Für den ökonomischen Erfolg konzentrierender Solarkraftwerke und für die Effizienz-steigerung der Industrie durch Weiterverwendung von Abwärme sind skalierbare Hochtemperatur-Wärmespeicher zu vertretbaren Kosten unabdingbar. Bisher sind für dieses Anwendungsgebiet nur sensible Speicher kommerziell verfügbar. Denen gegenüber besitzen chemische Speicher zahlreiche Vorteile. Sie bieten höhere Speicherdichten, geringere Wärmeverluste, die Möglichkeit zur Wärmetransformation durch Variation des Reaktionsdrucks und eine Vielzahl von Reaktionssystemen für eine optimale Prozess-integration. Jedoch befinden sie sich noch in der Entwicklungsphase. Die reversible Gas-/Feststoffreaktion von Calciumoxid und Wasserdampf zu Calcium-hydroxid geschieht bei Temperaturen von 400 – 600 °C und ist damit optimal für solarthermische Anwendungen geeignet. Für die Entwicklung eines Speichers ist neben der thermochemischen Charakterisierung des Speichermaterials ein effizientes, skalierbares Reaktorkonzept nötig. Ein Reaktor mit bewegtem Reaktionsbett ermöglicht die Trennung der zwei charakteristischen Speichergrößen Leistung und Kapazität und stellt damit einen wirtschaftlichen Speicher in Aussicht. Die vorliegende Arbeit befasst sich mit Aufbau und Inbetriebnahme eines neuen Teststandes, in welchem ein innovatives Reaktordesign erprobt werden soll. Sie beschreibt die Auslegung einer planaren Reaktorgeometrie, die einen Schwerkraftfluss des Bettes und die Modularisierung für größere Anlagen gewährleistet. Bei Vorversuchen stellt sich die homo-gene Bewegung des Reaktionsbettes aufgrund dessen Kompressibilität als schwierig heraus. Der angestrebte homogene Massenfluss des Reaktionsmaterials kann durch die ursprünglich eingesetzten Feindosiereinheiten nicht erzielt werden. Sie zeigen sich jedoch für die Temperierung des Speichermediums und die Gasdichtheit des Reaktionsraumes als geeignet. Das homogene Ausfließen wird einer separaten Austragshilfe zugeteilt, welche konstruiert und umgesetzt wird. Experimente mit einem Schaureaktor identifizieren eine Zahnwelle als beste Option. Für einen kommerziellen Speicher wird ein Schlitzschieber empfohlen. Ebenso erfolgen Auslegung und Errichtung der peripheren Anlagenteile, wie z.B. die Fertigung eines Druckhalters zur Steuerung der Reaktionstemperatur. Am Teststand werden somit alle Vorbereitungen abgeschlossen, um Heißversuche bei Reaktionstemperatur durchzuführen.:Kurzfassung.....................................................................II Aufgabenstellung ..............................................................III Inhaltsverzeichnis ..............................................................V Nomenklatur ...................................................................VII Abbildungs- und Tabellenverzeichnis ............................................IX Vorwort ........................................................................XI 1 Einleitung ................................................................... 1 2 Theorie thermischer Energiespeicher .......................................... 3 2.1 Beschreibung von Wärmespeichern ............................................ 3 2.2 Sensible Wärmespeicher ..................................................... 4 2.3 Latente Wärmespeicher....................................................... 9 2.4 Sorptive Wärmespeicher .....................................................12 2.5 Chemische Wärmespeicher ....................................................14 3 Spezifikation des thermochemischen Speichersystems ...........................17 3.1 Thermochemische Grundlagen .................................................17 3.2 Motivation der Aufgabenstellung ............................................20 3.3 Charakterisierung des Reaktionssystems .....................................21 4 Systembeschreibung des Speicherkonzepts ......................................26 4.1 Kurzdarstellung der Ausgangssituation ......................................26 4.2 Weiterentwicklung zum bewegten Reaktionsbett ...............................27 4.2.1 Theorie des bewegten Reaktionsbettes .....................................27 4.2.2 Konstruktion des Reaktors ................................................28 4.2.3 Förderung des Speichermaterials ..........................................31 4.3 Periphere Anlagenteile .....................................................33 4.3.1 Anlagenschema ............................................................33 4.3.2 Entwurf des Druckhalters .................................................35 INHALTSVERZEICHNIS VI 4.3.3 Ausführung der Elektro- und Messtechnik ..................................37 5 Experimentelle Untersuchungen ................................................39 5.1 Versuchsdurchführung .......................................................39 5.2 Betrieb der Fördereinheiten ................................................40 5.3 Optimierung der Fördereinheiten ............................................44 5.3.1 Inaktive Mischpaddel .....................................................44 5.3.2 Modifizierte Mischpaddel .................................................47 5.4 Erkenntnisse ...............................................................49 6 Finales Konzept des Versuchsstandes ..........................................50 6.1 Lösungsansätze für den Massenfluss .........................................50 6.2 Gestaltung der Austragshilfe ...............................................54 7 Zusammenfassung und Ausblick .................................................57 Eidesstattliche Erklärung ......................................................59 Literatur- und Quellenverzeichnis ..............................................60 Anlagen ........................................................................63 A.1. Parametrierung des Temperaturwächters (Kapitel 4.3.3) .....................63 A.2. Inhalt des beigelegten Datenträgers (Einband) .............................63 A.3. Berechnung der Aufheizstrecke des Stickstoffstroms (Kapitel 4.3.1) ........64 A.4. Konstruktionszeichnung des Druckhalters (Kapitel 4.3.2) ...................65 A.5. Dampftafel: Sättigungsdampfdruck von Wasserdampf (Kapitel 4.3.2) ..........66 A.6. Stromlaufpläne und Baugruppenliste des Teststandes (Kapitel 4.3.3) ... ....67 A.7. Ermittlung der Kabelquerschnitte für Stromlaufplan (Kapitel 4.3.3) ........73 A.8. Parametrierung der Frequenzumrichter (Kapitel 5.1) ....................... 74 A.9. Ergebnisse der Kalibiermessungen (Kapitel 5.2) ............................75 A.10. Berechnungen zur Dynamik des Schlitzschiebers (Kapitel 6.1) ............. 76 A.11. Konstruktionszeichnungen der Austragshilfe (Kapitel 6.2) .................77

One of the most crucial issues nowadays is the protection of the environment and the replacement of fossil fuels, which are abundantly used around the world, with more efficient and renewable sources. The highest portion of global energy demands today is used in heating and cooling purposes. One way of alleviating the fossil-based thermal energy uses is to harvest excess thermal energy using thermochemical storage materials (TCMs) for use at heating/cooling demands at different times and locations. Along this, in this master’s thesis, a bench-scale thermochemical heat storage (TCS) system is numerically designed, as a part of a collaborative project: Neutrons for Heat Storage (NHS), funded by Nordforsk. The TCS system that is designed herein employs the reversible chemical reaction of ammonia with a metal halide (MeX) for a heat storage capacity of 0.5 kWh, respectively releasing and storing heat during absorption and desorption of ammonia into and from the MeX. This system is designed for low temperature heat applications, around 40-80 °C. SrCl2 is chosen as the metal halide to be used, based on the research outcomes in determining the most suitable materials conducted by NHS project partners. In the ammonia-SrCl2 system, only the absorption and desorption between SrCl2∙NH3 and SrCl2∙8NH3 are considered. The main reason is because absorption/desorption between the last ammine and SrCl2 undergoes at a significantly higher/lower reaction pressure (for a given temperature), with a significant volume change compared to the rest of the ammines, and therefore is practically less cost effective. This thesis also includes a detailed discussion of four different thermochemical storage designs from literature, found as the most relevant to the present TCS system study, which use the reaction between ammonia and metal halides. The first system that was examined is a TCS system built by the NHS project partners at Technical University of Denmark (DTU), owing to its similarities with the desired project, regarding the design and parameters the system uses. This system works in batch mode, only allowing either absorption (i.e. heat release) or desorption (i.e. heat storage) at a given cycle. Thus, upgrading the design of this TCS system at DTU is considered as a most-likely solution to the research objectives of this current thesis project. Moreover, the TCS system at DTU uses storage conditions and desorption temperature similar to the current project’s desired low temperature range of 40-80 °C. The second system discussed herein from literature uses two reactors for cold and heat generation, which means that both charging and discharging processes occur simultaneously. This simultaneous operability is the main reason that this particular system was examined in this thesis. The next discussed system from literature also uses two reactors, for absorption and desorption processes, which work reversibly when each process is completed, like in the desired concept of this project. These two systems (i.e., the secondly and the thirdly discussed systems) use the reversible solid-gas reaction for absorption and desorption between SrCl2∙NH3 and SrCl2∙8NH3, however, the conditions of pressure and temperature between them differ. The second system from literature operates at desorption and absorption at respective conditions of 96 °C, 15 bar and 87 °C, 11 bar while the third system discussed operates at 103 °C, 16 bar and 59 °C, 3 bar during desorption and absorption respectively. The last system from literature that is discussed herein provides the same desorption temperature of 80 °C. Inaddition this particular study suggests that the reaction of solid with gaseous NH3 is better (than the solid with liquid NH3 reaction) based on results derived from several different low-pressure experiments of the reactions. The main differences between all these discussed systems from literature, as opposed to the desired TCS system design in this thesis project, concern the systems’ operating mode and the pressure and temperature-conditions. The first difference is that only one of the examined systems pumps the solid VIII powder salt around the system in contrast to the others that keep the salt static inside the reactors and pumped only the ammonia around the system, as chosen in the current system. The second difference concerns the operating conditions during absorption and desorption reactions, where these different systems operate at a widely different pressure and temperature