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

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

The appraisal of mesophilic anaerobic digestion and thermophilic aerobic digestion in the treatment of municipal sludge in Ireland

It has been well documented that the optimum feedstock for anaerobic digesters consists of readily biodegradable compounds, as found in primary sludge or even a mixed substrate of primary and excess activated sludge. Due to the requirements of the Urban Wastewater Treatment Plant Directive of 1991, the quantities of secondary sludge generated is set to increase substantially. A pilot scale study was undertaken to evaluate the performance of both Mesophilic Anaerobic Digestion and Thermophilic Aerobic digestion in the treatment of secondary sludge. The results indicated that the anaerobic pilot scale digester achieved a greater solids destruction than the aerobic pilot plant averaging at 28% T.S. removal verses 20% for the aerobic digester, despite the fact that secondary sludge is the optimum feedstock for aerobic digestion. This can, however, be attributed to the greater biomass yield experienced with aerobic systems, and to the absence of Autothermal conditions. At present, the traditional technique of Mesophilic Anaerobic Digestion is in widespread application throughout Ireland, for the stabilisation of sewage sludge. There is only one Autothermal Thermophilic Aerobic Digester at present situated in Killarney, Co. Kerry. A further objectives of the study was to compare full-scale applications of Mesophilic Anaerobic Digestion to ATAD. Two Sludge Treatment plants, situated in Co. Kerry, were used for this purpose, and were assessed mainly under the following headings; process stability, solids reduction on average, the ATAD plant in Killarney has the advantage of producing a “Class A” Biosolid in terms of pathogen reduction, and can effectively treat double the quantity of sludge. In addition, economically the ATAD plant is cheaper to run, costing €190 / t.d.s verses €211 / t.d.s. for the anaerobic digester in Tralee. An overview of additional operational Anaerobic Digestion Plants throughout Ireland is also presented.

The appraisal of anaerobic digestion in Ireland to develop improved designs and operational practice

Mesophilic Anaerobic Digestion treating sewage sludge was investigated at five full-scale sewage treatment plants in Ireland. The anaerobic digestion plants are compared and evaluated in terms of design, equipment, operation, monitoring and management. All digesters are cylindrical, gas mixed and heated Continuously Stirred Tank Reactors (CSTR), varying in size from 130m3 to 800m3. Heat exchanger systems heat all digesters. Three plants reported difficulties with the heating systems ranging from blockages to insufficient insulation and design. Exchangers were modified and replaced within one year of operation at two plants. All but one plant had Combined Heat and Power (CHP) systems installed. Parameter monitoring is a problem at all plants mainly due to a lack of staff and knowledge. The plant operators consider pH and temperature the most important parameters to be measured in terms of successful monitoring of an anaerobic digester. The short time taken and the ease at which pH and temperature can be measured may favour these parameters. Three laboratory scale pilot anaerobic digesters were operated using a variety of feeds over at 144-day period. Two of the pilots were unmixed and the third was mechanically mixed. As expected the unmixed reactors removed more COD by retention of solids in the digesters but also produced greater quantities of biogas than the mixed digester, especially when low solids feed such as whey was used. The mixed digester broke down more solids due to the superior contact between the substrate and the biomass. All three reactors showed good performance results for whey and sewage solids. Scum formation occurred giving operational problems for mixed and unmixed reactors when cattle slurry was used as the main feed source. The pilot test was also used to investigate which parameters were the best indicators of process instability. These trials clearly indicated that total Volatile Fatty Acid (VFA) concentrations was the best parameter to show signs of early process imbalance, while methane composition in the biogas was good to indicate possible nutrient deficiencies in the feed and oxygen shocks. pH was found to be a good process parameter only if the wastewater being treated produced low bicarbonate alkalinities during treatment.

