Problemas associados à instalação de subestações de energia em malha urbana. Caso de estudo da subestação de parceiros em Leiria

No âmbito do desenvolvimento da dissertação do Mestrado de Engenharia Eletrotécnica – Sistemas Elétricos de Energia, surgiu a oportunidade de participar no desenvolvimento de um projeto integrante numa subestação de energia. O presente caso de estudo tem em vista a resolução de condicionantes na conceção desta subestação, tais como cumprir requisitos estéticos projetando todo o tipo de equipamentos dentro de edifícios, a ventilação das salas de transformação assim como insonorização de todo o ruído produzido de forma a cumprir os limites legais e não perturbar a vizinhança. A presente subestação de energia está situada numa zona urbana da cidade de Leiria, localidade de Parceiros, dando origem ao nome Subestação de Energia de Parceiros. Esta subestação pertence ao cliente Energias de Portugal, conhecida como EDP, e visa o melhoramento da distribuição do serviço eléctrico. As tradicionais subestações de energia, com aparência bastante desenquadrada dos meios urbanos, representam um entrave ao nível da aproximação destes centros de produção energética às zonas urbanas, comprometendo a melhoria da rede elétrica. Desta forma, foi implementada a tecnologia Gas-Insolated Switchgear e permite o enquadramento destes centros energéticos em zonas urbanas, constituindo mais um edifício urbano na zona onde se insere. Esta substitui os convencionais barramentos existentes nos Parques Exteriores de Aparelhagem das subestações e apresenta-se com dimensões muito reduzidas quando comparadas com as estruturas instaladas nestes parques. Dado que esta tecnologia é desenvolvida no sentido de permitir a construção destes centros energéticos em zonas urbanas, podem ser alojadas dentro de edifícios produzindo assim vantagens ao nível estético, não perturbando a paisagem. Dado que os principais equipamentos de funcionamento na subestação de Parceiros, nomeadamente o Transformador de Potência, se encontram instalados num edifício completamente fechado, foram construídas duas salas de ventilação, na parte superior deste edifício, cada uma adjacente a uma sala de transformação. O transformador instalado possui elevadas dimensões, pesando 53000 kg e contendo 11000 kg de óleo que em estado normal de funcionamento circula por quase todo o interior da máquina a elevadas temperaturas, provocando um aquecimento elevado no interior do edifício o que condiciona o bom funcionamento do transformador. Para ultrapassar esta condicionante foi realizado um estudo de um sistema de ventilação capaz de avaliar e controlar os valores térmicos existentes e proceder à circulação de ar, que será movimentado ou bloqueado, recorrendo a um sistema autónomo, mantendo a temperatura ideal nas salas de transformação. Este autómato é o cérebro de toda a cadeia lógica que, mediante as leituras efetuadas irá dar ordens de atuação aos diversos equipamentos. Apesar dos TP estarem protegidos dentro do edifício, estes produzem um maior ruído. A necessidade da existência do referido sistema de ventilação das divisões de funcionamento destas máquinas, implica a utilização de aparelhos que, apesar da sua evolução tecnológica os torna cada vez menos ruidosos, mas geram sempre alguma perturbação, o que pode representar um problema no cumprimento do regulamento geral do ruído.

Efeito da razão de submersão sobre os parâmetros hidrodinâmicos de uma coluna de recirculação de líquido através de um tubo exterior

No trabalho realizado nesta tese, procedeu-se ao estudo hidrodinâmico de uma coluna de borbulhamento de recirculação externa do líquido (CREL), que permitiu ampliar o conhecimento já existente sobre este tipo de colunas. Para realizar este estudo utilizaram-se líquidos viscosos Newtonianos, nomeadamente soluções aquosas de glicerina com viscosidades entre 0,007 e 0,522 Pa.s. Para a gama de caudais de ar injectados, 1,5x10-5 até 1,35x10-4 m3/s, o ar ascendia ao longo da coluna de borbulhamento sob a forma de bolhas tubulares. Após a realização dos ensaios, verificou-se que o regime de escoamento do líquido entre bolhas tubulares variou desde o tipo laminar até transição (1,9

