879 resultados para coke-washing wastewater
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This paper applies a policy analysis approach to the question of how to effectively regulate micropollution in a sustainable manner. Micropollution is a complex policy problem characterized by a huge number and diversity of chemical substances, as well as various entry paths into the aquatic environment. It challenges traditional water quality management by calling for new technologies in wastewater treatment and behavioral changes in industry, agriculture and civil society. In light of such challenges, the question arises as to how to regulate such a complex phenomenon to ensure water quality is maintained in the future? What can we learn from past experiences in water quality regulation? To answer these questions, policy analysis strongly focuses on the design and choice of policy instruments and the mix of such measures. In this paper, we review instruments commonly used in past water quality regulation. We evaluate their ability to respond to the characteristics of a more recent water quality problem, i.e., micropollution, in a sustainable way. This way, we develop a new framework that integrates both the problem dimension (i.e., causes and effects of a problem) as well as the sustainability dimension (e.g., long-term, cross-sectoral and multi-level) to assess which policy instruments are best suited to regulate micropollution. We thus conclude that sustainability criteria help to identify an appropriate instrument mix of end-of-pipe and source-directed measures to reduce aquatic micropollution.
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A 6-month-long, bench-scale simulation of an industrial wastewater stabilization pond (WSP) system was conducted to evaluate responses to several potential performance-enhancing treatments. The industrial WSP system consists of an anaerobic primary (1ry) WSP treating high-strength wastewater, followed by facultative secondary (2ry) and aerobic tertiary (3ry) WSPs in series treating lower-strength wastewater. The 1ry WSP was simulated with four glass aquaria which were fed with wastewater from the actual WSP system. The treatments examined were phosphorus supplementation (PHOS), phosphorus supplementation with pH control (PHOS+ALK), and phosphorus supplementation with pH control and effluent recycle (PHOS+ALK+RCY). The supplementary phosphorus treatment alone did not yield any significant change versus the CONTROL 1ry model pond. The average carbon to phosphorus ratio of the feed wastewater received from the WSP system was already 100:0.019 (i.e., 2,100 mg/l: 0.4 mg/l). The pH-control treatments (PHOS+ALK and PHOS+ALK+RCY) produced significant results, with 9 to 12 percent more total organic carbon (TOC) removal, 43 percent more volatile organic acid (VOA) generation, 78 percent more 2-ethoxyethanol and 14 percent more bis(2-chloroethyl)ether removal, and from 100- to 10,000-fold increases in bacterial enzyme activity and heterotrophic bacterial numbers. Recycling a 10-percent portion of the effluent yielded less variability for certain physicochemical parameters in the PHOS+ALK+RCY 1ry model pond, but overall there was no statistically-detectable improvement in performance versus no recycle. The 2ry and 3ry WSPs were also simulated in the laboratory to monitor the effect and fate of increased phosphorus loadings, as might occur if supplemental phosphorus were added to the 1ry WSP. Noticeable increases in algal growth were observed at feed phosphorus concentrations of 0.5 mg/l; however, there were no significant changes in the monitored physicochemical parameters. The effluent phosphorus concentrations from both the 2ry and 3ry model ponds did increase notably when feed phosphorus concentrations were increased from 0.5 to 1.0 mg/l. ^
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A bench-scale treatability study was conducted on a high-strength wastewater from a chemical plant to develop an alternative for the existing waste stabilization pond treatment system. The objective of this study was to determine the treatability of the wastewater by the activated sludge process and, if treatable, to determine appropriate operating conditions, and to evaluate the degradability of bis(2-chloroethyl)ether (Chlorex) and benzene in the activated sludge system. Four 4-L Plexi-glass, complete mixing, continuous flow activated sludge reactors were operated in parallel under different operating conditions over a 6-month period. The operating conditions examined were hydraulic retention time (HRT), sludge retention time (SRT), nutrient supplement, and Chlorex/benzene spikes. Generally the activated sludge system treating high-strength wastewater was stable under large variations of organic loading and operating conditions. At an HRT of 2 days, more than 90% removal efficiency with good sludge settleability was achieved when the organic loading was less than 0.4 g BOD$\sb5$/g MLVSS/d or 0.8 g COD/g MLVSS/d. At least 20 days of SRT was required to maintain steady operation. Phosphorus addition enhanced the performance of the system especially during stressed operation. On the average, removals of benzene and Chlorex were 73-86% and 37-65%, respectively. In addition, the low-strength wastewater was treatable by activated sludge process, showing more than 90% BOD removal at a HRT of 0.5 days. In general, the sludge had poor settling characteristics. The aerated lagoon process treating high-strength wastewater also provided significant organic reduction, but did not produce an acceptable effluent concentration. ^
