Descomposición fotoquímica de soluciones acuosas de dodecilbenceno sulfonato sódico en un fotoreactor anular contínuo de mezcla perfecta

La fotodescomposición de dodecilbencenosulfato sódico (DBS) se ha estudiado como un proceso de purificación del agua. Soluciones acuosas de DBS han sido irradiadas en un fotorreactor anular de mezcla perfecta, aplicándose el modelo de radiación cilíndrico esférico extenso.

Comparison of a deterministic and a data driven model to describe MBR fouling

Membrane bioreactors (MBRs) are a combination of activated sludge bioreactors and membrane filtration, enabling high quality effluent with a small footprint. However, they can be beset by fouling, which causes an increase in transmembrane pressure (TMP). Modelling and simulation of changes in TMP could be useful to describe fouling through the identification of the most relevant operating conditions. Using experimental data from a MBR pilot plant operated for 462days, two different models were developed: a deterministic model using activated sludge model n°2d (ASM2d) for the biological component and a resistance in-series model for the filtration component as well as a data-driven model based on multivariable regressions. Once validated, these models were used to describe membrane fouling (as changes in TMP over time) under different operating conditions. The deterministic model performed better at higher temperatures (>20°C), constant operating conditions (DO set-point, membrane air-flow, pH and ORP), and high mixed liquor suspended solids (>6.9gL-1) and flux changes. At low pH (<7) or periods with higher pH changes, the data-driven model was more accurate. Changes in the DO set-point of the aerobic reactor that affected the TMP were also better described by the data-driven model. By combining the use of both models, a better description of fouling can be achieved under different operating conditions

Pharmaceuticals occurrence in a WWTP with significant industrial contribution and its input into the river system

Occurrence and removal of 81 representative Pharmaceutical Active Compounds (PhACs) were assessed in a municipal WWTP located in a highly industrialized area, with partial water reuse after UV tertiary treatment and discharge to a Mediterranean river. Water monitoring was performed in an integrated way at different points in the WWTP and river along three seasons. Consistent differences between therapeutic classes were observed in terms of influent concentration, removal efficiencies and seasonal variation. Conventional (primary and secondary) treatment was unable to completely remove numerous compounds and UV-based tertiary treatment played a complementary role for some of them. Industrial activity influence was highlighted in terms of PhACs presence and seasonal distribution. Even if global WWTP effluent impact on the studied river appeared to be minor, PhACs resulted widespread pollutants in river waters. Contamination can be particularly critical in summer in water scarcity areas, when water flow decreases considerably

Towards integrated operation of membrane bioreactors : effects of aeration on biological and filtration performance

Two experimental studies evaluated the effect of aerobic and membrane aeration changes on sludge properties, biological nutrient removal and filtration processes in a pilot plant membrane bioreactor. The optimal operating conditions were found at an aerobic dissolved oxygen set-point (DO) of 0.5mgO2L-1 and a membrane specific aeration demand (SADm) of 1mh-1, where membrane aeration can be used for nitrification. Under these conditions, a total flow reduction of 42% was achieved (75% energy reduction) without compromising nutrient removal efficiencies, maintaining sludge characteristics and controlled filtration. Below these optimal operating conditions, the nutrient removal efficiency was reduced, increasing 20% for soluble microbial products, 14% for capillarity suction time and reducing a 15% for filterability. Below this DO set-point, fouling increased with a transmembrane pressure 75% higher. SADm below 1mh-1 doubled the values of transmembrane pressure, without recovery after achieving the initial conditions

Materiales vitrocerámicos a partir de lodos procedentes de una estación de depuración de aguas residuales urbanas (en la Ciudad de El-Sadat, Egipto)

La depuración de las aguas residuales urbanas es fuente de importantes volúmenes de lodos los cuales es preciso gestionar. En este trabajo se expone la posibilidad de aplicarles un proceso de gestión basado en la vitrificación y mediante el cual, además de inertizar los elementos contaminantes presentes en los lodos, se obtiene un material vitrocerámico con un importante valor añadido. Partiendo de la caracterización química (FRX), mineralógica (DRX) y térmica (ATD-TG) de estos lodos, se determina la formulación del vidrio original y su poder energético. Mediante ATD-TG, dilatometría y MEB, se ha determinado la temperatura de máxima velocidad de nucleación y la temperatura de crecimiento así como la morfología y tamaño de los núcleos formados que, en este caso, son nanométricos. En definitiva, se ha comprobado como la gestión de los residuos sólidos urbanos mediante la vitrificación es una alternativa a los vertederos y a la incineración.

