Electrokinetic treatment of environmental matrices. Contaminants removal and phosphorus recovery

There is a need to develop viable techniques for removal and recovery organic and inorganic compounds from environmental matrices, due to their ecotoxicity, regulatory obligations or potential supplies as secondary materials. In this dissertation, electro –removal and –recovery techniques were applied to five different contaminated environmental matrices aiming phosphorus (P) recovery and/or contaminants removal. In a first phase, the electrokinetic process (EK) was carried out in soils for (i) metalloids and (ii) organic contaminants (OCs) removal. In the case of As and Sb mine contaminated soil, the EK process was additionally coupled with phytotechnologies. In a second phase, the electrodialytic process (ED) was applied to wastes aiming P recovery and simultaneous removal of (iii) toxins from membrane concentrate, (iv) heavy metals from sewage sludge ash (SSA), and (v) OCs from sewage sludge (SS). EK enhanced phytoremediation showed to be viable for the remediation of soils contaminated with metalloids, as although remediation was low, it combines advantages of both technologies while allowing site management. EK also proved to be an effective remediation technology for the removal and degradation of emerging OCs from two types of soil. Aiming P recovery and contaminants removal, different ED cell set-ups were tested. For the membrane concentrates, the best P recovery was achieved in a three compartment (3c) cell, but the highest toxin removal was obtained in a two compartment (2c) cell, placing the matrix in the cathode end. In the case of SSA the best approach for simultaneous P recovery and heavy metals removal was to use a 2c-cell placing the matrix in the anode end. However, for simultaneous P recovery and OCs removal, SS should be placed in the cathode end, in a 2c-cell. Overall, the data support that the selection of the cell design should be done case-by-case.

Electrodialytic recovery of phosphorus and organic contaminants removal from sewage sludge

Phosphorus is a macronutrient essential to life which comes from phosphate rock, a non-renewable resource. Sewage sludge from wastewater treatment plants (WWTP) is a secondary resource rich in phosphorus that can be valorized. However, organic compounds are detected in sewage sludge, due to its non-polar and hydrophobic character, being considered an environmental risk. The present dissertation aims to study the efficiency of the electrodialytic process (ED) when applied to sewage sludge aiming phosphorus recovery and organic contaminants removal. Four organic compounds were analyzed: 17α-ethynylestradiol (EE2), bisphenol A (BPA), caffeine (Caf) and oxybenzone (MBPh). The experiments took place in an ED cell with two compartments and an anion exchange membrane, with the sludge in the cathode compartment. The experiments were carried out for three days with spiked sewage sludge (six assays). One control experiment was done without current, three experiments were carried out applying a constant current of 50, 75, and 100 mA and two experiments were carried out applying sequential currents: 50 mA, 75 mA and 100 mA and the opposite (100-75-50 mA). A qualitative and quantitative analysis of microorganisms existing in the samples was also done. At the end, the pH increased in the sewage sludge favoring phosphorus recovery. In terms of phosphorus, the highest recovery was achieved in the experiment run with 100 mA, where 70.3±2.0% of total phosphorus was recovered in the electrolyte. Generally, compounds degradation was favored by the current. Caf and MBPh achieved degradation percentages of 96.2±0.2% and 84.8±1.3%, respectively, in 100 mA assay. EE2 (83.1±1.7%) and BPA (91.8±4.6%) degradations were favored by 50 mA current. A total of 35 taxa from four different groups were identified, totalizing between 81,600-273,000 individuals per gram of initial sludges. After ED, microbial community population decreased between 47-98%. Arcella gibbosa represented 61% of the total observed organisms and revealed to be more tolerant to medium changes.