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La producción de aceite de oliva genera distintos subproductos entre los cuales el efluente o alpechín representa un serio problema mediambiental. En los países productores el alpechín es un residuo muy contaminante debido a su elevada composición orgánica, sus efectos inhibitorios y la tendencia de sus componentes a sufrir oxidación biológica. Estas características y la estacionalidad de su producción dificultan su eliminación. La industria del aceite de oliva está actualmente en expansión en Argentina. En Mendoza, dicha actividad tiene una gran tradición y un impacto ambiental considerable. El objetivo de este trabajo fue analizar los caracteres físico- químicos de los efluentes de fábricas de aceite oliva en Mendoza (Argentina) para conocer la realidad de la industria local y rever las especificaciones legales para efluentes. Los efluentes de dos fábricas fueron evaluados en tres puntos de muestreo: agua de entrada al proceso, salida de la fábrica y pileta de deposición final de los efluentes. Se analizó el contenido de iones, pH, conductividad eléctrica, DBO y DQO. Los resultados obtenidos permiten concluir que las características del efluente dependen del método de extracción utilizado y la eventual dilución con agua de lavado. La calidad del agua subterránea utilizada en el proceso no es un factor determinante para lograr un efluente fácilmente tratable. El problema medioambiental que se plantea es la producción de un efluente con alto contenido orgánico, salino y bajo pH, caracteres que impiden su vuelco en cursos de agua superficial o red de cloacas, por no cumplir con los requisitos indicados en la normativa vigente. Por lo tanto, las fábricas elaboradoras de aceite de oliva serán las encargadas de que dichos efluentes reciban un adecuado proceso de depuración que permita su eliminación o reutilización.
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Several studies conducted in urban areas have pointed out that road dust resuspension contributes significantly to PM concentration levels. Street washing is one of the methods proposed to reduce resuspended road dust contributions to ambient PM concentrations. As resuspended particles are mainly found in the coarse mode, published studies investigating the effects of street washing have focused on PM10 size fraction. As the PM2.5 mass fraction of particles originating from mechanical abrasion processes may still be significant we conducted a study in order to evaluate the effects of street washing on the mitigation of resuspension of fine particles. The PM2.5 mass concentration data were examined and integrated with the occurrence of street washing activities. In addition, the effect of the meteorological variability, traffic flow and street washing activities, on ambient PM2.5 levels was valuated by means of a multivariate regression model. The results revealed that traffic low is the most important factor that controls PM2.5 hourly concentrations while street washing activities did not influence fine particle mass levels.
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The self-ignition of all kind of powdery substances is a topic studied over the years, especially if the dusty substance is coal or substances related with coal because it may be a cause of energetic materials and human losses. But it is important to note that this is not the only risk in industrial plants that generate or store solid substances. Every combustible powders are potentially explosive and they may cause serious consequences if all the necessary factors are developed. Due to this potentially risk, it is essential a good characterization and knowledge of all the parameters involved in those processes.
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Although previous studies report on the effect of street washing on ambient particulate matter levels, there is a lack of studies investigating the results of street washing on the emission strength of road dust. A sampling campaign was conducted in Madrid urban area during July 2009 where road dust samples were collected in two sites, namely Reference site (where the road surface was not washed) and Pelayo site (where street washing was performed daily during night). Following the chemical characterization of the road dust particles the emission sources were resolved by means of Positive Matrix Factorization, PMF (Multilinear Engine scripting) and the mass contribution of each source was calculated for the two sites. Mineral dust, brake wear, tire wear, carbonaceous emissions and construction dust were the main sources of road dust with mineral and construction dust being the major contributors to inhalable road dust load. To evaluate the effectiveness of street washing on the emission sources, the sources mass contributions between the two sites were compared. Although brake wear and tire wear had lower concentrations at the site where street washing was performed, these mass differences were not statistically significant and the temporal variation did not show the expected build-up after dust removal. It was concluded that the washing activities resulted merely in a road dust moistening, without effective removal and that mobilization of particles took place in a few hours between washing and sampling. The results also indicated that it is worth paying attention to the dust dispersed from the construction sites as they affect the emission strength in nearby streets.
