Evaluation of green algae deployment for organic pollutant removal in urban wastewater through ERE-CALUX potency assessment

The interest of the scientific community towards organic pollutants in freshwater streams is fairly recent. During the past 50 years, thousands of chemicals have been synthesized and released into the general environment. Nowadays their occurrence and effects on several organism, invertebrates, fish, birds, reptiles and also humans are well documented. Because of their action, some of these chemicals have been defined as Endocrine Disrupters Compounds (EDCs) and the public health implications of these EDCs have been the subject of scientific debate. Most interestingly, among those that were noticed to have some influence and effects on the endocrine system were the estrone, the 17β-estradiol, the 17α-estradiol, the estriol, the 17α-ethinylestradiol, the testosterone and the progesterone. This project focused its attention on the 17β-estradiol. Estradiol, or more precisely, 17β-estradiol (also commonly referred to as E2) is a human sex hormone. It belongs to the class of steroid hormones. In spite of the effort to remove these substances from the effluents, the actual wastewater treatment plants are not able to degrade or inactivate these organic compounds that are continually poured in the ecosystem. Through this work a new system for the wastewater treatment was tested, to assess the decrease of the estradiol in the water. It involved the action of Chlorella vulgaris, a fresh water green microalga belonging to the family of the Chlorellaceae. This microorganism was selected for its adaptability and for its photosynthetic efficiency. To detect the decrease of the target compound in the water a CALUX bioassay analysis was chosen. Three different experiments were carried on to pursue the aim of the project. By analysing their results several aspects emerged. It was assessed the presence of EDCs inside the water used to prepare the culture media. C. vulgaris, under controlled conditions, could be efficient for this purpose, although further researches are essential to deepen the knowledge of this complex phenomenon. Ultimately by assessing the toxicity of the effluent against C. vulgaris, it was clear that at determined concentrations, it could affect the normal growth rate of this microorganism.

Implementation of enhanced biological phosphorus removal (ebpr) wastewater treatment processes enriched with different microbial communities

The EBPR (Enhanced Biological Phosphorus Removal) is a type of secondary treatment in WWTPs (WasteWater Treatment Plants), quite largely used in full-scale plants worldwide. The phosphorus occurring in aquatic systems in high amounts can cause eutrophication and consequently the death of fauna and flora. A specific biomass is used in order to remove the phosphorus, the so-called PAOs (Polyphosphate Accumulating Organisms) that accumulate the phosphorus in form of polyphosphate in their cells. Some of these organisms, the so-called DPAO (Denitrifying Polyphosphate Accumulating Organisms) use as electron acceptor the nitrate or nitrite, contributing in this way also to the removal of these compounds from the wastewater, but there could be side reactions leading to the formation of nitrous oxides. The aim of this project was to simulate in laboratory scale a EBPR, acclimatizing and enriching the specialized biomass. Two bioreactors were operated as Sequencing Batch Reactors, one enriched in Accumulibacter, the other in Tetrasphaera (both PAOs): Tetrasphaera microorganisms are able to uptake aminoacids as carbon source, Accumulibacter uptake organic carbon (volatile fatty acids, VFA). In order to measure the removal of COD, phosphorus and nitrogen-derivate compounds, different analysis were performed: spectrophotometric measure of phosphorus, nitrate, nitrite and ammonia concentrations, TOC (Total Organic Carbon, measuring the carbon consumption), VFA via HPLC (High Performance Liquid Chromatography), total and volatile suspended solids following standard methods APHA, qualitative microorganism population via FISH (Fluorescence In Situ Hybridization). Batch test were also performed to monitor the NOx production. Both specialized populations accumulated as a result of SBR operations; however, Accumulibacter were found to uptake phosphates at higher extents. Both populations were able to remove efficiently nitrates and organic compounds occurring in the feeding. The experimental work was carried out at FCT of Universidade Nova de Lisboa (FCT-UNL) from February to July 2014.

Ethanol Production from Hardboard Manufacturing Process Wastewater: Methods for Improving Product Yields from Hemicellulose Hydrolysates

Waste effluents from the forest products industry are sources of lignocellulosic biomass that can be converted to ethanol by yeast after pretreatment. However, the challenge of improving ethanol yields from a mixed pentose and hexose fermentation of a potentially inhibitory hydrolysate still remains. Hardboard manufacturing process wastewater (HPW) was evaluated at a potential feedstream for lignocellulosic ethanol production by native xylose-fermenting yeast. After screening of xylose-fermenting yeasts, Scheffersomyces stipitis CBS 6054 was selected as the ideal organism for conversion of the HPW hydrolysate material. The individual and synergistic effects of inhibitory compounds present in the hydrolysate were evaluated using response surface methodology. It was concluded that organic acids have an additive negative effect on fermentations. Fermentation conditions were also optimized in terms of aeration and pH. Methods for improving productivity and achieving higher ethanol yields were investigated. Adaptation to the conditions present in the hydrolysate through repeated cell sub-culturing was used. The objectives of this present study were to adapt S. stipitis CBS6054 to a dilute-acid pretreated lignocellulosic containing waste stream; compare the physiological, metabolic, and proteomic profiles of the adapted strain to its parent; quantify changes in protein expression/regulation, metabolite abundance, and enzyme activity; and determine the biochemical and molecular mechanism of adaptation. The adapted culture showed improvement in both substrate utilization and ethanol yields compared to the unadapted parent strain. The adapted strain also represented a growth phenotype compared to its unadapted parent based on its physiological and proteomic profiles. Several potential targets that could be responsible for strain improvement were identified. These targets could have implications for metabolic engineering of strains for improved ethanol production from lignocellulosic feedstocks. Although this work focuses specifically on the conversion of HPW to ethanol, the methods developed can be used for any feedstock/product systems that employ a microbial conversion step. The benefit of this research is that the organisms will the optimized for a company's specific system.

Regulations on E-Commerce Consumer Protection Rules in China and Europe Compared – Same Same but Different?

This article provides a comprehensive overview of the regulations on e-commerce protection rules in China and the European Union. It starts by giving a general overview of different approaches towards consumer protection in e-commerce. This article then scrutinizes the current legal system in China by mainly focusing on SAIC’s “Interim Measures for the Administration of Online Commodity Trading and Relevant Service Activities”. The subsequent chapter covers the supervision of consumer protection in e-commerce in China, which covers both the regulatory objects of online commodity trading and the applied regulatory mechanisms. While the regulatory objects include operating agents, operating objects, operating behavior, electronic contracts, intellectual property and consumer protection, the regulatory mechanisms for e-commerce in China combines market mechanism and industry self-discipline under the government’s administrative regulation. Further, this article examines the current European legal system in online commodity trading. It outlines the aim and the scope of EU legislation in the respective field. Subsequently, the paper describes the European approach towards the supervision of consumer protection in e-commerce. As there is no central EU agency for consumer protection in e-commerce transactions, the EU stipulates a framework for Member States’ institutions, thereby creating a European supervisory network of Member States’ institutions and empowers private consumer organisations to supervise the market on their behalf. Moreover, the EU encourages the industry to self- or co-regulate e-commerce by providing incentives. Consequently, this article concludes that consumer protection may be achieved by different means and different systems. However, even though at first glance the Chinese and the European system appear to differ substantially, a closer look reveals tendencies of convergence between the two systems.

