Start-up of horizontal anaerobic reactors with sludge blanket and fixed bed for wastewater treatment from coffee processing by wet method

In this study it was evaluated the start-up procedures of anaerobic treatment system with three horizontal anaerobic reactors (R1, R2 and R3), installed in series, with volume of 1.2 L each. R1 had sludge blanket, and R2 and R3 had half supporter of bamboo and coconut fiber, respectively. As an affluent, it was synthesized wastewater from mechanical pulping of the coffee fruit by wet method, with a mean value of total chemical oxygen demand (CODtotal) of 16,003 mg L-1. The hydraulic retention time (HRT) in each reactor was 30 h. The volumetric organic loading (VOL) applied in R1 varied from 8.9 to 25.0 g of CODtotal (L d)-1. The mean removal efficiencies of CODtotal varied from 43 to 97% in the treatment system (R1+R2+R3), stabilizing above 80% after 30 days of operation. The mean content of methane in the biogas were of 70 to 76%, the mean volumetric production was 1.7 L CH4 (L reactor d)-1 in the system, and the higher conversions were around at 0.20 L CH4 (g CODremoved)-1 in R1 and R2. The mean values of pH in the effluents ranged from 6.8 to 8.3 and the mean values of total volatile acids remained below 200 mg L-1 in the effluent of R3. The concentrations of total phenols of the affluent ranged from 45 to 278 mg L-1, and the mean removal efficiency was of 52%. The start-up of the anaerobic treatment system occurred after 30 days of operation as a result of inoculation with anaerobic sludge with active microbiota.

Performance of UASB reactors in two stages under different HRT and OLR treating residual waters of swine farming

In this study it was evaluated the effects of hydraulic retention time (HRT) and Organic Loading Rate (OLR) on the performance of UASB (Upflow Anaerobic Sludge Blanket) reactors in two stages treating residual waters of swine farming. The system consisted of two UASB reactors in pilot scale, installed in series, with volumes of 908 and 188 L, for the first and second stages (R1 and R2), respectively. The HRT applied in the system of anaerobic treatment in two stages (R1 + R2) was of 19.3, 29.0 and 57.9 h. The OLR applied in the R1 ranged from 5.5 to 40.1 kg CODtotal (m³ d)-1. The average removal efficiencies of chemical oxygen demand (COD) and total suspended solids (TSS) ranged, respectively, from 66.3 to 88.2% and 62.5 to 89.3% in the R1, and from 85.5 to 95.5% and 76.4 to 96.1% in the system (R1 + R2). The volumetric production of methane in the system (R1 + R2) ranged from 0.295 to 0.721 m³CH4 (m³ reactor d)-1. It was found that the OLR applied were not limiting to obtain high efficiencies of CODtotal and TSS removal and methane production. The inclusion of the UASB reactor in the second stage contributed to increase the efficiencies of CODtotal and TSS removal, especially, when the treatment system was submitted to the lowest HRT and the highest OLR.

Anaerobic reactors with biofilter and different diameter-length ratios in cassava starch industry wastewater treatment

The use of anaerobic reactors with media support in the treatment of wastewater from the cassava starch industry has emerged as a viable option because it allows the application of high organic loads and a significant reduction of the HDT needed for the treatment. This research aimed at studying the process of biodigestion in two anaerobic reactors with bamboo support, in the treatment of effluent of cassava starch, by evaluating their performance. The two reactors used present the following diameter: length ratio, 1:6 and 1:3. The organic loads applied to the systems were 0.519, 1.156, 1.471, 3.049, 4.347, 4.708 and 5.601g.L-1.d-1. Regarding the efficiency of removal of COD, TS and TVS, no statistically significant differences were obtained between the reactors. The two systems evaluated showed a stable behavior with respect to the VA/TA (volatile acidity/total alkalinity) for all submitted loads. The reactors tended to the maintenance of biogas production as a function of consumed COD for the last three organic loads applied, indicating an ability to withstand higher organic loads.

