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Neste trabalho avaliou-se o desempenho de um reator anaeróbio de fluxo ascendente e manta de lodo (UASB) no tratamento combinado de esgoto sanitário com o lançamento de lodo proveniente de tanques sépticos. O estudo foi desenvolvido em escala plena na Estação de Tratamento de Esgoto (ETE) do Campus I da Universidade de São Paulo (USP) em São Carlos-SP. Foram utilizados dois reatores UASB com 18,8 m³ cada, um reator (UASB I) com função de controle e o outro reator (UASB II) no qual foi descarregado o lodo séptico. A pesquisa foi dividida em duas etapas: a primeira compreendeu o início de operação e o monitoramento dos reatores e, da segunda fez parte os ensaios de lançamento de lodo séptico no sistema. A partida foi efetuada sem utilização de inóculo e os reatores foram operados com tempo de detenção hidráulica médio (TDH) de 8 h, vazão afluente média de 2,35 m³/h e velocidade ascensional de 0,6 m/h. Em seis meses de operação os reatores apresentaram eficiências médias de remoção de DQO nos reatores UASB I e UASB II iguais a 49% e 65%. Quanto à remoção de sólidos os reatores UASB I e UASB II atingiram remoção de 36% e 37% para ST e de 67% e 63% para SST, respectivamente. Após esse período, deu-se início ao estudo que avaliou o impacto do lançamento de lodo séptico no UASB II. Foram realizados três ensaios com diferentes volumes de lodo (1; 3 e 5 m³) descarregados na forma de pulso com vazão média de 5,24 m³/h. Os lodos sépticos utilizados na pesquisa foram coletados por caminhões limpa-fossa e descarregados em um reservatório (15 m³) na ETE para posterior lançamento no reator UASB II. Foram feitas as caracterizações das amostras dos lodos sépticos (coletadas no ato da descarga em cada ensaio), com as quais pôde-se constatar a heterogeneidade da composição desse tipo de resíduo e sua viabilidade de pós-tratamento anaeróbio. Nos ensaios foram realizados monitoramentos temporais logo após a descarga de lodo para acompanhamento da resposta ao pulso de carga imposto. No geral, o reator UASB apresentou capacidade de degradar aproximadamente 2/3 da carga orgânica lançada com o lodo séptico. Os resultados são um indicativo de que a disposição de lodo sépticos em reatores UASB, quando bem programada, é uma solução viável e de grande importância para o tratamento dos resíduos provenientes de tanques/fossas sépticas. / The performance of upflow anaerobic sludge blanket (UASB) in the sanitary wastewater combined treatment with sludge disposal of septic tanks was evaluated in this work. The study was carried out (full scale) in the Wastewater Treatment Plant (WTP) located in campus I of the University of Sao Paulo (USP), city of Sao Carlos, State of Sao Paulo, Brazil. Two UASB reactors were used; volume of each reactor ~ 18,8 m³. UASB I was the control reactor, and UASB II was the reactor in which the septic sludge was disposed. The research was divided in two steps: the first one, which has taken into account the beginning of reactors operation and, the second one, in which occurred the disposal of septic sludge in the reactors. The start-up was carried out without utilization of inoculums. Reactors were operated with an average hydraulic retention time of 8 hours, average influent flow rate of 2.35 m³/h, and upflow velocity of 0.6 m/h. In six months, reactors presented average removal efficiencies of COD in UASB I and UASB II of 48% and 65%, respectively. Concerning to the solid removal, UASB I and UASB II have achieved removal of 36% and 37% for TS, and 67% and 63% for TSS, respectively. After this period of time, the evaluation of disposal impact of septic sludge was started in UASB II. Three essays with different sludge volume (1, 3, and 5 m³) were carried out; sludge volume was disposed in a pulse way with average flow rate of 5.24 m³/h. Septic sludge utilized in the research was collected by clean septic tank trucks, and disposed in a reservoir (volume of 15 m³) in WTP, in order to allow further disposal in the UASB II. By the hand of characterization of septic sludge samples (collected when disposal was carried out), it was possible to verify the heterogeneity about composition of this kind of waste and its availability in terms of anaerobic post-treatment. Temporal monitoring after the sludge disposal was carried out in order to allow the accompaniment of results provided by the pulse. In general, UASB reactor presented capacity in terms of degradation of approximately 2/3 of the organic load disposed with septic sludge. The results are a good indicative that the disposal of septic sludge in UASB reactors is a viable solution, and it is very important for the treatment of wastes from septic tanks.