Biofiltration of Air/Styrene and Air/Styrene/Acetone mixtures in a bubble column reactor

The goal of this work was the treatment of polluted waste gases in a bubble column reactor (BCR), in order to determinate the maximum value of reactor’s efficiency (RE), varying the inlet concentration (C in) of the pollutants. The gaseous mixtures studied were: (i) air with styrene and (ii) air with styrene and acetone. The liquid phase used to contain the biomass in the reactor was a basal salt medium (BSM), fundamental for the microorganisms’ development. The reactor used in this project consists of a glass column of 620mm height and inside diameter 75mm. In all essays there were continually measured: pH, dissolved oxygen and liquid’s temperature. Temperature and pH were controlled (T=24ºC, 7.0 ≤ pH ≤ 7.7). In all experiments the liquid volume (including the biomass) used in the reactor was kept constant (1.5L) as well as the total gas flowrate (1 L/min). Concerning the goal of the work, some parameters were calculated: the organic load (OL), removal efficiency (RE), elimination capacity (EC), biomass concentration (xf) and dry biomass concentration (Xdw). In a first series of experiments, the gas mixture used was air with styrene, varying its concentration from 191 mg.m-3 to 6500 mg.m-3.It was concluded that the RE maximum value (97%) was obtained for C in Sty = 4200 mg.m-3. For the maximum tested value of C in Sty, RE obtained was 20%. In a second step, the gaseous mixture included acetone, varying C in Sty between 225 mg.m-3 and 2659 mg.m-3 and C in Ac between 153mg.m-3 and 1389 mg.m-3. The aim of these tests was the determination of C in Ac for which RE was maximum, obtaining C in Ac = 750 mg.m-3. A third series of experiments was performed, in which C in Ac was maintained equal to that value and C in Sty was varied until higher values (5422 mg.m-3). RE maximum values obtained in this last series were 100% for styrene and 40% for acetone. One important conclusion is the fact that the microorganisms available degrade better styrene than acetone. On the ambit of this study, it was possible to identify the species available in biomass: Xanthobacter antotrophicus py2, Enterobacter aerogenes, Nocardia, Corynebacterium Spp., Rhodococcus rhodochrous e Pseudomonas Sp.

