Au cours de cette thèse, les prévisions de la méthodologie d’Analyse de Cycle de Vie (ACV) sont améliorées, via l’exergie, pour l’analyse et l’éco-conception des procédés. Nous mettons l’accent sur le potentiel de l’analyse exergétique et de la Consommation d’Exergie Cumulée (CExC) dans l’évaluation du critère d’épuisement, de productivité et de recyclabilité des ressources naturelles. Dans ce cadre, les transferts de pollutions et les impacts environnementaux d’un système de traitement des eaux résiduaires (STEP) ont été analysés en relation avec l’exergie consommée (CExC) et de l’exergie détruite (étude a priori). L’étude montre que la décision est différente lorsque l’indicateur d’épuisement des ressources naturelles est basé sur la méthode CExC de celle basée sur la méthode CML. L’amélioration de l’éco-efficacité d’une STEP implique un recyclage des boues en agriculture. La stabilisation des boues par digestion anaérobie réduit le volume des boues et ainsi l’impact du transport en comparaison avec la stabilisation à la chaux. Toutefois, elle réduit le potentiel fertilisant des boues, d’une part, et augmente la consommation d’énergie et l’impact du réchauffement climatique à cause du traitement des retours en tête d’autre part. Bien que la valorisation du biogaz en cogénération réduise la dépendance énergétique de la STEP et améliore son éco-efficacité globale en comparaison avec le chaulage, elle n’offre pas la possibilité à un séchage des boues. Le séchage des boues constitue l’une des recommandations des agriculteurs, bien qu’il n’améliore pas le l’éco-efficacité globale de la STEP, en augmentant l’épuisement et l’exergie détruite des ressources brutes et du biogaz / The focus of the work has been to improve the predictions of Life Cycle Assessment (LCA) via exergy for processes analysis and eco-design. The potential of the exergetic analysis and Cumulative Exergy Consumption (CExC) in estimating the criterion of depletion, productivity and recyclability of natural resources has been investigated. In this context, the transfer of pollutants and the environmental impacts of a wastewater treatment system (WWTP) have been analyzed in relation with the consumed exergy (CExC) and the destroyed exergy. The study shows that decision is different if the indicator of depletion of natural resources is based on the method of CExC or on the CML method. The improvement of the overall eco-efficiency of a WWTP involves a recycling of sludge in agriculture. Stabilization of sludge by anaerobic digestion reduces the volume of sludge and consequently the impact of transport in comparison with the stabilization with lime. However, on one hand, it reduces the fertilizer potential of sludge. On the other hand it increases energy consumption and the impact of the global warming because of the treatment of digested sludge supernatant recycled to the WWTP. Although the recovery of biogas by cogeneration reduces the energy dependency of the WWTP and improves its overall eco-efficiency in comparison with the liming scenario, it does not provide the possibility for sludge drying. Drying the sludge is one of the recommendations of farmers, although it does not improve the overall eco-effectiveness of the WWTP, and increases the depletion and the destroyed exergy of raw resources and biogas

The suitability of water hyacinth in biogas production was evaluated as a means of waste management in the interests of sustainable energy production. Batch anaerobic digestion (AD) of water hyacinth was conducted to determine the optimal pre-treatment method for maximum methane production. Physical pre-treatment methods produced a highest cumulative methane of 2.3 L during batch AD. The selected pre-treatment method, hand-cutting, was further evaluated in a semi-continuous AD using both mono- and co-digestion. The emphasis was on identifying microbial communities involved and their response to organic loading rates (OLRs). The Illumina Miseq results proved that bacterial communities were more sensitive to disturbances caused by irregular OLRs as compared to archaeal communities. In addition, the variation in substrate nutrients as a result of mono- and co-digestion of water hyacinth, contributed to variations in the bacterial diversity. For example, Bacteroides and Petrimonas diversity varied between mono- and co-digestion. Overall, the study verified that water hyacinth is a suitable feedstock for biogas production and the simple pre-treatment methods are recommended. Furthermore, OLRs influenced the microbial community structure and associated biogas yield. / National Research Foundation (South Africa) / Environmental Science / M. Sc. (Environmental Science)

