Long-lived and short-lived volcanic vents often form in close proximity to one another. However, the processes that distinguish between these volcano types remain unknown. Here, I investigate the differences of long-lived (shield volcano) and short-lived (cinder cone) magmatic systems using two approaches. In the first, I use melt inclusion volatile contents for shield volcanoes and compare them to published data for cinder cones to investigate how shallow magma storage conditions differ between the two vent types in the Oregon Cascades. In the second, I model the primitive magmas that fed shield volcanoes and compare these compositions to those of nearby cinder cones to determine if the volcanoes are drawing magma from the same sources. The volatile concentrations suggest that long-lived and short-lived magmatic plumbing systems are distinct. Modeling of parental magmas and differentiation processes further suggest that long-lived and short-lived volcanoes have erupted lava from the same mantle magma source.

This PhD thesis experimentally studies the volumetric efficiency of gerotor pumps in aero-engine gas turbine oil systems. This efficiency is the ratio of the effective measured flow rate and the theoretical flow rate computed based on pump displacement. In case of low inlet pressure and high rotational speed, which is often the case in aeronautical applications, the pump performance is severely affected by cavitation. This phase change from liquid to vapour causes a large portion of the flow to be occupied by gas, reducing the volume available for the liquid and reducing the overall mass flow rate. Due to its nature, the lubrication oil used in gas turbine engines is subjected to aeration which is the dissolution of air in oil. The air is dissolved in the liquid at high ambient pressure and released at lower pressure causing more air to occupy the cavities inside the pump. The change in liquid aeration is a relatively slower phenomenon causing the variation of aeration to be delayed with respect to the actual pressure and therefore varying also accordingly to the previous oil condition.The essential part of the work presented in this thesis is based on experimental research realised at the ATM department. This was conducted on a dedicated oil system test rig. This rig is build to reproduce the complete set of operating conditions encountered in a flying embedded oil system. This test rig was modified and equipped with several specific measurement systems to acquire data on pump performance and oil aeration. Precisely, a series of single-phase performance characterisations and transients have been recorded. The oil aeration was measured with two density-based instruments. The pump outlet pressure was recorded with a high-frequency pressure transducer. A new set-up of the test rig was also developed to allow the testing of pumps in two-phase flows conditions. Two-phase flows performance characterisations and transients have then also been studied.The data processing provided information necessary to build empirical models and to understand pump and cavitation behaviours. The focus is on pump performance in cavitation. This justify the extensive use of the cavitation number indicating the tendency of a flow to experience cavitation in given conditions. The base models can be used to determine if a given condition leads to cavitation or not, and predict the pump efficiency in both cases. The high-frequency pressure measurements provided an efficient tool to detect cavitation. / Doctorat en Sciences de l'ingénieur et technologie / info:eu-repo/semantics/nonPublished

The 40 kg melt was degassed by two methods: Immersion of a degassing tablet in a melt by an immersion bell and an argon degassing through a lance with a porous plug. Up-gassing tablets were also used during the experiment. The method of double weighing was used for evaluation. No technically significant degassing was achieved using degassing tablets. After degassing with tablets was observed a decrease in DI (Dichte Index) value with increasing residence time. Excessive dosing of the tablet does not ensure a higher degassing effect, it only ensures a higher turbulence of the reaction. Preheating the degassing tablets before use does not affect degassing. By preheating the up-gassing tablets, their reactivity is reduced. Two immersion bells with different proportions were tested. The bells do not ensure a homogeneous dispersion of bubbles in the melt. By argon degassing through the porous plug, the melt was degassed to a value DI = 1,87 %. The consumption of argon for degassing smaller amounts of melt is higher than for degassing larger amounts of melt. Argon refining is more efficient than using tablets.