Development of an inspection regime for on-site domestic wastewater treatment systems

The overall purpose of this study was to develop a thorough inspection regime for onsite wastewater treatment systems, which is practical and could be implemented on all site conditions across the country. With approximately 450,000 onsite wastewater treatment systems in Ireland a risk based methodology is required for site selection. This type of approach will identify the areas with the highest potential risk to human health and the environment and these sites should be inspected first. In order to gain the required knowledge to develop an inspection regime in-depth and extensive research was earned out. The following areas of pertinent interest were examined and reviewed, history of domestic wastewater treatment, relevant wastewater legislation and guidance documents and potential detrimental impacts. Analysis of a questionnaire from a prior study, which assessed the resources available and the types of inspections currently undertaken by Local authorities was carried out. In addition to the analysis of the questionnaire results, interviews were carried out with several experts involved in the area of domestic wastewater treatment. The interview focussed on twelve key questions which were directed towards the expert’s opinions on the vital aspects of developing an inspection regime. The background research, combined with the questionnaire analysis and information from the interviews provided a solid foundation for the development of an inspection regime. Chapter 8 outlines the inspection regime which has been developed for this study. The inspection regime includes a desktop study, consultation with the homeowners, visual site inspection, non-invasive site tests, and inspection of the treatment systems. The general opinion from the interviews carried out, was that a standardised approach for the inspections was necessary. For this reason an inspection form was produced which provides a standard systematic approach for inspectors to follow. This form is displayed in Appendix 3. The development of a risk based methodology for site selection was discussed and a procedure similar in approach to the Geological Survey of Irelands Groundwater Protection Schemes was proposed. The EPA is currently developing a risk based methodology, but it is not available to the general public yet. However, the EPA provided a copy of a paper outlining the key aspects of their methodology. The methodology will use risk maps which take account of the following parameters: housing density, areas with inadequate soil conditions, risk of water pollution through surface and subsurface pathways. Sites identified with having the highest potential risk to human health and the environment shall be inspected first. Based on the research carried out a number of recommendations were made which are outlined in Chapter 10. The principle conclusion was that, if these systems fail to operate satisfactorily, home owners need to understand that these systems dispose of the effluent to the 'ground' and the effluent becomes part of the hydrological cycle; therefore, they are a potential hazard to the environment and human health. It is the owners, their families and their neighbours who will be at most immediate risk.

La Depuradora del segle XXI

A partir de la reflexió sobre la situació actual i futura de les depuradores d’aigües, s’estudia l’obtenció d’un model conceptual de possible depuradora del segle XXI, entenent l’EDAR del segle XXI com a una instal•lació quegestioni de manera òptima les aigües residuals urbanes d’una població mitjana. (El cas pràctic es concreta en l’EDAR de Figueres)

Estudio y propuestas de tratamiento de PPCP’s en aguas residuales

La reutilización de las aguas residuales es una parte esencial del uso sostenible del agua. Sin embargo, las actuales plantas de tratamiento no están preparadas para tratar determinados compuestos como los llamados “contaminantes emergentes”. Los hábitos de consumo actuales estan generando una serie de residuos o microcontaminantes que hace tan solo unos años no existian. Entre esas nuevas sustancias aparecen los PPCP’s (Pharmaceuticals & Personal Care Products) que son un amplio grupo de compuestos químicos utilizados en veterinaria, prácticas agrícolas, salut humana y cosmetología. El mayor problema que presentan estas substancias en la actualidad es el parcial desconocimiento sobre sus efectos, la ausencia de reglamentaciones que determinen las concentraciones máximas admisibles en los cauces de vertido, la reducción en procesos de depuración convencionales, así como los tratamientos específicos aplicables a su eliminación. Los objetivos del presente proyecto són: estudiar las tipologías de PPCP’s y sus influencias para la salud humana y el medio ambiente, estudiar los diferentes sistemas de tratamiento de aguas existentes en plantas depuradoras y evaluar su eficiencia en la depuración de PPCP

