Relative CO(2)/NH(3) selectivities of mammalian aquaporins 0-9

Previous work showed that aquaporin 1 (AQP1), AQP4-M23, and AQP5 each has a characteristic CO(2)/NH(3) and CO(2)/H(2)O permeability ratio. The goal of the present study is to characterize AQPs 0-9, which traffic to the plasma membrane when heterologously expressed in Xenopus oocytes. We use video microscopy to compute osmotic water permeability (P(f)) and microelectrodes to record transient changes in surface pH (ΔpH(S)) caused by CO(2) or NH(3) influx. Subtracting respective values for day-matched, H(2)O-injected control oocytes yields the channel-specific values P(f)* and ΔpH(S)*. We find that P(f)* is significantly >0 for all AQPs tested except AQP6. (ΔpH(S)*)(CO(2)) is significantly >0 for AQP0, AQP1, AQP4-M23, AQP5, AQP6, and AQP9. (ΔpH(S)*)(NH(3)) is >0 for AQP1, AQP3, AQP6, AQP7, AQP8, and AQP9. The ratio (ΔpH(S)*)(CO(2))/P(f)* falls in the sequence AQP6 (∞) > AQP5 > AQP4-M23 > AQP0 ≅ AQP1 ≅ AQP9 > others (0). The ratio (ΔpH(S)*)(NH(3))/P(f)* falls in the sequence AQP6 (∞) > AQP3 ≅ AQP7 ≅ AQP8 ≅ AQP9 > AQP1 > others (0). Finally, the ratio (ΔpH(S)*)(CO(2))/(-ΔpH(S)*)(NH(3)) falls in the sequence AQP0 (∞) ≅ AQP4-M23 ≅ AQP5 > AQP6 > AQP1 > AQP9 > AQP3 (0) ≅ AQP7 ≅ AQP8. The ratio (ΔpH(S)*)(CO(2))/(-ΔpH(S)*)(NH(3)) is indeterminate for both AQP2 and AQP4-M1. In summary, we find that mammalian AQPs exhibit a diverse range of selectivities for CO(2) vs. NH(3) vs. H(2)O. As a consequence, by expressing specific combinations of AQPs, cells could exert considerable control over the movements of each of these three substances

Efecto del aporte de nutrientes sobre la producción de macroalgas en condiciones de co-cultivo : crecimiento, biofiltración y características fisiológicas

Máster Oficial en Cultivos Marinos. Trabajo presentado como requisito parcial para la obtención del Título de Máster Oficial en Cultivos Marinos, otorgado por la Universidad de Las Palmas de Gran Canaria (ULPGC), el Instituto Canario de Ciencias Marinas (ICCM), y el Centro Internacional de Altos Estudios Agronómicos Mediterráneos de Zaragoza (CIHEAM)

Sviluppo di nuovi catalizzatori per la reazione di water gas shift a media temperatura

