In Ethiopia industrial effluents containing high contents of organic matter, nitrogen and heavy metals are discharged into inland surface waters with little or no pre-treatment. Significant pollution concerns related to these effluents include dissolved oxygen depletion, toxicity and eutrophication of the receiving waters. This has not only forced the government to formulate regulations and standards for discharge limits but also resulted in an increasing interest and development of methods and systems by which wastewater can be recycled and used sustainably. The need for technologies for environmentally friendly treatment of industrial wastes such as tannery wastewaters is therefore obvious. Biological processes are not only cost effective but also environmentally sound alternatives to the chemical treatment of tannery wastewaters. The aim of the research presented in this thesis was to develop and optimize processes for biological nitrogen removal from tannery wastewaters and to identify the most efficient denitrifying organisms in tannery wastewaters laden with toxic substances. A pilot plant consisting of a predenitrification anoxic system, aerated nitrification compartment and a sedimentation tank (clarifier) all arranged in series was developed and installed on the premises of Addis Ababa University, Ethiopia. In spite of high influent chromium and sulphide perturbations over the successive feeding phases, the performance of the pilot plant was encouraging. The overall removal efficiency of the pilot plant over the experimental feeding phases varied between 82-98% for total nitrogen, 95-98% for COD, 96-98% for BOD5, 46-95% for ammonia nitrogen, 95-99% for sulphide and 93-99% for trivalent Chromium. Six isolates from over 1000 pure cultures were identified as the most efficient denitrifying bacteria. From both cellular fatty acid profiles and 16S rRNA gene sequencing, the six selected strains were phylogenetically identified as Brachymonas denitrificans in the β-subdivision of the Proteobacteria. All the six strains contain cd1-type nitrite reductase. The efficient isolates characterized in this study are of great value because of their excellent denitrifying properties and high tolerance to the concentrations of toxic compounds prevailing in tannery wastewaters. Bio-augmentation of the pilot plant with this bacterium showed a clear correlation between in situ denitrifying activities measured by nitrate uptake rate, population dynamics of the introduced B.denitrificans monitored by fluorescent in situ hybridization and the pilot plant performance, suggesting that the strategy of introducing this species for enhancing process performance has potential applications. Moreover, the nitrate-reducing, sulphur-oxidizing bacteria (NR-SOB) were also found in the pilot plant in abundance with steady sulphide removal efficiency during the study period. This could provide opportunities for the application of biologically mediated simultaneous removal of sulphide and nitrogen from tannery effluents. In addition to enriching high consortia of denitrifiers in the anoxic system to attain high denitrification efficiency and also improving the overall nitrification efficiency of the system, the predenitrification-nitrification pilot process plant stimulated the activity of indigenous NR-SOB to simultaneously remove sulphide from the system. Thus, the pilot plant was found to be operationally efficient for the removal of nitrogen, organic matter and other pollutants from tannery wastewaters. Keywords: Biological nitrogen and sulphide removal, denitrifying bacteria, nitrate-reducing, sulphur-oxidizing bacteria, nitrate uptake rate, fluorescent in situ hybridization, pollution, tannery effluents.

This master thesis in energy optimization was made during the autumn of 2006 at Käppala wastewater treatment plant in Lidingö, Stockholm. A preceding thesis, where all electricity consumption was mapped, showed that the aeration in the biological treatment is the single largest consumer in the plant, and it is therefore of interest to reduce this cost. The oxygen control strategy used at Käppala WWTP is working well from a nutrient removal point of view, but not from an economic one. The last aerobic zones have a very low oxygen consumption during low loading periods which give rise to enhanced dissolved oxygen concentrations with excessive costs and reduced denitrification as a result. But also during periods of normal loading unnecessary high oxygen concentration are sometimes given. By modifying the aeration control strategy three full-scale experiments have been made, with the intention to reduce the air consumption. The experiments were carried out during week 37-50 in the autumn of 2006 and showed that savings could be made. The regular oxygen control at Käppala WWTP controls the oxygen level in the aerobic compartment with two DO-setpoints; one in the first aerobic zone and one in the last. The zones in between are controlled by an airflow fractionation depending on the oxygen level in the first and last zone. In the first strategy to be evaluated, all