Made available in DSpace on 2014-12-17T15:03:18Z (GMT). No. of bitstreams: 1 AnaxsandraCLD.pdf: 4126133 bytes, checksum: 2aa9935ad963ac39562a9933bf601f8a (MD5) Previous issue date: 2008-02-22 / Coordena??o de Aperfei?oamento de Pessoal de N?vel Superior / The disposal of sewage sludge is a growing problem face up to management of sanitary sevices. Otherwise, because its making process characteristic, the Ceramic Industry can tolerate the presence of this wastes as raw material. This study has as object to confirm the use of the sewage sluge in the Ceramic Industry like a sustentable alternative for its disposal. Futhermore, this study quests to evaluate the maximum proportion for incorporation of sludge wich result in technically and enviromentally suitable bricks. For found this proportion, the research consisted of (1) making of bricks in full scale, adde up 0%, 5%,10%, 15%, 20%, 25%,30%, 35% e 40% sludge, with size 220x105x45 mm, hand-molded by rammer and baked by industrial kiln; and (2) tecnical and enviromental evaluation of this bricks, according to Brazilian norms. The raw material uses were two distinct clays come from Goianinha/RN and sewage comes from a septic system tank and pumped into tank vehicle, of Natal/RN. The technical evaluation allowed to conclude the addiotion of the sludge brings about signifcant lost of mass and the water absorption grew up according to increase of sludge: every sludge-amended clay bricks absorved more water than control group. Thus, the compressive strength was signicantly decreased because the increase of sludge: bricks with 5% sludge added lost 45% of strength achieved at control group; the bricks made with 10 and 20% lost almost 70% of bigger strength. With up to 25% sludge added to the bricks, the streght decreased over 90%. Concerning heavy metal leaching, the two maximum proportion wich have tecnical approval, it means bricks sludge added with 15 and 20%, can say there is no risk of enviromental contamination using those bricks. This way, in this work context, it can to conclude the maximum proportion atends the technical and enviromental criterion is 20% / A disposi??o final adequada do lodo de esgoto constitui um problema crescente enfrentado pelos prestadores de servi?os de saneamento. Por outro lado, devido ?s suas caracter?sticas de produ??o, a Ind?stria Cer?mica possui uma enorme capacidade para absorver estes res?duos como parte de sua mat?ria-prima. O presente trabalho teve como objetivo avaliar o uso de lodo de esgoto na Ind?stria Cer?mica como alternativa sustent?vel para a disposi??o final do res?duo. Al?m disso, busca avaliar a dosagem m?xima de incorpora??o de lodo a qual resulte em tijolos maci?os t?cnica e ambientalmente vi?veis. Para determinar o percentual m?ximo de lodo de esgoto que pode ser incorporado ? massa cer?mica, o experimento consistiu (1) na fabrica??o de tijolos cer?micos em escala real contendo 0%, 5%,10%, 15%, 20%, 25%,30%, 35% e 40% de lodo, com as dimens?es de 220x105x45 mm, moldados em laborat?rio e queimados em forno industrial; e (2) na avalia??o t?cnica e ambiental desses tijolos, de acordo com as normas pertinentes. A massa cer?mica foi constitu?da por duas argilas com caracter?sticas distintas, provenientes do p?tio de sazonamento de uma ind?stria de blocos cer?micos, localizada no munic?pio de Goianinha/RN; e o lodo oriundo de uma empresa de caminh?es limpa-fossa da cidade do Natal/RN. As avalia??es t?cnicas permitiram concluir que a adi??o de lodo acarreta perda significativa da massa dos tijolos e que a absor??o de ?gua dos tijolos est? significativa e diretamente ligada ao aumento da dosagem de lodo: os tijolos fabricados com lodo, em todas as dosagens, absorveram mais ?gua do que o tijolo-testemunha. Destaca-se a dosagem de 25% que absorveu, em m?dia, 160% de ?gua a mais do que o tijolo-testemunha na sua etapa de fabrica??o. Por fim, a resist?ncia ? compress?o foi significativamente diminu?da com a adi??o de lodo: os tijolos com 5% de lodo perderam, em m?dia, cerca de 45% da resist?ncia obtida pelo tijolo-testemunha; os tijolos fabricados com 15 e 20% perderam na faixa de 70% da resist?ncia m?xima. As dosagens mais altas, de 25 e 30%, perderam cerca de 90% da resist?ncia do tijolo-testemunha. Em rela??o aos crit?rios de periculosidade, foram analisadas as duas maiores dosagens que obtiveram aprova??o t?cnica, ou seja, tijolos com dosagens de 15 e 20% de lodo; pode-se afirmar que n?o h? risco de contamina??o do meio-ambiente com a utiliza??o destes tijolos. Desta forma, para as condi??es especificadas nesta pesquisa, pode-se concluir que a dosagem m?xima de lodo que atende aos requisitos t?cnicos e ambientais ? de 20%

