrali della vibrazione associata. Questi risultati sono stati confrontati con quelli ottenuti applicando la procedura numerica proposta ai diversi modelli di macchina fresatrice implementati. Sono state individuate le criticità della procedura di modellazione delle macchine fresatrici a parametri concentrati, proposta in letteratura, che portano a previsioni erronee sulla stabilità delle lavorazioni. È stato mostrato come tali criticità vengano solo in parte superate con l’utilizzo dei modelli modali analitico-sperimentali proposti. Sulla base dei risultati ottenuti, è stato proposto un sistema automatico, basato su misure accelerometriche, per diagnosticare, in tempo reale, l’insorgenza del chatter durante una lavorazione. È stato realizzato un prototipo di tale sistema di diagnostica il cui funzionamento è stato provato mediante prove di lavorazione eseguite su due diverse macchine fresatrici CNC.

In such territories where food production is mostly scattered in several small / medium size or even domestic farms, a lot of heterogeneous residues are produced yearly, since farmers usually carry out different activities in their properties. The amount and composition of farm residues, therefore, widely change during year, according to the single production process periodically achieved. Coupling high efficiency micro-cogeneration energy units with easy handling biomass conversion equipments, suitable to treat different materials, would provide many important advantages to the farmers and to the community as well, so that the increase in feedstock flexibility of gasification units is nowadays seen as a further paramount step towards their wide spreading in rural areas and as a real necessity for their utilization at small scale. Two main research topics were thought to be of main concern at this purpose, and they were therefore discussed in this work: the investigation of fuels properties impact on gasification process development and the technical feasibility of small scale gasification units integration with cogeneration systems. According to these two main aspects, the present work was thus divided in two main parts. The first one is focused on the biomass gasification process, that was investigated in its theoretical aspects and then analytically modelled in order to simulate thermo-chemical conversion of different biomass fuels, such as wood (park waste wood and softwood), wheat straw, sewage sludge and refuse derived fuels. The main idea is to correlate the results of reactor design procedures with the physical properties of biomasses and the corresponding working conditions of gasifiers (temperature profile, above all), in order to point out the main differences which prevent the use of the same conversion unit for different materials. At this scope, a gasification kinetic free model was initially developed in Excel sheets, considering different values of air to biomass ratio and the downdraft gasification technology as particular examined application. The differences in syngas production and working conditions (process temperatures, above all) among the considered fuels were tried to be connected to some biomass properties, such elementary composition, ash and water contents. The novelty of this analytical approach was the use of kinetic constants ratio in order to determine oxygen distribution among the different oxidation reactions (regarding volatile matter only) while equilibrium of water gas shift reaction was considered in gasification zone, by which the energy and mass balances involved in the process algorithm were linked together, as well. Moreover, the main advantage of this analytical tool is the easiness by which the input data corresponding to the particular biomass materials can be inserted into the model, so that a rapid evaluation on their own thermo-chemical conversion properties is possible to be obtained, mainly based on their chemical composition A good conformity of the model results with the other literature and experimental data was detected for almost all the considered materials (except for refuse derived fuels, because of their unfitting chemical composition with the model assumptions). Successively, a dimensioning procedure for open core downdraft gasifiers was set up, by the analysis on the fundamental thermo-physical and thermo-chemical mechanisms which are supposed to regulate the main solid conversion steps involved in the gasification process. Gasification units were schematically subdivided in four reaction zones, respectively corresponding to biomass heating, solids drying, pyrolysis and char gasification processes, and the time required for the full development of each of these steps was correlated to the kinetics rates (for pyrolysis and char gasification processes only) and to the heat and mass transfer phenomena from gas to solid phase. On the basis of this analysis and according to the kinetic free model results and biomass physical properties (particles size, above all) it was achieved that for all the considered materials char gasification step is kinetically limited and therefore temperature is the main working parameter controlling this step. Solids drying is mainly regulated by heat transfer from bulk gas to the inner layers of particles and the corresponding time especially depends on particle size. Biomass heating is almost totally achieved by the radiative heat transfer from the hot walls of reactor to the bed of material. For pyrolysis, instead, working temperature, particles size and the same nature of biomass (through its own pyrolysis heat) have all comparable weights on the process development, so that the corresponding time can be differently depending on one of these factors according to the particular fuel is gasified and the particular conditions are established inside the gasifier. The same analysis also led to the estimation of reaction zone volumes for each biomass fuel, so as a comparison among the dimensions of the differently fed gasification units was finally accomplished. Each biomass material showed a different volumes distribution, so that any dimensioned gasification unit does not seem to be