Foram utilizadas 8 vacas Holandesas em lactação, distribuídas em um quadrado latino (4x4), replicado, conduzidos durante o verão, por um período de 72 dias. O objetivo desse trabalho foi estudar quatro níveis de dietas catiônicas, sobre a IMS, produção, composição e propriedades físico-químicas do leite, pH urinário, temperatura corporal e parâmetros ácido-base do sangue, em vacas após o pico de lactação. Para a manipulação do BCAD, foram adicionadas diferentes concentrações de bicarbonato de sódio nas dietas, obtendo-se os seguintes tratamentos: +150, +250, +400 e +500mEq/kg MS. A temperatura corporal das vacas não foi afetada pelo balanço cátion-aniônico da dieta. O bicarbonato, o pH, o CO2 total e a pCO2 do sangue aumentaram linearmente com o aumento do BCAD. A concentração de cálcio no sangue apresentou resposta quadrática, com maior valor para o menor BCAD. As concentrações de sódio e potássio do sangue não foram modificadas significativamente pelo BCAD e a concentração de cloro diminuiu linearmente com o aumento do BCAD. O aumento do BCAD resultou em aumento da ingestão de matéria seca e produção de leite. Não houve diferença significativa para as variáveis: porcentagem de gordura, densidade e índice crioscópico, do leite. O pH do leite aumentou linearmente e a acidez apresentou resposta cúbica, com o aumento do BCAD. Conclui-se que a manipulação do BCAD afeta o equilíbrio ácido-base das vacas, mesmo dentro de variação positiva. Devido ao aumento da IMS e da produção de leite, verificou-se efeito benéfico do uso de dietas catiônicas, para vacas após o pico de lactação. / Eight lactating Holsteins cows were distributed in 4 x 4 replicated Latin square, during the summer, for a period of 72 days. The objective of this research was to study the effect of four cationic diets levels, on the dry matter intake, milk production, composition, and physico-chemical parameters, urinary pH, body temperature and blood acid-base parameters, in cows, after the lactation peak. For DCAB manipulation were added different concentrations of sodium bicarbonate in the diets and the following treatments were obtainned: +150, +250, +400 e +500mEq/kg DM. The cows body temperature was not affected by dietary cation-anion balance. Blood bicarbonate, pH, total CO2 and pCO2 increased linearly with the increase of dietary CAB. Calcium concentration in the blood decreased quadratically with dietary CAB increased. Sodium and potassium concentration in the blood were not modified significantly with the DCAB and concentration of chloride decreased linearly with increase of DCAB. Increasing BCAD resulted in higher DM intake and milk yield. The diets did not affect milk fat percentage, density and crioscopic index. Milk pH increased linearly and acidity decreased cubically with the increase of dietary CAB. It was concluded that DCAB manipulation affected the acid-base status of cows, even inside of positive variation. Due to the increase of DM intake and milk yield, it was verified a beneficial effect of the cationic diets for cows after the lactation peak.