conditions as compared to the current system expectations. Thus, there are four main lessons that were learnt via this literature analysis, to improve the TCS system at DTU to the desired new system in this work. The first lesson is related to the reactants’ transportation mechanism that should be used in this system. Regarding this, it was decided to maintain the solid salt (metal halide) stationary inside each reactor (but not pumping it instead of ammonia), similar to the majority of designs discussed from literature. According to the second and third lessons, the solid-gas reaction is the most suitable solution and only the reactions of absorption and desorption between SrCl2∙NH3 and SrCl2∙8NH3 are considered, following the experience from literature (for the reasons explained earlier). The last lesson regards the system’s suitable operating conditions and more specifically the TCS system’s temperatures that should match the district heating temperatures. Thus, the temperature point that was chosen as a priority was 80 °C, from the range 40- 80 °C set in the partner project NHS. To maintain this condition, therefore, the most suitable condition of pressure of both reactions (according to the equilibrium pressure vs temperature curve) was chosen to be at around 8 bar. This same pressure was chosen for both reactions, since the pressure difference between these reactors and the storage of ammonia (i.e. from 8 to 10 bar) should be as small as possible due to the high costs that can arise in the case of a higher pressure difference (i.e. requiring more compressors and heat exchangers). Inspired by these literature cases, firstly a conceptually suitable TCS system was proposed in this project and after that the final desired system was designed and was implemented and evaluated numerically. The numerical design and optimization of the chosen TCS system was performed herein by using the software Aspen Plus (version 9), which contains both fluids and solids in a simulation environment, using consistent physical properties. This TCS system is designed to store and release heat at around 80 °C and 8 bar through absorption and desorption by using two identical reactors respectively. Each reactor includes the amount of around 1 kg (more specifically 0.985 kg) strontium chloride salt reacting with 1.7 kg of ammonia. A verification system is also modelled in Aspen, using available experimental data from literature. Here, the modelled novel system design was adapted to this chosen other system layout from literature which uses the same reaction pair, yet at different operating conditions. This adapted system design in Aspen was then used to verify the chosen configuration and the reliability of the constructed system for the NHS project. Good agreements between the modelled results in Aspen against the available experimental data of this verification model are obtained. A sensitivity analysis is also conducted herein on the proposed novel TCS system to identify the optimum operating conditions and the behaviour of the chosen most important parameters of the system. The designed system provides an energy storage capacity of 0.5 kWh for the specific amounts (in volumetric flow rates) of ammonia and monoammine of strontium chloride, that comes from the analysis, of 1.08696 e-05 kmol/s and 1.5528 e-06 kmol/s respectively. For these specific values of the HTF, the analysis showed that the volumetric flow rates of the heat and cold external sources must be 1.56 l/min (which is decreasing with the increase of the inlet HTF temperature) and 0.42 l/min (which is increasing with the increase of the inlet HTF temperature) respectively. In conclusion, this study presents an ammonia-SrCl2 TCS benchscale system design that allows continuous heat storage and release, in an easy-to-scale up design, also suggesting optimum operating conditions. / En av de mest avgörande frågorna i dag är skyddet av miljön och utfasningen av fossila bränslen som används allmänt över hela världen för mer effektiva och förnybara resurser. Den största delen av den globala energibehovet idag avser uppvärmnings- och kylapplikationer. Ett sätt att minska fossilbaserad termiskenergianvändning är att lagra överskottsvärmeenergi genom termokemiska lagringsmaterial (TCM) och använda den för värme- och kylbehov vid olika tidpunkter och platser. I samband med detta är ett termokemiskt värmelagringssystem numeriskt utformat i detta mastersexamensprojekt, som en del av ett samarbetsprojekt Neutrons for Heat Storage (NHS) finansierat av Nordforsk. Det termokemiska lagringssystemet (TCS) som är konstruerat utnyttjar den reversibla kemiska reaktionen av ammoniak med en metallhalogenid (MeX) för en värmelagringskapacitet på 0.5 kWh, och frigör och lagrar värme respektive under absorption och desorption av ammoniak till och från MeX. Systemet är designat för lågtemperaturuppvärmningstillämpningar runt 40-80 °C. SrCl2 väljs som det mest lämpliga metallhalogeniden för systemet, baserat på studier som utförts av NHS-projektpartnerna. I ammoniak SrCl2-systemet beaktas endast absorption och desorption mellan SrCl2NH3 och SrCl28NH3. De huvudsakliga orsakerna till detta är att absorptionen/desorptionen mellan den sista aminen och SrCl2 kräver ett betydligt högre/lägre reaktionstryck (för en given temperatur), och resulterar i en betydande volymförändring jämfört med resten av aminerna, och är därför praktiskt taget mindre kostnadseffektivt. Detta mastersexamensprojekt inkluderar en detaljerad genomgång av fyra olika TCS-system från litteratur som använder reaktionen mellan ammoniak och metallhalogenider. Dessa väljs