Made available in DSpace on 2014-12-17T15:03:20Z (GMT). No. of bitstreams: 1 AndressaDL.pdf: 2033503 bytes, checksum: bb95c834e7758cc771aaa11779a97e45 (MD5) Previous issue date: 2009-04-30 / Coordena??o de Aperfei?oamento de Pessoal de N?vel Superior / Sludge of Wastewater Treatment Plants (WTPs) disposal is a problem for any municipality, for this reason the amount of sludge production is now a key issue in selecting treatment methods. It is necessary to investigate new applications for this waste type, due to the restrictions imposed by the environmental organs. The raw materials used in the Red Ceramic, are generally very heterogeneous, for this reason, such materials can tolerate the presence of different types of wastes. In Rio Grande do Norte, the roof tiles production corresponds to 60,61% from the total of ceramic units produced. Due to the importance of the ceramic industry of roof tiles for the state, allied to the environmental problem of the sludge disposal, this work had for objective to verify the possibility of the incorporation of sewage sludge in ceramic body used for production of roof tiles. In the research, sludge originating from drying beds of WTP of the Central Campus from UFRN and clays originating from a ceramic industry from Goianinha/RN were used. The raw materials were characterized by techniques of: analysis of particles distribution by diffraction to laser; real density; consistence limits; chemical analysis by X-ray fluorescence; mineralogical analysis by X-ray diffraction; organic matter; and solids content. Five batches of roof tiles were manufactured in the approximate dosages of 2%, 4%, 6%, 8% and 10%. To evaluate the properties of each final product, tests of water absorption, impermeability, bending strength, leachability and solubility were accomplished. The roof tiles manufactured with sludge presented characteristics similar to the roof tiles without sludge in relation to the environmental risk. The results showed that it is possible to use approximately up to 4% of sludge in ceramic bodies for production of roof tiles. However, it is observed that the high amount of organic matter (71%) present in the sludge is shown as factor that limits the sludge incorporation in ceramic bodies, worsening the quality of the roof tiles. It is necessary the use of mixtures of different raw materials under point of view of the granulometry and of the other chemical and mineralogical properties for the obtaining of a satisfactory mass to the production of ceramic roof tiles / A disposi??o de lodo de Esta??es de Tratamento de Esgotos (ETEs) ? um problema para qualquer municipalidade, por isso a quantidade de lodo produzido ? hoje um assunto fundamental na sele??o de m?todos de tratamento. Faz-se necess?rio investigar novas aplica??es para esse tipo de res?duo, face ?s restri??es impostas pelos ?rg?os ambientais. As mat?rias-primas utilizadas na Cer?mica Vermelha, em geral, s?o muito heterog?neas, por isso podem tolerar a presen?a de tipos diferentes de res?duos. No Rio Grande do Norte, a produ??o de telhas corresponde a 60,61% do total de pe?as cer?micas produzidas. Dada a import?ncia da ind?stria cer?mica de telhas para o estado, aliada ? problem?tica ambiental da disposi??o de lodo, este trabalho teve por objetivo verificar a possibilidade da incorpora??o de lodo de esgotos em massa cer?mica utilizada para fabrica??o de telhas. Foram utilizados na pesquisa lodo proveniente dos leitos de secagem da ETE do Campus