931 resultados para mikro CHP


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Pós-graduação em Ciência Odontólogica - FOA

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Objectives. To research parental behavior and measure the weight of Nelore and Guzerat calves up to 120 days of age, collecting data from birth up to the first lactation. Materials and methods. Seven different corporal positions were considered to obtain specific data for each of the following categories: time to stand (TP), time to intend to feed after standing (TPTM), weight at birth (PN), weight at 120 days (P120), and time in contact with the calf (TCC). Additionally, independent variables were also evaluated, organized by class: weight at birth (CPN), number of calvings (CNP), order of calving in relation with the herd (CLPR), time of calving (CHP), and finally, hindering to feed (CTAT). Results. There was a significant result in favor of the Nelore race over the Guzerat race. The statistical averages for Nelore and Guzerat were: Time to stand averaged 71 and 153 minutes; time to intend to feed after standing, 39 minutes for Nelore and of 114 minutes for Guzerat. For variable weight at 120 days, Nelore reached an average of 122 kg, and Guzerat 109 kg. For the time in contact with the calf variable there was no significant variance between races. Conclusions. Results showed the superiority of the Nelore race, considering it better adapted to local environmental conditions.

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Zusammenfassung Die vorliegenden Arbeit beschäftigt sich mit den Synthesen und Charakterisierungen multifunktioneller, Arylamin-haltiger Polymere, welche sich als photorefraktive(PR)-Materialien eignen. Die Glastemperaturen (Tg) der angestrebten Materialien liegen deutlich über Raumtemperatur, um so den Pockels-Mechanismus zum Aufbau des PR-Effektes zu favorisieren. Hierzu sind zwei synthetische Konzepte, basierend auf Maleinimid-Methylvinylisocyanat-Reaktiv-Polymeren und Triphenylamin-haltigen Polymeren, entwickelt worden. Im Rahmen des Reaktiv-Polymer-Konzeptes konnten PR-Materialien mit den bisher größten Beugungs-Effizienzen sowie den schnellsten Ansprechzeiten für multifunktionelle hoch-Tg-Polymere dargestellt werden. Hierfür wurden Maleinimid-Methylvinylisocyanat-Reaktiv-Polymere synthetisiert welche an der Imid-Position über Spacer-Gruppen mit Carbazol-Einheiten funktionalisiert sind. Die Tg´s der Polymere konnten zwischen 60°C und 194°C eingestellt werden. Die Isocyanat-Gruppen wurden dann polymeranlog mit hydroxyalkyl-funktionalisierten Chromophoren umgesetzt. Die Kinetik des PR-Effektes dieser Materialien wird durch die Ladungsträger-Beweglichkeiten in den Proben bestimmt. Eine Steigerung der Farbstoff-Konzentrationen erhöht die PR-Leistungen der Materialien, behindert jedoch deren Kinetik.Das Triphenylamin-Polymer-Konzept verwendet Triphenylamine als Lochleiter. Hierfür wurden die radikalischen Polymerisations-Verhalten der Monomere p-Diphenylaminostyrol (DPAS) und erstmals p-Ditoluylaminostyrol (DTAS) untersucht. Die Monomere wurden durch spontane, freie und kontrollierte radikalische Verfahren polymerisiert. Mittels eines TEMPO-Derivates gelang der Aufbau von Block-Copolymeren. Poly-DPAS konnte, im Gegensatz zu Poly-DTAS, polymeranlog tricyanovinyliert werden. Dadurch lassen sich PDPAS-block-PTPAS-Copolymere selektiv im PDPAS-Block tricyanovinylieren. Diese Materialien weisen eine Tendenzen zur Mikro-Phasen-Separation auf.Die Strukturierung von PDPAS konnte durch Photo-Polymerisation mit einer Auflösung von wenigen mm demonstriert werden. Carbazol und Triphenylamin-haltige Materialien wurden mittels Cyclo-Voltametrie untersucht.

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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.