Performance of UASB reactors in two stages followed by post-treatment with activated sludge in wastewater batch of wet-processed coffee

In this study it was evaluated the efficiency of the treatment of wet-processed coffee wastewater in upflow anaerobic sludge blanket (UASB) reactors in two stages, in bench scale, followed by post-treatment with activated sludge in batch. The first UASB reactor was submitted to an hydraulic retention time (HRT) of 6.2 d and organic loading rates (OLR) of 2.3 and 4.5g CODtotal (L d)-1, and the second UASB reactor to HRT of 3.1 d with OLR of 0.4 and 1.4g CODtotal (L d)-1. The average values of the affluent CODtotal increased from 13,891 to 27,926mg L-1 and the average efficiencies of removal of the CODtotal decreased from 95 to 91%, respectively, in the UASB reactors in two stages. The volumetric methane production increased from 0.274 to 0.323L CH4 (L reactor d)-1 with increment in the OLR. The average concentrations of total phenols in the affluent were of 48 and 163mg L-1, and the removal efficiencies in the UASB reactors in two stages of 92 and 90%, respectively, and increased to 97% with post-treatment. The average values of the removal efficiencies of total nitrogen and phosphorus were of 57 to 80% and 44 to 60%, respectively, in the UASB reactors in two stages and increased to 91 and 84% with the post-treatment.

Anaerobic-aerobic treatment of swine wastewater in uasb and batch reactors in series

In this work it was evaluated the performance of two systems of swine wastewater treatment consisting of two-stage upflow anaerobic sludge blanket (UASB) reactors, with and without post-treatment in sequencing batch reactor (SBR), fed continuously, with aerobic phase. The UASB reactors in the first stage had 908 L in the sets I and II, and in the second stage 350 and 188 L, respectively. In the set II the post-treatment was performed in a SBR of 3,000 L. The hydraulic detention times in the anaerobic treatment systems were 100, 75 and 58 h in the set I; 87, 65 and 51 h in the set II; and 240 and 180 h in the SBR. The volumetric organic load applied in the first stage UASB reactors ranged from 6.9 to 12.6 g total COD (L d)-1 in the set I and 7.5 to 9.8 g total COD (L d)-1 in the set II. The average removal efficiencies of total COD, total phosphorus (Ptotal), and Kjeldahl and organic nitrogen (KN and Norg) in the anaerobic treatment systems were similar and reached maximum values of 97%, 64%, 68%, and 98%. In the SBR, the removal efficiencies of total COD and thermotolerant coliforms were up to 62 and 92% resulting, respectively, in effluent concentrations of 135 mg L-1 and 2x10(4)MPN (100 mL)-1. For Ptotal, total nitrogen (TN) and Norg, the average removal efficiencies in the SBR were up to 58, 25 and 73%, respectively.

COD, TSS, nutrients and coliforms removals in UASB reactors in two stages treating swine wastewater

The performance of two upflow anaerobic sludge blanket (UASB) reactors was evaluated in pilot scale (908 and 188 L), installed in series (R1 and R2), fed with swine wastewater with TSS around 5 and 13 g L-1. The UASB reactors were submitted to HDT of 36 and 18 h with VOL of 5.5 to 34.4 g COD (L d)-1 in the R1 and HDT of 7.5 e 3.7 h with VOL from 5.1 to 45.2 g COD (L d)-1 in the R2. The average removal efficiencies of COD ranged from 55 to 85% in the R1 and from 43 to 57% in the R2, resulting in values from 82 to 93% in the UASB reactors in two stage. Methane concentrations in the biogas were 69 to 74% with specific production from 0.05 to 0.27 L CH4 (g removedCOD)-1 in the R1 and of 0.10 to 0.12 L CH4 (g removedCOD)-1 in the R2. The average removal efficiencies were 61 to 75% for totalP, 39 to 69% for KN, 82 to 93% for orgN and 20 to 94% for Fe, Zn, Cu and Mn. The amN concentration were not reduced indicating the need to post-treatment for effluent disposal into water bodies. There were reductions of total coliforms from 99.8123 to 99.9989% and of thermotolerant coliforms from 99.9725 to 99.9999%. The conditions imposed to the UASB reactors in two stage provided high conversions of removedCOD into methane (up to 77%) and reductions of organic an inorganic pollution loads from swine wastewater.