För att minska klimatpåverkan är energisnåla processer och användning av fossilfria bränslen viktigt. Vid stabilisering av avloppsslam vid reningsverk är en vanlig metod rötning som förutom att ta hand om slammet även producerar biogas, ett fossilfritt bränsle med låga växthusgasutsläpp. Processer som drivs inom det mesofila temperaturområdet har visat sig vara stabila och ger en jämn gasproduktion. Det mesofila området sträcker sig mellan 25–40°C men de flesta processer drivs mellan 35–40°C. Den här studien undersöker möjligheten att sänka temperaturen inom det mesofila området för att få en lägre energiförbrukning och en energisnålare process. Då det är viktigt att biogasproduktionen inte försämras av en sänkt temperatur har skillnad i utrötningsgrad, metanpotential och utrötningstid undersökts vid tre olika temperaturer (32, 34,5 samt 37,5°C) via satsvisa utrötningsförsök. Utöver påverkan på biogasproduktionen har en energibalansberäkning utförts för rötkamrarna vid Uppsala reningsverk. Detta ger ett mått på hur stora vinster i värmeenergi en sänkt temperatur kan leda till. En betydande kostnad vid reningsverk är avvattningen av slam och det är därför viktigt att den inte riskerar att försämras om temperaturen sänks. Ett filtreringsförsök som mäter CST (Capillary Suction Time) ger ett mått på slammets avvattningsegenskaper och har därför utförts vid tre olika temperaturer. Resultaten visade ingen försämring i biogasproduktion vid en sänkning till 34,5°C och en minskning i metanpotential med 11 % vid en sänkning till 32°C. Nedbrytningshastigheten försämrades inte vid en sänkt temperatur. Vinster i form av lägre värmeförbrukning uppgick till 14 % vid sänkning till 34,5°C och 27 % vid sänkning till 32°C. Avvattningsförsöket visade ingen försämrad avvattning vid lägre temperaturer. Den här studien visar att det finns en möjlighet att sänka temperaturen i rötkammaren vid reningsverket i Uppsala och på så sätt sänka energiförbrukningen. För att bekräfta resultaten bör även kontinuerliga försök utföras men denna studie visar att det är möjligt att få en lyckad nedbrytning även i lägre mesofila temperaturer. Resultatet öppnar upp för fortsatta undersökningar om temperaturförändringar inom det mesofila området och kan leda till en optimering av rötningsprocessen och möjlighet att få en effektiv och energisnål produktion av biogas. / Energy efficient processes and the use of fossil free fuels play an important role in order to reduce the impact of climate change. Anaerobic digestion is a common way for stabilizing sewage sludge at wastewater treatment plants (WWTP). One of the benefits with anaerobic digestion is that it also produces biogas, a fossil free fuel with low greenhouse gas emissions. An operational temperature within the mesophilic range has proven to give a stable process with an unfluctuating production of gas. The mesophilic temperature range between 25-40°C but most processes are operated between 35-40°C. This study investigates the opportunity to lower the temperature within the mesophilic range in order to reduce energy consumption. It is important to maintain the production of biogas with a lower temperature. Therefore, the reduction in VS-content (VS-volatile solids), methane yield and time for degradation was determined by a BMP-experiment (BMP-Biochemical Methane Potential) in three different temperatures (32, 34.5 and 37.5°C). In order to quantify the reduction in heat consumption with lower operational temperatures the change in heat balance for a full-scale WWTP in Uppsala was calculated. A major part of the operational cost is dewatering of sludge and it is therefore important that it does not deteriorate with a lower temperature. The effect on the dewaterability at different temperatures was examined by a filterability test measuring CST (capillary suction time). The results from the study showed no significant difference in methane yield between 37.5°C and 34.5°C. The methane yield at 32°C was 11 % lower compared to 37.5°C but the degradation kinetic was not affected by a temperature change. The reduction in heat consumption was 14 % when the temperature was reduced to 34.5°C and 27 % when it was reduced to 32°C. The filterability test did not show a deterioration with lower temperatures. The study showed that it is possible to reduce the operational temperature for anaerobic digestion at the WWTP in Uppsala in order to reduce the energy consumption. To confirm these results a continuously experiment should be done, but this study shows that it is possible to get a successful degradation in a lower mesophilic temperature. This leads the way for further investigations within the mesophilic range and could lead to optimizing anaerobic digestion and the opportunity to get an energy efficient production of biogas.

No description available.