The aim of the present work was to get an overview of the steel cleanness in tool steel. Plant trial studies of three steel grades were done with different focuses. Firstly the change of the inclusion characteristics during the vacuum degassing in the ladle was looked upon. The top slag composition was altered and sampling was made before and after vacuum degassing and the results showed that the top slag composition has an effect on the inclusion composition. Thermodynamic calculations indicated that the oxygen activity for the steel/inclusion was twice as large as that of the steel/top slag before vacuum degassing. However, after vacuum degassing the oxygen activity values were close. In order to study the inclusion characteristics during vacuum degassing the process was interrupted at five pre-determined time points for sampling. During vacuum the number of the smaller inclusions was decreased. However, for the larger inclusions (&gt;11.2µm) the number of inclusions had increased. Throughout the degassing process the inclusion composition was found to approach the top slag composition and at the end of the process only one type of inclusion composition was found. The removal of hydrogen, nitrogen and sulphur was studied. Samples were taken before and after vacuum degassing. It was found that the removal kinetics of hydrogen and nitrogen can be described with first-order reactions. When 10 minutes of vacuum degassing have passed, the removal of hydrogen and nitrogen is more or less finished for the studied steel grades. Two steel grades with similar process route and with only a few differences in steel composition were studied. The sum of FeO and MnO was found to be a clear indicator for when reoxidation had taken place. The results from oxygen activity calculations indicate that calculations of oxygen activities with multivalence slag species such as Fe and Cr requires measurements for validations to ensure that reliable results are obtained. / Syftet med denna studie var att få en överblick av verktygsståls renhet. Studier på tre olika stålsorter utfördes. Inneslutningsbilden under vakuumbehandling undersöktes. Resultaten är baserade på industriförsök likväl som termodynamiska beräkningar. Försöken gjordes på två olika stålsorter där toppslaggens sammansättning varierades och stål- och slaggprover tog ut före och efter vakuumbehandling. Proverna analyserades för att bestämma den kemiska sammansättningen på stål och slagg, men inneslutningsbilden undersöktes också. Med hjälp av termodynamiska beräkningar beräknades syreaktiviteten för jämvikterna stål/inneslutning och stål/toppslag. Beräkningarna jämfördes sinsemellan samt med uppmätt syreaktivitet från stålsmältan. Resultaten visar att toppslaggens sammansättning har en påverkan på inneslutningarnas sammansättning. Specifikt så fanns att när CaO-halten i toppslaggen ökar syns en ökning av CaO i inneslutningssammansättningen. De termodynamiska beräkningarna visar att syreaktiviten för jämvikten stål/inneslutning är dubbelt så stor som den för jämvikten stål/topplagg före vakuumbehandling. Dock är syreaktiviteterna för de olika jämvikterna lika efter vakuumbehandlingen. För att studera hur inneslutningsbilden utvecklas under vakuumbehandling avbröts vakuumbehandlingen vid fem förutbestämda tidpunkter. Vid varje avbrott av vakuumbehandlingen togs stål- och slaggprover som analyserades för att bestämma totalsyre, inneslutningsmängd och inneslutningssammansättning. Före vakuumbehandlingen var antalet inneslutningar stort, medan antalet små inneslutningar minskade under vakuumbehandlingen. Däremot konstaterades att antalet stora inneslutningarna (&gt;11.2μm) ökade under avgasningen. Vad beträffar inneslutningssammansättningen syntes en variation i analys före vakuumbehandlingen som sedan förändrades till att likna toppslaggens sammansättning under vakuumbehandlingstiden. I slutet av processen märktes endast en typ av inneslutningssammansättning i stålsmältan. Vad som också noterades var att efter ungefär 10 minuter av vakuumbehandling så hade inneslutningsantalet nått sitt minimumvärde. För att erhålla rent stål är väte-, kväve- och svavelreningen också av stor vikt under vakuumbehandlingen. Dessa tre element studerades genom att prover togs vid olika tillfällen i processen; före, under (vid fem olika förutbestämda tidpunkter) och efter vakuumbehandling. De kemiska sammansättningarna för stål- och slaggproverna användes för att beräkna väte-, kväve- och svavelreningarna. Beräkningarna visade att för väte och kväve så kan kinetiken beskrivas med en förstagradsekvation. Specifikt så gäller detta för stålsorten i studien, samt under förutsättningen att svavelhalten är lägre än 0,003 vikts-%. Dessutom så visade resultaten att väte- och kvävereningen är i stort sett klar för den studerade stålsorten efter 10 minuters vakuumbehandling. När det gäller svavel så kan en förstagradsekvation inte användas vid beräkningarna Istället uppvisar svavel en tendens att följa jämviktshalten av svavel genom hela avgasningsprocessen. Genom att kontrollera processen finns stora möjligheter att erhålla en bra renhet på stålet. Två stålsorter studerades i denna specifika studie, där de hade en liknande processväg samt endast ix några små skillnader i stålanalysen. Stål- och slaggprover samlades in och analyserades. Summan av FeO och MnO visade sig vara en klar indikation på när reoxidation har skett, men mängden "carry-over" slagg från ljusbågsugnen kunde inte predikteras med hjälp av någon specifik indikator. Dessutom så beräknades syreaktiviten och beräkningarna jämfördes sedan med uppmätt syre i stålet. Resultaten indikerar att beräkningar av syreaktivitet med toppslagger som innehåller multivalenselement, såsom Fe och Cr, kräver valideringar med mätningar för att trovärdiga predikteringar ska erhållas. / <p>QC 20160523</p>

