ABSTRACT
Abstract Waste produced by the construction sector is a problem that has grown over the last few years. Construction and demolition waste makes up about 50% by mass of the total solid waste produced in Brazil. One alternative by which to reduce this volume is recycling this material in the form of aggregates. However, it is necessary to analyze the environmental risk that the use of recycled aggregates can entail for adjacent soil and the water table. The purpose of this work was to evaluate pervious concrete samples that contained recycled aggregates and to subject them to leaching tests. The results were compared with the limits established by the Italian methodology. Aggregates with 10, 25, 50, and 100% ceramic were used, as well as a recycled concrete aggregate and a natural aggregate. With the exception of the 25% ceramic trial, all the treatments introduced chromium to the water in which they were immersed, with accumulated concentrations varying from 0.009 to 0.099 mg L-1. Cadmium was found in higher quantities, with cumulated concentrations between 0.104 and 0.417 mg L-1. Sulfate concentrations were higher after 24 h of immersion, with a maximum release of 71.7 mg L-1. The concrete made with 100% ceramic aggregate leached more chromium and sulfate than the other aggregates.
Subject(s)
Water/analysis , Solid Waste , Construction Industry , Percolation/methods , Ceramics/chemistry , Environmental Hazards , Brazil , Recycling , ItalyABSTRACT
ABSTRACT Constructed wetlands might be an alternative for communities away from urban centers and not served by a domestic wastewater treatment system. The purpose of this study was to provide instructions for the implementation of subsurface flow constructed wetland systems. To that end, we gathered information regarding the construction aspect, plants, and operational parameters used in systems which already operate in the country and the respective efficiency of these sets after previous treatment. The system in real scale proposed by Oliveira et al. (2005) was prominent among those that presented the highest efficiency. It was preceded by upflow anaerobic reactor built in brick, with macrophyte of the Typha genre, crushed stone at the entry and exit of the system, and sand in its intermediate portion. It required 1.04 m² surface area per inhabitant in humid temperate climate and hot summer, 1.71 m³ d-1 flow, and one-day hydraulic detention. The considerations presented here might help the construction of this kind of system, regarding dimensional and operational criteria.
RESUMO As wetlands construídas podem ser uma alternativa para comunidades afastadas de centros urbanos que não são atendidas por rede de tratamento de esgoto. Visando à orientação para implantação do sistema de wetlands construídas de fluxo subsuperficial, foi levantada uma série de informações a respeito dos aspectos construtivos, das plantas e parâmetros operacionais utilizados em sistemas já em funcionamento no país e a respectiva eficiência do conjunto, após um tratamento precedente. Entre os sistemas que apresentaram melhor eficiência, destacou-se o de Oliveira et al. (2005) em escala real, precedido por reator anaeróbio de fluxo ascendente, construído em alvenaria, com a macrófita do gênero Typha, brita na entrada e saída do sistema e areia na parte intermediária, com uma área superficial de 1,04 m2 por habitante de clima temperado úmido com verão quente, vazão de 1,71 m3 d-1 e tempo de detenção hidráulica de um dia. A elaboração das considerações apresentadas neste trabalho pode auxiliar na construção desse tipo de sistema, construído nos critérios de dimensionamento e operação.
ABSTRACT
Avaliou-se a influência do bicarbonato de sódio (NaHCO3) no desempenho do reator anaeróbio batelada sequencial com biomassa imobilizada tratando vinhaça a 55 e a 35ºC. O reator foi preenchido com espuma de poliuretano e agitado a 300 rpm. A adaptação a 55ºC estendeu-se por 50 dias, tendo o reator sido alimentado com vinhaça (DQO de 0,3 a 1,0 g/L). Para a operação a 35ºC, procedeu-se inicialmente ao enriquecimento da população metanogênica, durante 21 dias, com substrato à base de etanol (2,5 gDQO/L). Posteriormente, cargas orgânicas volumétricas (COV) de 0,85 a 5,70 gDQO/L.d foram aplicadas no reator a 55ºC, com suplementação de 1,2 a 0,4 gHCO3-/gDQO. A 35ºC, o reator foi submetido a COV de 2,85 a 36,0 gDQO/L.d com 0,4 a 0,2 gHCO3-/gDQO. A remoção de DQO variou de 43 a 78 por cento a 55ºC e de 75 a 85 por cento a 35ºC. A suplementação de alcalinidade mostrou-se essencial para a estabilidade do processo, sendo requerida em menor quantidade a 35ºC.
The influence of the sodium bicarbonate (NaHCO3) on the performance of an anaerobic sequencing batch biofilm reactor treating vinasse at 55 and 35ºC was evaluated. The reactor was filled with polyurethane foam and agitated at 300 rpm. The acclimatization period at 55ºC lasted 50 days, and the reactor was fed with vinasse (COD from 0.3 to 1.0 g/L). A previous enrichment of methanogenic population was provided for the reactor operated at 35ºC, feeding it with an ethanol based substrate (2.5 gCOD/L) during 21 days. Further on, organic loading rates (OLR) ranging from 0.85 to 5.70 gCOD/L.d were applied to the reactor at 55ºC, supplemented with 1.2 to 0.4 gHCO3-/gCOD. At 35ºC the reactor was subjected to OLR ranging from 2.85 to 36.0 gCOD/L.d with 0.4 to 0.2 gHCO3-/gCOD. COD removal ranged from 43 to 78 percent at 55ºC and from 75 to 85 percent at 35ºC. Alkalinity supplementation was found to be essential for process stability, but the amount required was lower at 35ºC.