här eftersom dessa anses vara de mest relevanta (från litteratur) jämfört med det valda systemet i denna studie. Det första undersökta systemet är ett system byggt av NHS-projektpartnerna vid Danmarks Tekniska Universitet (DTU). Detta har valts på grund av likheterna med det önskade systemet i det aktuella mastersexamensprojektet, vad gäller systemdesign och parametrar. Detta system fungerar i batch-läge, vilket endast tillåter antingen absorption (dvs värmeavgivning) eller desorption (dvs värmelagring) under en specifik cykel. Således kan en uppgraderad design av detta TCS-system vid DTU möjligen vara en lämplig lösning på forskningsmålen för detta mastersexamensprojekt. Dessutom använder detta TCS-system från DTU ganska liknande driftsförhållanden (temperaturer och tryck) i nivå med det aktuella projektets önskade lågtemperaturintervall på 40-80 °C. Det andra systemet från den litteratur som diskuterats använder två reaktorer för kyla och värmeproduktion, vilket innebär att både laddningsoch urladdningsprocesser sker samtidigt. Denna samtidiga operation är främst anledningen till att systemet undersöktes, eftersom detta är en önskad funktion att uppnå i det aktuella projektet. Nästa system från den litteratur som diskuteras häri använder också två reaktorer för absorptions- och desorptionsprocesser, som fungerar reversibelt när varje process är klar, precis som önskat i detta projekt. Dessa två system (dvs det andra och det tredje diskuterade systemen) använder den reversibla fastgasreaktionen för absorption och desorption mellan SrCl2NH3 och SrCl28NH3, dock vid olika tryck- och temperaturförhållanden. Det andra systemet arbetar nämligen under kombinationer av absorption och desorption av 96 °C, 15 bar och 87 °C, 11 bar, medan det tredje systemet arbetar vid 103 °C, 16 bar respektive 59 °C, 3 bar. Det sista systemet som diskuterats från litteraturen arbetar vid samma temperatur som det önskade systemet gör (dvs. 80 ° C) och genom olika lågtrycksexperiment visar att den fasta salt-gasreaktionen är ett bättre val än reaktionen av det fasta saltet med flytande gasreaktion. De viktigaste skillnaderna mellan alla dessa diskuterade system från litteratur i motsats till det önskade TCS-system i detta mastersexamensprojekt, avser systemdriftläge samt deras tryck och X temperaturförhållanden. Den första skillnaden är att endast ett av alla undersökta system pumpar saltet i fast pulverform, till skillnad från de andra som håller saltet stillastående i reaktorerna och endast pumpar ammoniak. Den andra skillnaden gäller driftsförhållandena under absorptions- och desorptionsreaktioner där dessa system arbetar vid mycket olika tryck- och temperaturförhållanden jämfört med det nuvarande systemet. Således, från översynen av alla system, finns det fyra huvudsakliga lärdomar för att förbättra TCS-systemet vid DTU till det önskade nya systemet. Den första är relaterad till reaktanttransportmekanismen som bör användas i detta system. I detta avseende har det beslutats att hålla det fasta saltet (metallhalogenid) stillastående i varje reaktor (men inte pumpa det istället för ammoniak), till skillnad från de flesta system i litteraturen. Enligt dem andra och tredje lektionerna är den fasta gasreaktionen den mest lämpliga lösningen och endast reaktionerna på absorption och desorption mellan SrCl2∙NH3 och SrCl2∙8NH3 bör övervägas enligt erfarenheten från litteraturen (av de skäl som förklarats tidigare). Den sista lärdomen avser systemets lämpliga driftsförhållanden och mer specifikt TCS-systemets temperaturer för att matcha fjärrvärmetemperaturerna. Den temperaturpunkten valts som prioritet, från området 40-80 °C inställt av moderprojektet NHS, sattes till 80 °C. För att bibehålla detta tillstånd var det lämpligaste tryckvillkoret för båda reaktionerna (enligt jämviktstrycket kontra temperaturkurva) valdes att ligga på cirka 8 bar. Samma tryck valdes för båda reaktionerna, eftersom tryckskillnaden mellan dessa reaktorer och lagring av ammoniak (dvs. från 8 till 10 bar) borde vara så liten som möjligt på grund av de höga kostnaderna som kan uppstå vid högre tryckskillnad (dvs. fler kompressorer krävs och värmeväxlare). Inspirerad av denna litteratur föreslogs för det första ett konceptuellt lämpligt TCS-system i detta mastersexamensprojekt, varefter det slutliga systemet implementerades och utvärderades numeriskt för de önskade förhållandena. Den numeriska utformningen och optimeringen av det valda TCS-systemet utfördes här med hjälp av programvaran Aspen Plus (version 9), som innehåller både vätskor och fasta ämnen i en simuleringsmiljö, med konstant fysiska egenskaper. Detta TCS-system är utformat för att lagra och släppa värme vid cirka 80 °C och 8 bar genom absorption och desorption med användning av två identiska reaktorer respektive. Varje reaktor innefattar cirka 1 kg (närmare bestämt 0.985 kg) strontiumkloridsalt reagerande med 1.7 kg ammoniak. Ett verifieringssystem modelleras också i Aspen med hjälp av tillgängliga experimentella data från litteraturen. I detta anpassades den modellerade nya systemdesignen till denna valda andra verifieringssystemlayout från litteratur, som använder samma reaktionspar, men under olika driftsförhållanden. Denna anpassade systemdesign i Aspen användes sedan för att verifiera den valda konfigurationen och tillförlitligheten för det designade systemet för NHS-projektet. Här erhålls ett bra avtal för denna verifieringssystemdesign mellan Aspenmodellresultaten och experimentdata. Här utförs också en känslighetsanalys för det utformade TCSsystemet i det aktuella projektet för att identifiera de optimala driftsförhållandena och beteendet för de valda viktigaste parametrarna i systemet. Det konstruerade systemet ger en energilagringskapacitet på 0.5 kWh för de specifika mängderna (i volymflöde) av ammoniak och monoamin av strontiumklorid, som kommer från analysen, av 1.08696 e-05 kmol/s och 1.5528 e-06 kmol/s respektive. För dessa specifika värden på värmeöverföringsvätskan visade analysen att de volymetriska flödeshastigheterna för värme och kalla yttre källor måste vara 1.56 l/min (vilket minskar när temperaturen på värmeöverföringsvätskan ökar) och 0.42 l/min (som ökar när temperaturen på värmeöverföringsvätskan ökar). Sammanfattningsvis presenterar denna studie ett ammoniak-SrCl2 TCS-bänkskålsystem som möjliggör kontinuerlig värmelagring och frigöring, har en design som är lätt att anpassa och föreslår också optimala driftsförhållanden.

