Il existe aujourd’hui une prise de conscience croissante visant à considérer les résidus de biomasse comme source potentielle d’énergie, de matériaux et de produits chimiques. Dans ce contexte, le projet européen Mobile Flip vise à développer des unités mobiles de conversion de biomasse pour la valorisation de ressources agricoles et forestières non exploitées. L’une des technologies proposées est la torréfaction, traitement thermique doux entre 200 et 300°C pendantquelques minutes et en défaut d’oxygène. Le solide torréfié présente des propriétés proches de celles du charbon et convient à la combustion ou à la gazéification. En même temps, des matières volatiles sont relâchées, dont des espèces condensables potentiellement à haute valeur ajoutée en chimie. Il est donc crucial de caractériser le solide torréfié et les espèces volatiles afin d’optimiser le procédé jusqu’à l’échelle industrielle. Jusqu’à présent, peu de travaux ont simultanément cherché à caractériser et à modéliser le comportement du solide et des espèces volatiles produites en torréfaction en fonction des conditions opératoires et du type de biomasse. De plus, ces travaux portaient sur un nombre réduit de biomasses. La composition macromoléculaire de la biomasse en cellulose, hémicelluloses et lignine impacte de manière déterminante les produits de torréfaction. Cependant, les essais de torréfaction avec ces constituants sont peu nombreux et généralement réalisés avec des composants commerciaux peu représentatifs de la biomasse brute. L’objectif de ces travaux de thèse est d’étudier l’influence des caractéristiques de la biomasse, principalement représentée par sa composition en cellulose, hémicellulose et lignine, sur le comportement global de la biomasse en torréfaction, tant en termes de perte de masse du solide que de production d’espèces volatiles, en fonction des conditions opératoires. 14 représentants des principales familles de biomasse (bois feuillus, bois résineux, sous-produits agricoles et plantes herbacées) ont été sélectionnés pour cette étude. Une procédure d’extraction optimisée a été proposée pour obtenir des fractions de cellulose, hémicellulose et lignine de 5 biomasses de référence. Les données expérimentales ont été obtenues en utilisant une thermobalance couplée à une chromatographie gazeuse et une spectrométrie de masse via un système de boucles de stockage chauffées (ATG-GC/MS). La cinétique de dégradation du solide et les profils de formation des espèces volatiles ont été étudiés au cours des expériences de torréfaction incluant une partie non-isotherme (200 à 300°C, 3°C/min) suivie d’une partie isotherme (300°C, 30 min), dans des conditions expérimentales assurant le régime chimique. Les résultats obtenus avec les biomasses brutes montrent que la composition macromoléculaire de la biomasse est un facteur clé influant sur son comportement en torréfaction. Par conséquent, l’hétérogénéité de la ressource se traduit par une diversité de comportements en torréfaction, en particulier pour les biomasses agricoles. Il a été observé un comportement très différent pour les composants extraits comparés aux composants commerciaux, particulièrement dans le cas de la cellulose. Ceci montre que l’usage commun de composants commerciaux pour bâtir les modèles de torréfaction n’est pas pertinent. L'impact des caractéristiques des composants macromoléculaires sur le comportement en torréfaction a été aussi mis en évidence, particulièrement en ce qui concerne la composition en sucres des hémicelluloses et la cristallinité de la cellulose. En outre, des différences de profils de production des espèces volatiles ont été observées, même pour des composés de même nature chimique. A partir de ces résultats, un modèle de torréfaction basé sur la contribution additive de la cellulose, des hémicelluloses et de la lignine extraites est proposé pour décrire le comportement global de la