The Role of Forest Soils in a Northern New England Effluent Management System

The Carrabassett Valley Sanitary District in Carrabassett Valley, Maine has utilized both a forest spray irrigation system and a Snowfluent™ system for the treatment of their wastewater effluent. This study was designed to evaluate potential changes in soil properties after approximately 20 years of treatment in the forested spray irrigation site and three years of treatment in the field Snowfluent™ site. In addition, grass yield and composition were evaluated on the field study sites. After treatment with effluent or Snowfluent™, soils showed an increase in soil exchangeable Ca, Mg, Na, and K, base saturation, and pH. While most constituents were higher in treated soils, available P was lower in treated soils compared to the controls. This difference was attributed to higher rates of P mineralization from soil organic matter due to an irrigation effect of the treatment, depleting available P pools despite the P addition with the treatment. Most of the differences due to treatment were greatest at the surface and diminished with depth. Depth patterns in soil properties mostly reflected the decreasing influence of organic matter and its decomposition products with depth as evidenced by significantly higher total C in the surface compared to lower horizons. There were decreasing concentrations of total N, and exchangeable or extractable Ca, Mg, Na, K, Mn, Zn, and P with depth. In addition, there was decreasing BS with depth, driven primarily by declining exchangeable Ca and Mg. Imgation with Snowfluent™ altered the chemical composition of the grass on the site. All element concentrations were significantly higher in the grass foliage except for Ca. The differences were attributed to the additional nutrients and moisture derived from the Snowfluent™. The use of forest spray imgation and Snowfluent™ as a wastewater treatment strategy appears to work well. The soil and vegetation were able to retain most of the applied nutrients, and do not appear to be moving toward saturation. Vegetation management may be a key tool for managing nutrient accumulation on the grass sites as the system ages.

Performance enhancement of large industrial wastewater stabilization ponds

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. ^

Bench-scale evaluation of the activated sludge process for treatment of a high -strength chemical plant wastewater

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. ^

Remediation of feedlot effluents using aquatic plants

Feedlots have increased in several regions of Argentina, particularly in the Pampas. The absence of adequate treatments of the effluents produced in these establishments creates serious problems to the society. Phytoremediation can be defined as inexpensive and environmentally sustainable strategy used to remove pollutants by plants. The aim of this study was to evaluate the remediation potential of two macrophyte species (Eichhornia crassipes and Hydrocotyle ranunculoides) on a feedlot effluent. This effluent was treated with these species for 31 days. Control and macrophyte treatments decreased dissolved inorganic nitrogen (DIN), Kjeldahl nitrogen (Kj N), biological oxygen demand (BOD), chemical oxygen demand (COD), total dissolved salts (TDS), total phosphorus (TP), Pb, Zn and Cr levels. At macrophyte treatments, relatively constant pH levels were kept and decreased EC and TDS values were obtained compared to control, mitigating the release of contaminants and potential greenhouse gases to the atmosphere. Moreover, significant increases in biomass were obtained, being higher in E. crassipes. The results allow concluding that the presence of aquatic plants increases the removal rates of nutrients, organic matter and heavy metals from wastewater in approximately 10-17 days for a feedlot effluent with high organic load.

Estudio de la digestión anaerobia en dos fases para el tratamiento de las aguas residuales de despulpe del beneficiado húmedo del café

Debido al aumento de los estándares de calidad exigidos internacionalmente, así como por una mayor presión sobre la industria mediante legislaciones ambientales más rigurosas, el sector cafetalero está obligado a buscar, a través de la investigación, un sistema adecuado de tratamiento para las aguas residuales generadas en el beneficiado húmedo del café. En este trabajo se evaluó el funcionamiento de la digestión anaerobia para el tratamiento de las aguas residuales de despulpe. Para ello, se utilizaron dos sistemas anaerobios, uno en una etapa (UASB), y otro con separación de fases (2PUASB). Se investigó el efecto en la digestión anaerobia de tres cargas orgánicas volumétricas (OLR) y de las dos configuraciones de reactor usadas. Los valores de OLR de operación en el sistema UASB variaron en un intervalo de 3.6-4.1 kgCOD m-3 d-1, con una tasa de recirculación del efluente de 1.0. El sistema 2PUASB fue alimentado con OLR similares a las que se emplearon en el sistema en una etapa. El reactor de acidificación fue cargado a 11.0 kgCOD m-3 d-1, mientras que en el reactor metanogénico varió en el intervalo de 2.6-4.67 kgCOD m-3 d-1. El uso de reactores UASB en una etapa y en dos fases, bajo las mismas condiciones de operación ya descritas, propiciaron el logro de una eficiencia de degradación de COD total superior al 75% y al 85% para la COD soluble, respectivamente. Sin embargo, el sistema en dos fases mostró mejores resultados en el tratamiento de este tipo de agua residual, no solo en cuanto a eficiencia de eliminación de la carga orgánica contaminante así como una menor concentración de ácidos grasos volátiles (VFA) en el efluente. Obtenidas las mejores condiciones de trabajo, fue evaluada la separación de fases bajo el efecto de la recirculación. Los grupos de fermentaciones producidos fueron similares a los obtenidos en el experimento sin recirculación, indicando que está última no afectó la composición relativa de los VFA del reactor anaerobio, por lo que no cambió el patrón de degradación del residuo. Una tasa de recirculación de 1.0 del efluente del reactor metanogénico al reactor acidogénico mejoró significativamente el proceso, ya que se incrementó la conversión de los VFA (31%), la eliminación de la fracción total y soluble del residuo tratado (6.5%) y la reducción del consumo de alcalinizante (39%); manteniendo similares producciones de metano. El uso de la digestión anaerobia en dos fases demostró una mejora en la estabilidad del proceso y un incremento de la eficiencia de operación y de la producción de metano, respectivamente.Tesis Doctoral Yans Guardia Puebla Abstract ix ABSTRACT Due to the increase of quality standards internationally demanded, as well as for a greater pressure on the industry by means of more rigorous environmental legislations, the coffee sector is forced to search, through the research, an appropriated treatment system for coffee wet wastewaters generated. In this work the performance of the anaerobic digestion for the coffee wet wastewater treatment was evaluated. For it, two anaerobic systems, one in single-stage (UASB), and another with two-phase (2PUASB) were used. The effect in the anaerobic digestion of three organic loading rates (OLR) and of two reactor configurations used was investigated. OLR operation values in UASB system varied in an interval of 3.6-4.1 kgCOD m-3 d-1, with a recycle rate of the effluent of 1.0. 2PUASB system was fed with OLR similar to those that were used in the reactor in a stage. The acidification reactor was loaded to 11.0 kgCOD m-3 d-1, whereas in the methanogenic reactor varied in the interval of 2.6-4.67 kgCOD m-3 d-1. The use of single-stage and two-phase UASB reactors, under the same operation conditions already before described, a total COD removal efficiency of 75% and 85% for the soluble COD removal efficiency, respectively, was achieved. However, two-phase system showed better results in the treatment of this wastewater type, not only as for removal efficiency of loading organic polluting as well as a smaller volatile fatty acid (VFA) concentration in the effluent. Obtained the best work conditions, the two-phase system under the effect of the recycle was evaluated. Fermentations groups produced were similar to those obtained in the experiment without recycle, indicating that it last one do not affect the relative composition of VFA of the anaerobic reactor, for that reason the degradation pattern of the residue does not change. A recycle rate of 1.0 of the effluent of the methanogenic reactor to the acidogenic reactor improved the process significantly, since it was increased the VFA conversion (31%), the removal of total and soluble fraction of the residue treated (6.5%) and the decrease of the alkalinity consumption (39%); maintaining similar methane productions. The use of the two-phase anaerobic digestion demonstrated to an improvement in the stability of the process and an increase of the operation efficiency and methane production, respectively.

