Understanding the drivers of climate change requires knowledge about the global carbon (C) cycle. Although inland waters play an important role in the C cycle by emitting and burying C, streams and lakes are in general overlooked in bottom-up approached C budgets. In this thesis I estimated emissions of carbon dioxide (CO2) and methane (CH4) from all lakes and streams in a 15 km2 subarctic catchment in northern Sweden, and put it in relation to the total catchment C exchange. I show that high-latitude aquatic systems in general and streams in particular are hotspots for C emission to the atmosphere. Annually, the aquatic systems surveyed in this study emitted about 10.8 ± 4.9 g C m-2 yr-1 (ca. 98 % as CO2) which is more than double the amount of the C laterally exported from the catchment. Although the streams only covered about 4% of the total aquatic area they emitted ca. 95% of the total aquatic C emission. For lake emissions, the ice break-ups were the most important annual events, counting for ca. 45% of the emissions. Overall, streams dominated the aquatic CO2 emission in the catchment while lakes dominated CH4 emission, 96 % and 62 % of the totals, respectively. When summing terrestrial and aquatic C fluxes together it showed that the aquatic emissions alone account for approximately two thirds of the total annual catchment C loss. The consequence of not including inland waters in bottom-up derived C budgets is therefore a risk of overestimating the sink capacity of the subarctic landscape. However, aquatic systems can also act as C sinks, by accumulating C in sediment and thereby storing C over geological time frames. Sediment C burial rates were estimated in six lakes from a chronology based on 210Pb dating of multiple sediment cores. The burial rate ranged between 5 - 25 g C m-2 yr-1, which is of the same magnitude as lake C emissions. I show that the emission:burial ratio is about ten times higher in boreal compared to in subarctic-arctic lakes. These results indicate that the balance between lakes C emission and burial is both directly and indirectly dependent on climate. This process will likely result in a future increase of C emissions from high-latitude lakes, while the C burial capacity of these same lakes sediments weaken.

Ce travail a pour objectif de comprendre les mécanismes mis en jeu lors de l'application d'un gradient de champ magnétique sur le développement d'une flamme de diffusion laminaire décrochée. Les propriétés de ce type de flamme dépendent beaucoup des vitesses d'éjection, de la géométrie du brûleur et du nombre de Scmidt des carburants. Nous avons ici considéré une configuration d'une flamme laminaire de diffusion de méthane/air, issue d'un brûleur coaxial, débouchant dans de l'air ambiant. Le champ magnétique est généré par un aimant permanent. L'étude expérimentale montre que la hauteur de décrochage est très sensible au débit d'air mais peu au débit de méthane. L'application du champ magnétique permet de réduire la hauteur de décrochage et renforce la stabilité de la flamme. L'étude numérique a été conduite dans le cas sans et avec champ, à partir d'un code CFD dans lequel, deux modifications ont été apportées : ajout d'un modèle de rayonnement qui permet de prendre en compte les pertes radiatives des gaz chauds et prise en compte de l'influence du champ magnétique par l'ajout d'une force volumique dans l'équation de quantité de mouvement. Il a été montré que la hauteur de décrochage dépend fortement du débit d'air mais peu du débit de méthane. L'application du champ magnétique permet de réduire la vitesse de l'air et le gradient spatial de fraction massique de méthane, phénomènes importants dans la diminution de la hauteur de décrochage et dans l'augmentation de la vitesse de propagation de la flamme.