biomasse en torréfaction, et ceci pour les 5 biomasses de référence. / Nowadays, there is an increasing awareness on the importance of biomass waste as a renewable source of energy, materials and chemicals. In this context, the European project MOBILE FLIP aims at developing and demonstrating mobile conversion processes suitable with variousunderexploited agro- and forest based biomass resources in order to produce energy carriers, materials and chemicals. One of these processes is torrefaction, which consists in a mild thermal treatment, occurring typically between 200 and 300°C during a few tens of minutes in a defaultoxygen atmosphere. The solid product obtained has thermal and processing properties closer to coal, and thus is suitable as fuel for combustion or gasification. During torrefaction, condensable coproducts are released, that may also be source of “green” chemicals. It is therefore crucial to characterize them to optimize the torrefaction process and design industrial units. Up to now, only few works have been focused on characterizing and modelling both solid and condensable species during torrefaction versus operating conditions and feedstock type. Furthermore, these studies typically include a reduced number of biomasses. Cellulose, hemicellulose and lignin,which constitute biomass macromolecular composition, are determining properties to predict biomass behaviour during torrefaction. However, torrefaction tests on these constituents are rare and always based on commercial compounds, which were proved as little representative of the native biomass. The objective of this study is to analyse the influence of biomass characteristics, mainly represented by the macromolecular composition in cellulose, hemicellulose and lignin, on the global behaviour of biomass in torrefaction, both in terms of solid mass loss and of productionprofiles of the volatile species released, in function of the operating conditions.14 biomasses from the main biomass families (deciduouswood, coniferous wood, agricultural byproductsand herbaceous crops) were selected for this study. An optimized extraction procedure was proposed to recover cellulose, hemicellulose and lignin fractions from 5 reference biomasses. Experiments were performed on a thermogravimetric analyzer coupled to a gas chromatography mass spectrometer device through a heated storage loop system (TGA-GC/MS). Solid degradation kinetics and volatile release profiles were followed during torrefaction experiments combining non-isothermal (200 to 300°C at 3°C/min) and isothermal (300°C, 30 min) conditions, ensuring the chemical regime thanks to the appropriate operating conditions. The results obtained with the raw materials demonstrated that biomass macromolecular composition is a main factor influencing biomass behavior in torrefaction. Consequently, the heterogeneity of the resource results in a diverse behavior in torrefaction, particularly in the case of agricultural biomasses. The results with the extracted components evidenced their very different behavior compared to thecommercial compounds, particularly in the case of cellulose. This suggests that a limitation could be induced by the common use in literature of commercial components for torrefaction modelling. The impact on the characterization of macromolecular components was also shown to be prevailing in their behavior in torrefaction, especially in the case of hemicellulose sugar composition and cellulose crystallinity. Furthermore, differences in release kinetics of volatile species during torrefaction were observed, even for volatiles belonging to the same chemical family (acids, furans, ketones). Derived from these results, a torrefaction model based on the additive contribution of extracted cellulose, hemicelluloses and lignin to the global behavior of biomass in torrefaction was proposed, and this for the 5 representative biomasses.

