Suidés et tayassuidés du burdigalien V-a et du langhien V-b de lisbonne

Teeth and astragali were used for a biometrical study concerning suids from V-a (upper Burdigalian) and V-b (Langhian) divisions from Lisbon's Miocene series. The Hyotherium (V-b) are identical to those from french localities, hence they all belong in the same species H. soemmeringi. Bunolistriodon populations from V-a and V-b are homogenous; no significant difference between them has been found, inspite of different geological age. Both may be ascribed to B. lockharti. No evolutive trend was detected. The presence of another form close to the north african B. massai could not be confirmed either. French localities' Bunolistriodon populations also seem homogenous and conspecific with those from Lisbon. Notwithstanding its essentially homogenous character, there can be distinguished two sets in both V-a and V-b populations according to M3 size; this remains to be explained, since the last molars are the most likely to show a broad range of variation and are not unequivocally related to sexual dimorphism. Classification of the rare Tayassuidae has been confirmed. All known taxa are shown (see tableau I).

As barragens em Cabo Verde: Avaliação dos impactes ambientais, socioeconómicos e culturaisCaso de estudo “ A Barragem do Poilão”

Dissertação apresentada para cumprimento dos requisitos necessários à obtenção do grau de Mestre em Gestão do Território, área de especialização em Ambiente e Recursos Naturais

Modelling of a wastewater treatment plant using GPS-X

Dissertation to obtain the degree of Master in Chemical and Biochemical Engineering

Estudo e sugestões de melhorias de eficiência energética numa empresa do sector industrial de carnes

Desta dissertação resultou uma análise ao consumo energético associado aos produtos mais comerci-alizados por uma Empresa, inserida no sector industrial de carnes, e de respectivas medidas de ges-tão de energia eléctrica e de implementação de tecnologia térmica para optimizara a eficiência ener-gética da instalação. A avaliação realizada nesta dissertação permitiu identificar os processos que mais energia consomem, nomeadamente todos os produtos que envolvem a fumagem. Com base nes-tes resultados a empresa pode identificar as prioridades em termos de redução e melhoria da eficiên-cia energética. O estudo de gestão da energia eléctrica permitiu concluir que é mais proveitoso man-ter em funcionamento os processos pontuais durante os períodos nocturnos ou durante o fim-de-semana, permitindo, no segundo caso, obter uma poupança de 16% nos custos associados de cada vez que se colocar a linha de produção de peito de peru fumado entre o período semanal para o perí-odo entre sexta-feira e domingo, visto ser a linha de produção estudada que mais energia eléctrica consome. Na análise de pré-aquecimento dos fluidos utilizados na empresa através de recuperadores de calor, concluiu-se que é mais benéfico pré-aquecer a água utilizada para o processo de fumagem, visto obter-se uma poupança económica de 6 € e 11,8 m3 de gás natural por aplicação, ou seja, de cada vez que é utilizada água pré-aquecida através deste procedimento, tendo-se obtido valores de poupança energética entre 24 e 60% para os vários fluidos estudados.

Removal of organic contaminants from wastewater using the electrodialytic process

Pharmaceuticals and personal care products (PPCPs) are widely used on a daily basis. After their usage they reach the wastewater treatment plants (WWTPs). These compounds have different physico-chemical characteristics, which makes them difficult to completely remove in the WWTPs, througth conventional treatments. Currently, there is no legislation regarding PPCPs thresholds in effluent discharge. But, even at vestigial concentrations, these compounds enclose environmental risks due to, e.g., endocrine disruption potential. There is a need of alternative techniques for their removal in WWTPs. The main goal of this work was to assess the use of electrodialytic (ED) process to remove PPCPs from the effluent to be discharged. A two-compartment ED cell was used testing (i) the effluent position in the cell (anode and cathode compartment); (ii) the use of anion (AEM) and cation exchange membrane (CEM); (iii) the treatment period (6, 12 and 24 hours); (iv) effluent recirculation and current steps; (v) the feasibility of sequential treatments. Phosphorus (P) removal from effluent and energetic costs associated to the process were also evaluated. Five PPCPs were studied – caffeine (CAF), bisphenol A (BPA), 17 β-estradiol (E2), ethinyl estradiol (EE2) and oxybenzone (MBPh). The ED process showed to be effective in the removal when effluent is in the anode compartment. Oxidation is suggested to be the main removal process, which was between 88 and 96%, for all the compounds, in 6 hours. Nevertheless, the presence of intermediates and/or by-products was also observed in some cases. Effluent recirculation should have a retention time in the ED cell big enough to promote removal whereas the current steps (effluent in anode compartment) slightly increased removal efficiencies (higher than 80% for all PPCPs). The sequential set of ED treatment (effluent in anode compartment) showed to be effective during both periods with a removal percentage between 80 and 95% and 73 to 88% in the case of AEM and CEM, respectively. Again, the main removal process is strongly suggested to be oxidation in the anode compartment. However, there was an increase of BOD5 and COD, which might be explained by effluent spiking, these parameters limiting the effluent discharge. From these treatments, the use of AEM, enhanced the P removal from effluent to minimize risk of eutrophication. Energetic costs of the best set-up (6 hours) are approximately 0,8€/m3 of wastewater, a value considered low, attending to the prices of other treatment processes.