Removal of organic contaminants from wastewater using the electrodialytic process

Pharmaceuticals and personal care products (PPCPs) are widely used on a daily basis. After their usage they reach the wastewater treatment plants (WWTPs). These compounds have different physico-chemical characteristics, which makes them difficult to completely remove in the WWTPs, througth conventional treatments. Currently, there is no legislation regarding PPCPs thresholds in effluent discharge. But, even at vestigial concentrations, these compounds enclose environmental risks due to, e.g., endocrine disruption potential. There is a need of alternative techniques for their removal in WWTPs. The main goal of this work was to assess the use of electrodialytic (ED) process to remove PPCPs from the effluent to be discharged. A two-compartment ED cell was used testing (i) the effluent position in the cell (anode and cathode compartment); (ii) the use of anion (AEM) and cation exchange membrane (CEM); (iii) the treatment period (6, 12 and 24 hours); (iv) effluent recirculation and current steps; (v) the feasibility of sequential treatments. Phosphorus (P) removal from effluent and energetic costs associated to the process were also evaluated. Five PPCPs were studied – caffeine (CAF), bisphenol A (BPA), 17 β-estradiol (E2), ethinyl estradiol (EE2) and oxybenzone (MBPh). The ED process showed to be effective in the removal when effluent is in the anode compartment. Oxidation is suggested to be the main removal process, which was between 88 and 96%, for all the compounds, in 6 hours. Nevertheless, the presence of intermediates and/or by-products was also observed in some cases. Effluent recirculation should have a retention time in the ED cell big enough to promote removal whereas the current steps (effluent in anode compartment) slightly increased removal efficiencies (higher than 80% for all PPCPs). The sequential set of ED treatment (effluent in anode compartment) showed to be effective during both periods with a removal percentage between 80 and 95% and 73 to 88% in the case of AEM and CEM, respectively. Again, the main removal process is strongly suggested to be oxidation in the anode compartment. However, there was an increase of BOD5 and COD, which might be explained by effluent spiking, these parameters limiting the effluent discharge. From these treatments, the use of AEM, enhanced the P removal from effluent to minimize risk of eutrophication. Energetic costs of the best set-up (6 hours) are approximately 0,8€/m3 of wastewater, a value considered low, attending to the prices of other treatment processes.

Coupling organic substrate removal to methane production in a fully biological microbial electrolysis cell

Microbial electrolysis cells (MECs) are an innovative and emerging technique based on the use of solid-state electrodes to stimulate microbial metabolism for wastewater treatment and simultaneous production of value-added compounds (such as methane). This research studied the performance of a two-chamber MEC in terms of organic matter oxidation (at the anode) and methane production (at the cathode). MEC‟s anode had been previously inoculated with an activated sludge, whereas the cathode chamber inoculum was an anaerobic sludge (containing methanogenic microorganisms). During the experimentation, the bioanode was continuously fed with synthetic solutions in anaerobic basal medium, at an organic load rate (OLR) of around 1 g L-1 d-1, referred to the chemical oxygen demand (COD). At the beginning (Run I), the feeding solution contained acetate and subsequently (Run II) it was replaced with a more complex solution containing soluble organic compounds other than acetate. For both conditions, the anode potential was controlled at -0.1 V vs. standard hydrogen electrode, by means of a potentiostat. During Run I, over 80% of the influent acetate was anaerobically oxidized at the anode, and the resulting electric current was recovered as methane at the cathode (with a cathode capture efficiency, CCE, accounting around 115 %). The average energy efficiency of the system (i.e., the energy captured into methane relative to the electrical energy input) under these conditions was over 170%. However, reactor‟s performance decreased over time during this run. Throughout Run II, a substrate oxidation over 60% (on COD basis) was observed. The electric current produced (57% of coulombic efficiency) was also recovered as methane, with a CCE of 90%. For this run the MEC‟s average energy efficiency accounted for almost 170 %. During all the experimentation, a very low biomass growth was observed at the anode whereas ammonium was transferred through the cationic membrane and concentrated at the cathode. Tracer experiments and scanning electron microscopy analyses were also carried out to gain a deeper insight into the reactor performance and also to investigate the possible reasons for partial loss of performance. In conclusion, this research suggests the great potential of MEC to successfully treat low-strength wastewaters, with high energy efficiency and very low sludge production.