L'étude des fluides géologiques passe par la description précise des propriétés thermodynamiques des systèmes eau - gaz sur de larges gammes de températures, pressions et compositions à partir d'équations d'état. Les équations d'état cubiques de type Van der Waals couramment utilisées telles que Soave Redlich Kwong (SRK) ou Peng Robinson permettent des calculs simples à mettre en oeuvre sur de larges gammes de températures et de pressions à partir des paramètres critiques des fluides étudiés. En revanche, la précision de ces modèles se dégrade lorsque l'eau devient un composant majeur du mélange puisque ni l'association par liaisons hydrogène ni les interactions dipolaires ne sont prises en compte dans ces modèles.<br />Sur le principe de la factorisation des fonctions de partition, l'énergie de Helmholtz d'un fluide peut être écrite sous la forme de la somme des différentes contributions énergétiques. Le modéle développé ici pour H2O et H2S considère trois contributions : celle du fluide de référence de type Van der Waals prise en compte par une équation cubique, celle de l'association par liaison hydrogène par un terme issu du modèle Cubic Plus Association (CPA) et celle des interactions dipolaires entre molécules non liées par la théorie Mean Spherical Approximation (MSA). Le modèle CPAMSA ainsi proposé est à six paramètres ajustables dont trois sont des grandeurs physiques compatibles avec leur estimation expérimentale.<br />Les propriétés thermodynamiques de l'eau pure sont ainsi sensiblement mieux reproduites qu'avec le modèle CPA le long de l'équilibre liquide - vapeur et les extrapolations à plus hautes températures et pressions sont satisfaisantes. De même, la prise en compte des interactions dipolaires dans la molécule H2S améliore significativement les calculs volumétriques effectués avec une équation d'état cubique simple.<br />Des règles de mélange simples entre molécules dipolaires ont été élaborées afin de modéliser le système binaire H2O - H2S par une approche symétrique. Les compositions des phases à l'équilibre liquide - vapeur sont reproduites avec des écarts moyens aux données expérimentales inférieurs à 7% tout comme pour les systèmes H2O - CO2 et H2O - CH4. Excepté pour ce dernier système, les paramètres d'interaction binaire ajustés sur les données expérimentales sont proches de zéro confirmant que le modèle proposé prend bien en compte les principales contributions énergétiques de ces fluides.

Production of high-quality syngas from biomass gasification in a dual fluidised bed gasifier (DFBG) has made a significant progress in R&amp;D and Technology demonstration. An S&amp;M scale bio-automotive fuel plant close to the feedstock resources is preferable as biomass feedstock is widely sparse and has relatively low density, low heating value and high moisture content. This requires simple, reliable and cost-effective production of clean and good syngas. Indirect DFBGs, with steam as the gasification agent, produce a syngas of high content H2 and CO with 12-20 MJ/mn3 heating value. The Mid Sweden University (MIUN) gasifier, built for research on synthetic fuel production, is a dual fluidised bed gasifier. Reforming of tars and CH4 (except for methanation application) in the syngas is a major challenge for commercialization of biomass fluidised-bed gasification technology towards automotive fuel production. A good syngas from DFBGs can be obtained by optimised design and operation of the gasifier, by the use of active catalytic bed material and internal reforming. This thesis presents a series of experimental tests with different operation parameters, reforming of tar and CH4 with catalytic bed material and reforming of tar and CH4 with catalytic internal reformer.   The first test was carried out to evaluate the optimal operation and performance of the MIUN gasifier. The test provides basic information for temperature control in the combustor and the gasifier by the bed material circulation rate.    After proven operation and performance of the MIUN gasifier, an experimental study on in-bed material catalytic reforming of tar/CH4 is performed to evaluate the catalytic effects of the olivine and Fe-impregnated olivine (10%wtFe/olivine Catalyst) bed materials, with reference to non-catalytic silica sand operated in the mode of dual fluidised beds (DFB). A comparative experimental test is then carried out with the same operation condition and bed-materials but when the gasifier was operated in the mode of single bubbling fluidised bed (BFB). The behaviour of catalytic and non-catalytic bed materials differs when they are used in the DFB and the BFB. Fe/olivine and olivine in the BFB mode give lower tar and CH4 content together with higher H2+CO concentration, and higher H2/CO ratio, compared to DFB mode. It is hard to show a clear advantage of Fe/olivine over olivine regarding tar/CH4 catalytic reforming.    