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Zusammenfassung In der vorliegenden Arbeit wurden im Zuge derAjmalinbiosynthese in Rauvolfia serpentina die NADPH2abhängigen Reduktionsschritte des Alkaloids Vomilenin zu 17O Acetylnorajmalin genauer untersucht.Dabei konnte erstmals die exakte Reaktionsreihenfolgeaufgedeckt und die daran beteiligten Enzyme ausPflanzenzellsuspensionskulturen isoliert und aufgereinigtwerden. Die ausgearbeiteten, optimierten Reinigungsprotokolleführten in wenigen Stufen gezielt zu den voneinandergetrennten Reduktase Fraktionen. Durch die Trennung derReduktase Aktivitäten war der Grundstein gelegt, dasZwischenprodukt der Reaktion anzureichern und mitverschiedenen analytischen Verfahren als 2?-(R)-1.2Dihydrovomilenin zu identifizieren. Die daraufhin vergebenenBezeichnungen Vomilenin Reduktase (EC.1.5.1.32) und 1.2Dihydrovomilenin Reduktase (EC.1.3.1.73) zielen auf dasumzusetzende Substrat ab.Für die Vomilenin Reduktase konnte eine 4 stufige Reinigungüber (NH4)2SO4 Fällung, Anionen-austauschchromatographie mitSOURCE 30Q, Hydrophobe Interaktionschromatographie an SOURCE15Phe und Affinitätschromatographie mit 2’,5’ ADP Sepharoseausgearbeitet werden. Hierbei konnte die 1.2Dihydrovomilenin Reduktase schon nach dem erstensäulenchromatogra-phischen Schritt (S 30Q) abgetrenntwerden. Das am Ende der Proteinreinigung angefertigte SDSGel zeigte nur noch 3 Banden, von denen die beiden bei ca.40 und 43 kDa gelegenen Banden mit dem Aktivitätsverlaufder Vomilenin Reduktase korrelierten. Diese wurden einempartiellen Verdau mit der Endoproteinase LysC unterworfen,wobei jeweils 2 Spaltpeptide erhalten werden konnten.Die 1.2 Dihydrovomilenin Reduktase Reinigung umfaßte 6Reinigungsschritte mit (NH4)2SO4-Fällung, SOURCE 30QAnionenaustauschchromatographie, HydroxylapatitChromatographie, 2’,5’ ADP Sepharose-Chromatographie,Anionenaustausch an DEAE Sepharose und abschließen-denAnionenaustausch über MonoQ. Die resultierendeProteinfraktion wies eine ca. 200 fache Anreicherung an 1.2Dihydrovomilenin Reduktase auf. Auch hierbei wurde die nachSDS Gelelek-trophorese als 1.2 Dihydrovomilenin Reduktasebestimmte Proteinbande (bei ca. 48 kDa) sequen-ziert. Eskonnten vier Peptidfragmente erhalten werden, die ebenso wiedie sequenzierten Peptidstücke der 40 und 43 kDa Bande einehohe Homologie zu Oxidoreduktasen, im einzelnen zuCinnamoylalcohol- und Mannitol Dehydrogenasen, aufwiesen.Um die Identität der sequenzierten Proteinbanden zubestätigen, wurde über „reverse genetics“ die jeweilscodierende cDNA eruiert. Dafür wurden - ausgehend von denPeptidstücken der Mikro-sequenzierung - degenerierte Primerentwickelt und über PCR Teilbereiche der cDNA amplifiziert.Diese konnten für eine radioaktive Durchmusterung einerRauvolfia cDNA Bank herangezogen werden. Alternativ botallein die Kenntnis der spezifischen Nukleotidabfolge dieMöglichkeit der Gewinnung von 5’ und 3’ Ende derVollängenklone durch RACE PCR.Nach Abschluß dieser Arbeiten konnten für die 40 und 48 kDaBande je ein Vollängenklon und für die 43 kDa Bande 2Vollängenklone (Isoformen) gefunden werden. SämtlicheVollängenklone besitzen einen offenen Leserahmen, der durchnicht zu translatierende Bereiche am 5’ und 3‘ Endeeingefaßt wird. Um die entsprechenden Proteine produzierenzu können, mußten die dafür codierenden cDNA Bereiche dereinzelnen Klone in ein geeignetes Vektor Wirt-System(Expressionssystem) eingebracht werden.Nach erfolgreicher Umklonierung wurde die Expression durchIPTG Zugabe kontrolliert und Proteinrohextrakte aus denBakterienstämmen isoliert. Als Substrate wurden Vomilenin,das strukturisomere Alkaloid Perakin und aufgrund derHomologien zu Cinnamoylalcohol und Mannitol Dehydrogenasen Zimtaldehyd, Dihydrozimtaldehyd und D(-)Fructose getestet. In allen E. coli Stämmen konnte ein unspezifischesReduktionspotential nachgewiesen werden, ohne daß jedochVomilenin reduziert wurde. Die Testung der 1.2Dihydrovomilenin Reduktase Klone mußte wegen Substratmangelentfallen.Die weitere Charakterisierung der pflanzlichen Enzymeerbrachte eine enorm hohe Substratspezifität mit einer sichauf Rauvolfia beschränkenden taxonomischen Verbreitung.Die Molekulargewichtsbestimmung für die Vomilenin Reduktaseergab nach Größenausschluß-chromatographie an Superdex 75ein Gewicht von etwa 43 kDa. Das ebenfalls über Superdex 75ermittelte Molekulargewicht für die 1.2 DihydrovomileninReduktase lag bei ca. 49.8 kDa. Weiterhin wurde eine Metallionenabhängigkeit für dieVomilenin Reduktase aufgezeigt und die Cofaktorspezifitätsowie die pH und Temperatur Optima für beide Reduktasenbestimmt.