L’idrogeno è un elemento di elevato interesse economico, con una produzione industriale che supera i 55 x 1010 m3/anno e notevoli prospettive di sviluppo delle sue applicazioni. Attualmente l’idrogeno è prodotto principalmente in impianti di larga scala (circa 1000 m3/h) da combustibili fossili attraverso processi di steam reforming ed ossidazione parziale catalitica. Per aumentare la produzione di idrogeno un ruolo fondamentale è svolto dalla reazione di water gas shift (WGS) che abbatte il contenuto di CO, massimizzando la produzione di idrogeno. La reazione è condotta industrialmente in due stadi, operanti ad alta temperatura (HTS, circa 350 °C) e bassa temperatura (LTS, circa 250 °C), utilizzando rispettivamente catalizzatori a base di ferro o rame. Tuttavia, è evidente l’interesse per nuove formulazioni in grado di operare in un unico stadio a temperatura intermedia (MTS), mantenendo le caratteristiche ottimali di attività e stabilità. In questo lavoro di tesi, condotto in collaborazione con AIR LIQUIDE (F), è stato affrontato uno studio della reazione di WGS finalizzato allo sviluppo di nuove formulazioni attive e stabili nell’MTS. In particolare, sono stati sintetizzati precursori idrotalcitici Cu/Zn/Al (contenenti carbonati o silicati), con bassi contenuti di rame (diversamente da quanto riportato in letteratura), modulandone le proprietà chimico-fisiche, l’attività catalitica e la stabilità con il tempo di reazione. Si è osservato come i catalizzatori con minori contenuti di rame ed ottenuti da precursori contenenti carbonati mostrassero un’elevata attività e selettività nell’MTS, raggiungendo valori di conversione del CO analoghi a quelli all’equilibrio termodinamico già a 300 °C, indipendentemente dai valori del rapporto S/DG e del tempo di contatto. Tutti i catalizzatori mostrano un’elevata stabilità con il tempo di reazione, con incrementi del quantitativo del CO in uscita dopo 100h di circa lo 0,7 % v/v. I catalizzatori scaricati dopo le prove catalitiche evidenziano gli effetti dei processi di sinterizzazione (diminuzione dell’area superficiale ed incremento delle dimensioni dei cristalliti), la cui entità diminuisce al diminuire del contenuto di rame. Infine, confrontando l’attività dei migliori catalizzatori preparati in questo lavoro di tesi con quella di uno dei più utilizzati catalizzatori commerciali per la reazione di WGS a bassa temperatura, si sono osservati valori di attività analoghi, raggiungendo quelli di equilibrio per temperature  300°C, ma con una attività significativamente superiore nelle condizioni LTS, soprattutto considerando il valore del tempo di contatto inferiore a quelli comunemente utilizzati negli impianti industriali.

Genomic and transcriptional analysis of allergen genes in apple (Malus x domestica)