"Aluminum alloy cleanliness has been in the limelight during the last three decades and still remains as one of the top concerns in the aluminum casting industry. In general, cleaning an aluminum alloy refers to minimizing the following contaminants: 1) dissolved gases, especially hydrogen, 2) alkaline elements, such as sodium, lithium, and calcium, and 3) unwanted solid particles, such as oxides, carbides, and a variety of intermetallic compounds. Extensive research has resulted in significant improvements in our understanding of the various aspects of these contaminants, and in many foundries, melt-cleansing practices have been established and are routinely used. However, with the ever-increasing demands for improved casting properties, requirements for molten metal cleanliness has become extremely stringent. Rotary degassing is one of the most efficient ways of cleansing molten metals, thus removal of unwanted particles and dissolved hydrogen from molten aluminum alloys by rotary degassing has become a widely used foundry practice. Rotary degassing involves purging a gas into the molten alloy through holes in a rotating impeller. Monatomic dissolved hydrogen either diffuses into these gas bubbles or it forms diatomic hydrogen gas at the bubbles’ surface; in any case, it is removed from the melt with the rising bubbles. Simultaneously, solid particles in the melt collide with one another due to turbulence created by the impeller and form aggregates. These aggregates either settle to the furnace floor, or are captured by the rising gas bubbles and are also removed from the melt. The objective of this work is to understand the physical mechanisms underlying the removal of dissolved hydrogen and unwanted solid particles from molten aluminum alloys by the rotating impeller degasser, and to develop a methodology for the effective use of the degassing process by providing mathematical models and computer simulations of the process. The models and simulations can be used to optimize the process, design new equipment and determine the cause of specific operational problems."