Start-up of anaerobic reactors for slaughterhouse wastewater treatment

This study aimed to evaluate the start-up of a horizontal anaerobic fixed bed reactor (HAFBR) followed by an upflow anaerobic sludge blanket (UASB) for the slaughterhouse wastewater treatment. HAFBR was filled with bamboo rings and had 1.2 m in length, 0.10 m in diameter and volume of 7.5 L. The UASB had the volume of 15 L. The HAFBR and UASB operated at organic loading rate and hydraulic retention time average of 8.46 and 3.77 kg m-3 d-1 of COD and 0.53 and 0.98 days, respectively. During 150 days of monitoring system it was found pH 6.8, relatively high values of bicarbonate alkalinity (> 1000 mg L-1) and reduced values of volatile acids (70 to 150 mg L-1), which afforded average removal efficiencies of COD total and total suspended solids of the order of 31 and 23% in HAFBR and 79% and 63% in UASB. It can be concluded that the generation and consumption of bicarbonate alkalinity and total volatile acids, thereby maintaining the pH during the study indicated stable operation of the reactors. The COD removal in the reactors was satisfactory especially when it considers that the assessment was conducted in a period of adaptation of organisms to the effluent and also the high organic load applied during this period.

Fluid dynamic modelling and simulation of circulating fluidized bed reactors: importance of the interface turbulence transfer

The main objective of this work is to analyze the importance of the gas-solid interface transfer of the kinetic energy of the turbulent motion on the accuracy of prediction of the fluid dynamic of Circulating Fluidized Bed (CFB) reactors. CFB reactors are used in a variety of industrial applications related to combustion, incineration and catalytic cracking. In this work a two-dimensional fluid dynamic model for gas-particle flow has been used to compute the porosity, the pressure, and the velocity fields of both phases in 2-D axisymmetrical cylindrical co-ordinates. The fluid dynamic model is based on the two fluid model approach in which both phases are considered to be continuous and fully interpenetrating. CFB processes are essentially turbulent. The model of effective stress on each phase is that of a Newtonian fluid, where the effective gas viscosity was calculated from the standard k-epsilon turbulence model and the transport coefficients of the particulate phase were calculated from the kinetic theory of granular flow (KTGF). This work shows that the turbulence transfer between the phases is very important for a better representation of the fluid dynamics of CFB reactors, especially for systems with internal recirculation and high gradients of particle concentration. Two systems with different characteristics were analyzed. The results were compared with experimental data available in the literature. The results were obtained by using a computer code developed by the authors. The finite volume method with collocated grid, the hybrid interpolation scheme, the false time step strategy and SIMPLEC (Semi-Implicit Method for Pressure Linked Equations - Consistent) algorithm were used to obtain the numerical solution.

Revisitando os Clássicos da RAP

Este artigo revisita uma investigação realizada pelo Programa de Estudos de Administração Brasileira (Abras) em 2002, sobre os Clássicos da Revista de Administração Pública (RAP). Originalmente divulgado no formato de CD-ROM, como parte dos eventos comemorativos dos 35 anos de publicação ininterrupta daquele periódico, o texto discorre sobre a metodologia daquela investigação e revela 10 trabalhos que podem ser considerados os clássicos da revista. O banco de dados gerado pela pesquisa analisou cerca de 4.500 artigos de 13 revistas acadêmicas, registrando 887 citações aos artigos publicados pela RAP (total: cerca de 1.440) ao longo dos primeiros 35 anos de sua existência.