Apple consumption is highly recomended for a healthy diet and is the most important fruit produced in temperate climate regions. Unfortunately, it is also one of the fruit that most ofthen provoks allergy in atopic patients and the only treatment available up to date for these apple allergic patients is the avoidance. Apple allergy is due to the presence of four major classes of allergens: Mal d 1 (PR-10/Bet v 1-like proteins), Mal d 2 (Thaumatine-like proteins), Mal d 3 (Lipid transfer protein) and Mal d 4 (profilin). In this work new advances in the characterization of apple allergen gene families have been reached using a multidisciplinary approach. First of all, a genomic approach was used for the characterization of the allergen gene families of Mal d 1 (task of Chapter 1), Mal d 2 and Mal d 4 (task of Chapter 5). In particular, in Chapter 1 the study of two large contiguos blocks of DNA sequences containing the Mal d 1 gene cluster on LG16 allowed to acquire many new findings on number and orientation of genes in the cluster, their physical distances, their regulatory sequences and the presence of other genes or pseudogenes in this genomic region. Three new members were discovered co-localizing with the other Mal d 1 genes of LG16 suggesting that the complexity of the genetic base of allergenicity will increase with new advances. Many retrotranspon elements were also retrieved in this cluster. Due to the developement of molecular markers on the two sequences, the anchoring of the physical and the genetic map of the region has been successfully achieved. Moreover, in Chapter 5 the existence of other loci for the Thaumatine-like protein family in apple (Mal d 2.03 on LG4 and Mal d 2.02 on LG17) respect the one reported up to now was demonstred for the first time. Also one new locus for profilins (Mal d 4.04) was mapped on LG2, close to the Mal d 4.02 locus, suggesting a cluster organization for this gene family, as is well reported for Mal d 1 family. Secondly, a methodological approach was used to set up an highly specific tool to discriminate and quantify the expression of each Mal d 1 allergen gene (task of Chapter 2). In aprticular, a set of 20 Mal d 1 gene specific primer pairs for the quantitative Real time PCR technique was validated and optimized. As a first application, this tool was used on leaves and fruit tissues of the cultivar Florina in order to identify the Mal d 1 allergen genes that are expressed in different tissues. The differential expression retrieved in this study revealed a tissue-specificity for some Mal d 1 genes: 10/20 Mal d 1 genes were expressed in fruits and, indeed, probably more involved in the allergic reactions; while 17/20 Mal d 1 genes were expressed in leaves challenged with the fungus Venturia inaequalis and therefore probably interesting in the study of the plant defense mechanism. In Chapter 3 the specific expression levels of the 10 Mal d 1 isoallergen genes, found to be expressed in fruits, were studied for the first time in skin and flesh of apples of different genotypes. A complex gene expression profile was obtained due to the high gene-, tissue- and genotype-variability. Despite this, Mal d 1.06A and Mal d 1.07 expression patterns resulted particularly associated with the degree of allergenicity of the different cultivars. They were not the most expressed Mal d 1 genes in apple but here it was hypotized a relevant importance in the determination of allergenicity for both qualitative and quantitative aspects of the Mal d 1 gene expression levels. In Chapter 4 a clear modulation for all the 17 PR-10 genes tested in young leaves of Florina after challenging with the fungus V. inaequalis have been reported but with a peculiar expression profile for each gene. Interestingly, all the Mal d 1 genes resulted up-regulated except Mal d 1.10 that was down-regulated after the challenging with the fungus. The differences in direction, timing and magnitude of induction seem to confirm the hypothesis of a subfunctionalization inside the gene family despite an high sequencce and structure similarity. Moreover, a modulation of PR-10 genes was showed both in compatible (Gala-V. inaequalis) and incompatible (Florina-V. inaequalis) interactions contribute to validate the hypothesis of an indirect role for at least some of these proteins in the induced defense responses. Finally, a certain modulation of PR-10 transcripts retrieved also in leaves treated with water confirm their abilty to respond also to abiotic stress. To conclude, the genomic approach used here allowed to create a comprehensive inventory of all the genes of allergen families, especially in the case of extended gene families like Mal d 1. This knowledge can be considered a basal prerequisite for many further studies. On the other hand, the specific transcriptional approach make it possible to evaluate the Mal d 1 genes behavior on different samples and conditions and therefore, to speculate on their involvement on apple allergenicity process. Considering the double nature of Mal d 1 proteins, as apple allergens and as PR-10 proteins, the gene expression analysis upon the attack of the fungus created the base for unravel the Mal d 1 biological functions. In particular, the knowledge acquired in this work about the PR-10 genes putatively more involved in the specific Malus-V. inaequalis interaction will be helpful, in the future, to drive the apple breeding for hypo-allergenicity genotype without compromise the mechanism of response of the plants to stress conditions. For the future, the survey of the differences in allergenicity among cultivars has to be be thorough including other genotypes and allergic patients in the tests. After this, the allelic diversity analysis with the high and low allergenic cultivars on all the allergen genes, in particular on the ones with transcription levels correlated to allergencity, will provide the genetic background of the low ones. This step from genes to alleles will allow the develop of molecular markers for them that might be used to effectively addressed the apple breeding for hypo-allergenicity. Another important step forward for the study of apple allergens will be the use of a specific proteomic approach since apple allergy is a multifactor-determined disease and only an interdisciplinary and integrated approach can be effective for its prevention and treatment.

Sintesi di nanoparticelle polimeriche basate su acido(D,L-lattico-co-glicolico) per applicazioni in nanomedicina