Projecte d’instal·lacions sostenibles d’una masia rural aïllada

En aquest projecte es vol donar solució a la contaminació que es produeix a les llars ja sigui en forma de gasos d’efecte hivernacle o la contaminació d’aqüífers i rius per les aigües residuals d’aquestes. Els objectius a aconseguir són la disminució del consum d’energia de la llar, reduint així el consum de combustibles fòssils, amb la conseqüent disminució de gasos d’efecte hivernacle i l’estalvi econòmic que això suposa. I per altra banda la depuració de les aigües residuals, tot i que actualment totes les grans poblacions de Catalunya de més de 10.000 habitants ja disposen de EDARS i en pocs anys en tindran totes les de més de 2000 habitants. Però en aquest cas es tracta d’una població molt petita que no disposa de xarxa de clavegueram. En primer lloc s’ha plantejat un sistema de calefacció d’energia geotèrmica que ens permet aprofitar l’energia tèrmica que es va emmagatzemant a la terra degut a l’escalfor del sol i que ens permet extreure d’aquesta fins a ¾ parts de l’energia tèrmica necessària per el sistema de calefacció. En segon lloc es planteja un sistema de producció d’energia elèctrica per panells fotovoltaics que produeixi el consum elèctric anual familiar, tot i que no de forma directe, sinó venent l’energia a la xarxa elèctrica i comprant-la després de la xarxa. Per últim es projecta un sistema de depuració d’aigües per mitjà d’un aiguamoll artificial que permetrà a la casa, que no disposa de xarxa de clavegueram, retornar les aigües residuals en bones mediambientals a l’entorn rural que envolta l’edificació, sense perjudicar la fauna i els rius que l’envolten

Implementació d’un sistema de control avançat en una estació depuradora d’aigües residuals

Aquest projecte té com a objectiu la implementació d'un sistema de control avançat en una estació depuradora d'aigües residuals a la Vall del Ges, Torelló

Anàlisi comparativa dels processos emergents sharon i anammox per al tractament d’aigües amb una alta càrrega de nitrogen

Estudi de tractaments innovadors en aigües residuals amb elevada concentració de nitrogen mitjançant la tecnologia ANAMMOX (Anaerobic Ammonium Oxidation) i SHARON i posterior anàlisi teòrica de la gestió dels fangs residuals d’una EDAR

Proposta de millora de la qualitat de les aigües residuals de Sant Martí Sescorts

Diagnòsi de les aigües residuals de sant martí Sescorts i proposta de millora de la qualitat d' aquestes aigues residuals

Projecte d’una estació depuradora d’aigües residuals generades en un escorxador porcí amb una capacitat de sacrifici de 3.000 porcs diaris, al terme municipal d’Argentona, comarca del maresme (Barcelona)

Disseny i dimensionament de les obres i instal·lacions d’una depuradora per a un escorxador de porcí amb una capacitat de sacrifici de 3.000 porcs diaris. El present projecte es localitza al polígon Nord, al terme municipal d’Argentona, a la comarca del Maresme (Barcelona)

Projecte d'infraestructures d'un sector residencial a Tossa de Mar

Projecte de millores d'infrastructures de la urbanització de Santa Maria de Llorell (Tossa de Mar

Sistema intel•ligent d’ajuda a la decisió pel control remot de tecnologia de membranes per la depuració d’aigües

El principal objectiu del projecte consisteix en desenvolupar l’anàlisi, disseny,desenvolupament i implementació d’un sistema d’ajuda a la decisió (SAD) basat en elconeixement pel control remot i la supervisió de l’operació integrada d’estacionsdepuradores BRM (bioreactor de membranes) pe ra la depuració d’aigües residuals ambexigències de qualitat de reutilització de l’aigua tractada

Tractament fisicoquímic de les aigües i fangs d'un escorxador porcí

L’objectiu del present projecte és la proposta (disseny i estimació econòmica) d’un sistema de tractament de les aigües i els fangs generats a un escorxador porcí de Granollers. Per tal de portar a terme aquest estudi, es va realitzar una anàlisi de la situació prèvia a l’escorxador, del diagrama de flux de les instal·lacions existents, de les necessitats del sector, dels límits d’abocament fixats pel Reglament del Consorci del Besòs, i finalment de la caracterització de les aigües residuals generades (en quantitat i qualitat) així com dels fangs produïts. Arran d’aquesta anàlisi es va realitzar un estudi experimental d’optimització del tractament fisicoquímic, i en base als resultats es van generar diferents alternatives de tractament, es va simular el seu comportament, i es va fer una avaluació comparativa dels costos i rendiments estimats