Simulação de um sistema de tratamento de águas residuais de lamas ativadas

A modelação matemática de Estações de Tratamento de Águas Residuais (ETAR) tem sido uma ferramenta de enorme utilidade nas fases de projeto e de exploração destas estruturas de tratamento. O presente estudo teve por objetivo principal construir um modelo matemático da ETAR de Bragança, em particular do seu tratamento biológico de lamas ativadas, com vista a avaliar, compreender e otimizar o seu desempenho. A construção do modelo foi efetuada com recurso ao ambiente de simulação WRc STOAT 5.0. O processo de lamas ativadas foi descrito pelo modelo de referência ASAL3. O modelo construído foi calibrado e validado com base em dados experimentais de 2015, obtidos no âmbito do programa de controlo analítico da ETAR. O modelo foi ainda utilizado para avaliar a qualidade do efluente em resposta a alterações do caudal e composição do afluente, a alterações de condições operacionais e a outras alternativas de tratamento. O modelo mostrou-se bastante adequado na descrição da evolução mensal da qualidade do efluente final da ETAR relativamente aos parâmetros Sólidos Suspensos Totais (SST) e Carência Bioquímica de Oxigénio (CBO5), embora apresente uma tendência para os subestimar em 1,5 e 3,5 mg/L, respetivamente. Em relação ao azoto total, os valores simulados aproximaram-se dos valores reais, quando se aumentaram as taxas de recirculação interna para 400%, um fator de cerca de 4 vezes superior. Os resultados do modelo e dos cenários mostram e reforçam o bom desempenho e a operação otimizada da ETAR em relação a remoção de SST e CBO5. Em relação ao azoto total, a ETAR não assegura de forma sistemática uma eficiência elevada, mas apresenta um bom desempenho, face ao que o modelo consegue explicar para as mesmas condições operacionais. Através do estudo de cenários procurou-se encontrar alternativas de tratamento eficientes e viáveis de remoção de azoto total, mas não se identificaram soluções que assegurassem decargas de azoto abaixo dos limites legais. Os melhores resultados que se alcançaram para a remoção deste contaminante estão associados ao aumento das taxas de recirculação interna do sistema pré-anóxico existente e a uma configuração do tipo Bardenpho de quatro estágios com alimentação distribuída, em proporções iguais, pelos dois estágios anóxicos. Outras soluções que envolvam tecnologias distintas podem e devem ser equacionadas em projetos futuros que visem a melhoria de eficiência de remoção de azoto da ETAR.

Desenvolvimento de um aditivo natural à base de catequina: otimização da extração e estabilização a partir de frutos de Arbutus unedo L.

The common Mediterranean ornamental strawberry-tree (Arbutus unedo L.) produces an edible reddish sweet berry that is found to be bland and tasteless unless it is consumed overripe, otherwise it is discarded or used as basic agricultural sub residue. The bioactive properties of this fruit have been reported and related with phenolic compounds, mainly flavan-3-ols, such as catechin and procyanidins, which has opened the opportunity to exploit their extraction from alternative sources.The common Mediterranean ornamental strawberry-tree (Arbutus unedo L.) produces an edible reddish sweet berry that is found to be bland and tasteless unless it is consumed overripe, otherwise it is discarded or used as basic agricultural sub residue. The bioactive properties of this fruit have been reported and related with phenolic compounds, mainly flavan-3-ols, such as catechin and procyanidins, which has opened the opportunity to exploit their extraction from alternative sources. This study compares and optimizes the maceration, microwave and ultrasound extraction techniques in the recovery of a catechin extract from Arbutus unedo L. fruits and evaluate the stability of flavan-3-ols during storage and application processes. To obtain conditions that maximize the catechin extraction yield, a response surface methodology was used. Maceration and microwave extractions were found to be the most effective methods, capable of yielding 1.38±0.1 and 1.70±0.3 mg of catechin/g dry weight (dw) in the corresponding optimal extraction conditions. The optimal conditions for maceration were 93.2±3.7 min, 79.6±5.2 ºC and 23.1±3.7 % of ethanol, while for the microwave extraction were 42.2±4.1 min, 137.1±8.1 ºC and 12.1±1.1 % of ethanol. The microwave system was a quicker solution, conducting to slightly higher yields of catechin than maceration, but this one needed lower temperatures to reach similar yields. The ultrasound method was the least effective solution in terms of catechin yield extraction (0.71±0.1 mg/g at 42.4±3.6 min, 314.9±21.2 W and 40.3±3.8 %. ethanol). The stability was tested with of the catechin-enriched extract (60% flavan-3-ols and 22% catechin), obtained under the best maceration conditions, was tested. Therefore, catechin-enriched extracts were submitted to physical and chemical stability studies, considering the main affecting variables (time, temperature and pH): i) a stability study of the extracts during storage as powder system; and ii) a stability study of the extracts in simulated food environment (aqueous solution system). The measured responses were the flavan-3-ols and catechin contents, determined by HPLC-DAD, and the antioxidant activity of the extracts evaluated by hydrophilic assays. Mechanistic and phenomenological equations were used to describe the responses, and the optimal conditions for flavan-3-ols (including catechin) stability as powder extract during a month were pH= 5.4 and T= -20ºC; while its stability in aqueous solution remained during the 24 h of application at pH<4 and T<30ºC. This study compares and optimizes the maceration, microwave and ultrasound extraction techniques in the recovery of a catechin extract from Arbutus unedo L. fruits and evaluate the stability of flavan-3-ols during storage and application processes. To obtain conditions that maximize the catechin extraction yield, a response surface methodology was used. Maceration and microwave extractions were found to be the most effective methods, capable of yielding 1.38±0.1 and 1.70±0.3 mg of catechin/g dry weight (dw) in the corresponding optimal extraction conditions. The optimal conditions for maceration were 93.2±3.7 min, 79.6±5.2 ºC and 23.1±3.7 % of ethanol, while for the microwave extraction were 42.2±4.1 min, 137.1±8.1 ºC and 12.1±1.1 % of ethanol. The microwave system was a quicker solution, conducting to slightly higher yields of catechin than maceration, but this one needed lower temperatures to reach similar yields. The ultrasound method was the least effective solution in terms of catechin yield extraction (0.71±0.1 mg/g at 42.4±3.6 min, 314.9±21.2 W and 40.3±3.8 %. ethanol). The stability was tested with of the catechin-enriched extract (60% flavan-3-ols and 22% catechin), obtained under the best maceration conditions, was tested. Therefore, catechin-enriched extracts were submitted to physical and chemical stability studies, considering the main affecting variables (time, temperature and pH): i) a stability study of the extracts during storage as powder system; and ii) a stability study of the extracts in simulated food environment (aqueous solution system). The measured responses were the flavan-3-ols and catechin contents, determined by HPLC-DAD, and the antioxidant activity of the extracts evaluated by hydrophilic assays. Mechanistic and phenomenological equations were used to describe the responses, and the optimal conditions for flavan-3-ols (including catechin) stability as powder extract during a month were pH= 5.4 and T= -20ºC; while its stability in aqueous solution remained during the 24 h of application at pH<4 and T<30ºC.