Questo lavoro di tesi rientra nel progetto europeo SaveMe, al quale partecipa il gruppo di ricerca del dipartimento di chimica organica nel quale ho svolto l’attività di tirocinio. Obiettivo finale di tale progetto è la sintesi di nanoparticelle a base di PLGA (acido poli(D,L-lattico-co-glicolico)) superficialmente funzionalizzate con biomolecole, per l’impiego nel trattamento e nella diagnosi del cancro al pancreas. L’obiettivo da raggiungere nel primo anno di ricerca per il mio gruppo era la sintesi delle nanoparticelle centrali (core nanosystems). Nel presente lavoro sono quindi riportati i metodi di sintesi di polimeri derivati da PLGA e suoi copolimeri con PEG (polietilenglicole) aventi vari gruppi funzionali terminali: acidi idrossamici, amminici e acidi carbossilici. I polimeri sintetizzati sono stati caratterizzati tramite test colorimetrici qualitativi, 1H-NMR, 13C-NMR, spettrometria IR e TGA. Sono state sintetizzate nanoparticelle polimeriche (PNPs), con le tecniche Oil/Water (O/W) e nanoprecipitazione (NP), basate sui polimeri ottenuti, aventi quindi funzioni acide, idrossamiche ed amminiche sulla superficie. Su queste PNPs è stato effettuata una decorazione superficiale con nanoparticelle metalliche di maghemite (CAN-Maghemite). Le nanoparticelle polimeriche sono state caratterizzate tramite DLS e delle PNPs decorate sono state ottenute immagini TEM. Sono riportati inoltre i test di viabilità cellulare delle nanoparticelle ottenute.

New catalysts for the water gas shift reaction at middle-temperature

H2 demand is continuously increasing since its many relevant applications, for example, in the ammonia production, refinery processes or fuel cells. The Water Gas Shift (WGS) reaction (CO + H2O = CO2 + H2 DeltaH = -41.1 kJ.mol-1) is a step in the H2 production, reducing significantly the CO content and increasing the H2 one in the gas mixtures obtained from steam reforming. Industrially, the reaction is carried out in two stages with different temperature: the first stage operates at high temperature (350-450 °C) using Fe-based catalysts, while the second one is performed at lower temperature (190-250 °C) over Cu-based catalysts. However, recently, an increasing interest emerges to develop new catalytic formulations, operating in a single-stage at middle temperature (MTS), while maintaining optimum characteristics of activity and stability. These formulations may be obtained by improving activity and selectivity of Fe-based catalysts or increasing thermal stability of Cu-based catalysts. In the present work, Cu-based catalysts (Cu/ZnO/Al2O3) prepared starting from hydrotalcite-type precursors show good homogeneity and very interesting physical properties, which worsen by increasing the Cu content. Among the catalysts with different Cu contents, the catalyst with 20 wt.% of Cu represents the best compromise to obtain high catalytic activity and stability. On these bases, the catalytic performances seem to depend on both metallic Cu surface area and synergetic interactions between Cu and ZnO. The increase of the Al content enhances the homogeneity of the precursors, leading to a higher Cu dispersion and consequent better catalytic performances. The catalyst with 20 wt.% of Cu and a molar ratio M(II)/M(III) of 2 shows a high activity also at 250 °C and a good stability at middle temperature. Thus, it may be considered an optimum catalyst for the WGS reaction at middle temperature (about 300 °C). Finally, by replacing 50 % (as at. ratio) of Zn by Mg (which is not active in the WGS reaction), better physical properties were observed, although associate with poor catalytic performances. This result confirms the important role of ZnO on the catalytic performances, favoring synergetic interactions with metallic Cu.

Produzione di idrogeno mediante reforming ciclico dell'etanolo

This work deals with a study on the feasibility of a new process, aimed at the production of hydrogen from water and ethanol (a compound obtained starting from biomasses), with inherent separation of hydrogen from C-containing products. The strategy of the process includes a first step, during which a metal oxide is contacted with ethanol at high temperature; during this step, the metal oxide is reduced and the corresponding metallic form develops. During the second step, the reduced metal compound is contacted at high temperature with water, to produce molecular hydrogen and with formation of the original metal oxide. In overall, the combination of the two steps within the cycle process corresponds to ethanol reforming, where however COx and H2 are produced separately. Various mixed metal oxides were used as electrons and ionic oxygen carriers, all of them being characterized by the spinel (inverse) structure typical of Me ferrites: MeFe2O4 (Me=Co, Ni, Fe or Cu). The first step was investigated in depth; it was found that besides the generation of the expected CO, CO2 and H2O, the products of ethanol anaerobic oxidation, also a large amount of H2 and coke were produced. The latter is highly undesired, since it affects the second step, during which water is fed over the pre-reduced spinel at high temperature. The behavior of the different spinels was affected by the nature of the divalent metal cation; magnetite was the oxide showing the slower rate of reduction by ethanol, but on the other hand it was that one which could perform the entire cycle of the process more efficiently. Still the problem of coke formation remains the greater challenge to solve.