suitable for more than one biomass species. Nevertheless, since reactors diameters were found out quite similar for all the examined materials, it could be envisaged to design a single units for all of them by adopting the largest diameter and by combining together the maximum heights of each reaction zone, as they were calculated for the different biomasses. A total height of gasifier as around 2400mm would be obtained in this case. Besides, by arranging air injecting nozzles at different levels along the reactor, gasification zone could be properly set up according to the particular material is in turn gasified. Finally, since gasification and pyrolysis times were found to considerably change according to even short temperature variations, it could be also envisaged to regulate air feeding rate for each gasified material (which process temperatures depend on), so as the available reactor volumes would be suitable for the complete development of solid conversion in each case, without even changing fluid dynamics behaviour of the unit as well as air/biomass ratio in noticeable measure. The second part of this work dealt with the gas cleaning systems to be adopted downstream the gasifiers in order to run high efficiency CHP units (i.e. internal engines and micro-turbines). Especially in the case multi–fuel gasifiers are assumed to be used, weightier gas cleaning lines need to be envisaged in order to reach the standard gas quality degree required to fuel cogeneration units. Indeed, as the more heterogeneous feed to the gasification unit, several contaminant species can simultaneously be present in the exit gas stream and, as a consequence, suitable gas cleaning systems have to be designed. In this work, an overall study on gas cleaning lines assessment is carried out. Differently from the other research efforts carried out in the same field, the main scope is to define general arrangements for gas cleaning lines suitable to remove several contaminants from the gas stream, independently on the feedstock material and the energy plant size The gas contaminant species taken into account in this analysis were: particulate, tars, sulphur (in H2S form), alkali metals, nitrogen (in NH3 form) and acid gases (in HCl form). For each of these species, alternative cleaning devices were designed according to three different plant sizes, respectively corresponding with 8Nm3/h, 125Nm3/h and 350Nm3/h gas flows. Their performances were examined on the basis of their optimal working conditions (efficiency, temperature and pressure drops, above all) and their own consumption of energy and materials. Successively, the designed units were combined together in different overall gas cleaning line arrangements, paths, by following some technical constraints which were mainly determined from the same performance analysis on the cleaning units and from the presumable synergic effects by contaminants on the right working of some of them (filters clogging, catalysts deactivation, etc.). One of the main issues to be stated in paths design accomplishment was the tars removal from the gas stream, preventing filters plugging and/or line pipes clogging At this scope, a catalytic tars cracking unit was envisaged as the only solution to be adopted, and, therefore, a catalytic material which is able to work at relatively low temperatures was chosen. Nevertheless, a rapid drop in tars cracking efficiency was also estimated for this same material, so that an high frequency of catalysts regeneration and a consequent relevant air consumption for this operation were calculated in all of the cases. Other difficulties had to be overcome in the abatement of alkali metals, which condense at temperatures lower than tars, but they also need to be removed in the first sections of gas cleaning line in order to avoid corrosion of materials. In this case a dry scrubber technology was envisaged, by using the same fine particles filter units and by choosing for them corrosion resistant materials, like ceramic ones. Besides these two solutions which seem to be unavoidable in gas cleaning line design, high temperature gas cleaning lines were not possible to be achieved for the two larger plant sizes, as well. Indeed, as the use of temperature control devices was precluded in the adopted design procedure, ammonia partial oxidation units (as the only considered methods for the abatement of ammonia at high temperature) were not suitable for the large scale units, because of the high increase of reactors temperature by the exothermic reactions involved in the process. In spite of these limitations, yet, overall arrangements for each considered plant size were finally designed, so that the possibility to clean the gas up to the required standard degree was technically demonstrated, even in the case several contaminants are simultaneously present in the gas stream. Moreover, all the possible paths defined for the different plant sizes were compared each others on the basis of some defined operational parameters, among which total pressure drops, total energy losses, number of units and secondary materials consumption. On the basis of this analysis, dry gas cleaning methods proved preferable to the ones including water scrubber technology in al of the cases, especially because of the high water consumption provided by water scrubber units in ammonia adsorption process. This result is yet connected to the possibility to use activated carbon units for ammonia removal and Nahcolite adsorber for chloride acid. The very high efficiency of this latter material is also remarkable. Finally, as an estimation of the overall energy loss pertaining the gas cleaning process, the total enthalpy losses estimated for the three plant sizes were compared with the respective gas streams energy contents, these latter obtained on the basis of low heating value of gas only. This overall study on gas cleaning systems is thus proposed as an analytical tool by which different gas cleaning line configurations can be evaluated, according to the particular practical application they are adopted for and the size of cogeneration unit they are connected to.