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The aim of this thesis was to investigate novel techniques to create complex hierarchical chemical patterns on silica surfaces with micro to nanometer sized features. These surfaces were used for a site-selective assembly of colloidal particles and oligonucleotides. To do so, functionalised alkoxysilanes (commercial and synthesised ones) were deposited onto planar silica surfaces. The functional groups can form reversible attractive interactions with the complementary surface layers of the opposing objects that need to be assembled. These interactions determine the final location and density of the objects onto the surface. Photolithographically patterned silica surfaces were modified with commercial silanes, in order to create hydrophilic and hydrophobic regions on the surface. Assembly of hydrophobic silica particles onto these surfaces was investigated and finally, pH and charge effects on the colloidal assembly were analysed. In the second part of this thesis the concept of novel, "smart" alkoxysilanes is introduced that allows parallel surface activation and patterning in a one-step irradiation process. These novel species bear a photoreactive head-group in a protected form. Surface layers made from these molecules can be irradiated through a mask to remove the protecting group from selected regions and thus generate lateral chemical patterns of active and inert regions on the substrate. The synthesis of an azide-reactive alkoxysilane was successfully accomplished. Silanisation conditions were carefully optimised as to guarantee a smooth surface layer, without formation of micellar clusters. NMR and DLS experiments corroborated the absence of clusters when using neither water nor NaOH as catalysts during hydrolysis, but only the organic solvent itself. Upon irradiation of the azide layer, the resulting nitrene may undergo a variety of reactions depending on the irradiation conditions. Contact angle measurements demonstrated that the irradiated surfaces were more hydrophilic than the non-irradiated azide layer and therefore the formation of an amine upon irradiation was postulated. Successful photoactivation could be demonstrated using condensation patterns, which showed a change in wettability on the wafer surface upon irradiation. Colloidal deposition with COOH functionalised particles further underlined the formation of more hydrophilic species. Orthogonal photoreactive silanes are described in the third part of this thesis. The advantage of orthogonal photosensitive silanes is the possibility of having a coexistence of chemical functionalities homogeneously distributed in the same layer, by using appropriate protecting groups. For this purpose, a 3',5'-dimethoxybenzoin protected carboxylic acid silane was successfully synthesised and the kinetics of its hydrolysis and condensation in solution were analysed in order to optimise the silanisation conditions. This compound was used together with a nitroveratryl protected amino silane to obtain bicomponent surface layers. The optimum conditions for an orthogonal deprotection of surfaces modified with this two groups were determined. A 2-step deprotection process through a mask generated a complex pattern on the substrate by activating two different chemistries at different sites. This was demonstrated by colloidal adsorption and fluorescence labelling of the resulting substrates. Moreover, two different single stranded oligodeoxynucleotides were immobilised onto the two different activated areas and then hybrid captured with their respective complementary, fluorescent labelled strand. Selective hybridisation could be shown, although non-selective adsorption issues need to be resolved, making this technique attractive for possible DNA microarrays.

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The idea was to obtain nanowires in a chemical laboratory under convenient and simple conditions by employing templates. Thus it was possible to produce nanochains by interlinking of gold colloids synthesized by the two-phase-method of M. Brust with by making use of vanadiumoxide nanotubes as template. The length of the resulting nanowires is varying between 1100 nm and 200 nm with a diameter of about 16 nm. Due to a flexible linker the obtained nanowires are not completely rigid. These unique structural features could make them interesting objects for structuring and assembling in the nanoscale range. Another way to produce gold nanowires was realized by a two-step surface metallization procedure, using type I collagen fibres as a template. Gold colloids were used to label the collagen fibres by direct electrostatic interaction, followed by growth steps to enhance the size of the adsorbed colloidal gold crystals, resulting in a complete metallization of the template surface. The length of the resulting gold nanowires reaches several micrometers, with a diameter ~ 100 to 120 nm. To gain a deeper insight into the process of biomineralization the cooperative effect of self-assembled monolayers as substrate and a soluble counterpart on the nucleation and crystal growth of calcium phosphate was studied by diffusion techniques with a pH switch as initiator. As soluble component Perlucin and Nacrein were used. Both are proteins originally extracted from marine organisms, the first one from the Abalone shell and the second one from oyster pearls. Both are supposed to facilitate the calcium carbonate formation in vivo. Studies with Perlucin revealed that this protein shows a clear cooperative effect at a very low concentration with a hydrophobic surface promoting the calcium phosphate precipitation resulting in a sponge like structure of hydroxyapatite. The Perlucin molecule is very flexible and is unfolded by adsorbing to the hydrophobic surface and uncovers its active side. Hydrophilic surfaces did not have a deeper impact. Studies with Nacrein as additive have shown that the protein stabilizes octacalcium phosphate at room temperature on carboxylic self-assembled monolayer and at 34 °C on all other employed surfaces by interaction with the mineral. On the hydroxyl-, alkyl-, and amin-terminated self-assembled monolayers at room temperature the octacalcium phosphate get transformed to hydroxyapatite. Main analytical techniques which are used in this work are transmission electron microscopy, high resolution scanning electron microscopy, surface plasmon resonance spectroscopy, atomic force microscopy, Raman micro-spectroscopy and quartz crystal microbalance.

