ABSTRACT
We studied the peptide-degrading anaerobic communities of methanogenic reactors from two mesophilic full-scale modified upflow anaerobic sludge blanket (UASB) reactors treating brewery wastewater in Colombia. Most probable number (MPN) counts varied between 7.1 x 10(8) and 6.6 x 10(9) bacteria/g volatile suspended solids VSS (Methanogenic Reactor 1) and 7.2 x 10(6) and 6.4 x 10(7) bacteria/g (VSS) (Methanogenic Reactor 2). Metabolites detected in the highest positive MPN dilutions in both reactors were mostly acetate, propionate, isovalerate and, in some cases, negligible concentrations of butyrate. Using the highest positive dilutions of MPN counts, 50 dominant strains were isolated from both reactors, and 12 strains were selected for sequencing their 16S rRNA gene based on their phenotypic characteristics. The small-subunit rRNA gene sequences indicated that these strains were affiliated to the families Propionibacteriaceae, Clostridiaceae and Syntrophomonadaceae in the low G + C gram-positive group and Desulfovibrio spp. in the class d-Proteobacteria. The main metabolites detected in the highest positive dilutions of MPN and the presence of Syntrophomonadaceae indicate the effect of the syntrophic associations on the bioconversion of these substrates in methanogenic reactors. Additionally, the potential utilization of external electron acceptors for the complete degradation of amino acids by Clostridium strains confirms the relevance of these acceptors in the transformation of peptides and amino acids in these systems.
Subject(s)
Wastewater , Base Sequence , Gram-Negative Anaerobic Bacteria/genetics , Gram-Negative Anaerobic Bacteria/isolation & purification , Peptides/analysis , Peptides/genetics , RNA Stability , RNA, Bacterial , Sequential Biological Reactors , Metabolism , Methods , Methods , VirulenceABSTRACT
The effect of sequencing batch reactor (SBR) operating conditions on sludge macromolecular composition and the effect of sludge macromolecular composition on the anaerobic degradation of the sludge produced in SBR was investigated in this work. A SBR, fed with synthetic wastewater, was operated at different air flow rates. The resulting sludge was analyzed in terms of protein, carbohydrate, phospholipid and polyhydroxybutyrate concentrations. Methane production during anaerobic digestion of the sludge was also measured. Ammonium, nitrite, nitrate, dissolved oxygen and chemical oxygen demand (COD) track studies in the SBR were carried out in order to relate SBR performance and sludge macromolecular composition. The lowest air flow rate at which the SBR was operated was 2 l min-1, in which case the dissolved oxygen concentration was lower than 0.5 mg l-1 in the SBR and partial denitrification occurred during the feeding phase. An increased air flow rate caused a decrease in protein concentration, as well as an increase in carbohydrate concentration. Polyhydroxybutyrate (PHB) concentration in the sludge was independent of air flow rate. At different air flows, the methane production rates were similar, but the total volume of methane was greater during anaerobic digestion of the sludge produced at low air flow rates. These results indicate a strategy by which changes in sludge composition can optimize the operation of anaerobic sludge digesters.
Subject(s)
Wastewater/analysis , Wastewater/chemistry , Anaerobic Digestion/analysis , Chemical Waste Degradation , Carbon/chemistry , Hydroxybutyrates/analysis , Nitrogen/chemistry , Sequential Biological Reactors/methodsABSTRACT
Este trabalho teve como objetivo propor uma metodologia de dimensionamento para o volume do RSB. O desenvolvimento do modelo matemático para calcular o volume do reator foi realizado a partir da modelagem fenomenológica do comportamento do lodo. A metodologia ora proposta foi aplicada em estudo de caso para comparação com metodologias já consolidadas no dimensionamento do sistema de lodos ativados em batelada. A partir da metodologia apresentada neste trabalho, a determinação do volume do reator e do ciclo operacional mostrou que é possível contribuir para o dimensionamento do RSB sem transgredir o conhecimento da ação do lodo sobre a matéria orgânica e sem admitir fluxo contínuo no comportamento hidráulico do reator.
The purpose of this study was to propose a methodology for sizing SBR volumes. The mathematical model to calculate reactor volume was developed by modeling sludge behavior phenomena. The methodology proposed here was applied to a case study in order to compare it to already consolidated methods used to size the activated sludge batch system. The reactor volume and operational cycle were determined based on the method presented here, showing that it is possible to help size the SBR without challenging knowledge regarding the action of sludge on organic matter, and without allowing continuous flow into the hydraulic compartment of the reactor.
Subject(s)
Activated Sludges , Optimization of Sanitary Sewer Network , Sequential Biological Reactors , Activated SludgesABSTRACT
Este artigo apresenta uma metodologia para o dimensionamento racional de reatores biológicos para tratamento de esgoto pelo processo de lodos ativados com operação em bateladas, visando à remoção de carga orgânica. O método de cálculo desenvolvido equaciona todos os parâmetros simultaneamente envolvidos no processo, modelando a interação (decorrente do emprego de um mesmo tanque, alternadamente, como reator biológico e decantador final) dos fatores determinantes do desempenho da unidade de tratamento. O trabalho contém breve revisão da literatura concernente ao assunto estudado, seguida da dedução do modelo matemático proposto, de um roteiro de dimensionamento sugerido e de um exemplo de aplicação do método elaborado.