Central da UFRN e argilas provenientes de uma ind?stria cer?mica de Goianinha/RN. As mat?rias-primas foram caracterizadas por t?cnicas de: an?lise de distribui??o de part?culas por difra??o ? laser; densidade real; limites de consist?ncia; an?lise qu?mica por fluoresc?ncia de raios X; an?lise mineral?gica por difra??o de raios X; mat?ria org?nica; e teor de s?lidos. Foram fabricados cinco lotes de telhas nas dosagens aproximadas de 2%, 4%, 6%, 8% e 10%. Para avaliar as propriedades de cada produto final, foram realizados ensaios de absor??o de ?gua, impermeabilidade, carga de ruptura ? flex?o, lixivia??o e solubiliza??o. As telhas fabricadas com lodo apresentaram caracter?sticas semelhantes ?s telhas sem lodo no que diz respeito ao risco ambiental. Os resultados mostraram que ? poss?vel utilizar aproximadamente at? 4% de lodo em massas cer?micas para fabrica??o de telhas. Contudo, observa-se que a elevada quantidade de mat?ria org?nica (71%) presente no lodo mostra-se como fator limitante na incorpora??o de lodo em massas cer?micas, comprometendo a qualidade das telhas. Destaca-se a necessidade de utiliza??o de misturas de diferentes mat?rias-primas do ponto de vista granulom?trico e das outras propriedades qu?micas e mineral?gicas para a obten??o de uma massa satisfat?ria ? produ??o de telhas cer?micas

Neste trabalho avaliou-se o desempenho de um reator anaeróbio de fluxo ascendente e manta de lodo (UASB) no tratamento combinado de esgoto sanitário com o lançamento de lodo proveniente de tanques sépticos. O estudo foi desenvolvido em escala plena na Estação de Tratamento de Esgoto (ETE) do Campus I da Universidade de São Paulo (USP) em São Carlos-SP. Foram utilizados dois reatores UASB com 18,8 m³ cada, um reator (UASB I) com função de controle e o outro reator (UASB II) no qual foi descarregado o lodo séptico. A pesquisa foi dividida em duas etapas: a primeira compreendeu o início de operação e o monitoramento dos reatores e, da segunda fez parte os ensaios de lançamento de lodo séptico no sistema. A partida foi efetuada sem utilização de inóculo e os reatores foram operados com tempo de detenção hidráulica médio (TDH) de 8 h, vazão afluente média de 2,35 m³/h e velocidade ascensional de 0,6 m/h. Em seis meses de operação os reatores apresentaram eficiências médias de remoção de DQO nos reatores UASB I e UASB II iguais a 49% e 65%. Quanto à remoção de sólidos os reatores UASB I e UASB II atingiram remoção de 36% e 37% para ST e de 67% e 63% para SST, respectivamente. Após esse período, deu-se início ao estudo que avaliou o impacto do lançamento de lodo séptico no UASB II. Foram realizados três ensaios com diferentes volumes de lodo (1; 3 e 5 m³) descarregados na forma de pulso com vazão média de 5,24 m³/h. Os lodos sépticos utilizados na pesquisa foram coletados por caminhões limpa-fossa e descarregados em um reservatório (15 m³) na ETE para posterior lançamento no reator UASB II. Foram feitas as caracterizações das amostras dos lodos sépticos (coletadas no ato da descarga em cada ensaio), com as quais pôde-se constatar a heterogeneidade da composição desse tipo de resíduo e sua viabilidade de pós-tratamento anaeróbio. Nos ensaios foram realizados monitoramentos temporais logo após a descarga de lodo para acompanhamento da resposta ao pulso de carga imposto. No geral, o reator UASB apresentou capacidade de degradar aproximadamente 2/3 da carga orgânica lançada com o lodo séptico. Os resultados são um indicativo de que a disposição de lodo sépticos em reatores UASB, quando bem programada, é uma solução viável e de grande importância para o tratamento dos resíduos provenientes de tanques/fossas sépticas. / The performance of upflow anaerobic sludge blanket (UASB) in the sanitary wastewater combined treatment with sludge disposal of septic tanks was evaluated in this work. The study was carried out (full scale) in the Wastewater Treatment Plant (WTP) located in campus I of the University of Sao Paulo (USP), city of Sao Carlos, State of Sao Paulo, Brazil. Two UASB reactors were used; volume of each reactor ~ 18,8 m³. UASB