Temperature and feed strategy effects on sulfate and organic matter removal in an AnSBB

The objective of this work was to analyze the interaction effects between temperature, feed strategy and COD/[SO(4)(2-)] levels, maintaining the same ratio, on sulfate and organic matter removal efficiency from a synthetic wastewater. This work is thus a continuation of Archilha et al. (2010) who studied the effect of feed strategy at 30 degrees C using different COD/[SO] ratios and levels. A 3.7-L anaerobic sequencing batch reactor with recirculation of the liquid phase and which contained immobilized biomass on polyurethane foam (AnSBBR) was used to treat 2.0 L synthetic wastewater in 8 h cycles. The temperatures of 15, 22.5 and 30 degrees C with two feed strategies were assessed: (a) batch and (b) batch followed by fed-batch. In strategy (a) the reactor was fed in 10 min with 2 L wastewater containing sulfate and carbon sources. In strategy (b) 1.2 L wastewater (containing only the sulfate source) was fed during the first 10 min of the cycle and the remaining 0.8 L (containing only the carbon source) in 240 min. Based on COD/[SO(4)(2-)] = 1 and on the organic matter (0.5 and 1.5 gCOD/L) and sulfate (0.5 and 1.5 gSO(4)(2-)/L) concentrations, the sulfate and organic matter loading rates applied were 1.5 and 4.5 g/L.d, i.e., same COD/[SO(4)(2-)] ratio (=1) but different levels (1.5/1.5 and 4.5/4.5 gCOD/gSO(4)(2-)). When reactor feed was 1.5 gCOD/L.d and 1.5 gSO(4)(2-)/L.d, gradual feeding (strategy b) showed to favor sulfate and organic matter removal in the investigated temperature range, indicating improved utilization of the electron donor for sulfate reduction. Sulfate removal efficiencies were 87.9; 86.3 and 84.4%, and organic matter removal efficiencies 95.2; 86.5 and 80.8% at operation temperatures of 30; 22.5 and 15 degrees C, respectively. On the other hand, when feeding was 4.5 gCOD/L.d and 4.5 gSO(4)(2-)/L.d, gradual feeding did not favor sulfate removal, indicating that gradual feeding of the electron donor did not improve sulfate reduction. (C) 2011 Elsevier Ltd. All rights reserved.

On the use of reporter bacteria for measuring availability of organic contaminants