Recuperación de energía de la salmuera

Como consecuencia del proceso de desalación, se produce el vertido al mar de un agua de rechazo hipersalino o salmuera. La salinidad de este vertido es variable, dependiendo del origen de la captación y del proceso de tratamiento. Muchos de los hábitats y biocenosis de los ecosistemas marinos se encuentran adaptados a ambientes de salinidad casi constante y son muy susceptibles a los incrementos de salinidad originados por estos vertidos. Junto con el vertido de salmuera otro de los principales inconvenientes que plantean las plantas desaladoras es el alto consumo energético, con todas las desventajas que esto supone: alto coste del agua desalada para los consumidores, contaminación del medio... El desarrollo de los métodos de vertido, herramientas de gestión de la salmuera, estudios del comportamiento de la pluma salina… ha buscado la mitigación de estos efectos sobre los ecosistemas marinos. El desarrollo en membranas de ósmosis inversa, diseño de bombas y sistemas de recuperación de energía ha permitido también la reducción del consumo energético en las plantas de desalación. Sin embargo, estos campos parecen haber encontrado un techo tecnológico difícil de rebasar en los últimos tiempos. La energía osmótica se plantea como uno de los caminos a investigar aplicado al campo de la reducción del consumo energético en desalación de agua de mar, a través del aprovechamiento energético de la salmuera. Con esta tesis se pretende cumplir principalmente con los siguientes objetivos: reducción del consumo energético en desalación, mitigar el impacto del vertido sobre el medio y ser una nueva herramienta en la gestión de la salmuera. En el presente documento se plantea el desarrollo de un nuevo proceso que utiliza el fenómeno de la ósmosis directa a través de membranas semipermeables, y busca la sinergia desalación depuración, integrando ambos, en un único proceso de tratamiento dentro del ciclo integral del agua. Para verificar los valores de producción, calidad y rendimiento del proceso, se proyecta y construye una planta piloto ubicada en la Planta Desaladora de Alicante II, escalada de tal manera que permite la realización de los ensayos con equipos comerciales de tamaño mínimo. El objetivo es que el resultado final sea extrapolable a tamaños superiores sin que el escalado afecte a la certeza y fiabilidad de las conclusiones obtenidas. La planta se proyecta de forma que el vertido de una desaladora de ósmosis inversa junto con el vertido de un terciario convencional, se pasan por una ósmosis directa y a continuación por una ósmosis inversa otra vez, ésta última con el objeto de abrir la posibilidad de incrementar la producción de agua potable. Ambas ósmosis están provistas de un sistema de pretratamiento físico-químico (para adecuar la calidad del agua de entrada a las condiciones requeridas por las membranas en ambos casos), y un sistema de limpieza química. En todos los ensayos se usa como fuente de disolución concentrada (agua salada), el rechazo de un bastidor de ósmosis inversa de una desaladora convencional de agua de mar. La fuente de agua dulce marca la distinción entre dos tipos de ensayos: ensayos con el efluente del tratamiento terciario de una depuradora convencional, con lo que se estudia el comportamiento de la membrana ante el ensuciamiento; y ensayos con agua permeada, que permiten estudiar el comportamiento ideal de la membrana. Los resultados de los ensayos con agua salobre ponen de manifiesto problemas de ensuciamiento de la membrana, el caudal de paso a través de la misma disminuye con el tiempo y este efecto se ve incrementado con el aumento de la temperatura del agua. Este fenómeno deriva en una modificación del pretratamiento de la ósmosis directa añadiendo un sistema de ultrafiltración que ha permitido que la membrana presente un comportamiento estable en el tiempo. Los ensayos con agua permeada han hecho posible estudiar el comportamiento “ideal” de la membrana y se han obtenido las condiciones óptimas de operación y a las que se debe tender, consiguiendo tasas de recuperación de energía de 1,6; lo que supone pasar de un consumo de 2,44 kWh/m3 de un tren convencional de ósmosis a 2,28 kWh/m3 al añadir un sistema de ósmosis directa. El objetivo de futuras investigaciones es llegar a tasas de recuperación de 1,9, lo que supondría alcanzar consumos inferiores a 2 kWh/m3. Con esta tesis se concluye que el proceso propuesto permite dar un paso más en la reducción del consumo energético en desalación, además de mitigar los efectos del vertido de salmuera en el medio marino puesto que se reduce tanto el caudal como la salinidad del vertido, siendo además aplicable a plantas ya existentes y planteando importantes ventajas económicas a plantas nuevas, concebidas con este diseño. As a consequence of the desalination process, a discharge of a hypersaline water or brine in the sea is produced. The salinity of these discharges varies, depending on the type of intake and the treatment process. Many of the habitats and biocenosis of marine ecosystems are adapted to an almost constant salinity environment and they are very susceptible to salinity increases caused by these discharges. Besides the brine discharge, another problem posed by desalination plants, is the high energy consumption, with all the disadvantages that this involves: high cost of desalinated water for consumers, environmental pollution ... The development of methods of disposal, brine management tools, studies of saline plume ... has sought the mitigation of these effects on marine ecosystems. The development of reverse osmosis membranes, pump design and energy recovery systems have also enabled the reduction of energy consumption in desalination plants. However, these fields seem to have reached a technological ceiling which is difficult to exceed in recent times. Osmotic power is proposed as a new way to achieve the reduction of energy consumption in seawater desalination, through the energy recovery from the brine. This thesis mainly tries to achieve the following objectives: reduction of energy consumption in desalination, mitigation of the brine discharge impact on the environment and become a new tool in the management of the brine. This paper proposes the development of a new process, that uses the phenomenon of forward osmosis through semipermeable membranes and seeks the synergy desalination-wastewater reuse, combining both into a single treatment process within the integral water cycle. To verify the production, quality and performance of the process we have created a pilot plant. This pilot plant, located in Alicante II desalination plant, has been designed and built in a scale that allows to carry out the tests with minimum size commercial equipment. The aim is that the results can be extrapolated to larger sizes, preventing that the scale affects the accuracy and reliability of the results. In the projected plant, the discharge of a reverse osmosis desalination plant and the effluent of a convencional tertiary treatment of a wastewater plant, go through a forward osmosis module, and then through a reverse osmosis, in order to open the possibility of increasing potable water production. Both osmosis systems are provided with a physicochemical pretreatment (in order to obtain the required conditions for the membranes in both cases), and a chemical cleaning system. In all tests, it is used as a source of concentrated solution (salt water), the rejection of a rack of a conventional reverse osmosis seawater desalination. The source of fresh water makes the difference between two types of tests: test with the effluent from a tertiary treatment of a conventional wastewater treatment plant (these tests study the behavior of the membrane facing the fouling) and tests with permeate, which allow us to study the ideal behavior of the membrane. The results of the tests with brackish water show fouling problems, the flow rate through the membrane decreases with the time and this effect is increased with water temperature. This phenomenon causes the need for a modification of the pretreatment of the direct osmosis module. An ultrafiltration system is added to enable the membrane to present a stable behavior . The tests with permeate have made possible the study of the ideal behavior of the membrane and we have obtained the optimum operating conditions. We have achieved energy recovery rates of 1.6, which allows to move from a consumption of 2.44 kWh/m3 in a conventional train of reverse osmosis to 2.28 kWh / m3 if it is added the direct osmosis system. The goal of future researches is to achieve recovery rates of 1.9, which would allow to reach a consumption lower than 2 kWh/m3. This thesis concludes that the proposed process allows us to take a further step in the reduction of the energy consumption in desalination. We must also add the mitigation of the brine discharge effects on the marine environment, due to the reduction of the flow and salinity of the discharge. This is also applicable to existing plants, and it suggests important economic benefits to new plants that will be built with this design.