Afin de parvenir à une meilleure compréhension de la dynamique d’ascension et d’éruption des magmas basaltiques, nous avons réalisé des expériences de décompression à haute pression (200–25 MPa) et haute température (1200°C) spécifiquement orientées pour documenter la nucléation des bulles de gaz ; ce processus, qui constitue la première étape du dégazage magmatique, conditionne l’évolution de la phase gazeuse (force motrice des éruptions explosives) dans le conduit volcanique. Quatre principaux ensembles d’expériences ont été menés afin de mieux comprendre le rôle des volatils majeurs (H2O, CO2, S), ainsi que les effets de la vitesse d’ascension et de la présence de cristaux sur la cinétique de vésiculation (nucléation, croissance, coalescence) des bulles dans les magmas basaltiques. L’objectif est de comprendre les mécanismes qui contrôlent les caractéristiques texturales (nombre, taille, forme des bulles) et chimiques (teneur en volatils dissous, composition des gaz) des produits naturels et de les approcher expérimentalement. Dans ce sens, les verres expérimentaux ont été analysés avant et après décompression sur le plan textural (microtomographie par rayons X, MEB) et chimique (FTIR, microsonde électronique). Nos résultats démontrent une forte influence du CO2 sur les processus ainsi que sur le mode (équilibre vs. déséquilibre) de dégazage des magmas basaltiques, en lien avec des différences de solubilité et de diffusivité entre les espèces volatiles. Nos données, obtenues dans des conditions voisines des conditions naturelles, ont des implications volcanologiques pour l’interprétation des textures de bulles et des mesures de gaz en sortie de conduit, ainsi que, plus spécifiquement, pour la dynamique des éruptions paroxysmales au Stromboli. / For a better understanding of the dynamics of ascent and eruption of basaltic magmas, we have performed high pressure (200–25 MPa) and high temperature (1200°C) decompression experiments specifically oriented to document gas bubble nucleation processes. Bubble nucleation occurs first during magma degassing and, so, it is critical to understand bubble nucleation processes to constrain the evolution of the gas phase (which is the driving force of explosive eruptions) in the volcanic conduit. Four main sets of experiments were conducted to better assess the role of the major volatiles (H2O, CO2, S), as well as the effects of ascent rate and crystals, on bubble vesiculation (nucleation, growth, coalescence) kinetics in basaltic magmas. The aim of the study is to understand the mechanisms which control the textural (number, size, shape of bubbles) and the chemical (dissolved volatile concentrations, gas composition) characteristics of natural products, and also to approach them experimentally. In this way, experimental melts, before and after decompression, were analysed texturally (by X-ray microtomography and MEB) and chemically (by FTIR and electron microprobe). Our results demonstrate a strong influence of CO2 on degassing mode (equilibrium vs. disequilibrium) and mechanisms, which are shown to be controlled by differences in solubility and diffusivity between the main volatile species. Finally, our data, obtained under conditions closely approaching natural eruptions, have volcanological implications for the interpretation of bubble textures and gas measurements, as well as, more specifically, for the dynamics of Strombolian paroxysms.

Há uma demanda por competitividade entre as indústrias de aços, a fim de alcançar a excelência definida pelo termo clean steel. O processo de desgaseificação a vácuo (VD) ocorre durante o Refino Secundário de aços especiais. Sua principal função é remover gases indesejáveis, especialmente o hidrogênio. Entretanto, durante este processo, o fenômeno de flotação e a absorção de inclusões são reportados. O objetivo do presente trabalho foi estudar a viscosidade de escórias e a capacidade da estação de desgaseificação a vácuo do tipo tanque na limpeza de aços sob uma perspectiva industrial. Para realizar este objetivo, foram coletadas amostras de escória e aço antes e após a etapa de vácuo. Os resultados em limpeza de aço foram relacionados à energia de agitação durante o tratamento a vácuo (associada a um parâmetro cinético - βs) e ao efeito da viscosidade de escórias. É possível observar um decréscimo expressivo na população de inclusões entre as condições antes e após tratamento de desgaseificação a vácuo. A remoção de inclusões durante o vácuo atinge 64, 75 e 78% para as faixas de diâmetro de 2,5-5, 5-15 e ≥ 15 μm, respectivamente. Após o processo de desgaseificação, a composição das inclusões não-metálicas aproxima-se da composição química da escória. O processo de agitação na estação de desgaseificação a vácuo promove uma diminuição significativa na densidade de inclusões na faixa de diâmetro de 2,5-15 μm. Além disso, ao aumentar a intensidade do parâmetro cinético, a composição química de inclusões não-metálicas foi afetada e o teor de enxofre presente no aço líquido foi reduzido. Quanto às viscosidades efetiva das escórias, conclui-se que, para valores mais baixos (0,20 Pa.s) aumenta-se a capacidade da escória na remoção de inclusões, enquanto que valores mais altos (> 0,40 Pa.s) aparentaram ser prejudiciais à limpeza do aço. / There is a demand in competitiveness within the steel industry towards achieving excellence defined by clean steel term. The process of vacuum degassing (VD) occurs during the secondary refining of special steels. Its main function is to remove undesirable gases, primarily hydrogen. However, during this process, flotation phenomenon and inclusions absorption are reported. The aim of the present work was to study the slag viscosity and vacuum degassing (tank type) capacity in steel cleanliness from an industry perspective. To achieve this objective, slag and steel samples were taken before and after vacuum stage. The results in steel cleanliness were related to the stirring energy of the vacuum station (associated to a kinetic parameter – βs) and to the effect of slag viscosity. It is possible to observe an expressive decrease in the population of inclusions between the conditions before and after vacuum degassing treatment. The removal of inclusions during the vacuum stage reaches 64, 75 and 78% in the diameter ranges of 2,5-5, 5-15 and ≥ 15 μm, respectively. After the degassing process, the composition of non-metallic inclusions seemed to approach the slags’ chemical compositions. The stirring process in the vacuum degassing station promotes a significant decrease in the inclusion density with 2,5-15 μm diameter range. Also, by increasing the kinetic parameter intensity, the composition of non-metallic inclusions was affected. The sulfur content present in liquid steel was reduced. Regarding the effective viscosities of slags, it was concluded that lower values (0,20 Pa.s) increased slag capacity in inclusion removal, whereas higher values (> 0,40 Pa.s) was detrimental to steel cleanliness.