Natural environments are constantly challenged by the release of hydrophobic organic contaminants, which represent a threat for both the ecosystem and human health. Despite a substantial degradation by naturally occurring micro-organisms, a non negligible fraction of these pollutants tend to persist in soil and sediments due to their reduced accessibility to microbial degraders. This lack of 'bioavailability' is acknowledged as a key parameter for the natural and stimulated clean-up (bioremediation) of contaminated sites. We developed a bacterial bioreporter that responds to the presence of polyaromatic hydrocarbons (PAHs) by the production of the green fluorescent protein (GFP), based on the PAH-degrading bacterium Burkholderia sartisoli. We showed in this study that the bacterial biosensor B. sartisoli strain RP037 was faithfully reporting the degradation of naphthalene and phenanthrene (two PAHs of low molecular weight) via the production of GFP. What is more, the magnitude of GFP induction was influenced by change in the PAH flux triggered by a variety of physico-chemical parameters, such as the contact surface between the pollutant and the aqueous suspension. Further experiments permitted to test the influence of dissolved organic matter, which is an important component of natural habitats and can interact with organic pollutants. In addition, we tested the influence of two types of biosurfactants (tensio-active agents produced by living organisms) on phenanthrene's degradation by RP037. Interestingly, the surfactant's effects on the biodegradation rate appeared to depend on the type of biosurfactant and probably on the type of bacterial strain. Finally, we tagged B. sartisoli strain RP037 with a constitutively expressed mCherry fluorescent protein. The presence of mCherry allowed us to visualize the bacteria in complex samples even when GFP production was not induced. The new strain RP037-mChe embedded in a gel patch was used to detect PAH fluxes from a point source, such as a non-aqueous liquid or particles of contaminated soil. In parallel, we also developed and tested a so-called multiwell bacterial biosensor platform, which permitted the simultaneous use of four different reporter strains for the detection of major crude oil components (e.g., saturated hydrocarbons, mono- and polyaromatics) in aqueous samples. We specifically constructed the strain B. sartisoli RP007 (pPROBE-phn-luxAB) for the detection of naphthalene and phenanthrene. It was equipped with a reporter plasmid similar to the one in strain RP037, except that the gfp gene was replaced by the genes luxAB, which encoded the bacterial luciferase. The strain was implemented in the biosensor platform and detected an equivalent naphthalene concentration in oil spilled-sea water. We also cloned the gene for the transcriptional activator AlkS and the operator/promoter region of the operon alkSB1GHJ from the alkane-degrader bacterium Alcanivorax borkumensis strain SK2 in order to construct a new bacterial biosensor with higher sensitivity towards long-chain alkanes. However, the resulting strain showed no increased light emission in presence of tetradecane (C14), while it still efficiently reported low concentrations of octane (C8). RÉSUMÉ : Les écosystèmes naturels sont constamment exposés à nombre de contaminants organiques hydrophobes (COHs) d'origine industrielle, agricole ou même naturelle. Les COHs menacent à la fois l'environnement, le bien-être des espèces animales et végétales et la santé humaine, mais ils peuvent être dégradés par des micro-organismes tels que les bactéries et les champignons, qui peuvent être capables des les transformer en produits inoffensifs comme le gaz carbonique et l'eau. La biodégradation des COHs est cependant fréquemment limitée par leur pauvre disponibilité envers les organismes qui les dégradent. Ainsi, bien que la biodégradation opère partiellement, les COHs persistent dans l'environnement à de faibles concentrations qui potentiellement peuvent encore causer des effets toxiques chroniques. Puisque la plupart des COHs peuvent être métabolisés par l'activité microbienne, leur persistance a généralement pour origine des contraintes physico-chimiques plutôt que biologiques. Par exemple, leur solubilité dans l'eau très limitée réduit leur prise par des consommateurs potentiels. De plus, l'adsorption à la matière organique et la séquestration dans les micropores du sol participent à réduire leur disponibilité envers les microbes. Les processus de biodisponibilité, c'est-à-dire les processus qui gouvernent la dissolution et la prise de polluants par les organismes vivants, sont généralement perçus comme des paramètres clés pour la dépollution (bioremédiation) naturelle et stimulée des sites contaminés. Les hydrocarbures aromatiques polycycliques (HAPs) sont un modèle de COH produits par les activités aussi bien humaines que naturelles, et listés comme des contaminants chroniques de l'air, des sols et des sédiments. Ils peuvent être dégradés par un vaste nombre d'espèces bactériennes mais leur taux de biodégradation est souvent limité par les contraintes mentionnées ci-dessus. Afin de comprendre les processus de biodisponibilité pour les cellules bactériennes, nous avons décidé d'utiliser les bactéries elles-mêmes pour détecter et rapporter les flux de COH. Ceci a été réalisé par l'application d'une stratégie de conception visant à produire des bactéries `biocapteurs-rapporteurs', qui littéralement s'allument lorsqu'elles détectent un composé cible pour lequel elles ont été conçues. En premier lieu, nous nous sommes concentrés sur Burkholderia sartisoli (souche RP007), une bactérie isolée du sol et consommatrice de HAP .Cette souche a servi de base