The research activity described in this thesis is focused mainly on the study of finite-element techniques applied to thermo-fluid dynamic problems of plant components and on the study of dynamic simulation techniques applied to integrated building design in order to enhance the energy performance of the building. The first part of this doctorate thesis is a broad dissertation on second law analysis of thermodynamic processes with the purpose of including the issue of the energy efficiency of buildings within a wider cultural context which is usually not considered by professionals in the energy sector. In particular, the first chapter includes, a rigorous scheme for the deduction of the expressions for molar exergy and molar flow exergy of pure chemical fuels. The study shows that molar exergy and molar flow exergy coincide when the temperature and pressure of the fuel are equal to those of the environment in which the combustion reaction takes place. A simple method to determine the Gibbs free energy for non-standard values of the temperature and pressure of the environment is then clarified. For hydrogen, carbon dioxide, and several hydrocarbons, the dependence of the molar exergy on the temperature and relative humidity of the environment is reported, together with an evaluation of molar exergy and molar flow exergy when the temperature and pressure of the fuel are different from those of the environment. As an application of second law analysis, a comparison of the thermodynamic efficiency of a condensing boiler and of a heat pump is also reported. The second chapter presents a study of borehole heat exchangers, that is, a polyethylene piping network buried in the soil which allows a ground-coupled heat pump to exchange heat with the ground. After a brief overview of low-enthalpy geothermal plants, an apparatus designed and assembled by the author to carry out thermal response tests is presented. Data obtained by means of in situ thermal response tests are reported and evaluated by means of a finite-element simulation method, implemented through the software package COMSOL Multyphysics. The simulation method allows the determination of the precise value of the effective thermal properties of the ground and of the grout, which are essential for the design of borehole heat exchangers. In addition to the study of a single plant component, namely the borehole heat exchanger, in the third chapter is presented a thorough process for the plant design of a zero carbon building complex. The plant is composed of: 1) a ground-coupled heat pump system for space heating and cooling, with electricity supplied by photovoltaic solar collectors; 2) air dehumidifiers; 3) thermal solar collectors to match 70% of domestic hot water energy use, and a wood pellet boiler for the remaining domestic hot water energy use and for exceptional winter peaks. This chapter includes the design methodology adopted: 1) dynamic simulation of the building complex with the software package TRNSYS for evaluating the energy requirements of the building complex; 2) ground-coupled heat pumps modelled by means of TRNSYS; and 3) evaluation of the total length of the borehole heat exchanger by an iterative method developed by the author. An economic feasibility and an exergy analysis of the proposed plant, compared with two other plants, are reported. The exergy analysis was performed by considering the embodied energy of the components of each plant and the exergy loss during the functioning of the plants.

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L’attività della tesi riguarda le protesi mioelettriche, gli arti protesici maggiormente diffusi, le quali sono descrivibili come arti robotici in cui i segmenti artificiali sono attuati da giunti elettromeccanici alimentati da batterie ricaricabili ed attivati mediante segnali elettromiografici (segnali elettrici generati dalla contrazione dei muscoli). Tali protesi di arto superiore attualmente disponibili in commercio potrebbero essere inadeguate per una riabilitazione soddisfacente di alcuni pazienti con una amputazione di alto livello che richiedono una elevata funzionalità nella vita quotidiana. In questo contesto si inserisce l’attività di ricerca del Centro Protesi INAIL di Budrio di Vigorso, Bologna, e dell’Università di Bologna i quali stanno sviluppando nuovi arti protesici con il progetto a lungo termine di rendere disponibili svariate soluzioni di protesi di arto superiore in grado di soddisfare la maggior parte delle richieste degli amputati. Lo scopo di questa tesi è l’introduzione di un nuovo rotatore omerale attivo da integrare alla protesi di arto superiore disponibile presso i nostri laboratori. Per ottenere questo risultato è stata utilizzata una procedura di progettazione già consolidata in attività precedenti per lo sviluppo di una protesi di spalla a due gradi di libertà. Differenti modelli cinematici sono stati studiati tramite analisi cinematiche per determinare l’incremento delle prestazioni a seguito dell’introduzione del nuovo rotatore omerale attivo. Sono state inoltre condotte analisi cinetostatiche per definire le specifiche tecniche di riferimento (in termini di carichi agenti sul rotatore omerale) e per guidare il dimensionamento della catena di trasmissione di potenza del nuovo dispositivo protesico. Ulteriori specifiche tecniche sono state considerate per garantire l’irreversibilità spontanea del moto sotto carichi esterni (quando i giunti attivi della protesi non sono alimentati), per salvaguardare l’incolumità del paziente in caso di caduta, per misurare la posizione angolare del rotatore omerale (in modo da implementare strategie di controllo in retroazione) e per limitare i consumi e la rumorosità del dispositivo. Uno studio di fattibilità ha permesso la selezione della architettura ottimale della catena di trasmissione di potenza per il nuovo rotatore omerale. I criteri di scelta sono stati principalmente la limitazione del peso e dell’ingombro del nuovo dispositivo protesico. Si è quindi proceduto con la progettazione di dettaglio alla quale è seguita la costruzione di un prototipo del nuovo rotatore omerale presso i nostri laboratori. La tesi tratta infine una attività preliminare di sperimentazione che ha permesso di fare considerazioni sulle prestazioni del prototipo ed osservazioni importanti per le successive attività di revisione ed ottimizzazione del progetto del rotatore omerale.