Nível hemoglobínico em escolares da capital de São Paulo, Brasil

Com o objetivo de obter dados para avaliação do estado nutritivo dos escolares, o Serviço de Saúde Escolar da Secretaria da Educação do Estado de São Paulo, Brasil, realizou um inquérito laboratorial, usando como parâmetro a determinação da taxa hemoglobínica numa amostra de 20% dos 2.440 alunos do Grupo Escolar "Leonor Quadros", localizado em um bairro periférico da cidade de São Paulo. O método de exame utilizado constituiu na dosagem fotocolorimétrica da hemoglobina, empregando-se para isto um fotocolorímetro fabricado pelo Laboratório Ames do Brasil S/A. A taxa hemoglobínica média encontrada foi de 13,0 g%, sendo a média masculina de 13,09 g% e a feminina de 12,99g%. As taxas mínimas e máximas foram de 7,5 g% e 17,09 g%. Para melhor ordenação dos resultados, e de acordo com o nível hemoglobínico obtido, os escolares foram divididos em três grupos: o 1.° compreendendo escolares com nível hemoglobínico até 10,99 g%; o 2.º, entre 11,0 g% e 12,99g%, e o 3.°, acima de 13,0%. No primeiro grupo foram encontrados 2,3% dos alunos; no segundo, 36,2%, e no terceiro, 61,4%, verificando-se que 96% dos escolares apresentam nível hemoglobínico na faixa de 11,0 g% e mais. À vista dos resultados obtidos, considerou-se de razoável para bom o estado nutritivo dos escolares examinados.

Estudo epidemiológico sobre a silicose pulmonar na Região Sudeste do Brasil, através de inquérito em pacientes internados em hospitais de tisiologia

Com base no conhecimento de que a tuberculose pulmonar é freqüente complicação evolutiva da silicose (caracterizando a sílicotuberculose), foi realizado estudo visando a ampliar o conhecimento da epidemiologia desta doença profissional na Região Sudeste do Brasil, através do levantamento detalhado dos antecedentes ocupacionais de 3.440 pacientes masculinos, adultos, internados por tuberculose, em 27 Hospitais de Tisiologia, nos Estados de São Paulo, Rio de Janeiro e Minas Gerais (Brasil). Através da anamnese ocupacional foram detectados 327 "prováveis casos" de sílicotuberculose (9,5%). As leituras independentes e "cegas" das radiografias de tórax, feitas por três profissionais experientes em silicose (2 Pneumologistas e 1 Radiologista), confirmaram a presença de imagens positivas ou suspeitas de pneumoconiose, em 119 pacientes (3,5%). Esta proporção de casos de sílicotuberculose, aplicada ao número total de internações de adultos masculinos, ocorridas em 1977, e à freqüência da tuberculose em pacientes silicóticos, de acordo com a experiência brasileira (3,3%), permitiu estimar em 20.000 o número aproximado de portadores de silicose na Região Sudeste do Brasil. Idêntico raciocínio permitiu estimar em 5.100 o número de portadores de silicose no Estado de São Paulo, 6.900 no Rio de Janeiro e 7.400 em Minas Gerais. Com base na amostra de 119 casos de sílicotuberculose encontrados, são estudados alguns caracteres epidemiológicos da silicose nessa Região: idade dos pacientes, atividades ocupacionais exercidas e tempo de exposição. Concluiu-se pela importância da silicose como "problema de saúde pública" nessa Região, e como "doença profissional" que deveria merecer prioridade dos órgãos responsáveis pela Saúde Ocupacional no Brasil.

Confiabilidade diagnóstica dos transtornos mentais da versão para cuidados primários da Classificação Internacional das Doenças

OBJETIVO: Avaliar a confiabilidade da versão para teste do capítulo V - "Transtornos Mentais e do Comportamento", da décima revisão da Classificação Internacional das Doenças, Versão para Cuidados Primários (CID -10 CP), preparado pela Divisão de Saúde Mental da Organização Mundial da Saúde (OMS). MÉTODOS: Durante os meses de setembro e outubro de 1994 foram treinados médicos gerais comunitários (MGC) da Secretaria da Saúde e do Meio Ambiente do Estado do Rio Grande do Sul, no uso da citada versão, preparada para teste de campo, conforme o delineamento proposto pela OMS. RESULTADOS: Os resultados referem-se ao estudo sobre concordância dos diagnósticos atribuídos por 9 duplas de MGC a 440 pacientes de primeira consulta. O Kappa de Cohen para Transtorno de Saúde Mental, presente ou ausente, foi de 0,79 (IC 95%: 0,69 -- 0,88). CONCLUSÃO: O uso da CID-10 CP dará maior especificidade às informações e permitirá maior comunicação entre as equipes de saúde em nível de cuidados primários.