M. Tech (Department of Chemistry, Faculty of Applied and Computer Sciences) Vaal University of Technology. / In this study, analytical method for determining the chlorinated phenols in water was developed using High Performance Liquid Chromatography. The following four compounds which are 2, 4, 6- Trichlorophenol (2, 4, 6 TCP), 3-chlorophenol (3CP), 2, 4- Dichlorophenol (2, 4 DCP) and 4-chloro-3-methylphenol (4C3MP) were identified and quantified with a High Performance Liquid Chromatography (HPLC). The validation parameters tested were,: linearity, trueness, precision, detection limit of quantitation, sensitivity, specificity, selectivity. The linear calibration ranges of five standard solution from 1-10 ppm. The linearity ranges between 0.9298-0.9813. The activated carbon based on the waste macadamia nutshell activated carbon (MAC) was investigated for its potential uses as an adsorbent for chlorinated phenols removal and compared with grafted macadamia nutshell activated carbon (GMAC). The adsorbent was characterized with Fourier transform infrared spectrophotometer (FTIR), scanning electron microscope (SEM) and thermo gravimetric analysis (TGA). The parameters such as pH, temperature, contact time, concentration and adsorbent were investigated by adsorption technique. The strata C18E has been used before for the same reason and therefore the research was based on mimic the functional group of solid phase extraction (SPE) into macadamia activated carbon (MAC). The functional groups in SPE C18E are benzene and octadecyl. MAC was grafted with strata C18E functional groups to compare its potential with the SPE. The pseudo-first-order and pseudo-second-order kinetic models were applied to verify the experimental data. The pseudo-second order exhibited the best fit for the kinetic studies for MAC adsorption. Chemical removal of chlorinated phenols from wastewater is necessary to reduce harmful products on the environment and human health. Chlorinated phenols have been previously listed as some of the highest priority contaminants and as well as mainly important capability carcinogenic toxins released from chemical plants. Their availability in water supplies was perceived by their bad taste and smell. The acceptable chlorinated phenols concentration in portable water is 1 (mg/l) base on the approval of world health organization. The permanent checking of chlorinated phenols in environmental samples has a greater significance and stresses highly effectiveness, common selectively and great sensitively methods. The maximum uptake of Phenol using weighed mass of MAC was found to be 78 % and for GMAC was 84% for both 2,4,6TCP. t=250 min, pH=5, Co=1mg/l, T = 25 oC and m = 0.3 g/l were the optimum condition for Phenol-MAC system and GMAC system. Over all analysis of equilibrium model analysis indicates the fitness of Langmuir isotherm model to Phenol MAC adsorption system, suggesting a monolayer adsorption of phenol on the surface of MAC. Phenol adsorption capacity of MAC was found to be decreasing with increase in temperature suggesting that the adsorption process was exothermic in nature, which was further supported by the negative values of change in enthalpy. Characterization of MAC and GMAC confirmed the mesoporous texture, highly carbonaceous nature and a higher effective surface area of 912 m2/g. The highest phenol uptake capacity of GMAC was found to be 8.0049 mg/g. The optimal conditions for various process parameters are t = 250 min, pH=5, Co=1mg/l, T = 25 oC and m = 0.3 g/l were the optimum condition for Phenol-GMAC system. Like Phenol-MAC system, the kinetics studies confirmed that Phenol-GMAC adsorption system can be described by pseudo- second-order kinetics model. Equilibrium model analysis indicates the fitness of Langmuir isotherm model to Phenol-MAC adsorption system, suggesting a monolayer adsorption of phenol on the surface of GMAC. Phenol adsorption capacity of GMAC was found to be decreasing with increase in temperature suggesting that the adsorption process was exothermic in nature, which was further supported by the negative values of change in enthalpy. The negative values of Gibb’s free energy suggested that adsorption of phenol onto GMAC was a spontaneous process.

This diploma thesis deals with issues of fine and ultrafine particles formation during thermal decomposition and combustion of biomass. An introduction is devoted to a utilization of biomass as fuel. A following part describes the gas products emerging generally during combustion process. A current emission and air pollution situation in the Czech Republic as well as the health impacts of solid pollutants on human are also mentioned. Within an experimental measurement three basic factors that have impact on fine particles formation during combustion of beech wood (i. e. oxygen content in combustion atmosphere, type of the sample and size of the sample) were thoroughly analyzed. Attention was paid to a progress of thermal decomposition and combustion of sample with respect to the particles formation. Finally, a measurement of fine particles amount was accomplished in a real boiler successively with four different biomass pellet types.

Presented master's thesis focuses on the study of hydration of selected biocolloid substances, specifically humic substances (humic acids and fulvic acids), hyaluronic acid with three different molecular weight, chitosan and dextran. Interaction of biocolloids with water was studied by different methods. The effect of solubility, structure, functional groups in molecule on sorption and hydration ability of these biocolloids was investigated. In the case of hyaluronan the influence of molecular weight was also study. Differential scanning calorimetry DSC and perfusion calorimetry give results of heat of hydration, enthalpies and temperature of crystallization and melting. Thermogravimetric analysis TGA was used to determine the original moisture content of the samples.