O tratamento de esgotos é essencial à manutenção de suprimento de água nos centros urbanos em condições desejáveis à saúde pública. A carência de saneamento em nosso país mostra a necessidade de alternativas tecnológicas para o tratamento de esgotos. Na busca de novas opções, iniciou-se na CETESB em 1983, o estudo de sistemas compactos para tratamento direto de esgotos pela via anaeróbia. O reator anaeróbio de fluxo ascendente e manto de lodo (reator UASB) foi estudado em escala piloto e mostrou-se viável e eficiente, levando à necessidade de se efetuar o aumento de escala para o completo desenvolvimento da tecnologia. Um reator UASB de 120 m3 foi construído. Durante sete anos (de 1987 a 1993) funcionou sob observação, o que possibilitou o domínio da tecnologia. O sistema operou à temperatura ambiente em três períodos distintos. No primeiro período estudou-se as eficiências de remoção de matéria orgânica e a produção de gás e de lodo. Com tempo de retenção hidráulica médio de 6,5 horas, obteve-se efluente com 113 mg DQO/L, 48 mg DBO/L e 39 mg SST/L. As eficiências de remoção de DQO, DBO e SST foram respectivamente de 59, 65 e 76 por cento. A remoção de Coliformes totais e fecais ficou entre 70 e 90 por cento. Sua desinfecção através de métodos convencionais como cloração, ozonização ou radiação ultravioleta mostrou-se eficiente, a exemplo da maioria dos sistemas secundários de tratamento de efluentes. Obteve-se como fator de produção de lodo 0,2 kg ST/kg DQO da alimentação, sendo esta baixa produção de lodo uma das grandes vantagens do processo anaeróbio tendo em vista o custo e o trabalho que representam o tratamento e disposição do lodo no tratamento de esgotos. A produção de gás foi de 120 NL/kg de DQO alimentado. Efetuou-se também o acompanhamento microbiológico do lodo através de metodologia específica de acompanhamento de biomassa de biodigestores, o que possibilitou o aprimoramento dos conhecimentos da formação da biomassa no decorrer do processo. No segundo período de operação comprovou-se os resultados obtidos no primeiro período. No terceiro período de operação, apoiando-se nas técnicas de análise microbiológica da biomassa, estudou-se a partida a fim de diminuir o tempo para se atingir o regime estacionário. A utilização de inóculo não adaptado, como o lodo de esgoto de reator convencional, requer três a quatro meses para atingir o estado estacionário, com as eficiências relatadas. A partir da experiência adquirida são efetuadas recomendações e considerações para dimensionamento, partida, operação, manutenção e monitoramento para servir como guia aqueles que forem utilizar esta nova tecnologia. Após a partida o sistema apresenta reprodutibilidade, confiabilidade e estabilidade de operação. O controle do sistema, quando se trata de esgoto doméstico, é bastante simples, necessitando apenas remoção periódica de lodo, além da manutenção e limpeza. Há necessidade de remoção periódica de escuma. O dimensionamento do reator sofreu aperfeiçoamentos para melhorar a separação das três fases sólida, líquida e gasosa. Além dos critérios adotados anteriormente a partir do reator piloto de 106 L que possibilitou o estabelecimento de critérios como velocidade superficial no decantador de O,7 m3/m2/h, velocidade do líquido através da abertura inferior do decantador de 5 m3/m2/h e inclinação das paredes do decantador de 50°, observou-se que o transpasse entre a parede do decantador e do defletor de gases deve ter no mínimo 15 em para assegurar que o gás não desvie para dentro do decantador. O limite de velocidade no corpo do reator não deve ultrapassar 1 m3/m2h para garantir o acúmulo de lodo no reator. O lodo apresentou granulação com diâmetros de até 2 mm. Os processos de pós tratamento que vem sendo testados dão os polimentos necessários e adequados às diversas condições de reuso ou descarte do efluente. O sistema é hoje relativamente bastante utilizado, quando se leva em conta os parcos investimentos havidos no setor nos últimos anos. No Estado de São Paulo, a aplicação desta tecnologia foi efetuada através de um convênio entre a CETESB e o DAE-Sumaré, no Jardim Santa Maria, um loteamento de 1500 habitantes. Esse trabalho, mostrou a viabilidade de sua aplicação e comprovou os resultados obtidos, assim como várias experiências realizadas por outras instituições com processo anaeróbio também o demonstraram. No Estado do Paraná, o processo anaeróbio tem sido empregado sistematicamente para o tratamento de esgotos pela Companhia de Saneamento daquele Estado, a SANEPAR. A divulgação dessas experiências e de tantas outras existentes, deve proporcionar a confiança na tecnologia possibilitando sua expansão e a melhoria da qualidade de nossas águas. / Sewage treatment is essential to water supplying in urban nuclei with desirable conditions of public health. The lack of sanitation in our country shows the necessity of sewage treatment technologies compatible to our reality. Searching for new technologies, CETESB has started in 1983, the study of new compact anaerobic treatment systems for sewage. The UASB reactor was studied in pilot scale showing the need of scaling up for it\'s complete technological development. For this purpose a 120m3 UASB reactor was built. During seven years (from 1987 to 1993) the system worked with methodological observation, which made possible the mastering of the technology. The system operated at ambient temperature in three distinct periods. In the first one the performance of organic matter removal and the gas and sludge production were studied. The results showed effluent with 113 mg COD/L, 48 mg BOD/L and 39 mg SST/L with 6.5 hours of hydraulic retention time. The COD, BOD and SST removal performances were respectively 59, 65 and 76 per cent. The faecal and total Coliform removal showed values between 70 and 90 per cent. The effluent disinfection by conventional methods as chlorination, ozonation and ultra violet radiation has showed to be efficient, as the majority of effluent secondary treatment systems. The sludge production was 0.2 kg ST/kg COD in the feed. This low sludge