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Die Vergesellschaftung und Bindungsform von Arsen in Düngekalk wurde durch chemische und mineralogische Analysen sowie XANES/EXAFS-Messungen untersucht. Die durch-schnittliche As-Konzentration im Düngekalk (70 mg/kg) überschreitet den Grenzwert der DüMV (40 mg/kg). Arsen ist in Mn- (Romanechit) und Fe-Dendriten (Goethit, Ferrihydrit) angereichert. Seine Oxidationsstufe ist jeweils 5+. µ-EXAFS-Untersuchungen ergaben Hin-weise auf zweizähnige und einzähnige mononukleare Durchdringungskomplexe mit Eisen-oxid. Das Mobilisierungsverhalten von Arsen wurde durch sequentielle Extraktion des Dün-gekalks und Mobilisierungsversuche mit wassergesättigtem Boden untersucht. Die Lösung erfolgte vorwiegend im dritten Extraktionsschritt gemeinsam mit kristallinen Eisenoxiden. Unter moderat anoxischen Bedingungen war im Boden keine zusätzliche Mobilisierung von Arsen aus dem Düngekalk nachweisbar. Erhöhte As-Konzentrationen und As3+-Anteile im Porenwasser traten bei niedrigem Eh unabhängig von Kalkzugabe auf. Eine Kopplung des Arsen-Grenzwerts an den Eisenoxidgehalt erscheint sinnvoll. Ein Messaufbau für Mikro-XAS Imaging wurde in Betrieb genommen. Er ermöglicht die si-multane Erfassung einer Probenfläche von 26,6×6,6 mm² wahlweise im Transmissions- oder Fluoreszenzmodus mit der räumlichen Auflösung 52×52 µm² durch eine CCD-Kamera. Zur Datenverarbeitung wurden IDL-Programme sowie die Fernerkundungssoftware ENVI ver-wendet. Die Messergebnisse zeigen weniger Störungen und Rauschen als die Ergebnisse frü-herer Messungen mit einem Prototyp. Die Ergebnisse und Erfahrungen der Messungen liefern Hinweise für die weitere erfolgreiche Nutzung des Messaufbaus.