Bicarbonato é uma importante espécie química para os seres vivos, sendo o principal tampão celular, alem de apresentar uma negligenciada atividade redox. Isquemia é um evento no qual existe inibição do aporte de nutrientes e oxigênio, sendo a reperfusão o retorno do fluxo de nutrientes e oxigênio, que é acompanhada por alta produção de radicais livres e morte celular. Nessa tese estudamos o efeito da presença de bicarbonato durante a isquemia-reperfusão. Em nosso modelo nós mantivemos o pH constante e modulamos a quantidade de bicarbonato enquanto células, órgãos e animais foram submetidos a isquemia-reperfusão. Utilizamos condições sem a presença de bicarbonato, a concentração basal sanguínea e uma concentração mais alta simulando o acúmulo de bicarbonato em condições isquêmicas. Nesses diversos modelos mostramos que a presença de bicarbonato aumenta o dano provocado por isquemia-reperfusão e provoca um aumento do acúmulo de proteínas oxidadas. A presença do bicarbonato não modifica a respiração, produção de espécies reativas de oxigênio, ou a morfologia mitocondrial, também não detectamos mudança na atividade do proteassoma e nos indicadores de autofagia geral. Entretanto detectamos um acúmulo de marcadores autofágicos na fração mitocondrial indicando inibição da mitofagia. Essa inibição foi confirmada ao detectarmos o acúmulo de uma proteína degradada especificamente por mitofagia enquanto não houve mudança em outra degradada pelo proteassoma. Além disso, ao inibirmos farmacologicamente a autofagia, reproduzimos o fenótipo causado pelo bicarbonato mesmo na sua ausência. Em conclusão, a presença de bicarbonato é deletéria em condições de isquemia/reperfusão devido a inibição da mitofagia / Bicarbonate is an important molecule in all living being, acting as the main cellular buffer. However, its biological and redox activity has been mostly neglected to date. Ischemia is an event in which an inhibition of nutrient availablity and oxygen flow occurs, while reperfusion is the return of nutrients and oxygen, accompanied of a burst of reactive oxygen species production and cell death. Here, we studied the effects of bicarbonate during cardiac ischemia-reperfusion. In our model, we kept the pH stable and changed the concentration of the bicarbonate. We then subjected cells, organs and animals to ischemia-reperfusion under conditions where there was no presence, basal blood concentration or a higher concentration of bicarbonate. In these diverse models, we found that the presence of bicarbonate increased damage after a ischemia-reperfusion, and promoted the accumulation of oxidized proteins. Bicarbonate did not change respiration, production of reactive oxygen species or the morphology of the mitochondria. There were also no changes in proteasome activity and in global autophagy markers, although there was an accumulation of mitophagy markers. We also found that mitophagy was responsible for the increased damage observed, since pharmacological inhibiting of autophagy abolished the increased damage caused by the presence of bicarbonate. In conclusion the presence of bicarbonate is deleterious in ischemia-reperfusion due mitophagy inhibition

Lime-induced chlorosis has been recognized for many years as a problem where plants are grown on calcareous soils. There are many factors associated with and influencing this form of iron chlorosis and because of this it has been very difficult to determine the relationship between the factors and chlorosis. There are high concentrations of bicarbonate in calcareous soils. Because of this high concentration, it was believed that the presence of the bicarbonate ion was causing chlorosis. It has been proposed that the pH of the growth medium was the causitive factor of lime-induced chlorosis. Most calcareous soils have a pH range around 8.0. At this pH the solubility of iron is very low, and it was believed that chlorosis was a result of iron being insoluble at a high pH. Iron chlorosis has been induced in plants by increasing the phosphorus concentration in the growth medium. Iron phosphates have a low solubility and it was believed that the available iron was precipitated by the phosphates. The interference of metals such as calcium, nickel, cobalt, zinc, and copper appears to be a factor affecting the absorption of iron by plants. It was thought that an interfering ion (Ni, Co, Ca, Zn) may interfere with the translocation of iron in the malic or malonic acid complexes (Tiffin and Brown, 1962).

Forty-eight Holstein cows at Utah State Dairy Farm were blocked statistically according to date of calving, previous milk production, and numbers of lactation at parturition. The cattle were assigned randomly to one of four treatments within blocks. The four treatments included a base ration (control, treatment #1), base ration plus .8% of sodium bicarbonate (treatment #2), base ration plus .4% of magnesium oxide (treatment #3), and base ration plus both .8% of sodium bicarbonate and .4% of magnesium oxide (treatment #4). The research was conducted from February 1983 to November 1984. A formagraph was used to measure milk coagulation parameters and pH was determined. There was no significant difference in milk coagulation parameters or pH between the control and the buffer treatments. Milk parameters were significantly different in individual cow, week, and milk pH. Milk parameters did not appear to be dependent upon season. Curd firmness was significant in interaction of season and treatment. Significant variations in milk pH were observed in relation to week, season, and individual cow. Overall treatments, the clotting time, K20, and pH value increased each wee, and A30 decreased each week. The milk parameters and pH in each treatment were significant between weeks except K20 and A30 in treatment #3, and A30 in treatment #2 (p Somatic cell count was positively correlated with clotting time, K20, and pH and negatively correlated with A30. Milk pH was the most significant and had positive correlation coefficient with clotting time and firming rate and negative correlation coefficient with curd firmness.