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O presente estudo investigou a aplicação de dois tipos de AnSBBR (reatores anaeróbio com biofilme e operados em batelada e batelada alimentada sequenciais: com recirculação da fase líquida e com agitação) para produção de biohidrogênio tratando água residuária sintética (a base de soro de leite e lactose, respectivamente). O AnSBBR com recirculação da fase líquida, que foi o estudo principal do presente trabalho, apresentou problemas na produção de hidrogênio utilizando soro de leite como substrato. Algumas alternativas, como adaptação da biomassa com substratos puros de degradação mais fácil, controle do pH em valores muito baixos e diferentes formas de inoculação foram testadas, entretanto, sem obtenção de sucesso. A solução do problema foi obtida ao refrigerar o meio de alimentação a 4ºC para evitar a fermentação no frasco de armazenamento, retirar a ureia e a suplementação de nutrientes, e realizar lavagens periódicas do material suporte para retirada de parte da biomassa. Dessa forma eliminaram-se indícios de produção de H2S por possível ação de bactérias redutoras de sulfato (BRS) e atingiu-se uma produção estável de hidrogênio sem, entretanto, eliminar completamento o metano, que foi produzido em baixas concentrações. Depois de atingida a estabilidade, investigou-se a influência da concentração afluente de substrato, do tempo de enchimento e da temperatura na produção de biohidrogênio no AnSBBR com recirculação da fase líquida tratando soro de leite. O estudo da concentração afluente apresentou um ponto ótimo para a concentração de 5400 mgDQO.L-1, atingindo valores de 0,80 mol H2.mol-1 lactose e de 660 mL H2.L-1.d-1. O estudo do tempo de enchimento apresentou resultados similares para as condições analisadas. Com relação à temperatura, os melhores resultados foram obtidos com a temperatura mais baixa testada de 15ºC (1,12 mol H2.mol lactose-1 e 1080 mL H2.L-1.d-1), sendo que na temperatura mais alta testada (45°C) não ocorreu produção de hidrogênio. Para o AnSBBR com agitação mecânica, que foi um estudado complementar realizado pelo fato da lactose ser o principal complemento do soro de leite, o desempenho do biorreator foi avaliado de acordo com influência conjunta do tempo de ciclo (tC – 2, 3 e 4 h), da concentração afluente (CSTA – 3600-5400 mgDQO.L-1) e da carga orgânica volumétrica aplicada (COAV – 9,3, 12,3, 13,9, 18,5 e 27,8 mgDQO.L-1.d-1). Foram obtidos excelentes resultados: consumos de carboidratos (lactose), com valores médios sempre acima de 90% e uma produção estável de biohidrogênio em todas as condições estudadas, com metano em baixas concentrações apenas na condição de maior COAV. A diminuição do tC apresentou tendência clara de melhora sobre o RMCRC,n (rendimento molar entre hidrogênio produzido e carboidrato removido) apenas para as condições com menor concentração CSTA, havendo uma relação direta entre CSTA, e RMCRC,n em todos os valores de tC, exceto para o tempo de ciclo de 3 h, exatamente onde ocorreu produção de metano. O melhor valor de RMCRC,n obtido na operação com lactose (1,65 mol H2.mol Carboidrato-1) foi superior aos obtidos em outros trabalhos utilizando a mesma configuração de reator e sacarose como substrato. As análises filogenéticas mostraram que a maioria dos clones analisados foi semelhante à Clostridium. Além destes, clones filogeneticamente semelhantes com a Família Lactobacilaceae, especificamente Lactobacillus rhamnosus foram observados em menor porcentagem no reator, assim como clones com sequências semelhantes a Acetobacter indonesiensis.
