Made available in DSpace on 2014-06-11T19:32:53Z (GMT). No. of bitstreams: 0 Previous issue date: 2011-08-15Bitstream added on 2014-06-13T20:48:02Z : No. of bitstreams: 1 bruno_m_dr_jabo.pdf: 1408786 bytes, checksum: a69a3278194ba9d26df9d738e43e62fe (MD5) / Neste trabalho avaliou-se o desempenho do tratamento de águas residuárias do beneficiamento de café por via úmida em reatores anaeróbios de fluxo ascendente com manta de lodo (UASB), em dois estágios em escala de bancada, seguidos de um sistema de pós-tratamento com lodo ativado (PT) em batelada alimentada. O primeiro reator UASB (R1) foi submetido a tempo de detenção hidráulica (TDH) de 6,2 e 3,1 d e a cargas orgânicas volumétricas (COV) de 2,26; 4,64; 2,67 e 6,85 kg DQO total (m3 d)-1, e o segundo (R2) a TDH de 3,1 e 1,5 d e COV de 0,4; 2,4; 18,7 e 3,38 kg DQO total (m3 d)-1. Os valores médios de DQO total do afluente variaram de 13.891 a 28.602 mg L-1 e as eficiências médias de remoção de DQO total variaram de 96 a 97%, respectivamente, nos reatores UASB e PT. O teor médio de metano no biogás variou de 76 a 81%, no R1 e de 69 a 79% no R2. A produção volumétrica máxima de metano de 0,322 m3 CH4 (m3 reator d)-1 foi obtida com COV de 4,5 kg DQO (m3 d)-1 e TDH de 6,2 d no R1. Os valores médios de pH variaram de 7,2 a 7,6 e de 7,2 a 7,8 nos efluentes do R1 e R2. As concentrações médias de ácidos voláteis totais nos efluentes do R1 e R2 variaram de 103 a 1944 e 124 a 1132 mg de CH3COOH L-1 com o aumento da COV. As concentrações médias de fenóis totais no afluente variaram de 48 a 186 mg L-1 e as eficiências médias de remoção nos reatores UASB (R1+R2) variaram de 83 a 92%, respectivamente, e aumentaram para 89 e 95% com o pós-tratamento com lodo ativado. As eficiências médias de remoção de nitrogênio e fósforo total variaram de 57 a 80% e de 44 a 58%, respectivamente, nos reatores UASB em dois estágios e aumentaram para 82 e 82% com a inclusão do pós-tratamento. O sistema de tratamento composto... / In this work it was evaluated the efficiency of the up-flow anaerobic sludge blanket (UASB) reactors in two stages, in bench scale, followed by activated sludge treating coffee cherry pulping wastewater, submitted to hydraulic detention time (HDT) of 6.2 and 3,1 d in the first reactor (R1) and organic loading rate (OLR) ranging of 2.26, 4.64, 2,67 and 6,85 kg totalCOD (m3 d)-1, and the second reactor (R2) submitted to HDT of 3.1 and 1.55 d with OLR of 0.4, 2.4, 1.87 and 3.38 kg totalCOD (m3 d)-1. The average value of the total COD influent was ranged from 13.891 to 28.602 mg L-1 and the average value of removal efficiencies of the total COD ranged from 96 to 97%, respectively, in the system of treatment with the UASB reactors in two stages. The content of methane in the biogas varied from 76 to 81% in the R1 and from 69 to 79% in the R2. The maximum volumetric methane production of 0,322 m3 CH4 (m3 reactor d)-1 was obtained with OLR of 4.64 kg totalCOD (m3 reactor d)-1 and HDT of 6.2 d in the R1. The average values of pH ranged from 6.9 to 7.6 and 7.2 to 7.8 in the effluents of R1 and R2. The average total volatile acids concentrations of the effluents of the reactors UASB ranged from 103 to 1944 and 124 to 1132 mg of CH3COOH L-1 due to the increase of OLR. The average values of the total phenols of influent ranged of 47.8 to 186.5 mg L-1 and the average removal efficiencies ranged from 83 to 92% in the UASB reactors and with the start-up of the post-treatment system by activated sludge it was increased to 95%. The average value of the removal efficiencies of nitrogen and total phosphorus ranged from... (Complete abstract click electronic access below)

Made available in DSpace on 2014-06-11T19:27:22Z (GMT). No. of bitstreams: 0 Previous issue date: 2011-08-16Bitstream added on 2014-06-13T20:16:37Z : No. of bitstreams: 1 cangani_mt_me_jabo_parcial.pdf: 133174 bytes, checksum: 83fdce5233c859451850c9463579de75 (MD5) Bitstreams deleted on 2014-10-03T16:24:40Z: cangani_mt_me_jabo_parcial.pdf,Bitstream added on 2014-10-03T16:27:37Z : No. of bitstreams: 2 cangani_mt_me_jabo_parcial.pdf.txt: 17021 bytes, checksum: 1f48b80f9f09d5f8fc41694b0c3c56ea (MD5) 000681838.pdf: 3677573 bytes, checksum: 863c1c839ba825e42ba039dd26564761 (MD5) Bitstreams deleted on 2014-10-03T16:33:15Z: 000681838.pdf,Bitstream added on 2014-10-03T16:43:28Z : No. of bitstreams: 2 cangani_mt_me_jabo_parcial.pdf.txt: 