four zones in the aerated part were individually controlled with its own setpoint. Two different setpoint combinations were tested. By using the fact that the efficiency in the oxygen transfer rate was higher at low airflows, savings of approximately 16 % were achieved. In the second strategy tested, an ammonia-feedback control combined with a DO-feedback controlled the DO-set point in the first aerobic zone. This strategy adjusted the DO- set points to the loading variations, and this gave a decreased airflow of approximately 9 %. Finally the two strategies were combined. All zones were then controlled individually with DO-set points set by an ammonium-feedback and a DO-feedback. The strategy gave savings in the airflow of approximately 18 %. In all three trials the aerated zones were more efficiently used, and the estimated savings are 550 000 SEK/year, and with a preserved nutrient removal efficiency. / Under hösten 2006 har ett examensarbete om energieffektivisering på Käppalaverket på Lidingö utförts. Ett föregående examensarbete där all elenergiförbrukning kartlades visade att blåsmaskinerna i biosteget står för den enskilt största förbrukningen i verket och det är därför av intresse att minska denna kostnad. Syrestyrningsstrategin som används på Käppalaverket fungerar mycket bra ur reningssynpunkt, men är inte optimal ur energisynpunkt. Dels luftas de första aeroba zonerna för mycket vid låg belastning vilket ger upphov till kraftigt förhöjda syrekoncentrationer i de sista aeroba zonerna med höga luftningskostnader och risk för försämrad denitrifikation, men även under normal belastning har det visat sig att onödigt höga syrekoncentrationer ibland ges. Tre fullskaliga optimeringsförsök har utförts, med syfte att minska luftförbrukningen med bibehållen reningsgrad. Försöken pågick från vecka 37 till 50 hösten 2006, och visade att det finns möjlighet att spara energi genom att modifiera syrestyrningsstrategin. Den reguljära syreregleringen i Käppalaverket styr syrehalten i den aeroba bassängen mot två syrebörvärden; ett i den första luftade zonen och ett i den sista. Luftflödet till de mellanliggande zonerna styrs av luftflödesandelar beroende på syrehalten i dessa två zoner. Den första strategin som utvärderades styrde istället samtliga zoner individuellt med egna börvärden, där två olika strukturer på de satta börvärdena användes. Genom att utnyttja en högre effektivitet i syreöverföringshastigheten vid låga luftflöden uppnåddes luftflödesbesparingar på ca 16 % i första försöket. I den andra strategin styrdes syrebörvärdet i den första luftade zonen med hjälp av två återkopplingar, en från utgående ammoniumhalt och en från syrehalten i den sista luftade zonen. Tack vare att strategin anpassade syrebörvärdena efter belastningen av syretärande ämnen erhölls luftflödesbesparingar på ca 9 %. Slutligen kombinerades de två strategierna; samtliga zoner styrdes individuellt med börvärden satta av en ammonium-återkoppling och en syre-återkoppling. Strategin medförde luftflödesbesparingar på ca 18 %. I samtliga försök utnyttjades de luftade zonerna bättre, och besparingspotentialen uträknad från 2005 års elpriser blev som mest 550 000 SEK/år, detta med en bibehållen reningsgrad.

<p>In Ethiopia industrial effluents containing high contents of organic matter, nitrogen and heavy metals are discharged into inland surface waters with little or no pre-treatment. Significant pollution concerns related to these effluents include dissolved oxygen depletion, toxicity and eutrophication of the receiving waters. This has not only forced the government to formulate regulations and standards for discharge limits but also resulted in an increasing interest and development of methods and systems by which wastewater can be recycled and used sustainably. The need for technologies for environmentally friendly treatment of industrial wastes such as tannery wastewaters is therefore obvious. Biological processes are not only cost effective but also environmentally sound alternatives to the chemical treatment of tannery wastewaters.</p><p>The aim of the research presented in this thesis was to develop and optimize processes for biological nitrogen removal from tannery wastewaters and to identify the most efficient denitrifying organisms in tannery wastewaters laden with toxic substances. A pilot plant consisting of a predenitrification anoxic system, aerated nitrification compartment and a sedimentation tank (clarifier) all arranged in series was developed and installed on the premises of Addis Ababa University, Ethiopia. In spite of high influent chromium and sulphide perturbations over the successive feeding phases, the performance of the pilot plant was encouraging. The overall removal efficiency of the pilot plant over the experimental feeding phases varied between 82-98% for total nitrogen, 95-98% for COD, 96-98% for BOD5, 46-95% for ammonia nitrogen, 95-99% for sulphide and 93-99% for trivalent Chromium. Six isolates from over 1000 pure cultures were identified as the most efficient denitrifying bacteria. From both cellular fatty acid profiles and 16S