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The ubiquitous occurrence of pharmaceuticals and personal care products (PPCPs) in aquatic environments has raised concerns about potential adverse effects on aquatic ecology and human health. Certain pharmaceuticals have recently become a major focus of research to better understand the routes and persistence of these compounds once they enter into aquatic system. In this research, two model compounds were selected to represent pharmaceuticals that have been identified by recent research as being persistent; specifically, these compounds were trimethoprim (TMP, a basic antibiotic) and gemfibrozil (GEM, an acidic lipid regulator). Treatment of synthetic wastewater that contained these drugs was accomplished using wet-air oxidation (WAO). Pre- and post-treatment drug concentrations were determined by reversed-phase liquid chromatography. The influences of different operational conditions on removal efficiency of the drugs by WAO were evaluated, namely reaction time, initial drug concentration, oxygen concentration, and the amount and composition of additional organic matter used during WAO. The optimum removal efficiencies were found to be 91.9 % for TMP and 95.5 % for GEM.
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As the population of Colorado continues to grow, the impacts from individual sewage disposal systems, or onsite wastewater systems (OWS), are becoming more apparent. Increased use of OWS impacts not only water quality but land use and development as well. These impacts have led to the need for a new generation of wastewater regulations in the state, a transition from the historic prescriptive requirements to a more progressive, performance-based system. A performance-based system will allow smarter growth, improved water quality, and cost savings for both the regulatory agencies and the OWS industry in Colorado. This project outlines the challenges and essential elements required to make this transition, and provides guidance on how to meet the challenges and overcome barriers to implementing a performance code in Colorado.
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Póster presentado en 19th International Congress of Chemical and Process Engineering, Prague, Czech Republic August 28th-September 1st, 2010.
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A fast, simple and environmentally friendly ultrasound-assisted dispersive liquid-liquid microextraction (USA-DLLME) procedure has been developed to preconcentrate eight cyclic and linear siloxanes from wastewater samples prior to quantification by gas chromatography-mass spectrometry (GC-MS). A two-stage multivariate optimization approach has been developed employing a Plackett-Burman design for screening and selecting the significant factors involved in the USA-DLLME procedure, which was later optimized by means of a circumscribed central composite design. The optimum conditions were: extractant solvent volume, 13 µL; solvent type, chlorobenzene; sample volume, 13 mL; centrifugation speed, 2300 rpm; centrifugation time, 5 min; and sonication time, 2 min. Under the optimized experimental conditions the method gave levels of repeatability with coefficients of variation between 10 and 24% (n=7). Limits of detection were between 0.002 and 1.4 µg L−1. Calculated calibration curves gave high levels of linearity with correlation coefficient values between 0.991 and 0.9997. Finally, the proposed method was applied for the analysis of wastewater samples. Relative recovery values ranged between 71–116% showing that the matrix had a negligible effect upon extraction. To our knowledge, this is the first time that combines LLME and GC-MS for the analysis of methylsiloxanes in wastewater samples.
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To study the possibility of producing better water quality from municipal wastewater, a membrane bioreactor (MBR) pilot plant with flat sheet (FS) and hollow fiber (HF) membranes coupled with another pilot plant equipped with nanofiltration (NF)/reverse osmosis (RO) membranes were operated to treat municipal wastewater from the wastewater treatment plant (WWTP) Rincón de León, Alicante (Spain). This study was focused on improving the quality of the permeate obtained from the MBR process when complemented by NF or RO stages with respect to salinity, organic matter and nutrients. Furthermore, the removal efficiencies of 10 EMPs were evaluated, comparing the reductions achieved between the wastewater treatment by MBR (adsorption to sludge and biodegradation) and the later treatment using NF or RO (mainly size exclusion). The results showed that the high quality of water was obtained which is appropriate for reuse with salinity removal efficiencies higher than 97%, 96% for total organic carbon (TOC), 91% for nitrates View the MathML sourceNO3- and 99% for total phosphorous (TP). High removal efficiencies were obtained for the majority of the analyzed EMP compounds.
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Of all the costs associated with the operation and maintenance of wastewater treatment plants (WWTPs), those associated with energy use tend to be the most significant. From this point of view, it is hence logical that energy efficiency and saving strategies should be one of the current focuses of debate amongst those involved with the management of WWTPs. The present study's objective is to determine the correlation between size and energy consumption for a WWTP. To this end, 90 WWTPs currently in service were analysed and their energetic impact quantified in terms of kWh/m3 of water treated. The results obtained demonstrate that energy consumption ratio increases as the size of WWTPs decreases, either in terms of treatment volume or population equivalent served.