Co-simulazione e co-progetto non lineare/elettromagnetico di sistemi wireless non convenzionali

L’attività di ricerca contenuta in questa tesi si è concentrata nello sviluppo e nell’implementazione di tecniche per la co-simulazione e il co-progetto non lineare/elettromagnetico di sistemi wireless non convenzionali. Questo lavoro presenta un metodo rigoroso per considerare le interazioni tra due sistemi posti sia in condizioni di campo vicino che in condizioni di campo lontano. In sostanza, gli effetti del sistema trasmittente sono rappresentati da un generatore equivalente di Norton posto in parallelo all’antenna del sistema ricevente, calcolato per mezzo del teorema di reciprocità e del teorema di equivalenza. La correttezza del metodo è stata verificata per mezzo di simulazioni e misure, concordi tra loro. La stessa teoria, ampliata con l’introduzione degli effetti di scattering, è stata usata per valutare una condizione analoga, dove l’elemento trasmittente coincide con quello ricevente (DIE) contenuto all’interno di una struttura metallica (package). I risultati sono stati confrontati con i medesimi ottenibili tramite tecniche FEM e FDTD/FIT, che richiedono tempi di simulazione maggiori di un ordine di grandezza. Grazie ai metodi di co-simulazione non lineari/EM sopra esposti, è stato progettato e verificato un sistema di localizzazione e identificazione di oggetti taggati posti in ambiente indoor. Questo è stato ottenuto dotando il sistema di lettura, denominato RID (Remotely Identify and Detect), di funzioni di scansione angolare e della tecnica di RADAR mono-pulse. Il sistema sperimentale, creato con dispositivi low cost, opera a 2.5 GHz ed ha le dimensioni paragonabili ad un normale PDA. E’ stato sperimentata la capacità del RID di localizzare, in scenari indoor, oggetti statici e in movimento.

Sistemi catalitici per la reazione di water - gas shift a media temperatura

Negli ultimi anni l’interesse nei confronti dell’H2 è cresciuto notevolmente per l’aumento della richiesta energetica mondiale. Uno dei processi più importanti per la produzione di H2 utilizza la reazione di Water-Gas Shift (WGS) per il trattamento delle correnti in uscita dai processi di steam reforming o di ossidazione parziale catalitica. CO + H2O  CO2 + H2 ∆H0298 = -41,2 KJ/mol Sono quindi stati sviluppati sistemi catalitici attivi nella reazione di WGS a media temperatura (circa 300 °C). Partendo da sistemi catalitici a base di Cu/Zn/Al, ottenuti da precursori idrotalcitici e sviluppati in lavori di tesi precedenti, sono state effettuate modifiche nella composizione al fine di aumentarne l’attività e la stabilità. L’aggiunta di piccole quantità di Mg ha un effetto positivo sull’attività dei sistemi catalitici, con effetti più evidenti a 250 °C. Tuttavia, l’aumento del contenuto di Mg, sebbene migliori le proprietà fisiche del catalizzatore (area superficiale e dispersione del Cu) sia del campione calcinato che di quello scaricato dopo reazione, peggiora drasticamente l’attività catalitica. L’aggiunta di piccole quantità di Mg sembra portare alla stabilizzazione della specie attiva Cu+ e promuovere un meccanismo redox superficiale (Cu0 e Cu+). E’ possibile correlare la conversione del CO con il rapporto ZnO/Cu, confermando il ruolo nella reazione di WGS dell’interazione Cu0/ZnO libero. La sostituzione di Mg con Ba comporta un miglioramento delle prestazioni catalitiche, in particolare nelle condizioni MTS (300 °C), suggerendo una più facile dissociazione dell’acqua legata alla stabilizzazione degli ossidrili da parte dei siti basici. È però accompagnato da una diminuzione della stabilità nelle condizioni di reazione. L’aggiunta di piccole quantità di La, Ce o Zr (con un rapporto Al/R = 50 mol/mol) incrementa la stabilità termica, sia in termini di proprietà fisiche che di attività catalitica. A seguito dei cicli termici di invecchiamento accelerato, infatti, non si riscontrano importanti diminuzioni di attività catalitica, evidenziando un’elevata stabilità della fase attiva.