production is one of the biggest advantages of the anaerobic process, in view of the costly and great disturbances that represent the sludge treatment and disposal in the sewage treatment. The gas production was 120 NL/kg COD of the feed. The biomass growth was followed by means of a microbilogical analysis specially developed for biodigesters sludge. In the second operation period the results were confirmed. In the third operation period, also followed by means of microbiological technical analysis, the shortening of the start up time was studied. It was found that starting up with unacclimatized inoculum, the stationary condition takes three to four months to be achieved, with the performances related. Based on the experience gathered, recommendations are made for system design, start up, operation, maintenance and monitoring. After the start up, the system shows reproducibility, reliability and stable operation. For essentially domestic sewage, the control system is very simple, necessitating only periodical sludge removal in addition to the maintenance activities. There is necessity of periodically scum removal. The design of the reactor was changed to improve the separation of solid, liquid and gaseous phases. Besides the design criteria described before, based on pilot scale experience, such as surface velocity in the settler area of O.7 m3/m2.h, liquid velocity in the lower aperture of the settling chamber 5 m3/m2.h with minimum HRT of four hours and slope of settling chamber walls of 50°, it was observed that it needs 15 cm in the crossing between the settler wall and the gas deflector to assure no gas deviation to the settler compartment. The maximum upflow velocity in the reactor body is 1 m3/m2.h to warrant retention of sludge in the reactor. Pellets in sludge presented up to 2 mm in diameter. Post-treatments may be necessary to give the effluent the appropriated conditions for its reuse or discharge. Today, the system is quite used in Brazil, taking in account the low investments in the sector. In the State of Sao Paulo, an example of this technology transfer is the agreement signed by CETESB and DAE-Sumaré, at \"Jardim Sta. Maria\", a small community of 1500 inhabitants. This work confirmed the results obtained and showed the feasibility of its application. Other experiences made by other institutions with anaerobic process confirmed them as well. In the State of Parana, the anaerobic process has been employed systematically for sewage treatment by the State Sanitation Company. The diffusion of this experiences and of many others existing might provide the confidence in the technology, enabling its expansion and the improvement of the quality of our waters.

Reconnu par leur effet toxique, inhibiteur et corrosif, les sulfures (S2-, SH-, SH2) sont un sous-produit indésirable de la digestion anaérobie des boues de station de traitement des eaux domestiques de la ville de Marrakech, Maroc (STEP). Ils proviennent essentiellement de la réduction "dissimilatrice" des composés soufrés (SO4 2-, SO3 2-, S2O4 2- ..) contenus dans ces boues. Ce processus est réalisé par un groupe bactérien anaérobie appelé bactéries sulfatoréductrices (BSR). Une fois dans le biogaz, les sulfures sous forme gazeuse réduisent en plus la durée de vie des installations et des équipements de la STEP. Elle est ainsi dotée d’installations biologiques et physico-chimiques lui permettant d’éliminer ces sulfures avant la transformation du biogaz en énergie électrique. Cependant, ces procédés sont onéreuses et grandes consommatrices d’énergies. D’où l’idée de minimiser la production des sulfures au sein même des digesteurs anaérobies. Pour cela, il était nécessaire d’abord de connaître les microorganismes à l'origine de la production des sulfures (BSR), ceux potentiellement impliqués dans leur élimination (bactéries sulfo-oxydantes), et d’un groupe de microorganismes fermentaires (Synergistetes) intervenant dans le bon fonctionnement de la digestion anaérobie. Ces études ont été menées à la fois sur des d'approches moléculaires et culturales. Les résultats obtenus, ont permis de comprendre comment ces groupes bactériens, d’intérêts écologique et économique importants, interviennent dans la digestion anaérobie des boues de la STEP permettant à la fois d’accélérer les processus d’oxydation de la matière organique combinée à la réduction des composés soufrés et de minimiser la concentration des en sulfure dans le biogaz. / Recognized by their toxic, inhibitory and corrosive effect, sulfides (S2-, SH-, H2S) are an undesirable by-product of the anaerobic digestion of from domestic wastewater treatment plants sludge in the city of Marrakech, Morocco (WWTP). They produced mainly by the dissimilatory reduction of sulfur compounds (SO42-, SO32-, S2O42-) contained in these sludges. This process is performed by an anaerobic bacterial group called sulfate reducing bacteria (SRB). Once in the biogas, the sulfides in gaseous form shorten in addition the lifetime of the installations and equipments of the WWTP. It is thus equipped with biological and physicochemical installations allowing it to eliminate these sulfides before the transformation of biogas into electrical energy. However, these processes are expensive and consume large amounts of energy. Hence the idea of minimizing the production of sulfides within anaerobic digesters. For this, it was first necessary to know the microorganisms originating of the production of sulfides (SRB), those potentially involved in their elimination (sulfur oxidizing bacteria), and a group of fermentative microorganisms (Synergistetes) involved in the good functioning of the anaerobic digestion. These studies were conducted on both molecular and cultural approaches. The results obtained allowed to understand how these bacterial groups, of great ecological and economic interest, are involved in the anaerobic digestion of sludge from the WWTP, which both accelerates the oxidation processes of the organic matter combined with the reduction of sulfur compounds and to minimize the concentration of sulfide in biogas.