In order to significantly reduce the tar/CH4 contents, an internal reformer, referred to as the FreeRef reformer, is developed for in-situ catalytic reforming of tar and CH4 using Ni-catalyst in an environment of good gas-solids contact at high temperature.  A study on the internal reformer filled with and without Ni-catalytic pellets was carried out by evaluation of the syngas composition and tar/CH4 content. It can be concluded that the reformer with Ni-catalytic pellets clearly gives a higher H2 content together with lower CH4 and tar contents in the syngas than the reformer without Ni-catalytic pellets. The gravimetric tar content decreases from 25 g/m3 down to 5 g/m3 and the CH4 content from 11% down below 6% in the syngas.   The MIUN gasifier has a unique design suitable for in-bed tar/CH4 catalytic reforming and continuously internal regeneration of the reactive bed material. The novel design in the MIUN gasifier increases the gasification efficiency, suppresses the tar generation and upgrades the syngas composition. / Gasification-based Biorefinery for Mechanical Pulp Mills

As same as other countries in the world, China is also facing the problem of a severe shortage of energy. Specifically, the demand for natural gas is rising explosively after the energy consumption structure has changed from oil to gas. Due to various reasons and motivations, shale has been considered having great reserves and believed in alleviating the energy crisis. Nevertheless, the massive investment in developing shale has a disappointing interest with low-yielding production. Scholars have done many researches and experiments for investigating the causes and increasing the productivity of shale formation, in field and in laboratory respectively. Based on the statistics, more details, and further discussion, in this dissertation a probable method for more effectively producing was demonstrated. Although the hydro-fracturing technology has been conducted in field frequently, sometimes the decrease of permeability has been observed after the treatment. To figure out this phenomenon, the investigation started from the basic characterization of matrix. Believed in the most component in shale, quartz consisted of silica which could dissolve in fluid. Been assigned as variables, temperature, pH, and salinity have been implemented for explanation of dissolution. Temperature played a great role in the process. Combined with confining pressure, the reconsolidation happened inside samples. Through more experiments the mechanism of reconsolidation has been discovered that both confining pressure and temperature are necessary for gelling in fracture. Perspective on the whole formation, well logs were a super supplement to laboratory experiments. It serviced not only a further confirmation, but also pointed out the relationship between desorption capacity and different components. Samples from upper and lower formations have been used for going further. The exchange which exists between N2 and CH4 could be a great idea to exploit gas from reservoir. Feldspar supported space for adsorbed gas, and it was also easy to release. In contrast, the organic matter in which a network of pores developed has ability to trap the gas deeply because of the specific surface area. Quartz had positive effect on production because of containing the organic matter, while the influence of clay minerals on adsorption and desorption could be neglected. Based on the analysis of reconsolidation and desorption, an idea has been conceived using foam as fracturing fluid for increasing gas production. Compared to the pure fluid, foam has less water, which could prevent the reconsolidation. Nitrogen could be the gas to foam. The exchange between N2 and CH4 will increase the production of gas. In order to serve the condition that increases the time of exchange and makes negative effect on reconsolidation simultaneously, the foaming test with ABS and K12 has been evaluated first. For better stability of foam more experiment have been done. Three formulas were recommended which could keep the balance between the increasing viscosity and decreasing volume. The work interpreted in this thesis has enhanced our understanding of microscopic properties of shale and was expected to make contribution to further research of fracturing and production design.