Avaliação do desempenho energético e da qualidade do ar de uma piscina coberta

Este trabalho teve como propósito fazer uma avaliação do desempenho energético e da qualidade do ar no interior das instalações de uma Piscina Municipal Coberta, localizada na zona norte de Portugal, sendo estabelecidos os seguintes objetivos: caracterização geral da piscina, no que respeita aos seus diferentes espaços e equipamentos, cálculo dos consumos térmicos e elétricos bem como o registo das concentrações de elementos poluentes para controlo da qualidade do ar no interior da piscina, tendo como base a legislação atualmente em vigor. A caracterização geral da piscina permitiu verificar algumas inconformidades como a temperatura da água nos tanques de natação que tem valores superiores aos recomendados e a sala de primeiros socorros que não possui acesso direto ao exterior. Acrescente-se que o pavimento nos chuveiros da casa de banho feminina e os valores de pH para água do tanque grande e pequeno não estão sempre dentro da gama de recomendação. O caudal da renovação de ar está a ser operado manualmente e quando está a funcionar a 50% da sua capacidade máxima, que acontece numa parte do dia, apenas consegue renovar 77,5% do caudal recomendado pelo RSECE. Para se obter o valor recomendado é necessário ter pelo menos 7 horas com o caudal a 100% da capacidade máxima. A avaria na UTA2 originou que 40% dos registos diários da humidade relativa interior estivessem fora da gama de valores recomendados e que esta é fortemente dependente da humidade no exterior e pode ser agravada quando as portas dos envidraçados da nave são abertas. Analisando ainda a quantidade de água removida na desumidificação do ar com a água evaporada em condições de Outono-Inverno ou Primavera-Verão, este estudo permitiu concluir que todas as combinações demonstraram a necessidade de desumidificação salvo a combinação Outono-Inverno e UTA2 a funcionar a 100% da sua capacidade máxima. Os isolamentos das tubagens na sala das caldeiras foram observados e comparados com as soluções recomendadas pelas empresas especialistas e verificou-se que alguns estão mal colocados com parcial ou total degradação, promovendo perdas térmicas. No caso das perdas calorificas por evaporação, estas representaram cerca de 67,78% das perdas totais. Como tal, estudou-se a aplicação de uma cobertura sobre o plano de água durante o período de inatividade da piscina (8 horas) e verificou-se que o resultado seria uma poupança de 654,8 kWh/dia, na ausência de evaporação da água, mais 88,00 kWh/dia do período da UTA2 a funcionar a 50% da sua capacidade, perfazendo um total de 742,8 kWh/dia. A aplicação da cobertura permite obter um VAL de valor positivo, uma TIR de 22,77% e sendo este valor superior ao WACC (Weight Average Cost of Capital), o projeto torna-se viável com um Pay-Back de 3,17 anos. Caracterizou-se também o consumo total diário em eletricidade, e verificou-se que as unidades de climatização, as bombas de circulação de água, a iluminação, e outros equipamentos representam, respetivamente, cerca de 67,81, 25,26, 2,68 e 3,91% da energia elétrica total consumida. Por fim, a análise à qualidade do ar no interior da nave em Maio e Setembro identificou que as concentrações de ozono apresentavam valores no limite do aceitável em Maio e superiores ao valor de emissão em Setembro. Os compostos orgânicos voláteis também apresentavam valores em Maio 4,98 vezes superior e em Setembro 6,87 vezes superior aos valores máximos exigidos pelo D.L. nº 79/2006. Houve ainda altas concentrações de radão registadas na casa dos filtros, em Maio com um valor 11,49 vezes superior, no entanto esse valor desceu em Setembro para 1,08 vezes, mesmo assim superior ao exigido pelo D.L. nº 79/2006.

Air pollution from traffic emissions in Oporto, Portugal: health and environmental implications

Air pollution represents a serious risk not only to environment and human health, but also to historical heritage. In this study, air pollution of the Oporto Metropolitan Area and its main impacts were characterized. The results showed that levels of CO, PM10 and SO2 have been continuously decreasing in the respective metropolitan area while levels of NOx and NO2 have not changed significantly. Traffic emissions were the main source of the determined polycyclic aromatic hydrocarbons (PAHs; 16 PAHs considered by U.S. EPA as priority pollutants, dibenzo[a,l]pyrene and benzo[j]fluoranthene) in air of the respective metropolitan area. The mean concentration of 18 PAHs in air was 69.9±39.7 ng m−3 with 3–4 rings PAHs accounting for 75% of the total ΣPAHs. The health risk analysis of PAHs in air showed that the estimated values of lifetime lung cancer risks considerably exceeded the health-based guideline level. Analytical results also confirm that historical monuments in urban areas act as passive repositories for air pollutants present in the surrounding atmosphere. FTIR and EDX analyses showed that gypsum was the most important constituent of black crusts of the characterized historical monument Monastery of Serra do Pilar classified as “UNESCO World Cultural Heritage”. In black crusts, 4–6 rings compounds accounted approximately for 85% of ΣPAHs. The diagnostic ratios confirmed that traffic emissions were the major source of PAHs in black crusts; PAH composition profiles were very similar for crusts and PM10 and PM2.5.

Remediation efficiency of vapour extraction of sandy soils contaminated with cyclohexane: influence of air flow rate, water and natural organic matter content

Abstract This work reports the analysis of the efficiency and time of soil remediation using vapour extraction as well as provides comparison of results using both, prepared and real soils. The main objectives were: (i) to analyse the efficiency and time of remediation according to the water and natural organic matter content of the soil; and (ii) to assess if a previous study, performed using prepared soils, could help to preview the process viability in real conditions. For sandy soils with negligible clay content, artificially contaminated with cyclohexane before vapour extraction, it was concluded that (i) the increase of soil water content and mainly of natural organic matter content influenced negatively the remediation process, making it less efficient, more time consuming, and consequently more expensive; and (ii) a previous study using prepared soils of similar characteristics has proven helpful for previewing the process viability in real conditions.