I was the control reactor, and UASB II was the reactor in which the septic sludge was disposed. The research was divided in two steps: the first one, which has taken into account the beginning of reactors operation and, the second one, in which occurred the disposal of septic sludge in the reactors. The start-up was carried out without utilization of inoculums. Reactors were operated with an average hydraulic retention time of 8 hours, average influent flow rate of 2.35 m³/h, and upflow velocity of 0.6 m/h. In six months, reactors presented average removal efficiencies of COD in UASB I and UASB II of 48% and 65%, respectively. Concerning to the solid removal, UASB I and UASB II have achieved removal of 36% and 37% for TS, and 67% and 63% for TSS, respectively. After this period of time, the evaluation of disposal impact of septic sludge was started in UASB II. Three essays with different sludge volume (1, 3, and 5 m³) were carried out; sludge volume was disposed in a pulse way with average flow rate of 5.24 m³/h. Septic sludge utilized in the research was collected by clean septic tank trucks, and disposed in a reservoir (volume of 15 m³) in WTP, in order to allow further disposal in the UASB II. By the hand of characterization of septic sludge samples (collected when disposal was carried out), it was possible to verify the heterogeneity about composition of this kind of waste and its availability in terms of anaerobic post-treatment. Temporal monitoring after the sludge disposal was carried out in order to allow the accompaniment of results provided by the pulse. In general, UASB reactor presented capacity in terms of degradation of approximately 2/3 of the organic load disposed with septic sludge. The results are a good indicative that the disposal of septic sludge in UASB reactors is a viable solution, and it is very important for the treatment of wastes from septic tanks.

The first part of the thesis is focused on the problems related to sludge and evaluates sludge disposal from waste treatment plants. The thesis mentions factors influencing method selection of sludge disposal as well as it compares sludge disposal in the Czech Republic and in the other states of the EU. It describes a complete waste treatment line and sludge disposal in the area of sludge treatment and disposal. It deals with sludge disintegration and describes the most effective methods of disintegration. The second part of the thesis describes an experimental part of disintegration of waste treatment sludge. An experiment was conducted in the school laboratory in a way of thermal disintegration in the double-surface pressure tank. The disintegration was conducted to temperatures of 60 °C, 90 °C, 120 °C, 150 °C, and 180 °C. We monitored dependence of the sludge dry residue content on disintegration temperature as well as content of suspended solids in liquid fraction (FUGAT). It was possible to choose optimal temperature of disintegration in accordance with processed results.

The first part of the thesis is focused on the problems related to sludge and evaluates sludge disposal from waste treatment plants. The thesis mentions factors influencing method selection of sludge disposal as well as it compares sludge disposal in the Czech Republic and in the other states of the EU. It describes a complete waste treatment line and sludge disposal in the area of sludge treatment and disposal. It deals with sludge disintegration and describes the most effective methods of disintegration. The second part of the thesis describes an experimental part of disintegration of waste treatment sludge. An experiment was conducted in the school laboratory in a way of thermal disintegration in the double-surface pressure tank. The disintegration was conducted to temperatures of 60 °C, 90 °C, 120 °C, 150 °C, and 180 °C. We monitored dependence of the sludge dry residue content on disintegration temperature as well as content of suspended solids in liquid fraction (FUGAT). It was possible to choose optimal temperature of disintegration in accordance with processed results.