Made available in DSpace on 2017-07-10T19:25:17Z (GMT). No. of bitstreams: 1 Clori Antonio Pontello.pdf: 3010074 bytes, checksum: 5e0d1daabf222439b9ee242e767883cf (MD5) Previous issue date: 2005-05-31 / Manioca starch mills generate a high amount of outflow and environmental concerns due to its high pollutant wastewater. Use of stabilization ponds is very common for the treatment of wastewater on the transformation of manioca root sector. However, in winter time, coincidently with the harvesting and crushing period a fall on the treatment system may occur due to the decreasing of environmental temperature. The present study aims at evaluating the effect of plastic canvass on the stability and keeping the anaerobic pond temperature treating the outflow of cassava. The system consisted of two reactors simultaneously supplied, with net volume of 15.98m3 each, 10 day hydraulic retaining time, continuously supplied, without pH correction and without temperature control. Air temperature and daily outflowing and inflowing of the reactors were monitorized for a period of one year. Both physical and chemical analyses were performed measuring pH, BOD5, COD, TSS, FSS, and VSS of the reactors outflowing and iinflowing in monthly frequency. The daily temperatures measured on the covered reactors were superior than on the uncovered ones. An efficiency of 10% on COD, and 15% on BOD5 were observed on the covered reactor. The plastic canvass covered reactor showed less oscilations with greater stability in keeping temperatures, mainly in periods of low temperature, showing a better performance on the treatment of cassava processing outflow. / As fecularias de mandioca geram um volume de efluente significativo e de elevada preocupação ambiental, devido a sua elevada carga poluidora. É muito comum a utilização de lagoas de estabilização para o tratamento de águas residuárias do setor de transformação de raiz de mandioca. Entretanto, nos períodos de inverno, coincidindo com o período de safra e esmagamento, observa-se uma queda na eficiência dos sistemas de tratamento que podem ocorrer em razão da diminuição da temperatura ambiente. O presente trabalho buscou avaliar o efeito da cobertura plástica na estabilidade e manutenção da temperatura de lagoa anaeróbia, tratando efluente de fecularia de mandioca. O sistema foi constituído de dois reatores alimentados em paralelos, com volume útil de 15,98m3 cada, tempo de detenção hidráulico de 10 dias, alimentação contínua, sem correção de pH e sem controle de temperatura. Durante o período de um ano, foram monitoradas as temperaturas do ar, entrada e saída dos reatores com medições realizadas diariamente. Efetuou-se análise físicoquímica medindo-se o pH, DBO5, DQO, SSS, SST, SSF e SSV do afluente e efluente dos reatores com freqüência mensal. As temperaturas diárias medidas no reator coberto foram superiores ao descoberto. Observou-se eficiência de 10% na DQO e 15% na DBO5 superiores para o reator coberto. O coberto com lona plástica apresentou menores oscilações com maior estabilidade na manutenção das temperaturas, principalmente nos períodos de baixas temperaturas, mostrando maior desempenho no tratamento de efluente de fecularia de mandioca.