à la construction d'un circuit génétique permettant la formation de la protéine autofluorescente GFP dès que les cellules détectent le naphtalène ou le phénanthrène, deux HAP de faible masse moléculaire. En effet, nous avons pu montrer que la bactérie obtenue, la souche RP037 de B. sartisoli, produit une fluorescence GFP grandissante lors d'une exposition en culture liquide à du phénanthrène sous forme cristalline (0.5 mg par ml de milieu de culture). Nous avons découvert que pour une induction optimale il était nécessaire de fournir aux cellules une source additionnelle de carbone sous la forme d'acétate, ou sinon seul un nombre limité de cellules deviennent induites. Malgré cela, le phénanthrène a induit une réponse très hétérogène au sein de la population de cellules, avec quelques cellules pauvrement induites tandis que d'autres l'étaient très fortement. La raison de cette hétérogénéité extrême, même dans des cultures liquides mélangées, reste pour le moment incertaine. Plus important, nous avons pu montrer que l'amplitude de l'induction de GFP dépendait de paramètres physiques affectant le flux de phénanthrène aux cellules, tels que : la surface de contact entre le phénanthrène solide et la phase aqueuse ; l'ajout de surfactant ; le scellement de phénanthrène à l'intérieur de billes de polymères (Model Polymer Release System) ; la dissolution du phénanthrène dans un fluide gras immiscible à l'eau. Nous en avons conclu que la souche RP037 détecte convenablement des flux de phénantrène et nous avons proposé une relation entre le transfert de masse de phénanthrène et la production de GFP. Nous avons par la suite utilisé la souche afin d'examiner l'effet de plusieurs paramètres chimiques connus dans la littérature pour influencer la biodisponibilité des HAP. Premièrement, les acides humiques. Quelques rapports font état que la disponibilité des HAP pourrait être augmentée par la présence de matière organique dissoute. Nous avons mesuré l'induction de GFP comme fonction de l'exposition des cellules RP037 au phénanthrène ou au naphtalène en présence ou absence d'acides humiques dans la culture. Nous avons testé des concentrations d'acides humiques de 0.1 et 10 mg/L, tandis que le phénanthrène était ajouté via l'heptamethylnonane (HMN), un liquide non aqueux, ce qui au préalable avait produit le plus haut flux constant de phénanthrène aux cellules. De plus, nous avons utilisé des tests en phase gazeuse avec des concentrations d'acides humiques de 0.1, 10 et 1000 mg/L mais avec du naphtalène. Contrairement à ce que décrit la littérature, nos résultats ont indiqué que dans ces conditions l'expression de GFP en fonction de l'exposition au phénanthrène dans des cultures en croissance de la souche RP037 n'était pas modifiée par la présence d'acides humiques. D'un autre côté, le test en phase gazeuse avec du naphtalène a montré que 1000 mg/L d'acides humiques abaissent légèrement mais significativement la production de GFP dans les cellules de RP037. Nous avons conclu qu'il n'y a pas d'effet général des acides humiques sur la disponibilité des HAP pour les bactéries. Par la suite, nous nous sommes demandé si des biosurfactants modifieraient la disponibilité du phénanthrène pour les bactéries. Les surfactants sont souvent décrits dans la littérature comme des moyens d'accroître la biodisponibilité des COHs. Les surfactants sont des agents tensio-actifs qui augmentent la solubilité apparente de COH en les dissolvant à l'intérieur de micelles. Nous avons ainsi testé si des biosurfactants (des surfactants produits par des organismes vivants) peuvent être utilisé pour augmenter la biodisponibilité du phénanthrène pour la souche B. sartisoli RP037. Premièrement, nous avons tenté d'obtenir des biosurfactants produits par une autre bactérie vivant en co-culture avec les biocapteurs bactériens. Deuxièmement, nous avons utilisé des biosurfactants purifiés. La co-cultivation en présence de la bactérie productrice de lipopeptide Pseudomonas putida souche PCL1445 a augmenté l'expression de GFP induite par le phénanthrène chez B. sartisoli en comparaison des cultures simples, mais cet effet n'était pas significativement différent lorsque la souche RP037 était co-cultivée avec un mutant de P. putida ne produisant pas de lipopeptides. L'ajout de lipopeptides partiellement purifiés dans la culture de RP037 a résulté en une réduction de la tension de surface, mais n'a pas provoqué de changement dans l'expression de GFP. D'un autre côté, l'ajout d'une solution commerciale de rhamnolipides (un autre type de biosurfactants produits par Pseudomonas spp.) a facilité la dégradation du phénanthrène par la souche RP037 et induit une expression de GFP élevée dans une plus grande proportion de cellules. Nous avons ainsi conclu que les effets des biosurfactants sont mesurables à l'aide de la souche biocapteur, mais que ceux-ci sont dépendants du type de surfactant utilisé conjointement avec le phénanthrène. La question suivante que nous avons abordée était si les tests utilisant des biocapteurs peuvent être améliorés de manière à ce que les flux de HAP provenant de matériel contaminé soient détectés. Les tests en milieu liquide avec des échantillons de sol ne fournissant pas de mesures, et sachant que les concentrations de HAP dans l'eau sont en général extrêmement basses, nous avons conçu des tests de diffusion dans lesquels nous pouvons étudier l'induction par les HAPs en fonction de la distance aux cellules. Le biocapteur bactérien B. sartisoli souche RP037 a été marqué avec une seconde protéine fluorescente (mCherry), qui est constitutivement exprimée dans les cellules et leur confère une fluorescence rouge/rose. La souche résultante RP037-mChe témoigne d'une fluorescence rouge