Normalizar la utopía: Un proyecto de sistematización de la normativa en vivienda social = Normalizing Utopia: A Project of Systematization of Regulations on Social Housing

La presente tesis doctoral aborda el estudio del proyecto de vivienda colectiva social desde la noción de norma, entendida desde la sistematización o normalización de los instrumentos del proyecto arquitectónico de vivienda protegida. Esto es, desde una idea de tipificación taxonómica en cuanto ajuste a un conjunto de reglas comunes productoras de sistemas normativos. La hipótesis de partida se basa en la consideración de la vivienda pública como un laboratorio de estudio histórico de los ideales de confort y calidad de vida. Este campo de pruebas ha constituido una sólida base que ha servido como punto de encuentro muy particular entre proyecto y normativa desde las primeras vanguardias europeas hasta la actualidad. El principal objetivo de la investigación es la revalorización de una normativa de vivienda que ha producido ejemplos de innegable calidad en el contexto nacional e internacional, así como un intento de actualización de su codificación. La investigación se sirve de los instrumentos específicos de la disciplina arquitectónica para explicar una disociación detectada desde la segunda mitad del siglo pasado entre la utopía del proyecto social de vivienda y el pragmatismo de la norma que lo regula, más allá de los aspectos sociales y culturales asociados a las nuevas composiciones familiares, las tecnologías cambiantes, los ritos domésticos contemporáneos o el valor creciente del tiempo libre. La propuesta de una nueva terminología que aborde nuevas relaciones en el acercamiento al proyecto de vivienda desde la normativa española deriva en un conjunto de estrategias de proyecto desde las que proponer sistemas normativos. Dichas estrategias se basan principalmente en mecanismos de cualificación espacial que permitan un nuevo acercamiento entre dichas normas y las formas de habitar actuales. ABSTRACT This doctoral thesis deals with the study of the project of social collective housing from the notion of rule, understanding it from the systematization or standardization of the instruments of architectural project for social housing. Thus, it deals with an idea of taxonomic typification as an adjustment to a set of common rules which produce regulation systems. The initial hypothesis is based on the consideration of public housing as a laboratory for studying the historical ideals of comfort and quality of life. This testing ground has been a solid base that has served as a very specific meeting point between project and regulations from the first European avant‐garde to nowadays. The main objective of this research is the revaluation of housing regulations, which have produced examples of undeniable quality in the national and international stage, as well as an attempt to update their codification. The research assumes the specific tools of the discipline of architecture for explaining a dissociation detected between the utopia of the project for social housing and the pragmatism of the regulations from the second half of last century, beyond social and cultural aspects associated to the new family arrangements, the changing technologies, the contemporary domestic rituals or the rising value of leisure time. The proposal of a new terminology that tackles new relations in the approach to housing project from the Spanish legislation results in a set of strategies to propose regulation systems. Those strategies are mainly based on mechanisms for spatial qualification which allow a new approach between these rules and the current ways of living.

State of the Art and Future Trends in Grid Codes Applicable to Isolated Electrical Systems

Isolated electrical systems lack electrical interconnection to other networks and are usually placed in geographically isolated areas—mainly islands or locations in developing countries. Until recently, only diesel generators were able to assure a safe and reliable supply in exchange for very high costs for fuel transportation and system operation. Transmission system operators (TSOs) are increasingly seeking to replace traditional energy models based on large groups of conventional generation units with mixed solutions where diesel groups are held as backup generation and important advantages are provided by renewable energy sources. The grid codes determine the technical requirements to be fulfilled by the generators connected in any electrical network, but regulations applied to isolated grids are more demanding. In technical literature it is rather easy to find and compare grid codes for interconnected electrical systems. However, the existing literature is incomplete and sparse regarding isolated grids. This paper aims to review the current state of isolated systems and grid codes applicable to them, specifying points of comparison and defining the guidelines to be followed by the upcoming regulations.

State of the Art and Future Trends in Grid Codes Applicable to Isolated Electrical Systems

Electrical power systems are changing their traditional structure, which was based on a little number of large generating power plants placed at great distances from loads by new models that tend to split the big production nodes in many smaller ones. The set of small groups which are located close to consumers and provide safe and quality energy is called distributed generation (DG). The proximity of the sources to the loads reduces losses associated with transportation and increases overall system efficiency. DG also favors the inclusion of renewable energy sources in isolated electrical systems or remote microgrids, because they can be installed where the natural resource is located. In both cases, as weak grids unable to get help from other nearby networks, it is essential to ensure appropriate behavior of DG sources to guarantee power system safety and stability. The grid codes sets out the technical requirements to be fulfilled for the sources connected in these electrical networks. In technical literature it is rather easy to find and compare grid codes for interconnected electrical systems. However, the existing literature is incomplete and sparse regarding isolated electrical systems and this happens due to the difficulties inherent in the pursuit of codes. Some countries have developed their own legislation only for their island territory (as Spain or France), others apply the same set of rules as in mainland, another group of island countries have elaborated a complete grid code for all generating sources and some others lack specific regulation. This paper aims to make a complete review of the state of the art in grid codes applicable to isolated systems, setting the comparison between them and defining the guidelines predictably followed by the upcoming regulations in these particular systems.