Le couple zéolite/H2O, qui présente une densité énergétique importante et remplit les conditions d’innocuité requises pour un système de stockage de chaleur pour l’habitat, est mis en œuvre dans réacteur modulaire à lit fixe. Un modèle monodimensionnel de transferts couplés de masse et de chaleur dans un lit fixe de grains de zéolite parcourus par un flux d'air humide été élaboré. Ce dernier a été conçu de façon à pouvoir intégrer rapidement des données sur de nouvelles générations de matériaux et coupler le réacteur à d’autres modèles : bâtiment/sous-station/quartier. L'étape de validation expérimentale montre que le modèle permet une estimation satisfaisante de l'autonomie, la durée d'amorçage et la puissance moyenne fournie en phase de décharge ainsi que la durée de charge. Ce modèle est donc un bon outil de dimensionnement et de pilotage du réacteur. L'analyse de sensibilité a montré que l'amélioration des prévisions du modèle requiert une évaluation plus précise de la chaleur complémentaire de sorption et de la porosité du lit. Après avoir estimé les besoins de chauffage d'une maison BBC deux dimensionnements ont été proposés afin d'effacer soit l'hyper-pointe de 18h - 20h soit la semaine la plus froide. Si la première stratégie aboutit à un système de stockage plus compact, la seconde permet de réduire le nombre de cycles marche/arrêt. Pour un îlot de 50 maisons BBC, la notion de foisonnement est considérée lors de l'estimation des besoins en chauffage pendant la semaine la plus froide. La phase de charge du système de stockage se ferait par le biais de la chaleur fatale récupérée dans l'industrie. Pour des stratégies d'effacement similaires (semaine la plus froide en hiver), un volume équivalent de 544 litres par maison dans l'îlot suffit pour répondre aux besoins de chauffage à Nancy contre 580 litres pour une maison BBC seule. / Heat storage systems for residential house heating could contribute to smoothing the load curve and would help prevent the use of the most polluting power plants or electricity imports during consumption peaks. Thermochemical heat storage systems are suitable for the intended application since they have high energy densities and low thermal losses. This thesis focuses on the design of an adsorption heat storage system that would be used to shed the load curve of the heating device of a house or residential district during the winter peak consumption periods. The zeolite/H2O pair, which has interesting features such as a high energy density and meets the conditions of safety required for a heat storage system for housing, is implemented in a modular fixed bed reactor. A 1D pseudo-homogeneous model was developed in order to simulate the performance of a fixed bed of zeolite during the adsorption and desorption of water. The latter was designed so as to facilitate the integration of data on new generations of materials and model couplings. The need to obtain data on the sorption properties of the zeolite/H2O pair to have reliable simulation results has been demonstrated, particularly at low partial pressures of water vapor and under the operating conditions selected. The experimental validation phase shows that the pseudo-homogeneous model provides a satisfactory estimate of criteria such as the autonomy, the responsiveness and the average power delivered during the discharging phase and the charging time. The model is thus a good sizing and management tool of the reactor. A sensitivity analysis, with the method of Morris, showed that improved model estimates require a more accurate assessment of the additional heat of sorption and porosity of the bed. After assessing the heating needs of the LEB house with a thermal model of the latter in cold climate conditions, two heat storage reactors were sized in order to shed the heating system's load curve either between 6 and 8pm or during the coldest week of the year. While the first strategy results in a more compact storage system, the second makes it possible to reduce the number of on/off cycles. The need for predictive control for monitoring the storage system was highlighted. As for the residential district of 50 LEB houses, diversity is considered when estimating the heating needs of the latter during the coldest week in Nancy. The heat source during the charging phase of the container would be industrial waste heat. During the coldest week, two sizings are suggested. For similar load shedding strategies, the comparison of the equivalent storage volume per house in the district with the storage volume for a single house serves highlights the importance of taking into account diversity. In order to meet the heating needs in Nancy, an equivalent volume of 544 liters per house in the district is sufficient whereas 580 liters are needed for a LEB house.