constitutive mais n'induit la fluorescence verte qu'en présence de naphtalène ou de phénanthrène. La présence d'un marqueur fluorescent constitutif nous permet de visualiser les biocapteurs bactériens plus facilement parmi des particules de sol. Un test de diffusion a été conçu en préparant un gel fait d'une suspension de cellules mélangées à 0.5 % d'agarose. Des bandes de gel de dimensions 0.5 x 2 cm x 1 mm ont été montées dans des chambres d'incubation et exposées à des sources de HAP (soit dissouts dans du HMN ou en tant que matériel solide, puis appliqués à une extrémité de la bande). En utilisant ce montage expérimental, le naphtalène ou le phénanthrène (dissouts dans du HMN à une concentration de 2.5 µg/µl) ont induit un gradient d'intensité de fluorescence GFP après 24 heures d'incubation, tandis que la fluorescence mCherry demeurait comparable. Un sol contaminé par des HAPs (provenant d'un ancien site de production de gaz) a induit la production de GFP à un niveau comparable à celui du naphtalène. Des biocapteurs bactériens individuels ont également détecté un flux de phénanthrène dans un gel contenant des particules de sol amendées avec 1 et 10 mg/g de phénanthrène. Ceci a montré que le test de diffusion peut être utilisé pour mesurer des flux de HAP provenant de matériel contaminé. D'un autre côté, la sensibilité est encore très basse pour plusieurs sols contaminés, et l'autofluorescence de certains échantillons rend difficile l'identification de la réponse de la GFP chez les cellules. Pour terminer, un des points majeurs de ce travail a été la production et la validation d'une plateforme multi-puits de biocapteurs bactériens, qui a permis l'emploi simultané de plusieurs souches différentes de biocapteurs pour la détection des constituants principaux du pétrole. Pour cela nous avons choisi les alcanes linéaires, les composés mono-aromatiques, les biphényls et les composés poly-aromatiques. De plus, nous avons utilisé un capteur pour la génotoxicité afin de détecter la `toxicité globale' dans des échantillons aqueux. Plusieurs efforts d'ingénierie ont été investis de manière à compléter ce set. En premier lieu, chaque souche a été équipée avec soit gfp, soit luxAB en tant que signal rapporteur. Deuxièmement, puisqu'aucune souche de biocapteur n'était disponible pour les HAP ou pour les alcanes à longues chaînes, nous avons spécifiquement construit deux nouveaux biocapteurs. L'un d'eux est également basé sur B. sartisoli RP007, que nous avons équipé avec le plasmide pPROBE-phn-luxAB pour la détection du naphtalène et du phénanthrène mais avec production de luciférase bactérienne. Un autre est un nouveau biocapteur bactérien pour les alcanes. Bien que nous possédions une souche Escherichia coli DHS α (pGEc74, pJAMA7) détectant les alcanes courts de manière satisfaisante, la présence des alcanes à longues chaînes n'était pas rapportée efficacement. Nous avons cloné le gène de l'activateur transcriptionnel A1kS ainsi que la région opérateur/promoteur de l'opéron alkSB1GHJ chez la bactérie dégradant les alcanes Alcanivorax borkumensis souche SK2, afin de construire un nouveau biocapteur bactérien bénéficiant d'une sensibilité accrue envers les alcanes à longues chaînes. Cependant, la souche résultante E. coli DHSα (pAlk3} n'a pas montré d'émission de lumière augmentée en présence de tétradécane (C14), tandis qu'elle rapportait toujours efficacement de basses concentrations d'octane (C8). De manière surprenante, l'utilisation de A. borkumensis en tant que souche hôte pour le nouveau plasmide rapporteur basé sur la GFP a totalement supprimé la sensibilité pour l'octane, tandis que la détection de tétradécane n'était pas accrue. Cet aspect devra être résolu dans de futurs travaux. Pour calibrer la plateforme de biocapteurs, nous avons simulé une fuite de pétrole en mer dans une bouteille en verre ouverte de 5L contenant 2L d'eau de mer contaminée avec 20 ml (1%) de pétrole brut. La phase aqueuse a été échantillonée à intervalles réguliers après la fuite durant une période allant jusqu'à une semaine tandis que les principaux contaminants pétroliers étaient mesurés via les biocapteurs. L'émission de bioluminescence a été mesurée de manière à déterminer la réponse des biocapteurs et une calibration intégrée faite avec des inducteurs types a servi à calculer des concentrations d'équivalents inducteurs dans l'échantillon. E. coli a été utilisée en tant que souche hôte pour la plupart des spécificités des biocapteurs, à l'exception de la détection du naphtalène et du phénanthrène pour lesquels nous avons utilisé B. sartisoli. Cette souche, cependant, peut être employée plus ou moins selon la même procédure. Il est intéressant de noter que le pétrole répandu a produit une apparition séquentielle de composés dissouts dans la phase aqueuse, ceux-ci .étant détectables par les biocapteurs. Ce profil contenait d'abord les alcanes à courtes chaînes et les BTEX (c'est-à dire benzène, toluène, éthylbenzène et xylènes), apparaissant entre des minutes et des heures après que le pétrole a été versé. Leurs concentrations aqueuses ont par la suite fortement décru dans l'eau échantillonnée après 24 heures, à cause de la volatilisation ou de la biodégradation. Après quelques jours d'incubation, ces composés sont devenus indétectables. Les HAPs, en revanche, sont apparus plus tard que les alcanes et les BTEX, et leur concentration a augmenté de pair avec un temps d'incubation prolongé. Aucun signal significatif n'a été mis en évidence avec le biocapteur pour le biphényl ou pour la génotoxicité. Ceci démontre l'utilité de ces biocapteurs, spécifiquement pour la détection des composés pétroliers, comprenant les alcanes à courtes chaînes, les BTEX et les HAPs légers.