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Tesis por compendio / [ES] El consumo actual de combustibles fósiles supone la emisión de millones de megatones de CO2 cada año, lo que ha tenido consecuencias potencialmente catastróficas como el efecto invernadero, la acidificación de los océanos y la eutrofización de las aguas, entre otras. Por lo tanto, la utilización de CO2 para la producción de combustibles y productos químicos de valor ha atraído mucho interés a lo largo de los años, especialmente empleando luz solar. A lo largo de los años, se han probado una gran variedad de materiales para tecnologías fotocatalíticas, principalmente TiO2, CdS, LDH, MOF y nitruros de carbono, entre otros. A pesar de esto, todos estos materiales adolecen de importantes inconvenientes, como una insuficiente captación de luz, estabilidad o baja producción. Y, por lo tanto, su aplicación en posibles tecnologías industriales fotocatalíticas es muy limitada a nivel industrial. Además de los procesos fotocatalíticos, que se componen principalmente de portadores de carga fotogenerados que facilitan las reacciones redox, los procesos fototérmicos representan una alternativa atractiva para las futuras tecnologías solares. La amplia utilización del espectro solar, el rápido calentamiento por irradiación de luz a través de "nanocalentadores" y "electrones calientes" que interactúan con sustratos son algunas de las características que conducen a los altos rendimientos catalíticos que generalmente se observan en las reacciones fototérmicas. En la presente tesis doctoral, se han empleado diferentes materiales, como clústeres de Fe incrustados en grafeno dopado con nitrógeno, hidroxiapatita dopada con Co y nanopartículas de Ru soportadas sobre titanato de estroncio, como catalizadores fototérmicos para la hidrogenación selectiva de CO2 a CO o metano, tanto en flujo discontinuo como continuo. Admás, se han investigado muchos factores que influyen en esta reacción, como la naturaleza de los grupos/nanopartículas metálicas incrustadas, las cantidades de dopantes y la influencia de la irradiación incidente, entre otros. Además de la catálisis fototérmica, la actual tesis doctoral también aborda procesos fotocatalíticos como la ruptura del agua o la reducción del O2 a H2O2, empleando nuevos compuestos de nitruro de carbono. Ya sea sensibilizando el fotocatalizador para la absorción de luz visible o mejorando las propiedades electrónicas mediante la formación de heterouniones, se lograron resultados fotocatalíticos notables. / [CA] El consum actual de combustibles fòssils suposa l'emissió de milions de megatons de CO2 cada any, cosa que ha tingut conseqüències potencialment catastròfiques com l'efecte hivernacle, l'acidificació dels oceans i l'eutrofització de les aigües, entre d'altres. Per tant, la utilització de CO2 per a la producció de combustibles i productes químics de valor ha atret molt interès al llarg dels anys, especialment emprant llum solar. Al llarg dels anys, s'han provat una gran varietat de materials per a tecnologies fotocatalítiques, principalment TiO2, CdS, LDH, MOF i nitrurs de carboni, entre d'altres. Tot i això, tots aquests materials pateixen importants inconvenients, com una insuficient captació de llum, estabilitat o baixa producció. I, per tant, la seva aplicació a possibles tecnologies industrials fotocatalítiques és molt limitada a nivell industrial. A més dels processos fotocatalítics, que es componen principalment de portadors de càrrega fotogenerats que faciliten les reaccions redox, els processos fototèrmics representen una alternativa atractiva per a les futures tecnologies solars. L'àmplia utilització de l'espectre solar, l'escalfament ràpid per irradiació de llum a través de "nanoescalfadors" i "electrons calents" que interactuen amb substrats són algunes de les característiques que condueixen als alts rendiments catalítics que generalment s'observen en les reaccions fototèrmiques. En aquesta tesi doctoral, s'han emprat diferents materials, com clústers de Fe incrustats en grafè dopat amb nitrogen, hidroxiapatita dopada amb Co i nanopartícules de Ru suportades sobre titanat d'estronci, com a catalitzadors fototèrmics per a la hidrogenació selectiva de CO2 a CO o metà, tant en flux discontinu com continu. A més, s'han investigat molts factors que influeixen en aquesta reacció, com ara la naturalesa dels grups/nanopartícules metàl·liques incrustades, les quantitats de dopants i la influència de la irradiació incident, entre d'altres. A més de la catàlisi fototèrmica, l'actual tesi doctoral també aborda processos fotocatalítics com ara la ruptura de l'aigua o la reducció de l'O2 a H2O2, emprant nous compostos de nitrur de carboni. Ja sigui sensibilitzant el fotocatalitzador per a l'absorció de llum visible o millorant les propietats electròniques mitjançant la formació d'heterounions, es van assolir resultats fotocatalítics notables. / [EN] Fossil fuel consumption accounts for millions of megatons of CO2 emitted every year, which has led to potentially catastrophic consequences such as the greenhouse effect, ocean acidification and water eutrophication, besides others. Thus, the utilization of CO2 for fuels and value chemicals has attracted much interest over the years, especially employing solar light. Over the years, a variety of promising materials have undergone trial for potential photocatalytic technologies, mainly TiO2, CdS, LDHs, MOFs and carbon nitrides among others, yet all these materials suffer from important drawbacks such as insufficient light harvesting, stability, or low production