This thesis considers the implications of changes in the supply of resources for photosynthesis, with regard for modes of carbon acquisition employed by aquatic plants of the River Murray. Carbon supplies are inherently more variable for aquatic plants than for those in terrestrial environments, and variations are intensified for plants in semi-arid regions, where water may be limiting. In changeable environments the most successful species are likely to be those with flexible carbon-uptake mechanisms, able to accommodate variations in the supply of resources. Studies were made of plants associated with wetland habitats of the Murray, including Crassula helmsii, Potamogeton tricarinatus, P. crispus and Vallisneria americana. The aim was to elucidate the mechanisms of carbon uptake and assimilation employed, and to determine how flexibility in carbon uptake and/or assimilation physiology affect survival and distribution. Stable carbon isotopes were used to explore the dynamics of carbon uptake and assimilation, and fluorescence was used to identify pathways and photosynthetic capacity. The studies suggest that physiological flexibility is adaptive survival in changeable environments, but probably does not enhance the spread or dominance of these species. V. americana is a known bicarbonate-user, and it is shown here that it uses the Crassulacean Acid Metabolism (CAM) photosynthetic pathway under specific conditions (high light intensity near the leaf tips) concurrently with HCO[subscript]3 - uptake, while leaves deeper in the water continue to use the C[subscript]3 pathway, with CO₂ as the main carbon source. However, V. americana does not use CAM when under stress, such as exposure to high light and temperature. The diversity of carbon uptake and assimilation mechanisms in this species may explain its competitive ability in habitats associated with the Murray. In this way it is able to maximise use of light throughout the water column. In shallow, warm water, where leaves are parallel to the surface, CAM ability is likely to be induced along the length of the leaf, allowing maximal use of carbon and light. The amphibious C. helmsii is shown to use CAM on submergence, even where water levels fluctuate within 24 hours. This allows continued photosynthesis in habitats where level fluctuations prevent access to atmospheric CO₂. It appears that stable conditions are most favourable for growth and dispersal, and that the spread of C. helmsii is mainly by the aerial form. Carbon uptake by P. tricarinatus under field conditions is compared with that of P. crispus to demonstrate differences in productivity associated with aqueous bicarbonate and atmospheric CO₂ use. P. tricarinatus uses HCO[subscript]3 - uptake to promote growth toward the surface, so that CO₂ can be accessed by floating leaves. Atmospheric contact provides access to light and removes the limitation of aqueous diffusive resistance to CO₂, thereby increasing photosynthetic capacity above that provided by submerged leaves. / http://proxy.library.adelaide.edu.au/login?url= http://library.adelaide.edu.au/cgi-bin/Pwebrecon.cgi?BBID=1320380 / Thesis (Ph.D) -- University of Adelaide, School of Earth and Environmental Sciences, 2008

Le photosystème II (PSII) est un complexe multi-protéique qui utilise l'énergie solaire pour oxyder l'eau et réduire des quinones. Le site catalytique d'oxydation de l'eau est localisé coté lumen du complexe, alors, que le site de réduction comprenant deux quinones (QA et QB) et un fer non-hémique est localisé sur le coté stromal du complexe membranaire. Dans cette thèse j'ai étudié les deux cotés accepteur et donneur d'électrons du PSII.QA*- et QB*- sont couplés magnétiquement au fer non-hémique donnant de faibles signaux RPE. Le fer non-hémique possède quatre ligands histidines et un ligand (bi)carbonate échangeable. Le formate peut échanger le ligand (bi)carbonate induisant un ralentissement dans le transfert d'électrons. Ici, je décris une modification du signal RPE de QB*- Fe2+ lorsque le formate est substitué au (bi)carbonate. J'ai aussi découvert un second signal RPE dû à la présence du formate à la place du (bi)carbonate lorsque QB est doublement réduit. De plus, j'ai trouvé que les signaux RPE natifs de QA*- Fe2+ et QB*- Fe2+ possèdent une signature intense encore jamais détectée. Tous les signaux RPE rapportés dans cette thèse devraient faciliter le titrage redox de QB par RPE. J'ai aussi observé que QB*- peut oxyder le fer non-hémique à l'obscurité en anaérobie. Cette observation implique qu'au moins dans une fraction des centres, le couple QB*-/QBH2 possède un potentiel redox plus haut que supposé. La quantification du nombre de centres où cette oxydation du fer se produit par le couple QB*-/QBH2 reste à faire. La réduction du PSII par le dithionite génère un signal modifié de QA*-Fe2+, un changement structural du PSII observé par électrophorèse. Cela peut indiquer la réduction d'un pont disulfure à l'intérieur du PSII. Concernant le site d'oxydation de l'eau, j'ai étudié la première étape de l'assemblage du site catalytique (Mn4Ca), en suivant l'oxydation du Mn2+ par RPE en bande X et haut champ. J'ai mis au point des conditions expérimentales permettant le piégeage du premier intermédiaire et j'ai aussi trouvé une incohérence avec des travaux publiés dans la littérature. J'ai aussi trouvé que le dithionite pouvait réduire le site catalytique Mn4Ca, en formant des états sur-réduits qui peuvent correspondre aux intermédiaires de l'assemblage du cluster Mn4Ca.

Intracellular pH was monitored at the cytosolic surface of plasma membrane solute transporters (Na+/H+/nucleoside co-transporters, or Cl-/HCO3- exchangers), using pH-sensitive fluorescent proteins (FPs), dual emission green FP (deGFP4) and a monomeric red FP Nectarine (mNect), whose development and characterization are also reported here. Human concentrative nucleoside transporter, hCNT3, mediates Na+/H+/nucleoside co-transport. We describe a new approach to monitor H+/uridine co-transport in HEK293 cells. pH changes at the intracellular surface of hCNT3 were monitored by fusing mNect to the cytoplasmic N-terminus of hCNT3 (mNect.hCNT3) or an inactive hCNT3 mutant (mNect.hCNT3-F563C). Cells were incubated at the permissive pH for H+-coupled nucleoside transport, pH 5.5, under both Na+-free and Na+-containing conditions. In mNect.hCNT3-expressing cells (but not under negative control conditions) the rate of acidification increased in media containing 0.5 mM uridine, providing the first direct evidence for H+-coupled uridine transport. At pH 5.5, there was no significant difference in uridine transport rates (coupled H+ flux) in the presence or absence of Na+. This suggests that in acidic Na+-containing conditions, 1 Na+ and 1 H+ are transported/uridine molecule, while in acidic Na+-free conditions, 1 H+ alone is transported/uridine. In acid environments, including renal proximal tubule and intestine, H+/nucleoside co-transport may drive nucleoside accumulation by hCNT3. Microdomains, discrete regions of altered cytosolic solute concentration, are enhanced by rapid solute transport and slow diffusion rates. pH-regulatory membrane transporters, like the Cl-/HCO3- exchanger AE1, could nucleate H+ microdomains, since AE1 has a rapid transport rate and cytosolic H+ diffusion is slow. As AE1 drives Cl-/HCO3- exchange, differences in pH, near and remote from AE1, were monitored simultaneously by deGFP4 fused to AE1 (deGFP4.AE1) and mNect.hCNT3-F563C. deGFP4.AE1-mNect.hCNT3-F563C distance was varied by co-expression of different amounts of the two proteins in HEK293 cells. As the deGFP4.AE1-mNect.hCNT3-F563C distance increased, mNect.hCNT3-F563C detected the cytosolic pH change with a time delay and reduced rate of pH change, compared to deGFP4.AE1. Carbonic anhydrase activity was essential for H+ microdomain formation. H+ diffusion along the plasma membrane was 60-fold slower than to the cytosolic ER-surface. During physiological HCO3- transport, a H+ microdomain 0.3 µm in diameter develops around AE1, which will affect nearby pH-sensitive processes.

