Usinas Termelétricas (UTEs), compostas por ciclo simples a vapor e ciclo combinado, são instalações industriais que consomem elevadas quantidades de água, sobretudo por conta de suas operações de resfriamento e de geração de vapor. Paralelamente, tem-se observado a redução de oferta deste recurso em muitas regiões onde se encontram instaladas unidades termelétricas, fato que suscita a preocupação, o debate e a pesquisa acerca do desenvolvimento de tecnologias e estratégias direcionadas à mitigação do consumo e reaproveitamento de água em UTEs. Em contrapartida, do mesmo modo que UTEs são intensivas no consumo de água, esta é também produzida na forma de vapor em escalas significativas como resultado do processo de combustão. Contudo, a parcela de água produzida é lançada para a atmosfera juntamente com os demais gases produzidos (CO2, N2, O2, SO2). Frente a esse contexto, este trabalho se divide em duas etapas distintas. A primeira voltada à estimativa da quantidade de água e demais componentes presentes nos gases de combustão de trinta e seis UTEs brasileiras, dentre as quais vinte e duas são movidas a gás natural (ciclos simples e combinados) e quatorze a carvão mineral (ciclos simples). Tais estimativas levam em conta as condições ambientais do local de operação, a eficiência típica do ciclo e a composição do combustível empregado. A segunda etapa trata da modelagem e da simulação, sob diferentes condições operacionais (pressão, temperatura de resfriamento e porcentagem de vapor de água nos gases), de um condensador duplo tubo vertical operando sob regime de convecção natural no lado do resfriamento, a partir do qual se estuda o processo de condensação do vapor de água na presença dos demais gases produzidos, estes conhecidos como gases não condensáveis (GNC). Tais simulações tem o propósito de avaliar as taxas de recuperação de água capazes de serem obtidas por meio do condensador/processo idealizado. / Single and combined steam cycle thermoelectric plants are power plants that consume high amounts of water, mainly from the cooling and steam generation operations. At the same time, there have been a reduction in the supply of this resource in many regions where thermoelectric units are installed. This fact increases the concern, discussion, and research on the development of technologies and new strategies directed to the mitigation of the consumption and reutilization of water. On the other hand, likewise UTEs are intensive in water consumption, they also produce it at significant amounts of steam from the combustion process, and that amount of water produced is released to the atmosphere together with gases produced (CO2, N2, O2, SO2). In this sense, this work is divided into two distinct parts. The first one is aimed at estimating the amount of water and other components present in the flue gases of thirty Brazilian thermal power plants, of which twenty-two are powered by natural gas (single and combined cycles) and eight moved by coal (single cycles). Such estimates consider environmental conditions of the operation site, typical cycle efficiency, and fuel composition employed. The second part deals with a numerical modeling and simulation, at different operating conditions (pressure, cooling temperature, and water vapor content in the gases), of a double vertical tube condenser operating by natural convection on the cooling side, from which the condensation process of the water vapor is studied in the presence of the other gases produced (known as non-condensable gases, NCG). These simulations have the fundamental purpose of evaluating the rates of condensate that can be recovered by means of the condenser/idealized process.

Catalytic pyrolysis technology is one of the thermochemical platforms used to produce high quality bio-oil and chemicals from biomass feedstocks. In the catalytic pyrolysis process, the biomass is rapidly heated under inert atmosphere in the presence of an acid catalyst or zeolite to promote deoxygenation and cracking of the primary vapors into hydrocarbons and small oxygenates. This dissertation examines the utilization of conventional fluid catalytic cracking (FCC) catalyst in the fractional catalytic pyrolysis of hybrid poplar wood. The influence of Y-zeolite content, steam treatment, addition of ZSM-5 additive, process conditions (temperature, weight hourly space velocity (WHSV) and vapor residence time) and recycling of the non-condensable gases (NCG) on the product distribution and the quality of the bio-oil were investigated. The first part of the study demonstrates the influence of catalytic property of FCC catalyst on the product distribution and quality of the bio-oil. It was found that FCC catalyst with higher Y-zeolite content produces higher coke yield and lower organic liquid fraction (OLF). Conversely, FCC catalyst with lower Y-zeolite content results in lower coke yield and higher OLF. The results showed that higher Y-zeolite content extensively cracks dehydrated products from cellulose decomposition and demethoxylates phenolic compounds from lignin degradation. The Y-zeolite promoted both deoxygenation and coke forming reactions due to its high catalytic activity and large pore size. Higher Y-zeolite content increased the quality of the bio-oil with respect to higher heating value (HHV), pH, density, and viscosity. The steam treatment at 732 oC and 788 oC decreased the total BET surface area of the FCC catalyst. The findings suggest that steam treatment reduces the coking tendency of the FCC catalyst and enhances the yield of the OLF. Analysis of the bio-oils showed that the steamed FCC catalyst produces bio-oil with lower viscosity and density. Gas chromatography and 13C-NMR spectrometry suggest that steam treatment affect the catalyst selectivity in the formation of CO, CO2, H2, CH4, C2-C5 hydrocarbons and aromatic hydrocarbons. The addition of ZSM-5 additive to the FCC catalyst was found to alter the characteristic/functionality of the catalytic medium. The product slate showed decrease in coke yield and increase in OLF with increase in ZSM-5 additive. The FCC/ZSM-5 additive hybrid catalysts produced bio-oils with relatively lower viscosity and higher pH value. The formation of CO2, CH4, and H2 decreased whilst C5 and aromatic hydrocarbons increased with increase in ZSM-5 additive level. The second part of the work assesses the effect of operating conditions on the catalytic pyrolysis process. The response surface methodology study showed reaction temperature to be the most influential statistically significant independent variable on char/coke yield, concentration of non-condensable gases, carbon content, oxygen content, pH and viscosity of the bio-oils. The WHSV was the most important statistically significant independent variable that affects the yield of organic liquid and water. Adequate and statistically significant models were generated for the prediction of the responses with the exception of viscosity. Recycling of the NCG in the process was found to potentially increase the liquid yield and decrease char/coke yield. The experiments with the model fluidizing gases showed that CO/N2, CO2/N2, CO/CO2/N2 and H2/N2 increase the liquid yield and CO2/N2 decrease char/coke yield. The results showed that recycling of NCG increases the higher heating value and the pH of the bio-oil as well as decreases the viscosity and density. The concept of recycling the NCG in the catalytic cracking of biomass vapors with FCC catalyst improved the overall process. The evaluation of the reactivity of conventional FCC catalyst towards bio-based molecules provide essential direction for FCC catalyst formulation and design for the production of high quality bio-oils from catalytic pyrolysis of biomass. / Ph. D.

Dropwise condensation, which collects the condensate liquid in the form of droplets, has attracted a growing interest due to much higher heat transfer coefficient. One important and challenging issue in dropwise condensation is the presence of non-condensable gas (NCG) which drastically reduces its heat transfer performance. Concerning the mechanism understanding, this thesis is aiming to investigate dropwise condensation in case of NCG by combing different methods. Firstly, convective dropwise condensation out of moist air is experimentally investigated under controllable conditions. In modeling, some crucial aspects are reasonably captured: the coupled heat and mass transfer during droplet growth by a multi-scale droplet growth model; the inter-droplet interaction defined by a distributed point sink method; the enhancement of the convective mass transfer using the droplet Sherwood number. Furthermore, a multi-component multi-phase thermal pseudopotential-based LB model is developed to advance the directly numerical simulation of dropwise condensation.