La reutilización de efluentes depurados en España: retrospectiva, desarrollo del marco normativo, estudio de las tecnologías de regeneración frente a los biorreactores de membrana y sus costes en función del uso

La reutilización de efluentes depurados siempre ha sido una opción en lugares con déficit coyuntural o estructural de recursos hídricos, se haya o no procedido a la regulación y planificación de esta práctica. La necesidad se crea a partir de las demandas de una zona, normalmente riego agrícola, que ven un mejor desarrollo de su actividad por contar con este recurso. España es el país de la UE que más caudal reutiliza, y está dentro de los diez primeros a nivel mundial. La regulación de esta práctica por el RD 1620/2007, ayudó a incorporar la reutilización de efluentes depurados a la planificación hidrológica como parte de los programas de medidas, con objeto de mitigar presiones, como son las extracciones de agua superficial y subterránea, o mejoras medioambientales evitando un vertido. El objeto de este trabajo es conocer la situación de la reutilización de efluentes depurados en España, los diferentes escenarios y planteamientos de esta actividad, el desarrollo del marco normativo y su aplicabilidad, junto a los tratamientos que permiten alcanzar los límites de calidad establecidos en la normativa vigente, en función de los distintos usos. Además, se aporta un análisis de costes de las distintas unidades de tratamiento y tipologías de líneas de regeneración, tanto de las utilizadas después de un tratamiento secundario como de otras opciones de depuración, como son los biorreactores de membrana (MBRs). Para el desarrollo de estos objetivos, en primer lugar, se aborda el conocimiento de la situación de la reutilización en España a través de una base de datos diseñada para cubrir todos los aspectos de esta actividad: datos de la estación depuradora de aguas residuales (EDAR), de la estación regeneradora (ERA), caudales depurados, reutilizados, volúmenes utilizados y ubicación de los distintos usos, tipos de líneas de tratamiento, calidades del agua reutilizada, etc. Las principales fuentes de información son las Confederaciones Hidrográficas (CCHH) a través de las concesiones de uso del agua depurada, las entidades de saneamiento y depuración de las distintas comunidades autónomas (CCAA), ayuntamientos, Planes Hidrológicos de Cuenca (PHC) y visitas a las zonas más emblemáticas. Además, se revisan planes y programas con el fin de realizar una retrospectiva de cómo se ha ido consolidando y desarrollando esta práctica en las distintas zonas de la geografía española. Se han inventariado 322 sistemas de reutilización y 216 tratamientos de regeneración siendo el más extendido la filtración mediante filtro arena seguido de una desinfección mediante hipoclorito, aunque este tratamiento se ha ido sustituyendo por un físico-químico con decantación lamelar, filtro de arena y radiación ultravioleta, tratamiento de regeneración convencional (TRC), y otros tratamientos que pueden incluir membranas, tratamientos de regeneración avanzados (TRA), con dosificación de hipoclorito como desinfección residual, para adaptarse al actual marco normativo. El uso más extendido es el agrícola con el 70% del caudal total reutilizado, estimado en 408 hm3, aunque la capacidad de los tratamientos de regeneración esperada para 2015, tras el Plan Nacional de Reutilización de Aguas (PNRA), es tres veces superior. Respecto al desarrollo normativo, en las zonas donde la reutilización ha sido pionera, las administraciones competentes han ido desarrollando diferentes recomendaciones de calidad y manejo de este tipo de agua. El uso agrícola, y en zonas turísticas, el riego de campos de golf, fueron los dos primeros usos que tuvieron algún tipo de recomendación incluso reglamentación. Esta situación inicial, sin una normativa a nivel estatal ni recomendaciones europeas, creó cierta incertidumbre en el avance de la reutilización tanto a nivel de concesiones como de planificación. En la actualidad sigue sin existir una normativa internacional para la reutilización y regeneración de efluentes depurados. Las recomendaciones de referencia a nivel mundial, y en concreto para el uso agrícola, son las de la OMS (Organización Mundial de la Salud) publicadas 1989, con sus posteriores revisiones y ampliaciones (OMS, 2006). Esta norma combina tratamientos básicos de depuración y unas buenas prácticas basadas en diferentes niveles de protección para evitar problemas sanitarios. Otra normativa que ha sido referencia en el desarrollo del marco normativo en países donde se realiza esta práctica, son las recomendaciones dadas por la Agencia Medioambiente Estadunidense (USEPA, 2012) o las publicadas por el Estado de California (Título 22, 2001). Estas normas establecen unos indicadores y valores máximos dónde el tratamiento de regeneración es el responsable de la calidad final en función del uso. Durante 2015, la ISO trabajaba en un documento para el uso urbano donde se muestra tanto los posibles parámetros que habría que controlar como la manera de actuar para evitar posibles riesgos. Por otro lado, la Comisión Europea (CE) viene impulsando desde el 2014 la reutilización de aguas depuradas dentro del marco de la Estrategia Común de Implantación de la Directiva Marco del Agua, y fundamentalmente a través del grupo de trabajo de “Programas de medidas”. Para el desarrollo de esta iniciativa se está planteando sacar para 2016 una guía de recomendaciones que podría venir a completar el marco normativo de los distintos Estados Miembros (EM). El Real Decreto 1620/2007, donde se establece el marco jurídico de la reutilización de efluentes depurados, tiende más a la filosofía implantada por la USEPA, aunque la UE parece más partidaria de una gestión del riesgo, donde se establecen unos niveles de tolerancia y unos puntos de control en función de las condiciones socioeconómicas de los distintos Estados, sin entrar a concretar indicadores, valores máximos o tratamientos. Sin embargo, en la normativa estadounidense se indican una serie de tratamientos de regeneración, mientras que, en la española, se hacen recomendaciones a este respecto en una Guía sin validez legal. Por tanto, queda sin regular los procesos para alcanzar estos estándares de calidad, pudiendo ser éstos no apropiados para esta práctica. Es el caso de la desinfección donde el uso de hipoclorito puede generar subproductos indeseables. En la Guía de recomendaciones para la aplicación del RD, publicada por el Ministerio de Agricultura y Medioambiente (MAGRAMA) en 2010, se aclaran cuestiones frecuentes sobre la aplicación del RD, prescripciones técnicas básicas para los sistemas de reutilización, y buenas prácticas en función del uso. Aun así, el RD sigue teniendo deficiencias en su aplicación siendo necesaria una revisión de la misma, como en las frecuencias de muestreo incluso la omisión de algunos parámetros como huevos de nematodos que se ha demostrado ser inexistentes tras un tratamiento de regeneración convencional. En este sentido, existe una tendencia a nivel mundial a reutilizar las aguas con fines de abastecimiento, incluir indicadores de presencia de virus o protozoos, o incluir ciertas tecnologías como las membranas u oxidaciones avanzadas para afrontar temas como los contaminantes emergentes. Otro de los objetivos de este trabajo es el estudio de tipologías de tratamiento en función de los usos establecidos en el RD 1620/2007 y sus costes asociados, siendo base de lo establecido a este respecto en la Guía y PNRA anteriormente indicados. Las tipologías de tratamiento propuestas se dividen en líneas con capacidad de desalar y las que no cuentan con una unidad de desalación de aguas salobres de ósmosis inversa o electrodiálisis reversible. Se