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Im Rahmen dieser Arbeit wurden drei neue Modelle zur funktionellen Mimiese biologischer Membranen im Bereich der Bionanotechnologie entwickelt. Um den Rahmen der notwendigen Faktoren und Komponenten für biomimetische Membranmodelle abzustecken, wurde das biologische Vorbild im Bezug auf Zusammensetzung, Organisation und Funktion analysiert. Die daraus abgeleiteten Erkenntnisse erlauben das Erreichen von biologisch relevanten Membranwiderständen im Bereich von mehreren MOhm cm2 und eine gute lokale Fluidität. Ein weiteres Ziel dieser Arbeit war die Entwicklung einer Hierachie unterschiedlich stark von der Festkörperoberfläche entkoppelter Membranen zur Vergrößerung des submembranen Raumes. Diese Ziele konnten realisiert werden. Das auf archaealen Etherlipiden basierende DPTL-System wurde analog dem biologischen Vorbild stereoselektiv synthetisiert und ist in der Lage die Membran bei maximaler Elongation des TEG-Spacers mit mehr als 2 nm von der Oberfläche zu entkoppeln. Die erzielten Wiederstände liegen im hohen ein- bis zweistelligen MOhm-Bereich, die Kapazität entspricht mit 0,5 µF cm-2 ebenfalls dem Wert biologischer Membranen. Die Membraneigenschaften wurden mit Hilfe von SPS, EIS, IR-Spektroskopie, QCM, AFM und Kontaktwinkelmessungen charakterisiert. Die Funktionalität und lokale Fluidität der DPTL-Membran konnte anhand des Valinomycin vermittelten K+-Transports über die Membran gezeigt werden. Fluide Elektroden oder laterale Verdünnung mit TEGL erlauben den Einbau größerer Ionenkanäle. Lipo-Glycopolymere (LGP) mit unterschiedlichen Kettenlängen wurden mit Hilfe der kontrollierten radikalischen Polymerisation mit einer PD < 1.2 synthetisiert. Es zeigte sich, daß die Vororientierung der LGPs auf dem LB-Trog, gefolgt von einem LB-Übertrag auf einen funktionalisierten Träger mit photoreaktivem SAM, nach Belichten des Systems zu einer verlässlichen kovalenten Anbindung der supramolekularen LGP-Architektur führt. Da die Lipo-Glycopolymerketten am Glycopolymerterminus nur mit oberflächennahen Repetiereinheiten an die photoaktivierte Oberfläche binden, sind sie in der Lage Oberflächenrauhigkeiten des Festkörpersubstrates auszugleichen. Die photochemische Immobilisierung von funktionell orientierten supramolekularen LGP-Architekturen auf Goldoberflächen resultiert in tBLMs mit großen vertikalen Enkopplungen der Membran von der Festkörperoberfläche (>8 nm). Der funktionelle Ionentransport von Kaliumionen durch Valinomycin zeigt eine ausreichende lokale Fluidität der Membran die mit einem guten Membranwiderstand (mehrere MOhm) kombiniert ist. Große Membran-Oberflächenentkopplungen konnten mit Hilfe plasmapolymerisierter elektrophiler Polymere erreicht werden. Filmdicken von 50 nm sind mit homogener Oberfläche und Rauhigkeiten im Bereich von Nanometern möglich. Das System zeigt interessante fluide Eigenschaften mit guten Erholungsraten bei FRAP-Experimenten (Diffusionskonstanten von etwa 17 mikro m2 s-1). Die elektrischen Eigenschaften liegen mit Widerständen von wenigen kOhm unterhalb der für gute Membranmimikrie notwendigen Werte. Erstmalig konnte gezeigt werden, daß mit Hilfe dieser Methode inerte Polymere/Plastikträger (zum Beispiel Polypropylen und TOPAS) in effizienter Weise kovalent mit reaktiven Polymeroberflächen modifiziert werden können (Anwendung als DNA-Chip ist beschrieben).

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Stylolites are rough paired surfaces, indicative of localized stress-induced dissolution under a non-hydrostatic state of stress, separated by a clay parting which is believed to be the residuum of the dissolved rock. These structures are the most frequent deformation pattern in monomineralic rocks and thus provide important information about low temperature deformation and mass transfer. The intriguing roughness of stylolites can be used to assess amount of volume loss and paleo-stress directions, and to infer the destabilizing processes during pressure solution. But there is little agreement on how stylolites form and why these localized pressure solution patterns develop their characteristic roughness.rnNatural bedding parallel and vertical stylolites were studied in this work to obtain a quantitative description of the stylolite roughness and understand the governing processes during their formation. Adapting scaling approaches based on fractal principles it is demonstrated that stylolites show two self affine scaling regimes with roughness exponents of 1.1 and 0.5 for small and large length scales separated by a crossover length at the millimeter scale. Analysis of stylolites from various depths proved that this crossover length is a function of the stress field during formation, as analytically predicted. For bedding parallel stylolites the crossover length is a function of the normal stress on the interface, but vertical stylolites show a clear in-plane anisotropy of the crossover length owing to the fact that the in-plane stresses (σ2 and σ3) are dissimilar. Therefore stylolite roughness contains a signature of the stress field during formation.rnTo address the origin of stylolite roughness a combined microstructural (SEM/EBSD) and numerical approach is employed. Microstructural investigations of natural stylolites in limestones reveal that heterogeneities initially present in the host rock (clay particles, quartz grains) are responsible for the formation of the distinctive stylolite roughness. A two-dimensional numerical model, i.e. a discrete linear elastic lattice spring model, is used to investigate the roughness evolving from an initially flat fluid filled interface induced by heterogeneities in the matrix. This model generates rough interfaces with the same scaling properties as natural stylolites. Furthermore two coinciding crossover phenomena in space and in time exist that separate length and timescales for which the roughening is either balanced by surface or elastic energies. The roughness and growth exponents are independent of the size, amount and the dissolution rate of the heterogeneities. This allows to conclude that the location of asperities is determined by a polimict multi-scale quenched noise, while the roughening process is governed by inherent processes i.e. the transition from a surface to an elastic energy dominated regime.rn

