The work of this thesis has been focused on the characterization of metallic membranes for the hydrogen purification from steam reforming process and also of perfluorosulphonic acid ionomeric (PFSI) membranes suitable as electrolytes in fuel cell applications. The experimental study of metallic membranes was divided in three sections: synthesis of palladium and silver palladium coatings on porous ceramic support via electroless deposition (ELD), solubility and diffusivity analysis of hydrogen in palladium based alloys (temperature range between 200 and 400 °C up to 12 bar of pressure) and permeation experiments of pure hydrogen and mixtures containing, besides hydrogen, also nitrogen and methane at high temperatures (up to 600 °C) and pressures (up to 10 bar). Sequential deposition of palladium and silver on to porous alumina tubes by ELD technique was carried out using two different procedures: a stirred batch and a continuous flux method. Pure palladium as well as Pd-Ag membranes were produced: the Pd-Ag membranes’ composition is calculated to be close to 77% Pd and 23% Ag by weight which was the target value that correspond to the best performance of the palladium-based alloys. One of the membranes produced showed an infinite selectivity through hydrogen and relatively high permeability value and is suitable for the potential use as a hydrogen separator. The hydrogen sorption in silver palladium alloys was carried out in a gravimetric system on films produced by ELD technique. In the temperature range inspected, up to 400°C, there is still a lack in literature. The experimental data were analyzed with rigorous equations allowing to calculate the enthalpy and entropy values of the Sieverts’ constant; the results were in very good agreement with the extrapolation made with literature data obtained a lower temperature (up to 150 °C). The information obtained in this study would be directly usable in the modeling of hydrogen permeation in Pd-based systems. Pure and mixed gas permeation tests were performed on Pd-based hydrogen selective membranes at operative conditions close to steam-reforming ones. Two membranes (one produced in this work and another produced by NGK Insulators Japan) showed a virtually infinite selectivity and good permeability. Mixture data revealed the existence of non negligible resistances to hydrogen transport in the gas phase. Even if the decrease of the driving force due to polarization concentration phenomena occurs, in principle, in all membrane-based separation systems endowed with high perm-selectivity, an extensive experimental analysis lack, at the moment, in the palladium-based membrane process in literature. Moreover a new procedure has been introduced for the proper comparison of the mass transport resistance in the gas phase and in the membrane. Another object of study was the water vapor sorption and permeation in PFSI membranes with short and long side chains was also studied; moreover the permeation of gases (i.e. He, N2 and O2) in dry and humid conditions was considered. The water vapor sorption showed strong interactions between the hydrophilic groups and the water as revealed from the hysteresis in the sorption-desorption isotherms and thermo gravimetric analysis. The data obtained were used in the modeling of water vapor permeation, that was described as diffusion-reaction of water molecules, and in the humid gases permeation experiments. In the dry gas experiments the permeability and diffusivity was found to increase with temperature and with the equivalent weight (EW) of the membrane. A linear correlation was drawn between the dry gas permeability and the opposite of the equivalent weight of PFSI membranes, based on which the permeability of pure PTFE is retrieved in the limit of high EW. In the other hand O2 ,N2 and He permeability values was found to increase significantly, and in a similar fashion, with water activity. A model that considers the PFSI membrane as a composite matrix with a hydrophilic and a hydrophobic phase was considered allowing to estimate the variation of gas permeability with relative humidity on the basis of the permeability in the dry PFSI membrane and in pure liquid water.

Chromatography represents one of the most important and widely used unit operation in the biotechnology industry. However this technique suffers from several limitations such as high pressure drop, slow mass transfer through the diffusive pores and strong dependence of the binding capacity on flow rate. In this work, affinity membranes with improved capacity have been considered as an alternative technology for the capturing step in antibody manufacturing. Several affinity membranes have been prepared starting from various membrane supports. Different affinity ligands have been utilized like Protein A, the natural ligand of choice for antibodies, as well as synthetic ligands that exhibit affinity for the Fc portion of antibodies. The membranes have been characterized in detail: binding and elution performance was evaluated in adsorption experiments using pure IgG solutions, while membrane selectivity was evaluated using complex solutions like a cell culture supernatant. The most promising affinity membranes were extensively tested in dynamic experiments. The effects of operating parameters like feed concentration and flow rate on separation performances like binding capacity, selectivity and process yield have been studied in detail in order to find the optimal conditions for binding and elution steps. The membranes have been used over several complete chromatographic cycles to evaluate the effects of ageing and of membrane regeneration on dynamic binding capacity. A novel mathematical model is proposed that can describe all the chromatographic steps involved in the membrane affinity chromatography process for protein purification. The mathematical description is based on the species continuity equation coupled with a proper binding kinetic equation, and suitable to describe adequately the dispersion phenomena occurring both in the micro-porous membranes as well as in the extra-column devices used in the system. The model considers specifically all the different chromatographic steps, namely adsorption, washing and elution. The few relevant fitting parameters of the model were derived from a calibration with the experimental affinity cycles performed with pure IgG solutions, then the model is used to describe experimental data obtained in chromatographic cycles carried out with complex feeds as the cell culture supernatant. Simulations reveal a good agreement with experimental data in all the chromatography steps, both in the case of pure IgG solutions and for the cell culture supernatant considered.