outputs, hence limiting their application in potential photocatalytic industrial technologies. Besides photocatalytic processes, mainly comprising of photogenerated charge carriers that facilitate redox reactions, photothermal processes represent an attractive alternative for future solar technologies. Broad utilization of the solar spectrum, strong heating upon light irradiation through "nano-heaters" and possibly "hot electrons" interacting with either semiconductors or substrate molecules are some characteristics that lead to the high catalytic outputs generally observed in photothermal reactions. In the current doctoral thesis, different materials such as Fe clusters imbedded on nitrogen doped graphene, Co doped hydroxyapatite and Ru nanoparticles supported on strontium titanate have been employed as photothermal catalysts for the photothermal hydrogenation of CO2 to either CO or methane, under both batch and flow conditions. Thus, many factors influencing this reaction have been investigated, such as the nature of embedded metallic clusters/nanoparticles, dopant amounts and the power of incident irradiation among others. Besides photothermal catalysis, the current doctoral thesis also addresses photocatalytic processes such as water splitting or O2 reduction to H2O2, employing novel carbon nitride composites. By either sensitizing the photocatalyst for visible light absorption or enhancing the electronic properties through heterojunction formation, remarkable photocatalytic outputs were achieved. / Szalad, H. (2024). Production of Solar Fuels Employing Different Materials Via Photocatalytic or Photothermal Pathways [Tesis doctoral]. Universitat Politècnica de València. https://doi.org/10.4995/Thesis/10251/206848 / Compendio

Cette thèse touche à la problématique des échanges de gaz aux interfaces entre la géosphère, la biosphère, l'hydrosphère et l'atmosphère par l'intermédiaire du monitoring géochimique des gaz appliqué aux sites de stockage géologiques du CO2. Au niveau de l'axe « Métrologie », nous avons développé une plate-forme de monitoring géochimique continu, in situ et déportée par spectrométrie FTIR/Raman pour la mesure des gaz du sol (CO2, CH4, N2, O2, H2O). Des protocoles de quantification ont été développés pour la mesure par télédétection infrarouge terrestre en mode passif du CO2, CH4, SO2, H2S dans l'atmosphère. Au niveau des axes « Monitoring » et « Modélisation », les mesures de gaz du sol à proximité du puits d'injection de Rousse (Pilote CO2 Total, Lacq/Rousse, France) sur plus de sept cycles saisonniers ont montré une anti-corrélation entre la teneur en CO2 et les variations du niveau piézométrique de la nappe. Cette relation a permis de modéliser l'enveloppe de variabilité « naturelle » de la teneur en CO2 dans le sol, qui constitue un élément clé pour la surveillance des sites de stockage. Les variations majeures de teneur en CO2 sont attribuées à des processus de dissolution/libération de CO2 par la nappe, jouant un rôle de pompe à CO2. La concentration en CO2 en surface (+1m) serait gouvernée par les variations de teneur en CO2 du sol. Les mesures par télédétection FTIR des gaz dans l'atmosphère ont permis d'établir pour la première fois une simulation expérimentale 3D des enveloppes de CO2 à l'aplomb du site d'injection. Ces résultats constituent un premier pas vers la mise en place d'un outil de surveillance des panaches gazeux dans l'atmosphère / This study is based on the problematic of gas exchanges at the interface between the geosphere, biosphere, hydrosphere and atmosphere through the geochemical monitoring of gas applied to CO2 geological storage sites. Concerning the "Metrological" aspect, we developed and implemented an in situ continuous geochemical monitoring station, based on coupling FTIR/ Raman spectrometry for measuring soil gas (O2, N2, CO2, CH4 and H2O) close to the injection wells of Rousse 1 (CCS Total pilot, Lacq-Rousse, France). We also developed protocols to identify and quantify CO2, CH4, SO2, H2S in the atmosphere (plume) by passive remote sensing FTIR. On the "Monitoring" and "Modelling" aspects, the continuous recording of soil CO2 concentration during more than 7 seasonal cycles indicate that CO2 concentration in the soil was anti-correlated with changes in piezometric level of the groundwater. This correlation was used to model the limits of natural variability of CO2 content in the soil, which is a key to CCS sites monitoring. The main fluctuations in soil CO2 content was assigned to a dissolution/release process of CO2 by the perched water table, acting as a CO2 pump. The CO2 concentration at the near surface (+ 1 m) would be governed by changes of the soil CO2 content. FITR remote sensing measurement of atmospheric gases allowed for the first time to perform an experimental 3D simulation of CO2 layers on the injection site. This type of experimental simulation is a first step for the monitoring of gases in the atmosphere