rRNA gene sequencing, the six selected strains were phylogenetically identified as Brachymonas denitrificans in the β-subdivision of the Proteobacteria. All the six strains contain cd1-type nitrite reductase. The efficient isolates characterized in this study are of great value because of their excellent denitrifying properties and high tolerance to the concentrations of toxic compounds prevailing in tannery wastewaters. Bio-augmentation of the pilot plant with this bacterium showed a clear correlation between in situ denitrifying activities measured by nitrate uptake rate, population dynamics of the introduced B.denitrificans monitored by fluorescent in situ hybridization and the pilot plant performance, suggesting that the strategy of introducing this species for enhancing process performance has potential applications.</p><p>Moreover, the nitrate-reducing, sulphur-oxidizing bacteria (NR-SOB) were also found in the pilot plant in abundance with steady sulphide removal efficiency during the study period. This could provide opportunities for the application of biologically mediated simultaneous removal of sulphide and nitrogen from tannery effluents. In addition to enriching high consortia of denitrifiers in the anoxic system to attain high denitrification efficiency and also improving the overall nitrification efficiency of the system, the predenitrification-nitrification pilot process plant stimulated the activity of indigenous NR-SOB to simultaneously remove sulphide from the system. Thus, the pilot plant was found to be operationally efficient for the removal of nitrogen, organic matter and other pollutants from tannery wastewaters.</p><p><b>Keywords:</b> Biological nitrogen and sulphide removal, denitrifying bacteria, nitrate-reducing, sulphur-oxidizing bacteria, nitrate uptake rate, fluorescent in situ hybridization, pollution, tannery effluents.</p>

Estudou-se nesta pesquisa o processo de lodos ativados para pós-tratamento do efluente proveniente de um reator anaeróbio compartimentado, que recebe esgoto sanitário. Isso se deu em vários ensaios em sistema descontínuo (\"batch\'\') para avaliar a biodegradabilidade dessa água residuária e em um ensaio em sistema contínuo com finalidade de melhorar a qualidade do efluente final e determinar os coeficientes cinéticos, os parâmetros a\' e b \', a taxa de utilização de oxigênio e o coeficiente &#945. Também realizaram-se ensaios hidrodinâmicos para verificação do tipo de reator utilizado. A pesquisa desenvolveu-se com base em uma célula de aeração, em escala de laboratório, composta por quatro câmaras (reatores) que possuíam tanque de aeração e decantador secundário justapostos, separados por uma cortina fixa. Não houve controle de temperatura nos dois sistemas utilizados. No ensaio em sistema contínuo quatro reatores foram operados simultaneamente com as respectivas idades do lodo de 5, 10, 15 e 20 dias durante 35 dias. O tempo de detenção hidráulico foi mantido próximo de 8 horas. Nesse ensaio os reatores quando se encontravam estabilizados dinamicamente, apresentaram remoção superior a 95% para DBO bruta, 90% para DBO filtrada, 87% para DQO bruta, 80% para DQO filtrada e 95% para SST. Mesmo não sendo realizado processo adicional para remoção de nutrientes, os reatores, após a estabilização dinâmica, apresentaram remoção de fosfato de até 28% e de nitrogênio amoniacal até níveis de não serem detectados pelos métodos de análises utilizados. Os ensaios hidrodinâmicos mostraram que os reatores são do tipo mistura completa. / In this work the activated sludge process for post-treatment of effluent anaerobic baffled reactor which receives sanitary sewage was studied. This was established during various experiments in batch system to evaluate the biodegradable of this wastewater and also in an experiment of continuous system aiming to improve the quality of the final effluent and to determine the kinetic coefficients, the a\' and b\' parameters, the oxygen uptake rate and the &#945 coefficient. Hydrodynamic tests to verify the type of reactor used in this research were also perfonned. The work was developed and based on an aeration cell bench-scale, composed of four chambers (reactors) which had an aeration tank and a secondary settling tank in the same chamber, separated by a fixed baffle. Temperature control was not used in both systems. In the experiment of continuous system, four reactors were simultaneously operated with sludge age of 5, 10, 15 and 20 days during 35 days. The hidraulic retention time was maintained at around 8 hours. When the reactors were dynamically stabilized, they showed an average removal superior to 95% for BOD (biochemical oxygen demand), 90% for filtrated BOD, 87% for COD (chemical oxygen demand), 80% for filtrated COD and 95% for TSS (total suspended solids). Without additional process of nutrient removal, after the dynamic stabilization the reactors presented up to 28% of total phosphate removal and ammonia nitrogen up to levels of not being detected by the analyses methods used. The hydrodynamic tests showed that the reactors are of the complete-mix type.