Polymer blends constitute a valuable way to produce relatively low cost new materials. A still open question concerns the miscibility of polyethylene blends. Deviations from the log-additivity rule of the newtonian viscosity are often taken as a signature of immiscibility of the two components. The aim of this thesis is to characterize the rheological behavior in shear and elongation of five series of LLDPE/LDPE blends whose parent polymers have been chosen with different viscosity and SCB content and length. Synergistic effects have been measured for both zero shear viscosity and melt strength. Both SCB length and viscosity ratio between the components have been found to be key parameters for the miscibility of the pure polymers. In particular the miscibility increases with increasing SCB length and with decreasing the LDPE molecular weight and viscosity. This rheological behavior has significant effects on the processability window of these blends when the uni or biaxial elongational flows are involved. The film blowing is one of the processes for which the synergistic effects above mentioned can be crucial. Small scale experiments of film blowing performed for one of the series of blends has demonstrated that the positive deviation of the melt strength enlarges the processability window. In particular, the bubble stability was found to improve or disappear when the melt strength of the samples increased. The blending of LDPE and LLDPE can even reduce undesired melt flow instability phenomena widening, as a consequence, the processability window in extrusion. One of the series of blends has been characterized by means of capillary rheometry in order to allow a careful morphological analysis of the surface of the extruded polymer jets by means of Scanning Electron Microscopy (SEM) with the aim to detect the very early stages of the small scale melt instabilty at low shear rates (sharksin) and to follow its subsequent evolution as long as the shear rate was increased. With this experimental procedure it was possible to evaluate the shear rate ranges corresponding to different flow regions: smooth extrudate surface (absence of instability), sharkskin (small scale instability produced at the capillary exit), stick-slip transition (instability involving the whole capillary wall) and gross melt fracture (i.e. a large scale "upstream" instability originating from the entrance region of the capillary). A quantitative map was finally worked out using which an assessment of the flow type for a given shear rate and blend composition can be predicted.

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.

This work presents the results of theoretical and experimental characterization of thermodynamic, mechanical and transport properties in polymer solvent systems. The polymer solvent pairs considered ranged to those in which the polymer is rubbery, to those in which the initially glassy polymeric matrix is plasticized by the action of the low molecular weight species. Advanced Equation of State models have been adopted for thermodynamic modeling,along with a rigorous procedure that enables to extend their applicability to the non equilibrium, glassy region. Mass sorption kinetics had been modeled with phenomenological models and with advanced kinetic models. / Questo lavoro verte sulla caratterizzazione teorica e sperimentale delle proprietà termodinamiche, meccaniche e di trasporto di sistemi polimero-solvente. In particolare sono stati presi in considerazione sia sistemi polimero-solvente in cui la matrice polimerica si trova allo stato di gomma, che sistemi in cui la matrice polimerica esibisce comportamento vetroso, nonché sistemi nei quali si verifica la transizione vetrosa indotta dall'effetto plasticizzante del solvente. La modellazione termodinamica è stata effettuata utilizzando equazioni di stato avanzate e metodi idonei ad estenderne il campo di utilizzo alla condizione di non equilibrio, propria dello stato vetroso. Cinetiche di assorbimento non Fickiane sono state modellate utilizzando approcci fenomenologici e modelli cinetici avanzati.