PAH air pollution at a Portuguese urban area: carcinogenic risks and sources identification

This study aimed to characterize air pollution and the associated carcinogenic risks of polycyclic aromatic hydrocarbon (PAHs) at an urban site, to identify possible emission sources of PAHs using several statistical methodologies, and to analyze the influence of other air pollutants and meteorological variables on PAH concentrations.The air quality and meteorological data were collected in Oporto, the second largest city of Portugal. Eighteen PAHs (the 16 PAHs considered by United States Environment Protection Agency (USEPA) as priority pollutants, dibenzo[a,l]pyrene, and benzo[j]fluoranthene) were collected daily for 24 h in air (gas phase and in particles) during 40 consecutive days in November and December 2008 by constant low-flow samplers and using polytetrafluoroethylene (PTFE) membrane filters for particulate (PM10 and PM2.5 bound) PAHs and pre-cleaned polyurethane foam plugs for gaseous compounds. The other monitored air pollutants were SO2, PM10, NO2, CO, and O3; the meteorological variables were temperature, relative humidity, wind speed, total precipitation, and solar radiation. Benzo[a]pyrene reached a mean concentration of 2.02 ngm−3, surpassing the EU annual limit value. The target carcinogenic risks were equal than the health-based guideline level set by USEPA (10−6) at the studied site, with the cancer risks of eight PAHs reaching senior levels of 9.98×10−7 in PM10 and 1.06×10−6 in air. The applied statistical methods, correlation matrix, cluster analysis, and principal component analysis, were in agreement in the grouping of the PAHs. The groups were formed according to their chemical structure (number of rings), phase distribution, and emission sources. PAH diagnostic ratios were also calculated to evaluate the main emission sources. Diesel vehicular emissions were the major source of PAHs at the studied site. Besides that source, emissions from residential heating and oil refinery were identified to contribute to PAH levels at the respective area. Additionally, principal component regression indicated that SO2, NO2, PM10, CO, and solar radiation had positive correlation with PAHs concentrations, while O3, temperature, relative humidity, and wind speed were negatively correlated.

Numerical solution of a PDE system with non-linear steady state conditions that translates the air stripping pollutants removal

This work deals with the numerical simulation of air stripping process for the pre-treatment of groundwater used in human consumption. The model established in steady state presents an exponential solution that is used, together with the Tau Method, to get a spectral approach of the solution of the system of partial differential equations associated to the model in transient state.

Project, modelling and simulation of air stripping columns for the treatment of groundwater contaminated with volatile organic compounds

Volatile organic compounds are a common source of groundwater contamination that can be easily removed by air stripping in columns with random packing and using a counter-current flow between the phases. This work proposes a new methodology for the column design for any particular type of packing and contaminant avoiding the necessity of a pre-defined diameter used in the classical approach. It also renders unnecessary the employment of the graphical Eckert generalized correlation for pressure drop estimates. The hydraulic features are previously chosen as a project criterion and only afterwards the mass transfer phenomena are incorporated, in opposition to conventional approach. The design procedure was translated into a convenient algorithm using C++ as programming language. A column was built in order to test the models used either in the design or in the simulation of the column performance. The experiments were fulfilled using a solution of chloroform in distilled water. Another model was built to simulate the operational performance of the column, both in steady state and in transient conditions. It consists in a system of two partial non linear differential equations (distributed parameters). Nevertheless, when flows are steady, the system became linear, although there is not an evident solution in analytical terms. In steady state the resulting system of ODE can be solved, allowing for the calculation of the concentration profile in both phases inside the column. In transient state the system of PDE was numerically solved by finite differences, after a previous linearization.