No description available.

The need for replacing petroleum-based polymers has been increasing and bio-based polymers prove to be a suitable solution. The aim of this thesis was to synthesize bio-based resins with different chemical architectures to evaluate the effect of the structure on the properties and on their response to ageing and biodegradation. For this, three different bio-based thermoset resins have been synthesised by reacting one of three distinct core-molecules with lactic acid. The options of core-molecules chosen for this work were ethylene glycol, glycerol and pentaerythritol. Lactic acid was first reacted with a core-molecule by direct condensation, the resulting branched molecule was then end-functionalized with methacrylic anhydride. The amount of moles of lactic acid varied according to which core-molecule it was reacted with, but the chain length (n) was always maintained as three. Part of the samples were characterised by Fourier-transform infrared spectroscopy (FT-IR), differential scanning calorimetry (DSC), thermogravimetric analysis (TGA) and tensile test. DSC and TGA were used for determining the thermal behaviour. FT-IR was used to verify the first and second stage of the reaction and to ascertain the occurrence of the crosslinking reaction. Tensile test was done for investigation of mechanical properties. The ageing and biodegradation tests are useful to ascertain the material possible applications. Therefore, the samples that went through the process of ageing or biodegradation were also characterised in the end of the procedures to further check the effect of those processes on the specimens. The test results indicated that the PENTA/LA cured resin was the most stable thermally. The cured resin’s mechanical properties were similar to each other, so there was no comparison to make in this area. The samples proved to be affected by the biodegradation and the ageing processes, both in visual and structural aspects.

No description available.

El carácter adictivo del tabaco se debe fundamentalmente a la nicotina, mientras que su toxicidad se debe a una serie de sustancias tales como el monóxido de carbono, 1,3-butadieno, hidrocarburos policíclicos aromáticos (PAH) y las nitrosaminas específicas del tabaco (TSNAs), entre otros. La reducción de la toxicidad del humo del tabaco a través de la reducción de la emisión de los productos más problemáticos o la modificación de su composición en conjunto resultan alternativas muy interesantes, mientras se consigue la eliminación de este hábito. Se han localizado trabajos en la literatura encaminados a este fin. Con este objetivo, nuestro grupo de investigación lleva más de quince años estudiando el efecto que ciertos materiales micro y mesoporosos mezclados con el tabaco producen sobre la composición del humo obtenido en el proceso de fumado. En este sentido, en los últimos años se ha puesto de manifiesto la eficacia que presentan algunos silicatos mesoporosos, tales como SBA-15 y MCM-41 en la reducción de los alquitranes y la mayoría de los compuestos presentes en el humo del tabaco. Es por ello que se ha considerado que conocer el comportamiento de determinados compuestos específicos presentes en el humo de tabaco, como son la nicotina y dos nitrosaminas específicas del tabaco (NNK y NNN), los productos que se generan en su pirólisis y combustión, así como el efecto de los materiales mesoporosos mencionados en los procesos que tienen lugar durante el fumado del tabaco, sería de gran interés, y permitiría ayudar a diseñar productos de toxicidad reducida y menor carácter adictivo. A este respecto se han localizado muy escasos artículos en la bibliografía. Por todo ello, en el presente trabajo se aborda esta problemática y se plantea el estudio de la pirólisis de las dos nitrosaminas específicas del tabaco más cancerígenas, como son la 4-(N-metilnitrosoamino)-1-(3-piridinil)-butanona (NNK) y la N-nitrosonornicotina (NNN) mediante dos técnicas, TGA/FTIR y EGA/PY-GC/MS que son capaces de realizar experimentos a las velocidades de calefacción tan dispares que se dan en el proceso de fumado y tanto atmósfera inerte como atmósfera