Le bicarbonate de soude raffiné, produit industriellement par la société Solvay, est fabriqué dans des colonnes à bulles de grande taille, appelées les colonnes BIR. Dans ces colonnes, une phase gazeuse contenant un mélange d’air et dioxyde de carbone (CO2) est dispersée sous forme de bulles dans une solution aqueuse de carbonate et de bicarbonate de sodium (respectivement Na2CO3 et NaHCO3). Cette dispersion donne lieu à un transfert de CO2 des bulles vers la phase liquide. Au sein des colonnes, la phase gazeuse se répartit dans deux populations de bulles : des petites bulles (diamètre de quelques mm) et des grandes bulles (diamètre de quelques cm). Le transfert bulle-liquide de CO2 est couplé à des réactions chimiques prenant place en phase liquide, qui conduisent à la conversion du Na2CO3 en NaHCO3. Une fois la concentration de saturation dépassée, le NaHCO3 précipite sous forme de cristaux et un mélange liquide-solide est recueilli à la sortie de ces colonnes. Ce travail, réalisé en collaboration avec la société Solvay, porte sur l’étude et la modélisation mathématique des phénomènes de transfert de matière entre phases, couplés à des réactions chimiques, prenant place au sein d’une colonne BIR. L’association d’études sur des colonnes à bulles à l’échelle industrielle ou réduite (pilote) et d’études plus fondamentales sur des dispositifs de laboratoire permet de développer une meilleure compréhension du fonctionnement des colonnes BIR et d’en construire un modèle mathématique détaillé. L’objectif appliqué de ce travail est la mise au point d’un modèle mathématique complet et opérationnel d’une colonne BIR. Cet objectif est supporté par trois blocs de travail, dans lesquels différents outils sont développés et exploités. Le premier bloc est consacré à la modélisation mathématique du transfert bulle-liquide de CO2 dans une solution aqueuse de NaHCO3 et de Na2CO3. Ce transfert est couplé à des réactions chimiques en phase liquide qui influencent sa vitesse. Dans un premier temps, des modèles sont développés selon des approches unidimensionnelles classiquement rencontrées dans la littérature. Ces approches passent par une idéalisation de l’écoulement du liquide autour des bulles. Une expression simplifiée de la vitesse du transfert bulle-liquide de CO2, est également développée et validée pour le modèle de colonne BIR. Dans un second temps, une modélisation complète des phénomènes de transport (convection et diffusion), couplés à des réactions chimiques, est réalisée en suivant une approche bidimensionnelle axisymétrique. L’influence de la vitesse de réactions sur la vitesse de transfert est étudiée et les résultats des deux approches sont également comparés. Le deuxième bloc est consacré à l’étude expérimentale du transfert gaz-liquide de CO2 dans des solutions aqueuses de NaHCO3 et de Na2CO3. A cette fin, un dispositif expérimental est développé et présenté. Du CO2 est mis en contact avec des solutions aqueuses de NaHCO3 et de Na2CO3 dans une cellule transparente. Les phénomènes provoqués en phase liquide par le transfert de CO2 sont observés à l’aide d’un interféromètre de Mach-Zehnder. Les résultats expérimentaux sont comparés à des résultats de simulation obtenus avec un des modèles unidimensionnels développés dans le premier bloc. De cette comparaison, il apparaît qu’une mauvaise estimation de la valeur de certains paramètres physico-chimiques apparaissant dans les équations de ce modèle conduit à des écarts significatifs entre les grandeurs observées expérimentalement et les grandeurs estimées par simulation des équations du modèle. C’est pourquoi une méthode d’estimation paramétrique est également développée afin d’identifier les valeurs numériques de ces paramètres physico-chimiques sur base des résultats expérimentaux. Ces dernières sont également discutées. Dans le troisième bloc, nous apportons une contribution à l’étude des cinétiques de précipitation du NaHCO3 dans un cristallisoir à cuve agitée. Cette partie du travail est réalisée en collaboration avec Vanessa Gutierrez (du service Matières et Matériaux de l’ULB). Nous contribuons à cette étude par le développement de trois outils : une table de calcul Excel permettant de synthétiser les résultats expérimentaux, un ensemble de simulations de l’écoulement au sein du cristallisoir par mécanique des fluides numérique et une nouvelle méthode d’extraction des cinétiques de précipitation du NaHCO3 à