17021 bytes, checksum: 1f48b80f9f09d5f8fc41694b0c3c56ea (MD5) 000681838.pdf: 3677573 bytes, checksum: 863c1c839ba825e42ba039dd26564761 (MD5) Bitstreams deleted on 2014-10-03T16:48:55Z: 000681838.pdf,Bitstream added on 2014-10-03T16:49:46Z : No. of bitstreams: 1 000681838.pdf: 3677573 bytes, checksum: 863c1c839ba825e42ba039dd26564761 (MD5) Bitstreams deleted on 2014-10-27T11:47:08Z: 000681838.pdf,Bitstream added on 2014-10-27T11:48:04Z : No. of bitstreams: 1 000681838.pdf: 3677573 bytes, checksum: 863c1c839ba825e42ba039dd26564761 (MD5) / Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES) / Fundação de Amparo à Pesquisa do Estado de São Paulo (FAPESP) / Neste trabalho, avaliou-se o desempenho de dois conjuntos de reatores anaeróbios de fluxo ascendente com manta de lodo (UASB) instalados em série. Os conjuntos I e II foram compostos por dois reatores UASB em série com volumes de 908 e 350 L e de 908 e 188 L, respectivamente. No conjunto II, foi realizado pós tratamento do efluente em um reator operado em batelada sequencial (RBS) com alimentação contínua, com volume de 3000 L. As cargas orgânicas volumétricas (COV) aplicadas no primeiro reator dos conjuntos I e II variaram de 8,36 a 9,95 g DQO total (L d)-1 e de 7,83 a 11,6 g DQO total (L d)-1, respectivamente. As eficiências médias de remoção de DQO total, nitrogênio Kjeldahl (NK), fósforo total (P-total) foram elevadas e variaram de 95 a 97% e de 97 a 99%, de 64 a 67% e de 53 a 69%, e de 80 a 87% e de 71 a 89%, nos conjuntos I e II, respectivamente. As eficiências também foram elevadas para os metais Cu, Fe, Mn e Zn nos conjuntos I e II e variaram de 80 a 91% e de 63 a 80%, de 59 a 80% e de 51 a 72%, de 89 a 97% e de 81 a 98%, de 87 a 98% e de 91 a 99%, respectivamente. A semeadura do milho, foi realizado na safrinha 2009 e na safra 2009/2010, ambos em sistema de plantio direto e convencional, para a confecção de silagem. Os valores do pH observados na silagem não diferiram entre os tratamentos nas duas épocas de semeadura e nos sitemas de plantio direto e convencional. A adubação do milho para confecção de silagem, com dejeto bruto de suíno, com dejetos tratados em sistema anaeróbio e com os dejetos do pós-tratamento, quando comparada com a adubação mineral, não apresentou resultados com diferenças significativas na silagem na maioria dos atributos avaliados. O reúso dos efluentes tratados e do dejeto bruto, não promoveu alterações na nutrição da planta, porém os efluentes... / This study evaluated the performance of two sets of upflow anaerobic sludge blanket (UASB) installed in series. The sets I and II were composed of two UASB reactors in series with volumes of 908 and 350 L and 908 L and 188, respectively. In set II was conducted after the treatment of the effluent in a sequencing batch reactor (SBR) with continuous flux, with a volume of 3000 L. The volumetric organic loads (VOC) applied to the first reactor of the sets I and II ranged from 8.36 to 9.95 g total COD (L d) -1 and 7.83 to 11.6 g total COD (L d) -1, respectively. The average removal efficiencies of total COD, Kjeldahl nitrogen (NK), total phosphorus (total P) were high and ranged from 95 to 97% and 97 to 99%, 64 to 67% and 53 to 69% and 80 to 87% and 71 to 89% in clusters I and II, respectively. The efficiencies were also high for Cu, Fe, Mn and Zn in clusters I and II, and ranged from 80 to 91% and 63 to 80%, 59 to 80% and 51 to 72% from 89 to 97 and 81% to 98%, 87 to 98% and 91 to 99%, respectively. We carried out the swing of maize in the 2009 off-season and 2009/2010 season, both in no-tillage and conventional sistems for making silage. The pH values observed in the silage did not differ significantly between treatments in both seasons of swing and in the sistems of tillage and no-tillage. The fertilization of corn for silage making, with raw pig manure with waste treated in anaerobic system and the waste from the post-treatment compared to mineral fertilization, results showed no significant difference in silage in most parameters. The reuse of treated effluent and raw manure, did not promote changes in the nutrition of corn but the application of treated effluent increased concentrations of N readily available for plants in soil. Even in much larger doses applied compared to the raw waste, the treated effluent, promoted soil contamination by total coliforms and thermotolerant lower