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Membranen spielen eine essentielle Rolle bei vielen wichtigen zellulären Prozessen. Sie ermöglichen die Erzeugung von chemischen Gradienten zwischen dem Zellinneren und der Umgebung. Die Zellmembran übernimmt wesentliche Aufgaben bei der intra- und extrazellulären Signalweiterleitung und der Adhäsion an Oberflächen. Durch Prozesse wie Endozytose und Exozytose werden Stoffe in oder aus der Zelle transportiert, eingehüllt in Vesikel, welche aus der Zellmembran geformt werden. Zusätzlich bietet sie auch Schutz für das Zellinnere. Der Hauptbestandteil einer Zellmembran ist die Lipiddoppelschicht, eine zweidimensionale fluide Matrix mit einer heterogenen Zusammensetzung aus unterschiedlichen Lipiden. In dieser Matrix befinden sich weitere Bausteine, wie z.B. Proteine. An der Innenseite der Zelle ist die Membran über Ankerproteine an das Zytoskelett gekoppelt. Dieses Polymernetzwerk erhöht unter anderem die Stabilität, beeinflusst die Form der Zelle und übernimmt Funktionenrnbei der Zellbewegung. Zellmembranen sind keine homogenen Strukturen, je nach Funktion sind unterschiedliche Lipide und Proteine in mikrsokopischen Domänen angereichert.Um die grundlegenden mechanischen Eigenschaften der Zellmembran zu verstehen wurde im Rahmen dieser Arbeit das Modellsystem der porenüberspannenden Membranen verwendet.Die Entwicklung der porenüberspannenden Membranen ermöglicht die Untersuchung von mechanischen Eigenschaften von Membranen im mikro- bis nanoskopischen Bereich mit rasterkraftmikroskopischen Methoden. Hierbei bestimmen Porosität und Porengröße des Substrates die räumliche Auflösung, mit welcher die mechanischen Parameter untersucht werdenrnkönnen. Porenüberspannende Lipiddoppelschichten und Zellmembranen auf neuartigen porösen Siliziumsubstraten mit Porenradien von 225 nm bis 600 nm und Porositäten bis zu 30% wurden untersucht. Es wird ein Weg zu einer umfassenden theoretischen Modellierung der lokalen Indentationsexperimente und der Bestimmung der dominierenden energetischen Beiträge in der Mechanik von porenüberspannenden Membranen aufgezeigt. Porenüberspannende Membranen zeigen eine linear ansteigende Kraft mit zunehmender Indentationstiefe. Durch Untersuchung verschiedener Oberflächen, Porengrößen und Membranen unterschiedlicher Zusammensetzung war es für freistehende Lipiddoppelschichten möglich, den Einfluss der Oberflächeneigenschaften und Geometrie des Substrates, sowie der Membranphase und des Lösungsmittels auf die mechanischen Eigenschaften zu bestimmen. Es ist möglich, die experimentellen Daten mit einem theoretischen Modell zu beschreiben. Hierbei werden Parameter wie die laterale Spannung und das Biegemodul der Membran bestimmt. In Abhängigkeit der Substrateigenschaften wurden für freitragende Lipiddoppelschichten laterale Spannungen von 150 μN/m bis zu 31 mN/m gefunden für Biegemodulde zwischen 10^(−19) J bis 10^(−18) J. Durch Kraft-Indentations-Experimente an porenüberspannenden Zellmembranen wurde ein Vergleich zwischen dem Modell der freistehenden Lipiddoppelschichten und nativen Membranen herbeigeführt. Die lateralen Spannungen für native freitragende Membranen wurden zu 50 μN/m bestimmt. Weiterhin konnte der Einfluss des Zytoskeletts und der extrazellulä-rnren Matrix auf die mechanischen Eigenschaften bestimmt und innerhalb eines basolateralen Zellmembranfragments kartiert werden, wobei die Periodizität und der Porendurchmesser des Substrates das räumliche Auflösungsvermögen bestimmen. Durch Fixierung der freistehenden Zellmembran wurde das Biegemodul der Membran um bis zu einem Faktor 10 erhöht. Diese Arbeit zeigt wie lokal aufgelöste, mechanische Eigenschaften mittels des Modellsystems der porenüberspannenden Membranen gemessen und quantifiziert werden können. Weiterhin werden die dominierenden energetischen Einflüsse diskutiert, und eine Vergleichbarkeit zurnnatürlichen Membranen hergestellt.rn