High voltage discharge for degradation of organic contaminants in water

The pulsed dielectric barrier discharge (PDBD) and pulsed corona discharge (PCD) were compared for their efficiency to degrade phenol in water solution. Results show that PCD has higher efficiency than PDBD to degrade phenol. When initial pH of water solution was elevated, phenol degradation in the PCD reactor was significantly enhanced, although no considerable effect was seen in the PDBD reactor. The PCD reactor was also able to degrade lignin significantly, both in synthetically prepared solution and in pulp and paper mill wastewater. Water temperature did not affect phenol degradation; however, lignin was better oxidized at lower temperature.

Performance of an anaerobic-aerobic reactor and kinetic study of organic matter removal of cattle slaughterhouse effluent

This paper sought to evaluate the behavior of an upflow Anaerobic-Aerobic Fixed Bed Reactor (AAFBR) in the treatment of cattle slaughterhouse effluent and determine apparent kinetic constants of the organic matter removal. The AAFBR was operated with no recirculation (Phase I) and with 50% of effluent recirculation (Phase II), with θ of 11h and 8h. In terms of pH, bicarbonate alkalinity and volatile acids, the results indicated the reactor ability to maintain favorable conditions for the biological processes involved in the organic matter removal in both operational phases. The average removal efficiencies of organic matter along the reactor height, expressed in terms of raw COD, were 49% and 68% in Phase I and 54% and 86% in Phase II for θ of 11h and 8h, respectively. The results of the filtered COD indicated removal efficiency of 52% and k = 0.0857h-1 to θ of 11h and 42% and k = 0.0880h-1 to θ of 8h in the Phase I. In Phase II, the removal efficiencies were 59% and 51% to θ of 11h and 8h, with k = 0.1238h-1 and k = 0.1075 h-1, respectively. The first order kinetic model showed good adjustment and described adequately the kinetics of organic matter removal for θ of 11h, with r² equal to 0.9734 and 0.9591 to the Phases I and II, respectively.