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Il presente lavoro di tesi riguarda la sintesi di nanopolveri allumina-zirconia, seguendo tre differenti metodologie (sintesi per coprecipitazione, sintesi con il metodo dei citrati, sintesi idrotermale assistita da microonde) e il trattamento termico (calcinazione) delle polveri ottenute, mediante tecniche di riscaldamento convenzionali ed alternative (microonde). Lo scopo del lavoro è consistito nell’individuare, tra le tecniche esaminate, quella più idonea e conveniente, per la preparazione di nanopolveri cristalline 95 mol% Al2O3 – 5 mol% ZrO2 e nell’esaminare gli effetti che la calcinazione condotta con le microonde, ha sulle caratteristiche finali delle polveri, rispetto ai trattamenti termici convenzionali. I risultati ottenuti al termine del lavoro hanno evidenziato che, tra le tecniche di sintesi esaminate, la sintesi idrotermale assistita da microonde, risulta il metodo più indicato e che, il trattamento termico eseguito con le microonde, risulta di gran lunga vantaggioso rispetto a quello convenzionale. La sintesi idrotermale assistita da microonde consente di ottenere polveri nano cristalline poco agglomerate, che possono essere facilmente disaggregate e con caratteristiche microstrutturali del tutto peculiari. L’utilizzo di tale tecnica permette, già dopo la sintesi a 200°C/2ore, di avere ossido di zirconio, mentre per ottenere gli ossidi di alluminio, è sufficiente un ulteriore trattamento termico a basse temperature e di breve durata (400°C/ 5 min). Si è osservato, inoltre, che il trattamento termico condotto con le microonde comporta la formazione delle fasi cristalline desiderate (ossidi di alluminio e zirconio), impiegando (come per la sintesi) tempi e temperature significativamente ridotti. L’esposizione delle polveri per tempi ridotti e a temperature più basse consente di evitare la formazione di aggregati duri nelle nanopolveri finali e di contrastare il manifestarsi di fenomeni di accrescimento di grani, preservando così la “nanostruttura” delle polveri e le sue caratteristiche proprietà. / This thesis reports the synthesis of alumina-zirconia nanopowders, by means of three different routes (cooprecipitation, citrate route, microwave hydrothermal synthesis), followed by thermal treatment (calcination), performed by using conventional (muffle furnace) and alternative method (microwaves furnace). The aim of this work is to identify, over the experimented routes, the most convenient and suitable one, for the production of 95 mol% Al2O3 – 5 mol% ZrO2 nanocrystalline powders and to examine the effects, on powder features, of the microwave thermal treatment respect to conventional heating. The obtained results have shown that, among the tested routes, microwave hydrothermal synthesis is the most advantageous method, and that microwave hydrothermal heating is favourable respect to conventional treatment in the calcination step. It has been demonstrated that microwave hydrothermal synthesis allows to obtain nanocrystalline powders with unique characteristics, that can be easily grinded because of the absence of hard agglomerates. The so obtained powders are composed, since after the synthesis stage (200°C/2 hrs), of zirconium oxide and the crystallization of aluminium oxides was reached by using low temperature and short time (400°C/5 min) of calcination. Furthermore, the thermal treatment, performed by using microwave source, allows the formation of the desired crystalline phases at significant lower temperature and with reduced processing time (as observed for the synthesis) respect to conventional thermal treatment. The possibility to undergo, for the calcination steps, the powders to lower temperature and reduced time avoid the formation of hard aggregates and contrast grain coarsening, preserving the nanostructure of the powders and their innovative properties.