Prevalência de maus-tratos na terceira idade: revisão sistemática

OBJETIVO: Identificar estudos sobre prevalência de abuso na terceira idade e analisar a qualidade dos estudos. MÉTODOS: Revisão sistemática estudos de base populacional em bases de dados eletrônicos (PubMed, LILACS, Embase, ISI, PsycInfo), referente aos anos de 1988 a 2005. Foram incluídos os estudos de base populacional e excluídos os estudos sem definição metodológica delineada e estudos realizados em clientela de serviços especializados. RESULTADOS: Foram encontrados 440 artigos, mas apenas 11 artigos foram selecionados. A maioria dos artigos foi de corte transversal, apenas dois apresentaram desenho longitudinal. Os estudos foram conduzidos em diversas regiões do mundo, sobretudo dos Estados Unidos e da Europa. Observou-se variação nas definições de abuso. Os estudos de prevalência encontraram coeficientes de abuso físico entre 1,2% (Holanda) e 18% (Finlândia). CONCLUSÕES: Existe substancial variação de prevalência entre os países, parecendo haver uma variável cultural importante. Como o número de idosos é crescente no mundo, são necessários mais estudos de base populacional representativos dessa faixa etária para melhor compreensão do fenômeno.

Isolation of human fungi from soil and identification of two endemic areas of Cryptococcus neoformans and Coccidioides immitis

The present study was carried out in two different areas of Province of Cordoba, Argentina, where there was a suspicious of endemic mycosis. The previous data were the presence of a clinical case of pulmonary cryptococcosis in one area (Alta Gracia) and the previous findings of a high incidence of coccidioidin and cryptococcin reactors in the population of the second one (Villa Dolores). In both areas soil samples for fungi were studied and Cryptococcus neoformans was found in 2/25 samples from Alta Gracia. In Villa Dolores Coccidioides immitis was isolated in 2/40 samples, and C. neoformans in 1/40 samples. Delayed hypersensitivity test with cryptococcin was determined in the population from Alta Gracia and it was found to be 5.3%. Positive cutaneous tests with coccidioidin (33.8%) and cryptococcin (31.9%) in Villa Dolores were obtained. With these findings two endemic areas of systemic mycoses in Cordoba, Argentina were delimited.

Toxoplasmosis serology: an efficient hemagglutination procedure to detect IgG and IgM antibodies

In search of an efficient but simple, low cost procedure for the serodiagnosis of Toxoplasmosis, especially suited for routine laboratories facing technical and budget limitations as in less developed countries, the diagnostic capability of Hematoxo® , an hemagglutination test for toxoplasmosis, was evaluated in relation to a battery of tests including IgG- and IgM-immunofluorescence tests, hemagglutination and an IgM-capture enzymatic assay. Detecting a little as 5 I.U. of IgG antitoxoplasma antibodies, Hematoxo® showed a straight agreement as to reactivity and non-reactivity for the 443 non-reactive and the 387 reactive serum samples, included in this study. In 23 cases presenting a serological pattern of acute toxoplasmosis and showing IgM antibodies, Hematoxo® could detect IgM antibodies in 18, indicated by negativation or a significant decrease in titers as a result of treating samples with 2-mercapto-ethanol. However, a neat increase in sensitivity for IgM specific antibodies could be achieved by previously removing IgG from the sample, as demonstrated in a series of acute toxoplasmosis sera. A simple procedure was developed for this purpose, by reconstituting a lyophilized suspension of Protein A - rich Staphylococcus with the lowest serum dilution to be tested. Of low cost and easy to perform, Hematoxo® affords not only a practical qualitative procedure for screening reactors and non-reactors, as in prenatal services, but also quantitative assays that permit to titrate antibodies as well as to identify IgM antibodies.