Chromatography is the most widely used technique for high-resolution separation and analysis of proteins. This technique is very useful for the purification of delicate compounds, e.g. pharmaceuticals, because it is usually performed at milder conditions than separation processes typically used by chemical industry. This thesis focuses on affinity chromatography. Chromatographic processes are traditionally performed using columns packed with porous resin. However, these supports have several limitations, including the dependence on intra-particle diffusion, a slow mass transfer mechanism, for the transport of solute molecules to the binding sites within the pores and high pressure drop through the packed bed. These limitations can be overcome by using chromatographic supports like membranes or monoliths. Dye-ligands are considered important alternatives to natural ligands. Several reactive dyes, particularly Cibacron Blue F3GA, are used as affinity ligand for protein purification. Cibacron Blue F3GA is a triazine dye that interacts specifically and reversibly with albumin. The aim of this study is to prepare dye-affinity membranes and monoliths for efficient removal of albumin and to compare the three different affinity supports: membranes and monoliths and a commercial column HiTrapTM Blue HP, produced by GE Healthcare. A comparison among the three supports was performed in terms of binding capacity at saturation (DBC100%) and dynamic binding capacity at 10% breakthrough (DBC10%) using solutions of pure BSA. The results obtained show that the CB-RC membranes and CB-Epoxy monoliths can be compared to commercial support, column HiTrapTM Blue HP, for the separation of albumin. These results encourage a further characterization of the new supports examined.

Alcune patologie dell’occhio come la retinopatia diabetica, il pucker maculare, il distacco della retina possono essere curate con un intervento di vitrectomia. I rischi associati all’intervento potrebbero essere superati ricorrendo alla vitrectomia enzimatica con plasmina in associazione o in sostituzione della vitrectomia convenzionale. Inoltre, l’uso di plasmina autologa eviterebbe problemi di rigetto. La plasmina si ottiene attivando il plasminogeno con enzimi quali l’attivatore tissutale (tPA) e l’urochinasi ( uPA ) . La purificazione del plasminogeno dal sangue avviene normalmente attraverso cromatografia di affinità con resina. Tuttavia, le membrane di affinità costituiscono un supporto ideale per questa applicazione poiché possono essere facilmente impaccate prima dell’intervento, permettendo la realizzazione di un dispositivo monouso che fornisce un processo rapido ed economico. Obiettivo di questo lavoro è la preparazione di membrane di affinità per la purificazione del plasminogeno utilizzando L-lisina come ligando di affinità. Per questo scopo sono state usate membrane in cellulosa rigenerata ad attivazione epossidica, modificate con due diversi protocolli per l’immobilizzazione di L-lisina. La densità ligando è stata misurata mediante un saggio colorimetrico che usa l’acido arancio 7 come indicatore. La resa di immobilizzazione è stata studiata in funzione del tempo di reazione e della concentrazione di L-lisina. Le membrane ottimizzate sono state caratterizzate con esperimenti dinamici usando siero bovino e umano, i risultati sono stati confrontati con quelli ottenuti in esperimenti paralleli condotti con una resina commerciale di affinità con L-lisina. Durante gli esperimenti con siero, le frazioni provenienti da ogni fase cromatografica sono state raccolte e analizzate con HPLC ed elettroforesi SDS-PAGE. In particolare, l’elettroforesi dei campioni eluiti presenta una banda del plasminogeno ben definita indicando che le membrane di affinità con L-lisina sono adatte alla purificazione del plasminogeno. Inoltre, è emerso che le membrane hanno maggiore produttività della resina commerciale di riferimento. / Some eye conditions like diabetic rethinopaty, macular pukers, retinal detachment may benefit from vitreoctomy. Enzymatic vitreoctomy with plasmin is envisaged to augment or even replace conventional vitreoctomy by proposed means of less surgical risks. In addition, the use of autologous plasmin is beneficial since it avoids rejection problems. Plasmin can be obtained by conversion of plasminogen using a variety of enzymes, including tissue plasminogen activator (tPA) and urokinase plasminogen activator (uPA). The purification of plasminogen from blood is normally performed with bead-based affinity chromatography. However, for ophthalmology applications affinity membranes are ideally suited for the development of a disposable device to be used directly by the surgeon in the operating theatre, since they can be easily packed in small units providing a fast and economic process. Objective of this work was the preparation of affinity membranes for plasminogen purification using L-lysine as affinity ligand. To this aim epoxy activated regenerated cellulose membranes were used as a support for L-lysine immobilization. Two different binding protocols were tested and ligand density was measured using a colorimetric assay with Orange 7 as indicator. L-lysine immobilization yield has been studied as a function of reaction time and L-lysine concentration. The optimized membranes have been characterized in dynamic experiments using bovine and human serum; the results have been compared with the ones obtained in parallel experiments performed with a commercial L-lysine affinity resin used as a benchmark. During chromatographic experiments with serum, fractions have been collected and analyzed with both HPLC and SDS-PAGE electrophoresis. In particular, from SDS-PAGE gel electrophoresis a well-defined plasminogen band can be shown in the eluted samples indicating that the L-lysine affinity membranes are suitable for the purification of plasminogen. Furthermore, the membranes gave higher productivity than the commercial benchmark.