Pesticides and other micro-organic contaminants in freshwater sedimentary environments - a review

A wide range of issues relating to the presence and fate of pesticides and other micro-organic contaminants (MOCs) in surface freshwater sedimentary environments is reviewed. These issues include the sources, transport and occurrence of MOCs in freshwater environments; their ecological effects; their interaction with sedimentary material; and a range of processes related to their fate, including degradation, diffusion in bed sediments, bioturbation and slow contaminant release. An emphasis is placed on those processes-chemical, physical or biological-in which sediments play a role in determining the fate of micro-organics in freshwater environments. The issues of occurrence, source and transport, and the ecological effects of micro-organics are introduced more briefly, the focus where these aspects are concerned being largely on pesticides. In the concluding section, key points and issues relating to the study of micro-organics in freshwater environments are summarised and areas where initial or further research would be welcome are highlighted. It is hoped that this paper will both form a useful reference for workers in the field of micro-organic contaminants, and also stimulate new work in the freshwater environment and beyond. (C) 2003 Elsevier Science Ltd. All rights reserved.

Phylogenetic variation in the tolerance and uptake of organic contaminants

An investigation into the phylogenetic variation of plant tolerance and the root and shoot uptake of organic contaminants was undertaken. The aim was to determine if particular families or genera were tolerant of, or accumulated organic pollutants. Data were collected from sixty-nine studies. The variation between experiments was accounted for using a residual maximum likelihood analysis to approximate means for individual taxa. A nested ANOVA was subsequently used to determine differences at a number of differing phylogenetic levels. Significant differences were observed at a number of phylogenetic levels for the tolerance to TPH, the root concentration factor and the shoot concentration factor. There was no correlation between the uptake of organic pollutants and that of heavy metals. The data indicate that plant phylogeny is an important influence on both the plant tolerance and uptake of organic pollutants. If this study can be expanded, such information can be used when designing plantings for phytoremediation or risk reduction during the restoration of contaminated sites.

Pesticides and other micro-organic contaminants in freshwater sedimentary environments - a review

A wide range of issues relating to the presence and fate of pesticides and other micro-organic contaminants (MOCs) in surface freshwater sedimentary environments is reviewed. These issues include the sources, transport and occurrence of MOCs in freshwater environments; their ecological effects; their interaction with sedimentary material; and a range of processes related to their fate, including degradation, diffusion in bed sediments, bioturbation and slow contaminant release. An emphasis is placed on those processes-chemical, physical or biological-in which sediments play a role in determining the fate of micro-organics in freshwater environments. The issues of occurrence, source and transport, and the ecological effects of micro-organics are introduced more briefly, the focus where these aspects are concerned being largely on pesticides. In the concluding section, key points and issues relating to the study of micro-organics in freshwater environments are summarised and areas where initial or further research would be welcome are highlighted. It is hoped that this paper will both form a useful reference for workers in the field of micro-organic contaminants, and also stimulate new work in the freshwater environment and beyond. (C) 2003 Elsevier Science Ltd. All rights reserved.

New materials based on modified synthetic Nb2O5 as photocatalyst for oxidation of organic contaminants

Conselho Nacional de Desenvolvimento Científico e Tecnológico (CNPq)

Hydrogen and Methane Production, Energy Recovery, and Organic Matter Removal from Effluents in a Two-Stage Fermentative Process

This study evaluates the potential for using different effluents for simultaneous H-2 and CH4 production in a two-stage batch fermentation process with mixed microflora. An appreciable amount of H-2 was produced from parboiled rice wastewater (23.9 mL g(-1) chemical oxygen demand [COD]) and vinasse (20.8 mL g(-1) COD), while other effluents supported CH4 generation. The amount of CH4 produced was minimum for sewage (46.3 mL g(-1) COD), followed by parboiled rice wastewater (115.5 mL g(-1) COD) and glycerol (180.1 mL g(-1) COD). The maximum amount of CH4 was observed for vinasse (255.4 mL g(-1) COD). The total energy recovery from vinasse (10.4 kJ g(-1) COD) corresponded to the maximum COD reduction (74.7 %), followed by glycerol (70.38 %, 7.20 kJ g(-1) COD), parboiled rice wastewater (63.91 %, 4.92 kJ g(-1) COD), and sewage (51.11 %, 1.85 kJ g(-1) COD). The relatively high performance of vinasse in such comparisons could be attributed to the elevated concentrations of macronutrients contained in raw vinasse. The observations are based on kinetic parameters of H-2 and CH4 production and global energy recovery of the process. These observations collectively suggest that organic-rich effluents can be deployed for energy recovery with sequential generation of H-2 and CH4.

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.

Guide to cleaner technologies : organic coating removal.

"February 1994."