La bactérie hyperthermophile Thermotoga maritima a été cultivée dans un fermenteur dans lequel la concentration en O2 a été rigoureusement contrôlée. A 80°C et pH 7, il a été démontré que T. maritima pouvait survivre à des expositons de durées variables à l’O2 et qu’elle était capable de le consommer. La vitesse spécifique de consommation de l’O2 a été estimée à 73.6 µmoles O2.min-1.g protéines-1 lors d’une courte exposition à l’O2 (30 min). De longues expositions à l’O2 (20 h) nous ont permis de démontrer que la présence d’O2 ralentissait la croissance de T. maritima et conduisait à un shift du métabolisme vers la production de lactate aux dépens de l’acétate et à un arrêt de production d’H2. Dans ces conditions, il a été constaté que 73% du glucose était consommé selon un métabolisme partiellement oxydatif faisant intervenir simultanément les deux voies Embden-Meyerhof et Entner-Doudoroff de la glycolyse. En l’occurrence, l’oxydation incomplète du glucose est corrélée à la réduction de l’O2 en eau. Les études transcriptomiques ont montré que cette réduction de l’O2 résultait d’une cascade de réactions intermédiaires faisant intervenir des enzymes de type peroxydases [activation de l’expression des enzymes Ahp (alkyl hydroperoxyde réductase), Bcp1 et Bcp2 (thiol peroxydase thioredoxin-dépendante)] qui acheminent les électrons libérés via les radicaux libres. D’autres enzymes comme la rubréryhtrine et la neelarédoxine interviendraient pour détoxiquer les espèces réactives d’O2. Les électrons libérés seraient au final utilisés pour réduire l’O2 en H2O par l’enzyme FprA, dont l’expression varie en fonction du potentiel redox du milieu de culture. Ce schéma est proposé comme un des éléments essentiels du dispositif enzymatique permettant la consommation de l’O2 et la protection des cellules contre les effets des espèces réactives de l’oxygène chez T. maritima. / Batch cultures of the hyperthermophilic bacterium Thermotoga maritima were performed in a bioreactor where O2 concentrations in the gas phase were strictly controlled. At 80°C and pH 7, we demonstrated that T. maritima survived despite being exposed to oxygen at different times and that it consumed it. O2 uptake rate was estimated at 73.6 µmoles O2 min-1g proteins-1 during a short exposure to O2 (30 minutes). A long time exposure of T. maritima cultures to oxygen (20h) led to a drastic reduction in growth, together with a shift in glucose metabolism towards lactate instead of acetate production and a stop in H2 production. Under these conditions, it has been observed that 73% of glucose was partially oxidised by using both Embden-Meyerhof and Entner-Doudoroff glycolytic payhways. Uncomplete oxidation of glucose is correlated to a reduction of O2 to H2O. Transcription analyses revealed that this reductive process of O2 involved enzymes like peroxidases [activation of alkyl hydroperoxide reductase (ahp), bcp1 and thioredoxin-dependent thiol peroxidase (bcp 2)]. Moreover, genes encoding reactive oxygen species (ROS)-scavenging systems (neelaredoxin and rubrerythrin), were found to be upregulated during oxygen exposure. The oxygen reductase FprA, which expression was shown to depend on the redox level of the culture medium, is proposed as a primary consumer of O2. All these enzymes are essential for T. maritima to consume O2 consumption and to fight against the toxic effects of ROS in cells.

No description available.

Partial Nitritation/Anammox process (deammonification process), by which occurs oxidation of ammonium to nitrogen gas by autotrophic bacteria in anaerobic conditions, considered to be cost-effective and environmentally friendly method of nitrogen removal. Present research work focuses on achieving a high nitrogen removal degree, thanks to Anammox bacteria, while providing the best performance of the ongoing process. Integrated fixed-film activated sludge (IFAS) reactor was supplied with the main stream of the wastewater after UASB reactor, characterized by low concentration of nitrogen and organic matter. The bacteria ability to accommodate, were tested in the biofilm and in the activated sludge, depending on the different stages in which the process were being conducted. Batch test, such as Specific Anammox Activity (SAA), Nitrate Uptake Rate (NUR) and Oxygen Uptake Rate (OUR), were used for the evaluation of activity of various groups of bacteria. On the basis of laboratory analysis verified the values obtained from the batch tests. It was determined that a high degree of nitrogen removal (92% of NH4-N) was achieved thanks to the dominant activity of the Anammox bacteria, with low participation of other groups of bacteria. It was also proved, that Anammox bacteria activity were overwhelming in the biofilm. Dominant role of Ammonium Oxidizing Bacteria (AOB) was associated with high activity of Anammox bacteria, which together satisfyingly out-competed Nitrite Oxidizing Bacteria (NOB) and heterotrophic bacteria. It has been shown that Anammox bacteria quickly adapt to the new conditions and they are able to assume a dominant role, even in the case of inoculation of the reactor with the sludge from SBR. This allows conclude, that in the case of operational problems, the reactor can be supplied from another source, in order not to inhibit the process.