Non conventional biological treatment based on Trametes versicolor for the elimination of recalcitrant anticancer drugs in hospital wastewater

This work presents a study about the elimination of anticancer drugs, a group of pollutants considered recalcitrant during conventional activated sludge wastewater treatment, using a biological treatment based on the fungus Trametes versicolor. A 10-L fluidized bed bioreactor inoculated with this fungus was set up in order to evaluate the removal of 10 selected anticancer drugs in real hospital wastewater. Almost all the tested anticancer drugs were completely removed from the wastewater at the end of the batch experiment (8 d) with the exception of Ifosfamide and Tamoxifen. These two recalcitrant compounds, together with Cyclophosphamide, were selected for further studies to test their degradability by T. versicolor under optimal growth conditions. Cyclophosphamide and Ifosfamide were inalterable during batch experiments both at high and low concentration, whereas Tamoxifen exhibited a decrease in its concentration along the treatment. Two positional isomers of a hydroxylated form of Tamoxifen were identified during this experiment using a high resolution mass spectrometry based on ultra-high performance chromatography coupled to an Orbitrap detector (LTQ-Velos Orbitrap). Finally the identified transformation products of Tamoxifen were monitored in the bioreactor run with real hospital wastewater

Characterization and Control Strategies of an Integrated Chemical-Biological System for the Remediation of Toxic Pollutants in Wastewater: A case of study

In a previous work, a hybrid system consisting of an advanced oxidation process (AOP) named Photo-Fenton (Ph-F) and a fixed bed biological treatment operating as a sequencing batch biofilm reactor (SBBR) was started-up and optimized to treat 200 mg·L-1 of 4-chlorophenol (4-CP) as a model compound. In this work, studies of reactor stability and control as well as microbial population determination by molecular biology techniques were carried out to further characterize and control the biological reactor. Results revealed that the integrated system was flexible and even able to overcome toxic shock loads. Oxygen uptake rate (OUR) in situ was shown to be a valid tool to control the SBBR operation, to detect toxic conditions to the biomass, and to assess the recovery of performance. A microbial characterization by 16S rDNA sequence analysis reveals that the biological population was varied, although about 30% of the bacteria belonged to the Wautersia genus.

Estudi de la recuperació de la calor de les aigües residuals urbanes per la climatització d’una piscina

Estudi de la climatització d'una instal•lació esportiva,concretament una piscina coberta municipal, a partir de la calor recuperada de les aigües residuals urbanes (ARU) que produeix una població de 30.000 habitants. En la primera part de l'estudi s'ha calculat la potència màxima per cobrir les quatrenecessitats de la instal•lació en règim estacionari, que ha resultat ser de 265,8 kW,repartits en 69,1 kW per cobrir les necessitats del vas de la piscina, 102,5 kW percobrir les necessitats en l'aire interior de la sala de la piscina, 30,2 kW per cobrir lesnecessitats tèrmiques calorífiques de les sales annexes i 64 kW per cobrir lesnecessitats en la producció d'aigua calenta sanitària (ACS). A continuació també s'hadeterminat l'estimació de la despesa total anual de la instal•lació que és de 1.179MWh/any. El 48% aproximadament de la despesa total es destina a cobrir lesnecessitats del vas de la piscina, el 28% per cobrir la producció d'ACS, el 20% percobrir les necessitats de la sala de la piscina i el 4% per cobrir les necessitatscalorífiques a hivern de les sales annexes