oxidante. También se estudia el comportamiento de la nicotina en EGA/PY-GC/MS, con objeto de completar el ya realizado por nuestro grupo de investigación la técnica de TGA/FTIR. Se estudia el efecto que producen tres silicatos mesoporosos (dos SBA-15 y un MCM-41) que presentan propiedades texturales y morfológicas diferentes, en la pirólisis catalítica de los tres compuestos anteriormente mencionados. Además, se analiza el efecto de la temperatura y la atmósfera (inerte y oxidante), en la degradación de la nicotina y las dos nitrosaminas mencionadas, y en la composición de los gases generados tras su descomposición. Se ha comprobado que en atmósfera oxidante los procesos de descomposición suceden a temperaturas más bajas, siendo especialmente notable este efecto en el caso de la nicotina. Así mismo, la presencia de los tres catalizadores favorece los procesos de descomposición de estos compuestos en ambas atmósferas, modifican la distribución de productos y favorecen la formación de residuo carbonoso. Los principales productos de descomposición de la nicotina en atmósfera inerte son la 3-etil-piridina, la miosmina y, especialmente la 3-vinilpiridina, que aumentan su contribución al aumentar la temperatura. Algunos compuestos como la miosmina presentan un máximo en su evolución, lo que indica que experimentan procesos de craqueo. En atmósfera oxidante se produce un cambio muy significativo en la distribución de productos, además de la mayor reactividad ya mencionada. Los productos mayoritarios pasan a ser la 3-cianopiridina, la nicotirina, la miosmina, el dióxido de carbono y el agua. La 3-cianopiridina y la 3-hidroxipiridina, muestran una tendencia creciente con la temperatura, mientras que el resto de los compuestos presentan evidencias de reacciones secundarias, poniendo de manifiesto que la presencia de oxígeno en el medio favorece las reacciones de descomposición de la nicotina y de muchos de los productos generados. La nicotina genera cianuro de hidrógeno en ambas atmósferas. Los tres catalizadores estudiados aceleran el proceso de descomposición de la nicotina y conducen a una mayor formación de residuo carbonoso, siendo el MCM-41 el material que ocasiona un mayor efecto, probablemente debido a su mayor superficie específica y buena accesibilidad de su porosidad debida a su morfología (aunque presente un menor tamaño de poro que los otros catalizadores). En atmósfera inerte la presencia de SBA-15f (SBA-15 fibras), apenas modifica el comportamiento de la nicotina, mientras que tanto MCM-41 como SBA-15p (SBA-15 platelet) se reduce la formación de algunos compuestos como la 3-vinilpiridina, incrementándose la formación de otros como quinolina e isoquinolina. En atmósfera oxidante los cambios son más significativos, ya que todos los catalizadores favorecen las reacciones de oxidación y descarboxilación, incrementando la generación de dióxido de carbono y disminuyendo la formación de agua, especialmente MCM-41 y SBA15p. MCM-41 reduce notablemente la formación de 3-cianopiridina y de nicotirina al aumentar la temperatura, a diferencia de lo observado en la nicotina, tanto sola como en presencia de los dos SBA-15. Ambas nitrosaminas han presentado unos resultados en la línea de los comentados para la nicotina. Se ha observado que la degradación completa de ambos compuestos sucede a temperaturas ligeramente inferiores para atmósfera oxidante, y presenta variaciones en la composición de los gases generados. Se ha podido comprobar cómo, de los tres materiales estudiados, el MCM-41 es el que provoca mayor modificación de la degradación térmica de ambas nitrosaminas, favoreciendo la generación de residuo en atmósfera inerte. En cuanto a la composición de los productos generados tras la pirólisis de NNK, ambos SBA-15 han mostrado una modificación clara de la distribución de los mismos. También se ha podido observar como en el caso de la NNN, algunos de sus productos de descomposición reducen su contribución a máxima temperatura, observándose tendencias decrecientes y algún máximo en función de la temperatura. Por otro lado, los resultados de termogravimetría para ambas nitrosaminas se han ajustado a un sencillo modelo