Continuous-Flow Magnetic Separation with Permanent Magnets for Water Treatment

More efficient water treatment technologies would decrease the water bodies’ pollution and the actual intake of water resource. The aim of this thesis is an in-depth analysis of the magnetic separation of pollutants from water by means of a continuous-flow magnetic filter subjected to a field gradient produced by permanent magnets. This technique has the potential to improve times and efficiencies of both urban wastewater treatment plants and drinking water treatment plants. It might also substitute industrial wastewater treatments. This technique combines a physico-chemical phase of adsorption and a magnetic phase of filtration, having the potential to bond magnetite with any conventional adsorbent powder. The removal of both Magnetic Activated Carbons (MACs) and zeolite-magnetite mix with the addition of a coagulant was investigated. Adsorption tests of different pollutants (surfactants, endocrine disruptors, Fe(III), Mn(II), Ca(II)) on these adsorbents were also performed achieving good results. The numerical results concerning the adsorbent removals well reproduced the experimental ones obtained from two different experimental setups. In real situations the treatable flow rates are up to 90 m3/h (2000 m3/d).

Studio del comportamento catalitico nella reazione di Water Gas Shift a media ed alta temperatura

Per massimizzare la quantità di H2 nel gas di sintesi ottenuto dal processo di Steam Reforming (SR) si utilizza la reazione di Water Gas Shift (WGS): CO + H2O ⇆ CO2 + H2 ∆H0298 = - 41,2 KJ/mol Sulla base di sistemi catalitici Cu/Zn/Al si è cercato di modificarne la composizione per ottenere catalizzatori attivi e stabili in un intervallo di temperatura tra 350-450 °C, (High Temperature Shift o HTS), al fine di sostituire i tradizionali sistemi a base di Fe/Cr, in relazione alle limitazioni ambientali all’utilizzo del Cr e per poter operare con valori inferiori del rapporto S/DG. Si sono inoltre studiate le caratteristiche dei catalizzatori e le condizioni di reazione che favoriscono la produzione di metilammine ed alcoli nel processo a temperature intermedie, tra 300-350 °C (Middle Temperature Shift o MTS), in relazione alla disattivazione che questi composti comportano nel processo di SR a seguito del riciclo della fase acquosa dal reattore di WGS.

A chemical-loop approach for the generation of hydrogen by means of ethanol reforming

The work investigates the feasibility of a new process aimed at the production of hydrogen with inherent separation of carbon oxides. The process consists in a cycle in which, in the first step, a mixed metal oxide is reduced by ethanol (obtained from biomasses). The reduced metal is then contacted with steam in order to split the water and sequestrating the oxygen into the looping material’s structure. The oxides used to run this thermochemical cycle, also called “steam-iron process” are mixed ferrites in the spinel structure MeFe2O4 (Me = Fe, Co, Ni or Cu). To understand the reactions involved in the anaerobic reforming of ethanol, diffuse reflectance spectroscopy (DRIFTS) was used, coupled with the mass analysis of the effluent, to study the surface composition of the ferrites during the adsorption of ethanol and its transformations during the temperature program. This study was paired with the tests on a laboratory scale plant and the characterization through various techniques such as XRD, Mössbauer spectroscopy, elemental analysis... on the materials as synthesized and at different reduction degrees In the first step it was found that besides the generation of the expected CO, CO2 and H2O, the products of ethanol anaerobic oxidation, also a large amount of H2 and coke were produced. The latter is highly undesired, since it affects the second step, during which water is fed over the pre-reduced spinel at high temperature. The behavior of the different spinels was affected by the nature of the divalent metal cation; magnetite was the oxide showing the slower rate of reduction by ethanol, but on the other hand it was that one which could perform the entire cycle of the process more efficiently. Still the problem of coke formation remains the greater challenge to solve.