Thesis (M.S.)--Massachusetts Institute of Technology, Dept. of Materials Science and Engineering, 1981. / MICROFICHE COPY AVAILABLE IN ARCHIVES AND SCIENCE. / Includes bibliographical references. / by Kazuro Shirabe. / M.S.

<p>Biogas, a mixture of methane and carbon dioxide, is produced in the anaerobic digestion of sewage sludge. After anaerobic digestion, the digested sludge is often allowed to degas for one or two days. This gas is seldom utilised, but if the degassing could be accelerated, utilisation would be easier. Ultrasound can be used as a pretreatment method for waste activated sludge. It has a disintegrating effect on the sludge and causes lysis of bacteria in the sludge. It also speeds up the hydrolysis; the limiting step of anaerobic digestion of waste activated sludge. Ultrasound can be used to degas waterbased liquids. Ultrasonic degassing of sewage sludge has not been examined previously. The present study aims to investigate the effect of ultrasound on waste activated sludge as well as the potential of ultrasound to speed up the degassing of digested sludge. A semi-continuous, lab-scale digestion experiment was performed with four reactors: two receiving untreated sludge and two receiving treated sludge. The effect of the sonicator was 420 W and the treatment time was 6 min, which corresponds to an energy input of 8.4 kWh/m³. Total solids (TS) of the waste activated sludge was ~3.5 %. The ultrasonic treatment caused an increase in gas production of 13 %. There was no difference in methane content. The concentration of filterable chemical oxygen demand (fCOD) increased 375 %, or from 2.8 % to 11 % of total COD. In terms of energy loss/gain the increase in gas production resulted in a loss of 2.7 kWh/m³, i.e. more energy is needed to treat the sludge than the potential energy of the increased gas production. However, if the sludge is thickened to a TS >5 %, a net energy gain should be reached. The effect of ultrasound on the degassing of digested sludge was examined in three barrels. The degassing was measured with and without circulation as well as with ultrasonic treatment. The digested sludge had a gas emission rate of 115 L/(m³ day). No direct burst of gas occurred due to ultrasonic treatment. Over two days more gas was emitted from the barrel equipped with ultrasound, probably due to an induced post-digestion. Thus, ultrasonic pretreatment of waste activated sludge increases the biogas yield. It is inconclusive, whether ultrasonic treatment of digested sludge effects the degassing or not.</p>

<p>This thesis aims to measure the rate of radon loss from water in a systematic way. The dependence on surface area, temperature and concentration will be investigated. The experiments were done at UWC by creating radon using radium sources and then measuring the radon concentrations inside a vacuum chamber to obtain the speed of radon escape from the water. The results are compared to a model [Cal 2002] where the radon concentration in the air and hence the transfer rate is measured using a RAD7 radon detector. Since the equations cannot be solved analytically, a numerical solution is employed. The radon transfer velocity coefficient is found to be (1.9&plusmn / 0.5)&times / 10-6m/s. This value indicates that the escape of radon should not be a problem when a sample is open to the air for a minute or two.</p>