realiza esta división al tener actuaciones en zonas costeras donde el agua de mar entra en los colectores, adquiriendo el agua residual un contenido en sales que es limitante en algunos usos. Para desarrollar este objetivo se han estudiado las unidades de tratamiento más implantadas en ERAs españolas en cuanto a fiabilidad para conseguir determinada calidad y coste, tanto de implantación como de explotación. El TRC, tiene un coste de implantación de 28 a 48 €.m-3.d y de explotación de 0,06 a 0,09 €. m-3, mientras que, si se precisara desalar, este coste se multiplica por diez en la implantación y por cinco en la explotación. En caso de los usos que requieren de TRA, como los domiciliarios o algunos industriales, los costes serían de 185 a 398 €.m-3.d en implantación y de 0,14 a 0,20 €.m-3 en explotación. En la selección de tecnologías de regeneración, la capacidad del tratamiento en relación al coste es un indicador fundamental. Este trabajo aporta curvas de tendencia coste-capacidad que sirven de herramienta de selección frente a otros tratamientos de regeneración de reciente implantación como son los MBR, u otros como la desalación de agua de mar o los trasvases entre cuencas dentro de la planificación hidrológica. En España, el aumento de las necesidades de agua de alta calidad en zonas con recursos escasos, aumento de zonas sensibles como puntos de captación para potables, zonas de baño o zonas de producción piscícola, y en ocasiones, el escaso terreno disponible para la implantación de nuevas plantas depuradoras (EDARs), han convertido a los MBRs, en una opción dentro del marco de la reutilización de aguas depuradas. En este trabajo, se estudia esta tecnología frente a los TRC y TRA, aportando igualmente curvas de tendencia coste-capacidad, e identificando cuando esta opción tecnológica puede ser más competitiva frente a los otros tratamientos de regeneración. Un MBR es un tratamiento de depuración de fangos activos donde el decantador secundario es sustituido por un sistema de membranas de UF o MF. La calidad del efluente, por tanto, es la misma que el de una EDAR seguida de un TRA. Los MBRs aseguran una calidad del efluente para todos los usos establecidos en el RD, incluso dan un efluente que permite ser directamente tratado por las unidades de desalación de OI o EDR. La implantación de esta tecnología en España ha tenido un crecimiento exponencial, pasando de 13 instalaciones de menos de 5.000 m3. d-1 en el 2006, a más de 55 instalaciones en operación o construcción a finales del 2014, seis de ellas con capacidades por encima de los 15.000 m3. d-1. Los sistemas de filtración en los MBR son los que marcan la operación y diseño de este tipo de instalaciones. El sistema más implantado en España es de membrana de fibra hueca (MFH), sobre todo para instalaciones de gran capacidad, destacando Zenon que cuenta con el 57% de la capacidad total instalada. La segunda casa comercial con mayor número de plantas es Kubota, con membranas de configuración placa plana (MPP), que cuenta con el 30 % de la capacidad total instalada. Existen otras casas comerciales implantadas en MBR españoles como son Toray, Huber, Koch o Microdym. En este documento se realiza la descripción de los sistemas de filtración de todas estas casas comerciales, aportando información de sus características, parámetros de diseño y operación más relevantes. El estudio de 14 MBRs ha posibilitado realizar otro de los objetivos de este trabajo, la estimación de los costes de explotación e implantación de este tipo de sistemas frente a otras alternativas de tratamiento de regeneración. En este estudio han participado activamente ACA y ESAMUR, entidades públicas de saneamiento y depuración de Cataluña y Murcia respectivamente, que cuentan con una amplia experiencia en la explotación de este tipo de sistemas. Este documento expone los problemas de operación encontrados y sus posibles soluciones, tanto en la explotación como en los futuros diseños de este tipo de plantas. El trabajo concluye que los MBRs son una opción más para la reutilización de efluentes depurados, siendo ventajosos en costes, tanto de implantación como de explotación, respecto a EDARs seguidas de TRA en capacidades por encima de los 10.000 m3.d-1. ABSTRACT The reuse of treated effluent has always been an option in places where a situational or structural water deficit exists, whether regulatory and/or planning efforts are completed or not. The need arises from the demand of a sector, commonly agricultural irrigation, which benefits of this new resource. Within the EU, Spain is ahead in the annual volume of reclaimed water, and is among the top ten countries at a global scale. The regulation of this practice through the Royal Decree 1620/2007 has helped to incorporate the water reuse to the hydrological plans as a part of the programme of measures to mitigate pressures such as surface or ground water extraction, or environmental improvements preventing discharges. The object of this study is to gain an overview of the state of the water reuse in Spain, the different scenarios and approaches to this activity, the development of the legal framework and its enforceability, together with the treatments that achieve the quality levels according to the current law, broken down by applications. Additionally, a cost analysis of technologies and regeneration treatment lines for water reclamation is performed, whereas the regeneration treatment is located after a wastewater treatment or other options such as membrane bioreactors (MBR). To develop the abovementioned objectives, the state of water reuse in Spain is studied by means of a database designed to encompass all aspects of the activity: data from the wastewater treatment plants (WWTP), from the water reclamation plants (WRP), the use of reclaimed water, treated water and reclaimed water annual volumes and qualities, facilities and applications, geographic references, technologies, regeneration treatment lines, etc. The main data providers are the River Basin authorities, through the concession or authorization for water reuse, (sanitary and wastewater treatment managers from the territorial governments, local governments, Hydrological Plans of the River Basins and field visits to the main water reuse systems. Additionally, a review of different plans and programmes on wastewater treatment or water reuse is done, aiming to put the development and consolidation process of this activity in the different regions of Spain in perspective. An inventory of 322 reuse systems and 216 regeneration treatments has been gathered on the database, where the most extended regeneration treatment line was sand filtration followed by hypochlorite disinfection, even though recently it is being replaced by physical–chemical treatment with a lamella settling system, depth sand filtration, and a disinfection with ultraviolet radiation and hypochlorite as residual disinfectant, named conventional regeneration treatment (CRT), and another treatment that may include a membrane process, named advanced regeneration treatment (ART), to adapt to legal requirements. Agricultural use is the most extended, accumulating 70% of the reclaimed demand, estimated at 408 hm3, even though the expected total capacity of WRPs for 2015, after the implementation of the National Water Reuse Plan (NWRP) is three times higher. According to the development of the water reuse legal framework, there were pioneer areas where competent authorities developed different quality and use recommendations for this new resource. Agricultural use and golf course irrigation in touristic areas were the first two uses with recommendations and even legislation. The initial lack of common legislation for water reuse at a national or