Alpha, Omega end group functionalization of RAFT polymers based on pentafluorophenyl esters and methane thiosulfonates

While polymers with different functional groups along the backbone have intensively been investigated, there is still a challenge in orthogonal functionalization of the end groups. Such well-defined systems are interesting for the preparation of multiblock (co) polymers or polymer networks, for bio-conjugation or as model systems for examining the end group separation of isolated polymer chains. rnHere, Reversible Addition Fragmentation Chain Transfer (RAFT) polymerization was employed as method to investigate improved techniques for an a, w end group functionalization. RAFT produces polymers terminated in an R group and a dithioester-Z group, where R and Z stem from a suitable chain transfer agent (CTA). rnFor alpha end group functionalization, a CTA with an activated pentafluorophenyl (PFP) ester R group was designed and used for the polymerization of various methacrylate monomers, N-isopropylacrylamide and styrene yielding polymers with a PFP ester as a end group. This allowed the introduction of inert propyl amides, of light responsive diazo compounds, of the dyes NBD, Texas Red, or Oregon Green, of the hormone thyroxin and allowed the formation of multiblocks or peptide conjugates. rnFor w end group functionalization, problems of other techniques were overcome through an aminolysis of the dithioester in the presence of a functional methane thiosulfonate (MTS), yielding functional disulfides. These disulfides were stable under ambient conditions and could be cleaved on demand. Using MTS chemistry, terminal methyl disulfides (enabling self-assembly on planar gold surfaces and ligand substitution on gold and semiconductor nanoparticles), butynyl disulfide end groups (allowing the “clicking” of the polymers onto azide functionalized surfaces and the selective removal through reduction), the bio-target biotin, and the fluorescent dye Texas Red were introduced into polymers. rnThe alpha PFP amidation could be performed under mild conditions, without substantial loss of DTE. This way, a step-wise synthesis produced polymers with two functional end groups in very high yields. rnAs examples, polymers with an anchor group for both gold nanoparticles (AuNP) and CdSe / ZnS semi-conductor nanoparticles (QD) and with a fluorescent dye end group were synthesized. They allowed a NP decoration and enabled an energy transfer from QD to dye or from dye to AuNP. Water-soluble polymers were prepared with two different bio-target end groups, each capable of selectively recognizing and binding a certain protein. The immobilization of protein-polymer-protein layers on planar gold surfaces was monitored by surface plasmon resonance.Introducing two different fluorescent dye end groups enabled an energy transfer between the end groups of isolated polymer chains and created the possibility to monitor the behavior of single polymer chains during a chain collapse. rnThe versatility of the synthetic technique is very promising for applications beyond this work.