partir des résultats expérimentaux. Ces trois outils sont également utilisés de façon combinée pour estimer les influences de la fraction massique de solide et de l’agitation sur la cinétique de germination secondaire du NaHCO3. Enfin, la synthèse de l’ensemble des résultats de ces études est réalisée. Le résultat final est le développement d’un modèle mathématique complet et opérationnel des colonnes BIR. Ce modèle est développé en suivant l’approche de modélisation en compartiments, développée au cours du travail de Benoît Haut. Ce modèle synthétise les trois blocs d’études réalisées dans ce travail, ainsi que les travaux d’Aurélie Larcy (du service Transferts, Interfaces et Procédés de l’ULB) et de Vanessa Gutierrez. Les équations modélisant les différents phénomènes sont présentées, ainsi que la méthode utilisée pour résoudre ces équations. Des simulations des équations du modèle sont réalisées et discutées. Les résultats de simulation sont également comparés à des mesures effectuées sur une colonne BIR. Un accord raisonnable est observé. A l’issue de ce travail, nous disposons donc d’un modèle opérationnel de colonne BIR. Bien que ce modèle doive encore être optimisé et validé, il peut déjà être utilisé pour étudier l’effet des caractéristiques géométriques des colonnes BIR et des conditions appliquées à ces colonnes sur le comportement des simulations des équations du modèle et pour identifier des tendances. // The refined sodium bicarbonate is produced by the Solvay company using large size bubble columns, called the BIR columns. In these columns, a gaseous phase containing an air-carbon dioxyde mixture (CO2) is dispersed under the form of bubbles in an aqueous solution of sodium carbonate and sodium bicarbonate (Na2CO3 and NaHCO3, respectively). This dispersion leads to a CO2 transfer from the bubbles to the liquid phase. Inside these columns, the gaseous phase is distributed in two bubbles populations : small bubbles (a few mm of diameter) and large bubbles (a few cm of diameter). The bubble-liquid CO2 transfer is coupled with chemical reactions taking places in the liquid phase that leads to the conversion of Na2CO3 to NaHCO3. When the solution is supersaturated in NaHCO3, the NaHCO3 precipitates under the form of crystals and a liquid-solid mixture is extracted at the outlet of the BIR columns. This work, realized in collaboration with Solvay, aims to study and to model mathematically the mass transport phenomena between the phases, coupled with chemical reactions, taking places inside a BIR column. Study of bubble columns at the industrial and the pilot scale is combined to a more fundamental study at laboratory scale to improve the understanding of the BIR columns functioning and to develop a detailed mathematical modeling. The applied objective of this work is to develop a complete and operational mathematical modeling of a BIR column. This objective is supported by three blocks of work. In each block, several tools are developed and used. The first block is devoted to the mathematical modeling of the bubble-liquid CO2 transfer in an NaHCO3 and Na2CO3 aqueous solution. This transfer is coupled with chemical reactions in liquid phase, which affect the transfer rate. In a first time, mathematical models are developed following the classical one-dimensional approaches of the literature. These approaches idealize the liquid flow around the bubbles. A simplified expression of the bubble-liquid CO2 transfer rate is equally developed and validated for the BIR column model. In a second time, a complete modeling of the transport phenomena (convection and diffusion) coupled with chemical reactions is developed, following an axisymmetrical twodimensional approach. The chemical reaction rate influence on the bubble-liquid transfer rate is studied and the results of the two approaches are then compared. The second block is devoted to the experimental study of the gas-liquid CO2 transfer to NaHCO3 and Na2CO3 aqueous solutions. An experimental set-up is developed and presented. CO2 is put in contact with NaHCO3 and Na2CO3 aqueous solutions in a transparent cell. The phenomena induced in liquid phase by the CO2 transfer are observed using a Mach-Zehnder interferometer. The experimental results are compared to simulation results that are obtained using one of the one-dimensional model developed in the first block. From this comparison, it appears that a wrong estimation