European level created some doubts which affected the implementation of water reuse, both from a planning and a licensing point of view. Currently there is still a lack of common international legislation regarding water reuse, technologies and applications. Regarding agricultural use, the model recommendations at a global scale are those set by the World Health Organization published in 1989, and subsequent reviews and extensions about risk prevention (WHO, 2006). These documents combine wastewater treatments with basic regeneration treatments reinforced by good practices based on different levels of protection to avoid deleterious health effects. Another relevant legal reference for this practices has been the Environmental Protection Agency of the US (USEPA, 2012), or those published by the State of California (Title 22, 2001). These establish indicator targets and maximum thresholds where regeneration treatment lines are responsible for the final quality according to the different uses. During 2015, the ISO has worked on a document aimed at urban use, where the possible parameters to be monitored together with risk prevention have been studied. On the other hand, the European Commission has been promoting the reuse of treated effluents within the Common Implementation Strategy of the Water Framework Directive, mainly through the work of the Programme of Measures Working Group. Within this context, the publication of a recommendation guide during 2016 is intended, as a useful tool to fill in the legal gaps of different Member States on the matter. The Royal Decree 1620/2007, where the water reuse regulation is set, resembles the principles of the USEPA more closely, even though the EU shows a tendency to prioritize risk assessment by establishing tolerance levels and thresholds according to socioeconomic conditions of the different countries, without going into details of indicators, maximum thresholds or treatments. In contrast, in the US law, regeneration treatments are indicated, while in the Spanish legislation, the only recommendations to this respect are compiled in a non-compulsory guide. Therefore, there is no regulation on the different treatment lines used to achieve the required quality standards, giving room for inappropriate practices in this respect. This is the case of disinfection, where the use of hypochlorite may produce harmful byproducts. In the recommendation Guide for the application of the Royal Decree (RD), published by the Ministry of Agriculture and Environment (MAGRAMA) in 2010, clarifications of typical issues that may arise from the application of the RD are given, as well as basic technical parameters to consider in reuse setups, or good practices according to final use. Even so, the RD still presents difficulties in its application and requires a review on issues such as the sampling frequency of current quality parameters or even the omission of nematode eggs indicator, which have been shown to be absent after CRT. In this regard, there is a global tendency to employ water reuse for drinking water, including indicators for the presence of viruses and protozoans, or to include certain technologies such as membranes or advanced oxidation processes to tackle problems like emerging pollutants. Another of the objectives of this study is to provide different regeneration treatment lines to meet the quality requirements established in the RD 1620/2007 broken down by applications, and to estimate establishment and operational costs. This proposal has been based on what is established in the above mentioned Guide and NWRP. The proposed treatment typologies are divided in treatment trains with desalination, like reverse osmosis or reversible electrodialisis, and those that lack this treatment for brackish water. This separation is done due to coastal facilities, where sea water may permeate the collecting pipes, rising salt contents in the wastewater, hence limiting certain uses. To develop this objective a study of the most common treatment units set up in Spanish WRPs is conducted in terms of treatment train reliability to obtain an acceptable relationship between the required quality and the capital and operational costs. The CRT has an establishment cost of 28 to 48 €.m-3.d and an operation cost of 0.06 to 0.09 €.m-3, while, if desalination was required, these costs would increase tenfold for implementation and fivefold for operation. In the cases of uses that require ART, such as residential or certain industrial uses, the costs would be of 185 to 398 €.m-3.d for implementation and of 0.14 to 0.20 €.m-3 for operation. When selecting regeneration treatment lines, the relation between treatment capacity and cost is a paramount indicator. This project provides cost-capacity models for regeneration treatment trains. These may serve as a tool when selecting between different options to fulfill water demands with MBR facilities, or others such as sea water desalination plants or inter-basin water transfer into a water planning framework. In Spain, the requirement for high quality water in areas with low resource availability, the increasing number of sensitive zones, such as drinking water extraction, recreational bathing areas, fish protected areas and the lack of available land to set up new WWTPs, have turned MBRs into a suitable option for water reuse. In this work this technology is analyzed in contrast to CRT and ART, providing cost-capacity models, and identifying when and where this treatment option may outcompete other regeneration treatments. An MBR is an activated sludge treatment where the secondary settling is substituted by a membrane system of UF or MF. The quality of the effluent is, therefore, comparable to that of a WWTP followed by an ART. MBRs ensure a sufficient quality level for the requirements of the different uses established in the RD, even producing an effluent that can be directly treated in OI or EDR processes. The implementation of this technology in Spain has grown exponentially, growing from 13 facilities with less than 5000 m3.d-1 in 2006 to above 55 facilities operating by the end of 2014, 6 of them with capacities over 15000 m3.d-1. The membrane filtration systems for MBR are the ones that set the pace of operation and design of this type of facilities. The most widespread system in Spain is the hollow fiber membrane configuration, especially on high flow capacities, being Zenon commercial technology, which mounts up to 57% of the total installed capacity, the main contributor. The next commercial technology according to plant number is Kubota, which uses flat sheet membrane configuration, which mounts up to 30% of the total installed capacity. Other commercial technologies exist within the Spanish MBR context, such as Toray, Huber, Koch or Microdym. In this document an analysis of all of these membrane filtration systems is done, providing information about their characteristics and relevant design and operation parameters. The study of 14 full scale running MBRs has enabled to pursue another of the objectives of this work: the estimation of the implementation and operation costs of this type of systems in contrast to other regeneration alternatives. Active participation of ACA and ESAMUR, public wastewater treatment and reuse entities of Cataluña and Murcia respectively, has helped attaining this objective. A number of typical operative problems and their possible solutions are discussed, both for operation and plant design purposes. The conclusion of this study is that MBRs are another option to consider for water reuse, being advantageous in terms of both implementation and operational costs, when compared with WWTPs followed by ART, when considering flow capacities above 10000 m3.d-1.