Surface patterning with colloidal monolayers

This thesis focuses on the controlled assembly of monodisperse polymer colloids into ordered two-dimensional arrangements. These assemblies, commonly referred to as colloidal monolayers, are subsequently used as masks for the generation of arrays of complex metal nanostructures on solid substrates.rnThe motivation of the research presented here is twofold. First, monolayer crystallization methods were developed to simplify the assembly of colloids and to produce more complex arrangements of colloids in a precise way. Second, various approaches to colloidal lithography are designed with the aim to include novel features or functions to arrays of metal nanostructures.rnThe air/water interface was exploited for the crystallization of colloidal monolayer architectures as it combines a two-dimensional confinement with a high lateral mobility of the colloids that is beneficial for the creation of high long range order. A direct assembly of colloids is presented that provides a cheap, fast and conceptually simple methodology for the preparation of ordered colloidal monolayers. The produced two-dimensional crystals can be transformed into non-close-packed architectures by a plasma-induced size reduction step, thus providing valuable masks for more sophisticated lithographic processes. Finally, the controlled co-assembly of binary colloidal crystals with defined stoichiometries on a Langmuir trough is introduced and characterized with respect to accessible configurations and size ratios. rnSeveral approaches to lithography are presented that aim at introducing different features to colloidal lithography. First, using metal-complex containing latex particles, the synthesis of which is described as well, symmetric arrays of metal nanoparticles can be created by controlled combustion of the organic material of the colloids. The process does not feature an inherent limit in nanoparticle size and is able to produce complex materials as will be demonstrated for FePt alloy particles. Precise control over both size and spacing of the particle array is presented. rnSecond, two lithographic processes are introduced to create sophisticated nanoparticle dimer units consisting of two crescent shaped nanostructures in close proximity; essentially by using a single colloid as mask to generate two structures simultaneously. Strong coupling processes of the parental plasmon resonances of the two objects are observed that are accompanied by high near-field enhancements. A plasmon hybridization model is elaborated to explain all polarization dependent shifts of the resonance positions. Last, a technique to produce laterally patterned, ultra-flat substrates without surface topographies by embedding gold nanoparticles in a silicon dioxide matrix is applied to construct robust and re-usable sensing architectures and to introduce an approach for the nanoscale patterning of solid supported lipid bilayer membranes. rn

Catalizzatori per la reazione di Water Gas Shift a media ed alta temperatura

L’H2 è un vettore energetico di elevato interesse, utilizzato nell’industria chimica per la produzione di NH3 e CH3OH, oltre che per le reazioni di idrogenazione ed HDS. Un importante processo nella produzione di H2 è la reazione di Water Gas Shift (WGS), usata nel trattamento delle correnti uscenti dal reattore di Steam Reforming (SR) del metano: CO + H2O  CO2 + H2 ∆H0298K = -41,2 KJ/mol. Sulla base di precedenti lavori, sono stati sviluppati nuovi catalizzatori per la reazione WGS ad alta temperatura (HTS), alternativi ai tradizionali sistemi a base di Fe/Cr, in considerazione dei vincoli economici (elevati valori del rapporto vapore/gas secco o S/DG) ed ambientali (formazione di CrVI) di questi sistemi. Partendo da sistemi Cu/Zn/Al con un basso contenuto di rame, ottenuti da precursori tipo idrotalcite (HT), stato studiato l’effetto dell’aggiunta di piccole quantità di alcuni promotori sull’attività e stabilità dei catalizzatori ottenuti, osservando un effetto positivo sulle caratteristiche fisiche, come l’aumento dell’area superficiale e della dispersione della fase attiva. I campioni contenenti i promotori erano inoltre caratterizzati da una maggiore stabilità termica e, in alcuni casi, da un’attività catalitica superiore a quella del catalizzatore di riferimento privo di promotori. L’aggiunta di piccole quantità di alcali alla formulazione con la migliore attività portava ad un ulteriore aumento di attività e di stabilità, attribuibile ad una minore formazione di coke sulla superficie. I sistemi più interessanti potevano operare anche a bassi valori del rapporto S/DG, interessanti dal punto di vista industriale. Lo studio dell’adsorbimento di CO mediante FT-IR ha permesso di ipotizzare la possibile natura della fase attiva nei sistemi. Infine, lo studio è stato esteso a sistemi per la reazione di WGS a media temperatura (MTS), osservando anche in questo caso un positivo effetto legato all’aggiunta di promotori, con un aumento dell’attività catalitica e della stabilità con il tempo di reazione.