Submitted by Marco Antonio Oliveira da Silva (maosilva@ipen.br) on 2017-11-08T16:29:11Z No. of bitstreams: 0 / Made available in DSpace on 2017-11-08T16:29:11Z (GMT). No. of bitstreams: 0 / Nesse trabalho foram produzidas nanopartículas (NPs) de Gd2O3 e Er2O3 para aplicação como radiossensibilizadores em feixes de radioterapia. Elas foram sintetizadas no Laboratório de Interações Hiperfinas do IPEN pelo método da decomposição térmica e caracterizadas utilizando difração de raios-X, para verificar a estrutura cristalina, microscopia eletrônica de transmissão, para obter informações sobre forma, tamanho e distribuição de tamanho, análise por ativação neutrônica, por meio da qual foi possível determinar a pureza das amostras e calcular a concentração de gadolínio e érbio. Medições de magnetização e de espectroscopia de correlação angular γ-γ perturbada (PAC) foram realizadas a fim de estudar o comportamento magnético e a interação quadrupolar das partículas, respectivamente. Os resultados da caracterização mostram a formação de uma estrutura cristalina do tipo bixbyite, com aproximadamente 5 nm de diâmetro e estreita distribuição de tamanho, para as amostras pós-síntese. A determinação da massa de terra-rara em cada amostra foi importante para realizar a normalização nas medições de susceptibilidade magnética, tornando possível a visualização de um grande aumento na magnetização abaixo de 30 K, nas amostras pós-síntese, o que não é observado em partículas maiores, além de um aumento no momento magnético efetivo das NPs em relação aos respectivos bulks e uma mudança na temperatura de ordenamento antiferromagnético para o Er2O3. Os resultados da espectroscopia PAC evidenciam possíveis efeitos de superfície. A falta de uma frequência bem definida nas amostras de 5 nm indicam que a quantidade de 111In(111Cd) na superfície da partícula é maior do que no interior da mesma, fazendo com que a interação hiperfina do núcleo de prova com o host não seja evidente. Já a união da técnica de difração de raios-X com a espectroscopia PAC foi fundamental para o entendimento do dano causado às partículas pela irradiação com 60Co. Quanto às medições de radiossensibilização a dosimetria Fricke gel foi fundamental para a verificação de um fator de aumento de dose (DEF) de até 1,67 e 1,09 para NPs de Gd2O3 irradiadas com 60Co e 6MV, respectivamente. Nas mesmas condições, para as amostras de Er2O3, foram encontrados valores de DEF de até 1,37 e 1,06. Isso comprova os efeitos radiossensibilizadores dessas NPs. Os resultados alcançados nesse trabalho não apenas fornecem dados importantes para o estudo de NPs de terra-rara na área de física da matéria condensada como também uma base sólida para a aplicação desses elementos como radiossensibilizadores em feixes de radioterapia, possibilitando a utilização da imagem por ressonância magnética para localizar e obter a concentração dessas NPs dentro do paciente, aumentando assim a eficiência do tratamento do câncer. / Tese (Doutorado em Tecnologia Nuclear) / IPEN/T / Instituto de Pesquisas Energéticas e Nucleares - IPEN-CNEN/SP

Les sources d’énergies renouvelables représentent un gisement intéressant mais l’intermittence de leur production impose une meilleure anticipation des besoins et la mise en place d’un système de stockage d’énergie. Le stockage thermochimique par adsorption dans un système intégrant le couple zéolithe 13X/eau semble être une solution adaptée à un stockage de l’énergie à basse température pour une application aux bâtiments. Notre objectif consiste à reproduire le comportement de ce type de problèmes thermiques non-linéaires. En effet, une simulation précise et rapide du comportement du système sélectionné permettrait une régulation lors de son utilisation. Un modèle bidimensionnel de stockage d’énergie dans un adsorbeur cylindrique a été développé. La résolution numérique de ce modèle, dit d’ordre élevé, implique l’intégration d’un système de quelques centaines à quelques milliers d’équations fortement non-linéaires et couplés. Les coûts de calculs générés pouvant être prohibitifs, l’application d’une méthode de réduction a ainsi été envisagée afin de conserver les caractéristiques, le couplage des transferts de chaleur et de masse ainsi que les non-linéarités de ce modèle tout en limitant le temps de calculs. La projection de Galerkin des équations de ce dernier sur la base, obtenue grâce à une décomposition orthogonale aux valeurs propres, permet de construire un système dynamique d’ordre faible. Sa résolution est moins coûteuse que celle du modèle d’ordre élevé et reproduit correctement la dynamique de l’adsorbeur. / Renewable energy sources will play a key role in meeting future energy demand. One major criticism of those sources stands in their intermittency requiring both a more effective management of demand and efficient storage systems. We focus on thermo-chemical storage by adsorption-desorption mechanism. Eco friendly, economically viable and suitable with solar energy temperature range made the zeolite 13X - water pair ideal for buildings applications. We built an energy storage model in a cylindrical adsorber which contains the mentioned zeolite13X - water pair. Energy storage has been modeled to present coupled heat and mass transfers thanks to a bi-dimensional model. The numerical simulations lead to the time-space evolution of the heating fluid and adsorbent temperatures and pressure. These knowledge models include typically a great amount of coupled differential equations to solve and strong non linearities. The originality of this study is to build a knowledge model of coupled heat and mass transfer in an adsorber and use the Proper Orthogonal Decomposition (POD) and Galerkin projection to build a minimal model of lower dimension without significant loose of accuracy.