Tratamiento de vinazas provenientes de etanol en un reactor de lecho fluidizado inverso

En el estado de Veracruz, al sur de México, se ubican empresas dedicadas a la obtención de etanol a partir de melaza de azúcar de caña. Las más pequeñas, tienen una producción promedio de 20,000 L de alcohol/día. Los efluentes de la producción de etanol incluyen agua de enfriamiento de condensadores, agua del lavado de tanques de fermentación y vinazas, estas últimas son los efluentes más contaminantes en las destilerías, por su concentración de material orgánico biodegradable y no biodegradable. Las vinazas se generan en grandes volúmenes, produciéndose de 12 a 15 litros de vinazas por cada litro de alcohol destilado. Estos efluentes se caracterizan por tener altas temperaturas, pH ácido y una elevada concentración de DQO así como de sólidos totales. La determinación de la biodegradabilidad anaerobia de un agua residual, permite estimar la fracción de DQO que puede ser transformada potencialmente en metano y la DQO recalcitrante que queda en el efluente. Para el desarrollo de una prueba de biodegradabilidad, es importante considerar diversos factores relacionados con la composición del agua a tratar, composición de los lodos y las condiciones bajo las cuales se lleva a cabo la prueba. La digestión anaerobia de aguas residuales industriales es comúnmente usada en todo el mundo, ofrece significativas ventajas para el tratamiento de efluentes altamente cargados. Los sistemas anaerobios de tratamiento de aguas residuales industriales incluyen tecnologías con biopelículas, estos sistemas de tratamiento anaerobio con biopelícula son una tecnología bien establecida para el tratamiento de efluentes industriales. El Reactor de Lecho Fluidizado Inverso Anaerobio (LFI) ha sido diseñado para el tratamiento de aguas residuales de alta carga, teniendo como ventajas el empleo de un soporte que proporciona una gran superficie y un bajo requerimiento de energía para la fluidización del lecho. En el presente trabajo, se lleva a cabo el análisis de un proceso de producción de etanol, identificando a los efluentes que se generan en el mismo. Se encuentra que el efluente final está compuesto principalmente por las vinazas provenientes del proceso de destilación. En la caracterización de las vinazas provenientes del proceso de producción de etanol a partir de melaza de azúcar de caña, se encontraron valores promedio de DQO de 193.35 gDQO/L, para los sólidos totales 109.78 gST/L y pH de 4.64. Así mismo, en esta investigación se llevó a cabo una prueba de biodegradabilidad anaerobia, aplicada a la vinaza proveniente de la producción de etanol. En la caracterización de los lodos empleados en el ensayo se obtiene una Actividad Metanogénica Especifica de 0.14 g DQO/gSSV.d. El porcentaje de remoción de DQO de la vinaza fue de 62.7%, obteniéndose una k igual a 0.031 h-1 y una taza de consumo de sustrato de 1.26 gDQO/d. El rendimiento de metano fue de 0.19 LCH4/g DQOremovida y el porcentaje de biodegradabilidad de 54.1%. El presente trabajo también evalúa el desempeño de un LFI, empleando Extendospher® como soporte y tratando efluentes provenientes de la producción de etanol. El reactor se arrancó en batch y posteriormente se operó en continuo a diferentes Cargas Orgánicas Volumétricas de 0.5, 1.0, 3.3, 6.8 y 10.4 g DQO/L.d. Además, se evaluaron diferentes Tiempos de Residencia Hidráulica de 10, 5 y 1 días. El sistema alcanzó las siguientes eficiencias promedio de remoción de DQO: 81% para la operación en batch; 58, 67, 59 y 50 % para las cargas de 0.5, 1.0, 3.3, 6.8 g DQO/L.d respectivamente. Para la carga de 10.4 g DQO/L.d, la eficiencia promedio de remoción de DQO fue 38%, en esta condición el reactor presentó inestabilidad y disminución del rendimiento de metano. La generación de metano inició hasta los 110 días de operación del reactor a una carga de 1.0 g DQO/L.d. El sistema alcanzó un rendimiento de metano desde 0.15 hasta 0.34 LCH4/g DQO. Durante la operación del reactor a una carga constante de 6.4 g DQO/L.d, y un TRH de 1 día, se alcanzó una eficiencia promedio de remoción de DQO de 52%. In the state of Veracruz, to the south of Mexico, there are located companies dedicated to the production of ethanol from molasses of cane sugar. The smallest, have a average production of 20,000 L ethanol/day. The effluent of production of ethanol include water of condensers, water originated from the cleanliness of tanks of fermentation and vinasses, the above mentioned are more effluent pollutants in the distilleries, for the poor organic matter degradability. The vinasses are generated in high volumes, producing from 12 to 15 L of vinasses per every liter of distilled ethanol. These effluent are characterized by its high temperature, pH acid and a high concentration of DQO as well as high concentration of TS. The determination of the anaerobic degradability of a waste water, it allows to estimate the fraction of DQO that can be transformed potentially into methane and the recalcitrant DQO that stays in the effluent. For the development of degradability test, it is important to consider factors related to the composition of the water to be treated, composition of the sludge and the conditions under which the test is carried out. The anaerobic digestion of industrial wastes water is used commonly in the whole world, it offers significant advantages for the treatment of effluent highly loaded. The anaerobic treatment of industrial wastes water include technologies with biofilms, this anaerobic treatment whit biofilms systems, is a well-established technology for treatment of industrial effluents. The Anaerobic Inverse Fluidized Bed Reactor (IFBR) has been developed to provide biological treatment of high strength organic wastewater for their large specific surface and their low energy requirements for fluidization. In this work, there is carried out the analysis of a process of production of ethanol, identifying the effluent ones that are generated in the process. One determined that the effluent end is composed principally by the vinasses originated from the process of distillation. In the characterization of the vinasses originated from the process of production of ethanol from cane sugar molasses, there were average values of DQO of 193.35 gDQO/L, average values of solid of 109.78 gST/L and pH of 4.64. In this investigation there was carried out a anaerobic degradability test of the vinasses generated in the production of ethanol. In the characterization of the sludge used in the essay, the specific methanogenic activity (SMA) was 0.14 gDQO/gSSV.d. The average removal of DQO of the vinasses was 62.7 %, k equal to 0.031 h-1 was obtained one and a rate of removal substrate of 1.26 gDQO/d. The methane yield was 0.19 LCH4/gDQO removed and the anaerobic biodegradability was a 54.1 %. This study describes the performance of IFBR with Extendospher®, for the treatment of vinasses. The start-up was made in batch, increasing gradually the Organic Load Rate (OLR): 0.5, 1.0, 3.3, 6.8 and 10.4 g COD/L.d. Different Hydraulic Retention Times (HRT) were evaluated: 10, 5 and 1 days. During the operation in batch, the COD removal obtained was of 81 %, and for OLR of 0.5, 1.0, 3.3, 6.8 g COD/L.d the removal obtained was 58, 67, 59 and 50 % respectively. For a maximum OLR of 10.4 g COD/L.d, the COD removal was 38 %, and the system presented instability and decrease of the yield methane. The methane production initiated after 110 days of the start-up of the IFBR, to organic load rate of 1.0 g COD/L.d. The system reached values in the methane yield from 0.15 up to 0.34 LCH4/g CODremoved, for the different organic load rates. During the operation to a constant OLR of 6.4 g COD/L.d, and a HRT of 1 day, the Anaerobic Inverse Fluidized Bed Reactor reached a maximum efficiency of removal of 52 %.