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In der vorliegenden Arbeit wurden experimentelle Untersuchungen zu gepfropften Polymerfilmen durchgeführt. Dabei wurden endgepfropfte poly-methyl-methacrylate (PMMA) Bürsten hergestellt durch „grafting from“ Methoden und polystyrol (PS)/ poly-vinyl-methyl-ether (PVME) Polymerfilme gepfropft auf UV sensitiven Oberflächen untersucht. Zur Strukturuntersuchung wurden die hergestellten Systeme wurden mit Rasterkraftmikroskopie (engl.: Surface Probe Microscopy, SPM), Röntgen - und Neutronenreflektivitätsmessungen, sowie mit Röntgenstreuung unter streifenden Einfall (engl.: Grazing Incidence Small Angle X-Ray Scattering, GISAXS) untersucht. rnEs wurde gezeigt, dass ein aus der Transmissionsstreuung bekanntes Model auch für auch für die GISAXS Analyse polydisperser Polymerdomänen und Kolloidsysteme verwendet werden kann. Der maximale Fehler durch die gemachten Näherungen wurde auf < 20% abgeschätzt.rnErgebnisse aus der Strukturanalyse wurden mit mechanischen Filmeigenschaften verknüpft. Dazu wurden mechanische Spannungsexperimente durchgeführt. Hierzu wurden die zu untersuchenden Filme selektiv auf einzelne Mikro-Federbalken-Sensoren (engl.: Micro Cantilever Sensor, MCS) der MCS Arrays aufgebracht. Dies wurde durch Maskierungstechniken und Mikro-Kontaktdrucken bewerkstelligt. rnPhasenübergansexperimente der gepfropften PS/PVME Filme haben gezeigt, dass die Möglichkeit einer Polymer/Polymer Phasenseparation stark von Propfpunktdichte der gebundenen Polymerketten mit der Oberfläche abhängt. PS/PVME Filmsysteme mit hohen Pfropfpunktdichten zeigten keinen Phasenübergang. Bei niedrig gepfropften Filmsystemen waren hingegen Polymer/Polymer Phasenseparationen zu beobachten. Es wurde geschlussfolgert, dass die gepfropften Polymersysteme einen hinreichenden Grad an entropischen Freiheitsgraden benötigen um eine Phasenseparation zu zeigen. Mechanische Spannungsexperimente haben dabei das Verstehen der Phasenseparationsmechanismen möglich gemacht.rnAus Quellexperimenten dichtgepfropfter PMMA Bürsten, wurden Lösungsmittel-Polymer Wechselwirkungsparameter (-Parameter) bestimmt. Dabei wurde festgestellt, dass sich die erhaltenen Parameter aufgrund von Filmbenetzung und entropischen Effekten maßgeblich von den errechneten Bulkwerten unterscheiden. Weiterhin wurden nicht reversible Kettenverschlaufungseffekt beobachtet.

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In the field of organic optoelectronics, the nanoscale structure of the materials has huge im-pact on the device performance. Here, scanning force microscopy (SFM) techniques become increasingly important. In addition to topographic information, various surface properties can be recorded on a nanometer length scale, such as electrical conductivity (conductive scanning force microscopy, C-SFM) and surface potential (Kelvin probe force microscopy, KPFM).rnrnIn the context of this work, the electrical SFM modes were applied to study the interplay be-tween morphology and electrical properties in hybrid optoelectronic structures, developed in the group of Prof. J. Gutmann (MPI-P Mainz). In particular, I investigated the working prin-ciple of a novel integrated electron blocking layer system. A structure of electrically conduct-ing pathways along crystalline TiO2 particles in an insulating matrix of a polymer derived ceramic was found and insulating defect structures could be identified. In order to get insights into the internal structure of a device I investigated a working hybrid solar cell by preparing a cross cut with focused ion beam polishing. With C-SFM, the functional layers could be identified and the charge transport properties of the novel active layer composite material could be studied. rnrnIn C-SFM, soft surfaces can be permanently damaged by (i) tip induced forces, (ii) high elec-tric fields and (iii) high current densities close to the SFM-tip. Thus, an alternative operation based on torsion mode topography imaging in combination with current mapping was intro-duced. In torsion mode, the SFM-tip vibrates laterally and in close proximity to the sample surface. Thus, an electrical contact between tip and sample can be established. In a series of reference experiments on standard surfaces, the working mechanism of scanning conductive torsion mode microscopy (SCTMM) was investigated. Moreover, I studied samples covered with free standing semiconducting polymer nano-pillars that were developed in the group of Dr. P. Theato (University Mainz). The application of SCTMM allowed non-destructive imag-ing of the flexible surface at high resolution while measuring the conductance on individual pillarsrnrnIn order to study light induced electrical effects on the level of single nanostructures, a new SFM setup was built. It is equipped with a laser sample illumination and placed in inert at-mosphere. With this photoelectric SFM, I investigated the light induced response in function-alized nanorods that were developed in the group of Prof. R. Zentel (University Mainz). A block-copolymer containing an anchor block and dye moiety and a semiconducting conju-gated polymer moiety was synthesized and covalently bound to ZnO nanorods. This system forms an electron donor/acceptor interface and can thus be seen as a model system of a solar cell on the nanoscale. With a KPFM study on the illuminated samples, the light induced charge separation between the nanorod and the polymeric corona could not only be visualized, but also quantified.rnrnThe results demonstrate that electrical scanning force microscopy can study fundamental processes in nanostructures and give invaluable feedback to the synthetic chemists for the optimization of functional nanomaterials.rn

