Análise de séries temporais na operação de sistema de tratamento de águas residuárias de abatedouro de frango / Time series analysis on the operation of a poultry slaughterhouse wastewater treatment plant

Esse trabalho apresenta a avaliação de dados de operação de sistema de tratamento de águas residuárias de abatedouro de frango, através da análise de séries temporais. O objetivo principal foi a obtenção de modelo de previsão capaz de antecipar o controle da operação do sistema de tratamento de águas residuárias do abatedouro, constituindo subsídio para obtenção de estratégias de gestão do sistema de tratamento existente. Registros de 42 meses de parâmetros de monitoramento foram utilizados na modelagem de séries temporais. O modelo de ajuste exponencial para previsão dos valores de demanda química de oxigênio do efluente industrial e do afluente dos reatores biológicos apresentou bom ajuste (erro percentual absoluto da média aritmética menor que 20 por cento) com diferenças na capacidade de previsão menores que 15 por cento.

Performance and stability of an anaerobic fixed bed reactor subjected to progressive increasing concentrations of influent organic matter and organic shock loads.

Data on the performance of a horizontal-flow anaerobic immobilized biomass (HAIB) reactor subjected to step increases of organic loading rates (OLR) and to organic shock loads (OSL) are presented and discussed. The tubular reactor (100 cm long and 5 cm diameter) with a useful volume of 1995 mL was filled with polyurethane foam cubic matrices holding immobilized biomass and fed with synthetic wastewater. The reactor was operated at the controlled temperature of 30+/-1 degrees C and hydraulic retention time of 7 h. After about 15 days, the HAIB reactor attained operating stability. Thereafter, it was subjected to step increases of the applied OLR that ranged from 6.8 to 18.8 kg COD/m(3)d. After steady state had been achieved at each step, OSL corresponding to approximately three times the operating OLR were applied for 7 h. No disturbance was observed due to the step increase in OLR. An increase in effluent chemical oxygen demand (COD) and volatile fatty acids (VFA) concentrations and a decrease in the percentage of methane in the biogas were observed due to OSL applications. However, stability of the monitoring parameters was always restored approximately 17 h after the application of OSL for all conditions tested.