El sistema de depuració de tipus Fangs Actius constitueix una de les tècniques més esteses arreu del món pel tractament biològic de les aigües residuals. Els softwares de modelització i simulació permeten adquirir coneixements de forma ràpida i senzilla sobre el funcionament dels processos de fangs actius, dur a terme la comparació entre diferents tecnologies de tractament i determinar les estratègies d'operació més rentables d'una EDAR minimitzant els costos.L'objectiu de la present tesi consisteix en la identificació dels principals paràmetres cinètics i coeficients estequiomètrics que caracteritzen el procés de fangs actius a partir de la mesura de la velocitat de consum d'oxigen de la biomassa. En aquest sentit s'ha dissenyat i desenvolupat un Respiròmetre Tancat Seqüencial (RTS), un Respiròmetre Tancat (RT) i un Programa d'Anàlisi de Respirometries (PAR) per la determinació dels paràmetres cinètics més representatius i característics dels sistemes de fangs actius en diferents casos. / The Activated Sludge treatment system is one of the techniques more used around the world as a biologic treatment of waste water. Modelling and Simulation software's allow to get knowledge about the behaviour of Activated Sludge processes in a fast and easy way, to compare different treatment technologies and to determine which are the most economic operation strategies for a WWTP. The aim of this thesis consists of the identification of the main kinetic parameters and stoichiometric coefficients that characterize the Activated Sludge process using the measure of oxygen uptake rate of the biomass. Two different kind of instruments has been designed to measure the Activated Sludge respiration: a Sequential Closed Respirometre (RTS, from Respirometre Tancat Seqüencial) and a Closed Respirometre (RT from Respirometre Tancat). Also a Program for the Analysis of Respirometries (PAR from Programa d'Anàlisi de Respirometries) has been developed to determine the most representatives kinetics parameters and activated sludge characteristics in different cases.

O processo de tratamento de efluentes por lodos ativados é um dos processos de tratamento mais difundido em todo o mundo, devido principalmente a qualidade do efluente obtido. Entretanto, trata-se de um processo biológico dependente da atividade bacteriana para a estabilização da matéria orgânica proveniente dos esgotos e com isso, se faz necessária a manutenção das condições ideais para a sobrevivência e proliferação das bactérias e dos outros microrganismos envolvidos neste processo. Efluentes salinos causam um grande distúrbio na atividade celular dos microrganismos presentes neste processo. A análise biológica do lodo e a taxa de consumo de oxigênio são testes rápidos, práticos, baratos e sem geração de resíduos químicos e que foram adotados neste trabalho para acompanhar a eficiência do processo. Esses dois parâmetros são amplamente utilizados em pesquisas, porém ainda é sub-utilizado para efetivo monitoramento de Estações de Tratamento de Esgotos. Este presente trabalho investigou a influência da salinidade nos processos de lodos ativados através de parâmetros que levam em consideração a atividade metabólica dos organismos aeróbios e através do monitoramento da comunidade de protozoários indicadores biológicos do lodo ativado, os testes de respirometria e os testes da análise biológica do lodo, respectivamente. Os resultados da atividade metabólica são apresentados em forma de gráficos, em termos de taxa de consumo de oxigênio específico e porcentagem de inibição. Os resultados da qualidade biológica são apresentados em números de 0 a 10 de acordo com o Índice de Madoni (1994). Os resultados demonstraram a imediata intoxicação dos lodos ativados em concentrações de sal a partir da concentração mínima utilizada neste trabalho, que foi de 5 gL de NaCl. Para entender melhor o processo de intoxicação foi realizado experimentos de 96 horas de monitoramento após o choque de cloreto de sódio nos reatores com lodos ativados, os resultados não demonstraram melhoria no processo. Os resultados sugerem que os testes de taxa de consumo de oxigênio em consonância com os testes da qualidade biológica são eficientes e complementares para a avaliação da influência da salinidade no processo de lodos ativados. / Effluent treatment process by sludge activated is one of the most used processes of treatment all over the world, mainly because of the quality of the final effluent. However, this process is a biological one, and so, it depends on the bacterial activity to the stabilization of the organic matter of the sewage. Considering this, it is necessary to maintain the ideal conditions to the survival and proliferation of the bacteria responsible for the process. This work considered two parameters to evaluate the influence of the salinity in the sludge activated processes; these parameters are widely used in research, however, little used for the monitoring of the Wastewater Treatment Plants. The objectives of this work are to investigate the influence of the salinity through the respirometry test and the biological quality of the sludge. The results of the metabolic activity are presented in graphics, in terms of Oxygen Uptake Rate and percentage of inhibition. The results of the biological quality are presented in numbers by 0 to 10 according to the Mandonis Index (1994). The results show the intoxication of the sludge activated in saline concentrations higher than 5 g/L of NaCl in the saline shock, and it seems that efficiency do not get better even after 96 hours. The results suggests that the respirometry test and the biological quality test are efficient and complementary to the evaluation of salinity in the sludge activated processes.