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Lo scopo di questa tesi è quello di analizzare dapprima l’impatto ambientale di tali impianti e poi analizzare il contributo effettivo che oggi la tecnologia innovativa dei cicli Rankine organici può dare nella valorizzazione elettrica del calore di scarto di processi industriali, focalizzando l’obiettivo principalmente sulle turbine a gas ed eseguendo un caso di studio in un settore ancora poco esplorato da questa tecnologia, quello Oil&Gas. Dopo aver effettuato il censimento degli impianti a fonti fossili e rinnovabili, cogenerativi e non, presenti in Emilia-Romagna, è stato sviluppato un software chiamato MiniBref che permette di simulare il funzionamento di una qualsiasi centrale termoelettrica grazie alla possibilità di combinare la tecnologia dell’impianto con il tipo di combustibile consentendo la valutazione delle emissioni inquinanti ed i potenziali di inquinamento. Successivamente verranno illustrati gli ORC, partendo dalle caratteristiche impiantistiche e termodinamiche fino ad arrivare alla scelta del fluido organico, fondamentale per le performance del ciclo. Dopo aver effettuato una ricognizione dello stato dell’arte delle applicazioni industriali degli ORC nel recupero termico, verranno eseguite simulazioni numeriche per ricostruire gli ORC ed avere una panoramica il più completa ed attendibile delle prestazioni effettive di questi sistemi. In ultimo verranno illustrati i risultati di un caso di studio che vede l’adozione di recupero mediante ciclo organico in un’installazione esistente del settore Oil&Gas. Si effettuerà uno studio delle prestazione dell’impianto al variare delle pressioni massime e minime del ciclo ed al variare del fluido impiegato al fine di mostrare come questi parametri influenzino non solo le performance ma anche le caratteristiche impiantistiche da adottare. A conclusione del lavoro si riporteranno i risultati relativi all’analisi condotte considerando l’impianto ai carichi parziali ed in assetto cogenerativo.

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Considerando l'elevato grado di inquinamento del pianeta e la forte dipendenza delle attività antropiche dai combustibili fossili, stanno avendo notevole sviluppo e incentivazione gli impianti per la produzione di energia elettrica da fonti rinnovabili. In particolare, la digestione anaerobica è in grande diffusione in Italia. Lo studio in oggetto si prefigge l'obiettivo di determinare, mediante analisi di Life Cycle Assessment (LCA), i carichi ambientali di un impianto di digestione anaerobica, e della sua filiera, per valutarne l'effettiva ecosostenibilità. L'analisi considera anche gli impatti evitati grazie all'immissione in rete dell'energia elettrica prodotta e all'utilizzo del digestato in sostituzione dell'urea. Lo studio analizza sei categorie d'impatto: Global warming potential (GWP), Abiotic depletion potential (ADP), Acidification potential (AP), Eutrophication potential (EP), Ozone layer depletion potential (ODP) e Photochemical oxidant formation potential (POFP). I valori assoluti degli impatti sono stati oggetto anche di normalizzazione per stabilire la loro magnitudo. Inoltre, è stata effettuata un'analisi di sensitività per investigare le variazioni degli impatti ambientali in base alla sostituzione di differenti tecnologie per la produzione di energia elettrica: mix elettrico italiano, carbone e idroelettrico. Infine, sono stati analizzati due scenari alternativi all'impianto in esame che ipotizzano la sua conversione ad impianto per l'upgrading del biogas a biometano. I risultati mostrano, per lo scenario di riferimento (produzione di biogas), un guadagno, in termini ambientali, per il GWP, l'ADP e il POFP a causa dei notevoli impatti causati dalla produzione di energia elettrica da mix italiano che la filiera esaminata va a sostituire. I risultati evidenziano anche quanto gli impatti ambientali varino in base alla tipologia di alimentazione del digestore anaerobica: colture dedicate o biomasse di scarto. I due scenari alternativi, invece, mostrano un aumento degli impatti, rispetto allo scenario di riferimento, causati soprattutto dagli ulteriori consumi energetici di cui necessitano sia i processi di purificazione del biogas in biometano sia i processi legati alla digestione anaerobica che, nel caso dello scenario di riferimento, sono autoalimentati. L'eventuale conversione dell'attuale funzione dell'impianto deve essere fatta tenendo anche in considerazione i benefici funzionali ed economici apportati dalla produzione del biometano rispetto a quella del biogas.