This study shows how the composition of gases released from a single magmatic source may be modified during their ascending path. The main processes that influence the composition of the gases in these high temperature fumarolic environments, are: 1) interactions with wallrocks during gas ascent, which change the fugacities of the metal volatile species and affect the equilibrium between major species (fH2S/fSO2; fH2/fH2O); 2) mixing with meteoric water with consequent Cl adsorption, which may account for the Cl depletion of the gases; 3) remobilisation of previously formed sublimates and/or incrustation deposits. Comparison between the thermochemical models and the mineralogical composition of the silica tubes at Kudryavy and Satsuma-Iwojima volcanoes suggests that high fO2 due to the mixing of the gases with air during their injection into the atmosphere significantly reduces the volatility of several trace elements (As, Sb, Sn, Na, K, Tl, Te, Se and Cd). Comparisons between the enriched metals in aerosols and in the gases suggest that Mo, Pb, Bi, Na, K, Cu, Zn or Fe, which are enriched in the gases, are preferentially deposited in the gas conduits and vents whereas the highly volatile metals (Te, Tl, Sb, As and Se) and Cd condense in the plume.<p>This study determines the reactions that may occur during the alteration of rocks in high temperature fumarolic environments. Three different processes of alteration prevail: <p>(1) Acidic alteration which is characterized by the complete absence of clays, because the constant supply of gases to these systems allows for the pH values of the acidic fluids to be maintained low enough to prevent the precipitation of clay minerals. Complete leaching of all cations, except Si, from the primary silicates leads to important "silicification" of the wall rock. The primary mineral cations are leached in the following order: K, Na > Ca > Fe, Mg > Al > Si, Ti. The fluids enriched in these cations circulate in microcracks at different temperatures and different redox conditions and lead to the precipitation of secondary incrustations. At Kudryavy the incrustations are mainly sulfates. At Usu the lower sulfur/fluoride ratio of the gases allows the occurrence of aluminum fluoride incrustations. The order of primary minerals dissolution (olivine > plagioclase > pyroxene > matrix glass > Fe-Ti oxides) is established for both sites studied. <p>(2) Alteration by an oxidized volcanic gas, resulting from mixing with the atmosphere (500 to 300°C). At Kudryavy, thermochemical modeling suggests that anhydrite and anhydrous sulfates, which occur at intermediate temperatures, are formed by interactions of the rock with oxidized gas. <p>(3) The most important outcome of this work is the identification of the features of alteration by the volcanic gas that directly reacts with the rock at high temperatures (T > 500°C). The Kudryavy rocks show evidences for mineral transformations, which occur in the presence of the volcanic gas phase. Volcanic gas directly reacts with rocks at high temperatures (T > 500°C). The gas destabilizes the primary minerals, remobilizes the rock-bearing cations, and leads to the formation of second mineral assemblages. These transformations occur in situ, without significant mobility (gain or loss) of the cations. The high temperature secondary associations are characterized by the presence of andradite, hedenbergite, hercynite, tridymite/cristobalite. Anhydrite and anhydrous Al sulfate may occur within these mineral assemblages if the gas is oxidized.<p> / Doctorat en sciences, Spécialisation géologie / info:eu-repo/semantics/nonPublished

Die Vorhersage und Identifizierung von stabilen und metastabilen Stoffen ist ein wichtiges Instrument zur Bildung neuer Werkstoffe. Vor diesem Hintergrund gewinnen Konzepte einer rationalen Synthese zunehmend an Bedeutung: Die Berechnung der elektrochemischen Spannungsreihe für Festkörper und flüchtiger Phasen ermöglicht eine einfache Vorhersage der Reaktionswege. Unter Verwendung der elektrochemischen Spannungsreihe der Systeme As / P / O und As / P / X (X = F, Cl, Br, I) kann die Bildung von Elementallotropen über die Oxid- und Halogenidverbindungen in thermitischen Reaktionen abgeleitet werden. Die Analyse der Phasenbildung wird mit einer In-situ-Methode zur Überwachung von Gasphasenreaktionen gewonnen. Im Verlauf der Phasenformationen - zur Erreichung des Fest-Gas-Gleichgewichtes - können charakteristische Effekte beobachtet werden. / The prediction and identification of stable and metastable substances is an important tool to achieve new materials. With this objective in mind, concepts of a rational synthesis are gaining increasing importance: calculation of electromotive series of solids allows easy prediction of reaction pathways. Using the electromotive series of systems As/P/O and As/P/X (X = F, Cl, Br, I) the formation of element allotropes via the oxide and halide compounds in thermite type reactions can be deduced. The analysis of phase formation is acquired with an in situ method for monitoring gas-phase reactions. In the course of phase formations - attaining the solid-gas equilibrium state - characteristic effects can be observed.