O processo de tratamento de efluentes por lodos ativados é um dos processos de tratamento mais difundido em todo o mundo, devido principalmente a qualidade do efluente obtido. Entretanto, trata-se de um processo biológico dependente da atividade bacteriana para a estabilização da matéria orgânica proveniente dos esgotos e com isso, se faz necessária a manutenção das condições ideais para a sobrevivência e proliferação das bactérias e dos outros microrganismos envolvidos neste processo. Efluentes salinos causam um grande distúrbio na atividade celular dos microrganismos presentes neste processo. A análise biológica do lodo e a taxa de consumo de oxigênio são testes rápidos, práticos, baratos e sem geração de resíduos químicos e que foram adotados neste trabalho para acompanhar a eficiência do processo. Esses dois parâmetros são amplamente utilizados em pesquisas, porém ainda é sub-utilizado para efetivo monitoramento de Estações de Tratamento de Esgotos. Este presente trabalho investigou a influência da salinidade nos processos de lodos ativados através de parâmetros que levam em consideração a atividade metabólica dos organismos aeróbios e através do monitoramento da comunidade de protozoários indicadores biológicos do lodo ativado, os testes de respirometria e os testes da análise biológica do lodo, respectivamente. Os resultados da atividade metabólica são apresentados em forma de gráficos, em termos de taxa de consumo de oxigênio específico e porcentagem de inibição. Os resultados da qualidade biológica são apresentados em números de 0 a 10 de acordo com o Índice de Madoni (1994). Os resultados demonstraram a imediata intoxicação dos lodos ativados em concentrações de sal a partir da concentração mínima utilizada neste trabalho, que foi de 5 gL de NaCl. Para entender melhor o processo de intoxicação foi realizado experimentos de 96 horas de monitoramento após o choque de cloreto de sódio nos reatores com lodos ativados, os resultados não demonstraram melhoria no processo. Os resultados sugerem que os testes de taxa de consumo de oxigênio em consonância com os testes da qualidade biológica são eficientes e complementares para a avaliação da influência da salinidade no processo de lodos ativados. / Effluent treatment process by sludge activated is one of the most used processes of treatment all over the world, mainly because of the quality of the final effluent. However, this process is a biological one, and so, it depends on the bacterial activity to the stabilization of the organic matter of the sewage. Considering this, it is necessary to maintain the ideal conditions to the survival and proliferation of the bacteria responsible for the process. This work considered two parameters to evaluate the influence of the salinity in the sludge activated processes; these parameters are widely used in research, however, little used for the monitoring of the Wastewater Treatment Plants. The objectives of this work are to investigate the influence of the salinity through the respirometry test and the biological quality of the sludge. The results of the metabolic activity are presented in graphics, in terms of Oxygen Uptake Rate and percentage of inhibition. The results of the biological quality are presented in numbers by 0 to 10 according to the Mandonis Index (1994). The results show the intoxication of the sludge activated in saline concentrations higher than 5 g/L of NaCl in the saline shock, and it seems that efficiency do not get better even after 96 hours. The results suggests that the respirometry test and the biological quality test are efficient and complementary to the evaluation of salinity in the sludge activated processes.