Made available in DSpace on 2017-05-12T14:48:41Z (GMT). No. of bitstreams: 1 Clori Antonio Pontello.pdf: 3010074 bytes, checksum: 5e0d1daabf222439b9ee242e767883cf (MD5) Previous issue date: 2005-05-31 / Manioca starch mills generate a high amount of outflow and environmental concerns due to its high pollutant wastewater. Use of stabilization ponds is very common for the treatment of wastewater on the transformation of manioca root sector. However, in winter time, coincidently with the harvesting and crushing period a fall on the treatment system may occur due to the decreasing of environmental temperature. The present study aims at evaluating the effect of plastic canvass on the stability and keeping the anaerobic pond temperature treating the outflow of cassava. The system consisted of two reactors simultaneously supplied, with net volume of 15.98m3 each, 10 day hydraulic retaining time, continuously supplied, without pH correction and without temperature control. Air temperature and daily outflowing and inflowing of the reactors were monitorized for a period of one year. Both physical and chemical analyses were performed measuring pH, BOD5, COD, TSS, FSS, and VSS of the reactors outflowing and iinflowing in monthly frequency. The daily temperatures measured on the covered reactors were superior than on the uncovered ones. An efficiency of 10% on COD, and 15% on BOD5 were observed on the covered reactor. The plastic canvass covered reactor showed less oscilations with greater stability in keeping temperatures, mainly in periods of low temperature, showing a better performance on the treatment of cassava processing outflow. / As fecularias de mandioca geram um volume de efluente significativo e de elevada preocupação ambiental, devido a sua elevada carga poluidora. É muito comum a utilização de lagoas de estabilização para o tratamento de águas residuárias do setor de transformação de raiz de mandioca. Entretanto, nos períodos de inverno, coincidindo com o período de safra e esmagamento, observa-se uma queda na eficiência dos sistemas de tratamento que podem ocorrer em razão da diminuição da temperatura ambiente. O presente trabalho buscou avaliar o efeito da cobertura plástica na estabilidade e manutenção da temperatura de lagoa anaeróbia, tratando efluente de fecularia de mandioca. O sistema foi constituído de dois reatores alimentados em paralelos, com volume útil de 15,98m3 cada, tempo de detenção hidráulico de 10 dias, alimentação contínua, sem correção de pH e sem controle de temperatura. Durante o período de um ano, foram monitoradas as temperaturas do ar, entrada e saída dos reatores com medições realizadas diariamente. Efetuou-se análise físicoquímica medindo-se o pH, DBO5, DQO, SSS, SST, SSF e SSV do afluente e efluente dos reatores com freqüência mensal. As temperaturas diárias medidas no reator coberto foram superiores ao descoberto. Observou-se eficiência de 10% na DQO e 15% na DBO5 superiores para o reator coberto. O coberto com lona plástica apresentou menores oscilações com maior estabilidade na manutenção das temperaturas, principalmente nos períodos de baixas temperaturas, mostrando maior desempenho no tratamento de efluente de fecularia de mandioca.

Fossas e tanques sépticos são sistemas de pequeno porte utilizados para tratamento parcial do esgoto sanitário produzido nas áreas urbana e rural, quando não beneficiados por sistema de esgotamento sanitário. Tal utilização se justifica principalmente por ser tecnologia que não exige muita dedicação operacional e ser de simples implantação. Apesar da vasta utilização dessas unidades no Brasil, há pouca informação sobre a caracterização, as condições de coleta, transporte, tratamento e destino final de resíduo (lodo) produzido nesses sistemas. Nesse sentido, o presente trabalho tem como objetivo a caracterização do lodo produzido nessas unidades; e, também, a concepção, o desenvolvimento e a avaliação de uma unidade piloto para pré-tratamento de lodo de fossas e tanques sépticos. Essa unidade, constituída por grade, desarenador e flotador, foi instalada no Campus da Universidade de São Paulo, junto da Estação de Tratamento de Esgoto do Campus - área 1, e vista à remoção de sólidos grosseiros, areia e materiais flutuantes, antes de seu lançamento na Estação de Tratamento de Esgoto do Campus. Foi feita a caracterização do lodo de tanques sépticos coletado in situ e do lodo proveniente dos caminhões limpa-fossas, descarregando em tanque pulmão de 15000 litros. A caracterização do lodo proveniente dos caminhões limpa-fossas foi realizada em duas campanhas (coletas), sendo uma feita na primeira visita ao local pré-definido, e outra realizada aproximadamente seis meses após a primeira coleta. Com intuito de aprimorar o método de análise das amostras do lodo in situ, com finalidade de melhor fragmentar o material particulado, foi testado o uso de ultrassom. Também, foi realizada a caracterização do lodo de fossas e tanques sépticos na Central de Recebimento de Resíduos na cidade de Campinas-SP - SANASA - Sociedade de Abastecimento de Água e Saneamento AS. Para tanto, foram