of some physico-chemical parameter values leads to significative differences between the experimentally observed quantities and those estimated by simulation of the model equations. Therefore, a parametric estimation method is developed in order to estimate those parameters numerical values from the experimental results. The found values are then discussed. In the third block is presented a contribution to the NaHCO3 precipitation kinetic study in a stirred-tank crystallizer. This part of the work is realized in collaboration with Vanessa Gutierrez (Chemicals and Materials Department of ULB). Three tools are developed : tables in Excel sheet to synthetize the experimental results, a set of simulations of the flow inside the crystallizer by Computational Fluid Dynamic (CFD) and a new method to extract the NaHCO3 precipitation kinetics from the experimental measurements. These three tools are combined to estimate the influences of the solid mass fraction and the flow on the NaHCO3 secondary nucleation rate. Finally, the synthesis of all these results is realized. The final result is the development of a complete and operational mathematical model of BIR columns. This model is developed following the compartmental modeling approach, developed in the PhD thesis of Benoît Haut. This model synthetizes the three block of study realized in this work and the studies of Aurélie Larcy (Transfers, Interfaces and Processes Department of ULB) and those of Vanessa Gutierrez. The equations modeling the phenomena taking place in a BIR column are presented as the used method to solve these equations. The equations of the model are simulated and the results are discussed. The results are equally compared to experimental measurement realized on a BIR column. A reasonable agreement is observed. At the end of this work, an operational model of a BIR column is thus developed. Although this model have to be optimized and validated, it can already be used to study the influences of the geometrical characteristics of the BIR columns and of the conditions applied to these columns on the behaviour of the model equation simulations and to identity tendencies.

The link between anthropogenic emissions of CO2 with increased atmospheric CO2 levels and, in turn, with increased global temperature has been well established and accepted. Using aqueous ammonia to capture CO2 and produce an inexpensive nitrogen fertilizer, ammonium bicarbonate (ABC) has been thought as a feasible approach to CO2 sequestration. Due to the different concentrations of reactants and reaction conditions, different carbon-ammonium composites can be produced. In view of achieving a maximum of NH3 utilization in the capture of CO2, the product of ABC will be ideal. Hence the ABC in the products needs to be identified. Various analytical techniques were used to distinguish the ABC. FTIR, DSC, TGA and XRD techniques were used to qualitatively distinguish the ammonium bicarbonate from the ammonium salts. The carbon, hydrogen and nitrogen element analysis and Near Infrared (NIR) techniques were used as quantitative analysis of ABC. The AOTF-NIR Free Space spectrometer is an ideal tool for real-time, on-line measurements of ABC. Sample 01050401 and Sample 01060401 from the CO2 Scrubbing experiment by aqueous ammonia at WKU were determined by these techniques as ammonium bicarbonate and have very good quality as fertilizer in accordance with GB -3559-92 Agriculture Ammonium Bicarbonate National Standard of China. During fertilizer storage and application, an amount of ABC will decompose into NH3, H2O and CO2. Long-effect ABC (LEABC) is a product of co-crystallized dicyanodiamide (DCD) and ABC. In order to evaluate ABC fertilizer efficiency and its contribution to permanent carbon fixation, tests with Thermogravimetric Analysis (TGA) were conducted. The experiments by TGA indicated that the temperature and air flow rate have much less effect on the evaporation of the LEABC than on the ABC. Kinetic studies of ABC and LEABC gave their Activation Energy. At the 7.5% conversion rate, LEABC’s Activation Energy is 111.9 kJ/mole, which is greater than ABC’s Activation Energy 93.6 kJ/mole. The difference in Activation Energy explains the reason of different stability of ABC and LEABC.

Thesis (Ph.D.)--University of Alabama at Birmingham, 2009. / Title from PDF title page (viewed on Feb. 2, 2010). Includes bibliographical references.