Experimental assessment of pressure drop in air stripping columns

One important step in the design of air stripping operations for the removal of VOC is the choice of operating conditions, which are based in the phase ratio. This parameter sets on directly the stripping factor and the efficiency of the operation. Its value has an upper limit determined by the flooding regime, which is previewed using empirical correlations, namely the one developed by Eckert. This type of approach is not suitable for the development of algorithms. Using a pilot scale column and a convenient solution, the pressure drop was determined in different operating conditions and the experimental values were compared with the estimations. This particular research will be incorporated in a global model for simulating the dynamics of air stripping using a multi variable distributed parameter system.

Practical software improve design and performance of a randomly packed air stripping column for removing volatile organic compounds from water

STRIPPING is a software application developed for the automatic design of a randomly packing column where the transfer of volatile organic compounds (VOCs) from water to air can be performed and to simulate it’s behaviour in a steady-state. This software completely purges any need of experimental work for the selection of diameter of the column, and allows a choice, a priori, of the most convenient hydraulic regime for this type of operation. It also allows the operator to choose the model used for the calculation of some parameters, namely between the Eckert/Robbins model and the Billet model for estimating the pressure drop of the gaseous phase, and between the Billet and Onda/Djebbar’s models for the mass transfer. Illustrations of the graphical interface offered are presented.

Spectral solution for the air stripping pollutants removal dynamic model with non linear steady state conditions

This work deals with the numerical simulation of air stripping process for the pre-treatment of groundwater used in human consumption. The model established in steady state presents an exponential solution that is used, together with the Tau Method, to get a spectral approach of the solution of the system of partial differential equations associated to the model in transient state.

A New Approach in the Design of Air Stripping Columns for the Treatment of Groundwater Contaminated With Volatile Organic Compounds

Volatile organic compounds are a common source of groundwater contamination that can be easily removed by air stripping in columns with random packing and using a counter-current flow between the phases. This work proposes a new methodology for column design for any type of packing and contaminant which avoids the necessity of an arbitrary chosen diameter. It also avoids the employment of the usual graphical Eckert correlations for pressure drop. The hydraulic features are previously chosen as a project criterion. The design procedure was translated into a convenient algorithm in C++ language. A column was built in order to test the design, the theoretical steady-state and dynamic behaviour. The experiments were conducted using a solution of chloroform in distilled water. The results allowed for a correction in the theoretical global mass transfer coefficient previously estimated by the Onda correlations, which depend on several parameters that are not easy to control in experiments. For best describe the column behaviour in stationary and dynamic conditions, an original mathematical model was developed. It consists in a system of two partial non linear differential equations (distributed parameters). Nevertheless, when flows are steady, the system became linear, although there is not an evident solution in analytical terms. In steady state the resulting ODE can be solved by analytical methods, and in dynamic state the discretization of the PDE by finite differences allows for the overcoming of this difficulty. To estimate the contaminant concentrations in both phases in the column, a numerical algorithm was used. The high number of resulting algebraic equations and the impossibility of generating a recursive procedure did not allow the construction of a generalized programme. But an iterative procedure developed in an electronic worksheet allowed for the simulation. The solution is stable only for similar discretizations values. If different values for time/space discretization parameters are used, the solution easily becomes unstable. The system dynamic behaviour was simulated for the common liquid phase perturbations: step, impulse, rectangular pulse and sinusoidal. The final results do not configure strange or non-predictable behaviours.

Comparison of contaminant removal effectiveness and air change efficiency as indicator of air diffusion quality.

The ventilation efficiency concept is an attempt to quantify a parameter that can easily distinguish the different options for air diffusion in the building spaces. Thirteen strategies of air diffusion were measured in a test chamber through the application of the tracer gas method, with the objective to validate the calculation by Computational fluid dynamics (CFD). Were compared the Air Change Efficiency (ACE) and the Contaminant Removal Effectiveness (CRE), the two indicators most internationally accepted. The main results from this work shows that the values of the numerical simulations are in good agreement with experimental measurements and also, that the solutions to be adopted for maximizing the ventilation efficiency should be the schemes that operate with low speeds of supply air and small differences between supply air temperature and the room temperature.