coletadas amostras compostas de lodo descarregado por 24 caminhões. Foi feito teste complementar, com a finalidade de estudar a degradação do lodo flotado por processos anaeróbio e aeróbio. Mediante essas caracterizações pode-se constatar a grande heterogeneidade da composição do lodo e a elevada carga orgânica, que devem ser ponderados com relação a impactos no meio ambiente e em Estações de Tratamento de Esgoto. Contudo, nota-se a importância do pré-tratamento desse lodo antes de ser lançado em ETEs. A unidade piloto foi operada com diferentes taxas de aplicação superficial (80; 110; 140 e 200 \'M POT.3\'/\'M POT.2\'.dia), quando foram obtidas remoções de 91,7% de sólidos suspensos; 89,3% de DQO e 81,9% de óleos e graxas. Pelos resultados obtidos foi demonstrada a eficiência do sistema de flotação na remoção de óleos e graxas e dos sólidos suspensos. A digestão aeróbia do lodo flotado mostrou-se eficiente quando foi aplicado inócuo com período de aeração superior a 20 dias, sendo que foram obtidas eficiências de 88,3% e 90% para remoção de DQO e de óleos e graxas, respectivamente. / Septic tanks are small structures used for partial treatment of wastewater produced from urban and rural areas. It utilization is justify mainly by simplicity of construction and for being a technology that requires low operational dedication. Although it is a technology vastly used in Brazil, there is not much information about the characteristics of the waste dumped in there, and the conditions of collection, transport, and final destination of the sludge generated in the system. The objective of this research was characterize the sludge originated from septic tanks and to design, construct and evaluate a treatment unit model to be used for prior treatment of the sludge generated in those septic tanks. This unit, composed by a sieve, a degritter, and a flotation device, was assembled in the São Paulo University Campus, near the area 1 from the campus Wasterwater Treatment Plant (WWTP). It had the purpose to remove har solid particle, sand and the floating material before their entry in the Wasterwater Treatment Plant. Was made to characterize the sludge septic tank collected in situ and the sludge originated from the Septic Pumper Truck, unloaded into a tank of 15000 L. Furthermore, the characterization of the sludge originated from the Septic Pumper Truck was performed twice, once in the material collected in the first visit to the defined location and the other in the material collected about six months after the first collection. The use of ultrasound was tested to ameliorate the fragmentation of the particulate material and to improve the method of analysis of the sludge in situ. Additionally, it was characterized the sludge from septic tanks in the Waste Reception Center from the city of Campinas, São Paulo State - SANASA - Society of Water Supply and Sanitation in composite samples collected from 24 trucks during the unloading. Septic Pumper Truck in th Waste Receptation Center. A complementing test was performed in order to text the degradation of the floated sludge by anaerobic and aerobic processes. The characterizations revealed a great heterogeneity in the composition of the sludge and the high organic content, which should be taken in consideration regarding the impacts in the environment and in the WWTP. This underlines the importance of treatment of the sludge prior to discharging into the WWTP. The pilot plant was managed to work at different rates of surface sludge application (80, 110, 140 and 200 \'M POT.3\'/\'M POT.2\'.day). The 110 \'M POT.3\'/\'M POT.2\'.day rate displayed the highest efficiency with the removal of 91.7% of suspended solids, 89.3% of the chemical oxygen demand, and 81 9% of oils and waxes. The results showed the efficiency of the flotation system in the removal of suspended solids, oil and greases. The aerobic digestion of the floated material was efficient when it received inoculation with aeration period greater than 20 days, which allowed CDO the removal of 88.3% and 90% of oil and greases.

<p>Biogas är benämningen för metangas (CH₄) som är producerad via anaerob (syrefri) rötning av biologiskt material. I Linköping finns en av Sveriges största biogasanläggningar. Anläggningen drivs av Svensk Biogas AB som ägs av Tekniska Verken i Linköping AB (publ.). I anläggningen rötas stora mängder proteinrikt substrat vilket leder till höga halter av ammoniak (NH₃) och ammonium (NH₄⁺) i rötkammaren. Ammoniak (NH₃) är toxiskt för de metanbildare som i en välmående process står för den största delen av metangasproduktionen. Höga halter av ammoniak (NH₃) och ammonium (NH₄⁺) kan inhibera dessa metanbildare vilket leder till minskad gasproduktion.</p><p>Detta examensarbete syftar främst till att genom ett kontinuerligt rötkammarexperiment utreda om zeoliter är ett lämpligt hjälpmedel för att reducera ammonium (NH₄⁺) i en anaerob process. Vid sänkta halter ammonium (NH₄⁺) är hypotesen att de mikroorganismer som är aktiva i den mest effektiva metanbildningsvägen återetableras. Arbetet syftar även till att experimentellt utreda vilka effekter zeoliter i sin helhet har på den anaeroba processen. Zeoliters effekt vid låga zeolitkoncentrationer utreds i en serie utrötningsexperiment i batch. Dessutom har en materialstudie kring zeoliternas kapacitet i olika miljöer genomförts.