Polymeric membranes represent a promising technology for gas separation processes, thanks to low costs, reduced energy consumption and limited waste production. The present thesis aims at studying the transport properties of two membrane materials, suitable for CO2 purification applications. In the first part, a polyimide, Matrimid 5218, has been throughout investigated, with particular reference to the effect of thermal treatment, aging and the presence of water vapor in the gas transport process. Permeability measurements showed that thermal history affects relevantly the diffusion of gas molecules across the membrane, influencing also the stability of the separation performances. Subsequently, the effect of water on Matrimid transport properties has been characterized for a wide set of incondensable penetrants. A monotonous reduction of permeability took place at increasing the water concentration within the polymer matrix, affecting the investigated gaseous species to the same extent, despite the different thermodynamic and kinetic features. In this view, a novel empirical model, based on the Free Volume Theory, has been proposed to qualitatively describe the phenomenon. Moreover, according to the accurate representation of the experimental data, the suggested approach has been combined with a more rigorous thermodynamic tool (NELF Model), allowing an exhaustive description of water influence on the single parameters contributing to the gas permeation across the membrane. In the second part, the study has focused on the synthesis and characterization of facilitated transport membranes, able to achieving outstanding separation performances thanks to the chemical enhancement of CO2 permeability. In particular, the transport properties have been investigated for high pressure CO2 separation applications and specific solutions have been proposed to solve stability issues, frequently arising under such severe conditions. Finally, the effect of different process parameters have been investigated, aiming at the identification of the optimal conditions capable to maximize the separation performance.

Thesis (doctoral)--Technische Universität Berlin, 1982. / Includes bibliographical references (p. 647-671) and index.

Finding new ways to produce renewable energy is among the most important and strategic challenges of technology nowadays. Biomass is one of the ideal candidates for reliable and abundant renewable energy production, since it is largely available, universally distributed and potentially CO2 neutral, if utilized in a sustainable way. There are several processes for energy exploitation of biomass, including combustion, pyrolysis and gasification. However, traditional thermochemical technologies can be only effective with dry biomass, owing to energy considerations. As a consequence, wet biomass (e.g. municipal or agro-industrial wastes), which represents the greatest part of the overall biomass, cannot be converted into energy. This strong limitation can be overcome by a novel technology: supercritical water gasification (SCWG). SCWG is based on reacting biomass with water above its critical point (T > 374.1°C; P > 22.1 MPa). Thanks to the unique properties of supercritical water, high gaseous yields can be achieved, as well as reduced (or even null) tar and char production. Moreover, a H2-rich gas can be obtained. Therefore, high moisture content is not a drawback anymore, being water part of the process itself. In this thesis, SCWG is analyzed under different aspects. First of all, a comprehensive state of the art is traced. The work is then divided into two main sections: mathematical modeling and experimental activities. The first section reports three different modeling approaches for SCWG. In thermodynamic equilibrium modeling, a two-phase thermodynamic equilibrium model was built, enabling to predict products composition as a function of process parameters, as well as solids formation at equilibrium. Energy balances were also performed by means of such tool. The kinetics modeling approach was applied to methanol SCWG, developing an elementary reactions model able to highlight the main reaction pathways. Process modeling was then used to calculate the energy needs of a possible industrial SCWG process scheme, enabling to prove its energetic feasibility. The second part of the thesis deals with experimental tests, which were executed with both real biomass and model compounds. A first campaign was performed with glucose and glucose/phenol mixtures in small metallic batch autoclaves. The catalytic effect of the reactor material (stainless steel and Inconel 625) on the gasification products composition was discussed, as well as the influence of subcritical (350°C) and supercritical (400°C) reaction conditions. Moreover, the effect of phenol addiction, inhibiting glucose gasification, was observed. In a subsequent campaign, real biomass was gasified, including beech sawdust, municipal wastes, malt spent grains and hydrothermal char. The effect of the reactor material was studied, as well as the system behavior after long time runs (16 h) and the addiction of K2CO3 as a catalyst. Finally, glucose/phenol mixtures, with increasing phenol contents, were gasified in a continuous tubular reactor at 400°C and 25 MPa, between 10 and 240 s of residence time. Results showed that phenol is hardly gasified and that methanol is a key intermediate product.