cinético que permite estimar las áreas de cada uno de los procesos de pérdida de peso observados, pudiéndose realizar de esta forma un análisis más claro del efecto de los catalizadores utilizados basado en las distintas fracciones asociadas a cada uno de los procesos. El caso de la NNK presenta tres procesos de pérdida de peso a 194, 299 y 368 ºC en atmósfera inerte y tres procesos a 208, 299 y 648 ºC en atmósfera oxidante, siendo el principal el que tiene lugar a 299 ºC con un 81.8 y 66.4 % de contribución relativa para atmósfera inerte y oxidante, respectivamente. La NNN ha mostrado dos procesos de pérdida de peso, a 190 y 218 ºC en atmósfera inerte y a 180 y 207 ºC en oxidante. Los tres materiales mesoporosos estudiados han mostrado, para ambas nitrosaminas, modificaciones en la temperatura e intensidad de los procesos observados. Este efecto se hace más notable en aire donde se observa un nuevo proceso térmico a altas temperaturas, siendo especialmente notable este efecto con MCM-41. El experimento con este material para la NNK ha presentado cuatro procesos de pérdida de peso a 197, 232, 281, 414 ºC para atmósfera inerte y oxidante, variando la contribución relativa entre ellos. En el caso de la NNN, el experimento con MCM-41 ha mostrado tres procesos a 190, 218 y 260 ºC para atmósfera inerte y a 180, 207 y a 610 ºC en atmósfera oxidante. Para ambas nitrosaminas en atmósfera oxidante, los gases analizados para los tres materiales han mostrado un aumento considerable (principalmente por el MCM-41) de las bandas de CO2 y CO a temperaturas elevadas, respecto al experimento sin catalizador. Este aumento se ha debido a la degradación oxidativa del residuo carbonoso generado.

With a growing concern of climate change due to increased levels of CO2 in the atmosphere, carbon sequestration has been suggested as a possible solution for climate change mitigation. Biochar,a highly carbonaceous product produced through pyrolysis, is considered a viable option due to its content of stable carbon. This work covers the investigation of the possibility to produce biocharfrom four different feedstocks, namely peat, straw, horse manure and sewage sludge. The study includes a literature study and a five-week trial period at a 500 kW pilot plant, PYREG 500, in Högdalen. The thermal behaviour of the feedstocks, including garden waste, was investigated using thermogravimetric analysis (TGA). The TGA results were used to decide the optimal pyrolysis temperature for peat and straw at the pilot plant. The TGA results showed that the feedstocks behave differently when pyrolysed; the mass loss rate as well as the final mass loss varied. Physiochemical characterisation of the biochar was completed and the results were in agreement with previous studies. The produced biochar from straw and two types of peat had a C content above50 wt.% (76.6, 80.7, 79.2 wt.%) and low molar ratios of H/C (0.33, 0.36, 0.38) and O/C (0.032,0.023, 0.024). The pH increased as a consequence of pyrolysis and the biochars were alkaline (pH10.1, 8.5, 8.3). Polycyclic aromatic hydrocarbons (PAHs) were found in biochar from both strawand peat (8.26, 1.03, 5.83 mg/kg). In general, nutrients and heavy metals were concentrated in the biochar, except for Cd which decreased and Hg which could not be determined. The specific surface area of biochar from straw was considered small (21 m2/g) while biochar from peat had a higher specific surface area with a greater span (102-247 m2/g). The properties of the produced biochar were compared to the criteria included in the European Biochar Certificate and some of them were fulfilled, including the content of C, PAH and heavy metals. A flue gas analysis was completed when operating the pilot plant on straw pellets and it was showed that several emissions were released, including NO2, SOX, HCl and particulates, however, solely the emissions of NO2 exceed the regulations which will be applied in 2020. Regarding process design of a future pyrolysis plant, it is suggested that the means of material transport, particle separation, temperature control and quenching of biochar should be improved.

No description available.