</p><p>Materialstudien visade att den valda zeoliten som studerades, clinoptilolite, hade en maximal katjonbytarkapacitet på ≈ 19 mg NH₄⁺/g zeolit. Vidare konstaterades att zeoliter med mindre diameter än 1 mm har avsevärt bättre kapacitet än zeoliter med större diameter. I det kontinuerliga rötkammarexperimentet konstaterades att clinoptilolite kan användas i en rötkammare för att reducera ammoniumhalten (NH₄⁺). Detta utan att några allvarliga processtörningar uppstår. Cirka 175 g zeolit/l krävdes för att reducera ammoniumhalten (NH₄⁺) från 5300 mg NH₄⁺/l till 3200 mg NH₄⁺/l. Det är inte realistisktatt använda så stora mängder zeoliter i en fullskalig anläggning. Mikrobiologiskt sett observerades ingen förändring av de metanbildarna som dominerar den effektivaste metanbildningsvägen.</p><p>Resultaten från utrötningsförsöket i batch visade att zeolittillsatser av 5 g/l respektive 10 g/l hade en klart positiv effekt på metanbildningen jämfört utan zeolittillsats. I de batcher med 1-10 g zeolit/l startade metangasproduktionen ≈ 14 dagar tidigare än batcherna med 0 g zeolit/l. 16 dagar efter att experimentet startade hade batcherna med 5-10 g zeolit/l producerat ≈ 500 ml metangas (CH₄) jämfört med serien utan zeoliter som vid samma tidpunkt producerat ≈ 75 ml metangas (CH₄). Utrötningsgraden ökade i samtliga serier med zeolittillsats jämfört med serien utan zeoliter. Tillsatsen av 5 g zeolit/l ökade den specifika metangasproduktionen med ≈ 19 % jämfört med utan zeolittillsatser. Slutsatsen är att clinoptilolite i små koncentrationer, mellan 5-10 g/l, påverkar så väl kinetiken som utrötningsgraden för den anaeroba processen på ett positivt sett. Den optimala koncentrationen av clinoptilolite i en mesofil anaerob process bör ligga mellan 5-10 g zeolit/l.</p> / <p>Methane (CH₄) is formed by anaerobic (oxygen-free) digestion of biological materials. One of Sweden's largest biogas plants is placed in Linköping. The plant is operated by Svensk Biogas AB, which is owned by Tekniska Verken i Linköping AB (publ.). In their biogas plant a large amount of protein rich material is handled. High amounts of protein leads to high levels of ammonia (NH₃) and ammonium (NH₄⁺) in the digestion chamber. High levels of ammonia (NH₃) are toxic to the most dominant methane forming microorganism. High concentrations of ammonia (NH₃) and ammonium (NH₄⁺) can inhibit these methane forming microorganisms which may lead to a reduction in gas production.</p><p>This aim with this master thesis was to reduce high ammonium levels by adding zeolites to a lab scale continuous digestion chamber. The hypothesis is that at reduced levels of ammonium (NH₄⁺) the most effective methane forming microorganism will reestablish. This thesis also aims to experimentally investigate all types of effects that zeolites may have in an anaerobic digestion process. Which effect zeolites at low concentration have in a digestion chamber will be investigated by using lab scale batch digestion chambers. In addition, a material study on the capacity of the zeolites in different environments will be investigated.</p><p>The material study showed that the selected zeolite, clinoptilolite, had a cat ion exchange capacity around 19 mg NH₄⁺/g zeolite. It was also found that the zeolites with a diameter less than 1 mm had significantly better capacity than zeolites with larger diameter. In the continuous digestion experiment it was found that clinoptilolite can be used in a digestion chamber to reduce high levels of ammonium (NH₄⁺). This without any serious disorder on the process. Around 175 g zeolite/l was needed to reduce ammonium levels (NH₄⁺) from 5300 mg NH₄⁺/l to 3200 mg NH₄⁺/l. However, it is not realistic to use such large amounts of zeolites in a full-scale digestion chamber. No changes in the culture of methane forming microorganisms were found.</p><p>The results of the batch experiment showed that concentrations of 5 g zeolite/l and 10 g zeolite/l had a positive effect on the methanogenesis compared to batches without additives. In the batches with 1-10 g zeolite/l the forming of methane began about 14 days earlier than in the batches without any zeolites. After 16 days, batches with 5-10 g zeolite/l had produced about 500 ml of methane (CH₄), compared with series without additives, which at the same time had produced about 75 ml of methane (CH₄). The methane yield increased in all series which included zeolites compared to the batches without zeolites. Addition of 5 g zeolite/l increased the specific methane production by approximately 19 % compared to no additives. The conclusion is that clinoptilolite in small concentrations; 5-10 g/l have a positive effect on as well the kinetics as on the methane yield for the anaerobic process. The best concentration of zeolites in a mesophile anaerobic digestion chamber appears to be between 5-10 g zeolite/l.</p>