Cette thèse décrit le développement de procédés utilisables pour valoriser des extraits de bois afin de préparer : (1) des combustibles (hydrocarbures) liquides ; (2) des matériaux poreux avec des applications potentielles dans les domaines de l’énergie et l’environnement, notamment isolation thermique, catalyse, piégeage et séparation de micropolluants. Les extraits de bois en question sont des lignines, associées ou non à des tannins. Les deux types de matériaux sont actuellement peu valorisés, et l’on montre qu’ils peuvent être source de valeur ajoutée au travers des procédés rapportés dans ce mémoire / The present thesis describes the development of processes which can be used for valorizing wood extracts in the aim of preparing: (1) liquid (hydrocarbon) fuels; (2) porous materials with potential energy and environmental applications, namely thermal insulation, catalysis, abatement or separation of micropollutants. The wood extracts in question are lignins, associated or not with tannins. Both kinds of materials are presently poorly valorized, and it is shown here that they can lead to high added-value products through the processes reported in this PhD dissertation

Le soufre est présent dans les systèmes pétroliers à la fois sous forme organique et minérale. Il est impliqué dans de nombreuses réactions d'oxydoréduction qui affectent la qualité des huiles (par des réactions de sulfuration ou de désulfuration) et du gaz naturel (par la génération de H2S en contexte de réduction thermochimique des sulfates), ainsi que la porosité des roches réservoirs (par la dissolution de l'anhydrite ou la précipitation de soufre élémentaire ou de pyrobitume). Ces réactions sont gouvernées par la température (et dans une moindre mesure la pression), les conditions d'oxydoréduction et la composition chimique globale du système. La thèse comporte trois parties : (1) une étude thermodynamique des réactions chimiques impliquant le soufre dans les bassins sédimentaires ; (2) une étude expérimentale des réactions de sulfuration et de désulfuration des composés organiques ainsi que de la réduction thermochimique des sulfates; (3) une étude pétrographique et d'inclusions fluides sur des échantillons d'un réservoir carbonaté du bassin Pré-Caspien / Sulfur occurs in petroleum systems as both organic compounds and minerals as well as under different oxidation states. It is involved in a number of redox reactions which may impact the quality of crude oils (through sulfurization or desulfurization reactions) and natural gas (through the generation of H2S during thermochemical sulfate reduction), as well as the petrophysical properties of reservoir rocks (through the dissolution of anhydrite and the precipitation of elemental sulfur and pyrobitumen). These reactions are controlled by temperature (and to a lesser extent pressure), the redox conditions, and the overall chemical composition of the system representing the petroleum reservoir. The thesis consists of three parts: (1) a thermodynamic study of chemical reactions involving sulfur which occur in sedimentary basins; (2) an experimental simulation of sulfurization and desulfurization reactions of organic compounds, as well as of thermochemical sulfate reduction; and (3) a petrographic and fluid inclusion study of carbonate rock samples from a sulfur-rich hydrocarbon reservoir of the northern Caspian Sea

The prediction of detonation properties of the new generation of high-nitrogen energetic materials (HNEM) is based on knowledge of their heats of formation, which are sum of values of particular nitrogen heterocyclic fragments. The diploma thesis describes theoretical calculations of heats of formation in gas phase ?f H°(298,g) for series of azines (number of N atoms 2-6) and azoles (number of N atoms 2-5) by means of quantum chemical methods. The semiempirical methods as PM3, DFT methods utilizing isodesmic approach and finally thermochemical G-recipes were used. All calculated values of heats of formation were scrutinized and for future application to HNEM materials the DFT B3LYP/cc-pVTZ method and thermochemical recipe T1 were recommended.