Cette étude vise à développer un système de dépollution d'eau et de sédiments viticoles. Le glyphosate, diuron et 3,4-dichloroaniline (3,4-DCA) sont considérés, en tenant compte de la charge en cuivre. L'augmentation du temps de séjour des polluants dans le système et le choix de la bioaugmentation couplée à la phytoremédiation est la stratégie retenue. Chaque composante d'un triplet « sorbant-inoculum bactérien-plante » a été sélectionnée en laboratoire et le triplet mis en œuvre en microcosmes en conditions partiellement contrôlées. La sélection de matériaux sorbants dans différentes matrices liquides en présence des polluants seuls ou en mélange montre que les capacités de sorption des différents matériaux testés varient selon le polluant, sa formulation (seul ou en mélange) et la matrice liquide. Le sédiment se révèle être le meilleur sorbant pour le glyphosate ; le sable pour le diuron et le 3,4-DCA. Les performances de dissipation des colonies tolérantes isolées varient fortement selon le polluant. Le consortium sélectionné pour le procédé dissipe le glyphosate, le diuron et le 3,4-DCA en milieu liquide et complexe par ailleurs le cuivre. L'expérience en microcosmes montre que le temps de rétention hydraulique influe sur l'efficacité du système et que les matériaux sorbants sont efficaces. De plus les performances de dissipation atteintes sont bonnes. L'effet de la bioaugmentation sur les performances de dissipation n'est pas significatif pour le glyphosate et le 3,4-DCA, mais améliore en moyenne la dissipation du diuron. Un temps d'action prolongé dans la matrice solide s'avère nécessaire pour obtenir une bonne efficacité du procédé.

Coordenação de Aperfeiçoamento de Pessoal de Nível Superior / Agro-industrial effluents are capable of causing great impact on water bodies if released without adequate treatment. The removal of the organic load in the conventional biological treatments is achieved with high generation of sludge and energy consumption. The usual techniques of biological removal of nitrogen load demand high deployment and maintenance costs in wastewater treatment units. Seeking the development of a technology that can be employed in treatment units already in operation without high costs of installation and operation, an anaerobic and aerobic reactor using the technique of bioaugmentation and a fixed bed reactor for nitrification were built in scalebench. Real effluent was collected from a meat packing company and microorganisms of high rate of consumption for bioaugmentation were purchased commercially. The biological system was operated continuously with the anaerobic and aerobic reactor in sequence and with recirculation of supernatant from the anaerobic reactor to the nitrifying one. After percolating in the nitrifying reactor, the supernatant was drained back to the bottom of the anaerobic reactor, so that came in contact with the clay formed the bottom of it, making possible the denitrification of nitrogen compounds. Assays were performed under two conditions of flow rate: 2.5 and 5.0 L/day, resulting in organic loading conditions (COA) corresponding to 3.7 and 19.6 gDQOsolúvel/day under constant temperature of 30°C. The anaerobic reactor was evaluated at temperatures of 20 and 30ºC. The nitrification system was tested only for 19.6 gDQOsolúvel/day condition of load. The variations of chemical oxygen demand (COD), soluble COD, NH3, turbidity and suspended solids in each reactor and in the whole system were analized. Were obtained removal of 76.9% soluble COD in the system to the condition of lower COA and 71.1% to 19.6 gDQOsolúvel/day. The microorganisms tested presented solids generation rate (μ) from 0.035 to 0.19 gSSV/gSSV*day, these values are about 10 times lower than those reported for systems without bioaugmentation. The coefficients of biomass growth (Y) and maximum specific substrate consumption (k) were close to those systems without use of the bioaugmentation, indicating that the main advantage of this technique is the lower generation of sludge. It was found that the anaerobic system with bioaugmentation is more resistant to temperature changes compared to the usual system as to reduce the temperature 10°C, there was a reduction of only 27.6% for COD removal. The removal efficiency of NH3 in the system before and after use of the nitrifying reactor was 38.8 and 62%, respectively, indicating that binding of recirculation of the supernatant of the anaerobic reactor to a nitrification reactor designed specifically to allow removing the ammonia load in the effluent. / Efluentes agroindustriais são capazes de causar grande impacto em corpos d água se lançados sem tratamento adequado. A remoção da carga orgânica nos tratamentos biológicos convencionais é conseguida com elevada geração de lodo residual e consumo energético. As técnicas usuais de remoção biológica da carga nitrogenada demandam altos custos com implantação e manutenção nas unidades de tratamento de efluentes. Buscando o desenvolvimento de uma tecnologia que possa ser empregada em unidades de tratamento já em funcionamento sem elevados custos de instalação e operação, um reator aeróbio e um anaeróbio com uso da técnica da bioaumentação e um reator para nitrificação de leito fixo foram construídos em escala de bancada. Efluente real foi coletado de uma empresa frigorífica e microrganismos de alta taxa de consumo para a bioaumentação foram adquiridos comercialmente. O sistema biológico foi operado de forma contínua, com o reator anaeróbio e aeróbio em sequência e com recirculação do sobrenadante do anaeróbio ao reator nitrificante. Após percolar no reator nitrificante, este sobrenadante era drenado de volta ao fundo do reator anaeróbio, de forma com que entrasse em contato com o lodo formado ao fundo do mesmo e possibilitasse e denitrificação dos compostos nitrogenados. Os ensaios foram realizados sob duas condições de vazão: 2,5 e 5,0 L/dia, que resultaram em condições de carga orgânica aplicada (COA) correspondentes a 3,7 e 19,6 gDQOsolúvel/dia e sob temperatura mantida constante em 30ºC. O reator anaeróbio foi avaliado sob as temperaturas de 20 e 30ºC. O sistema de nitrificação foi testado somente para a condição de 19,6 gDQOsolúvel/dia de carga. Foram avaliadas as variações nos teores de DQO, DQO solúvel, NH3, turbidez e sólidos suspensos em cada reator e no sistema todo. Obteve-se até 76,9% de remoção de DQO solúvel no sistema para a condição de COA mais baixa e 71,1% para COA de 19,6 gDQOsolúvel/dia. Os microrganismos testados apresentaram taxa de geração de sólidos de 0,035 a 0,19 gSSV/gSSV*dia, valores estes em torno de 10 vezes menor que os reportados para sistemas sem bioaumentação. Os coeficientes de crescimento de biomassa (Y) e de taxa máxima específica de consumo de substrato (k) ficaram próximos aos valores para sistemas sem uso da bioaumentação, indicando que a principal vantagem do uso desta técnica está na baixa geração de lodo. Verificou-se que o sistema anaeróbio bioaumentado resiste melhor a variações de temperatura frente aos sistemas usuais, pois para redução de 10ºC na temperatura, observou-se a redução de apenas 27,6% na remoção de DQO. A eficiência de remoção de NH3 no sistema antes e depois da utilização do reator nitrificante em paralelo foi de 38,8 e 62%, respectivamente, indicando que a ligação do sistema de recirculação do sobrenadante do reator anaeróbio até um reator desenvolvido especificamente para nitrificação possibilita a remoção da carga amoniacal do efluente.

O óleo lubrificante mineral é amplamente utilizado no cenário mundial no funcionamento de máquinas e motores. No entanto, o ciclo de vida deste petro-derivado resulta na geração de um resíduo (óleo lubrificante usado), o qual é nocivo ao meio ambiente quando não descartado adequadamente ou reciclado. No Brasil, apesar das normas que tratam especificamente do armazenamento, recolhimento e destino de óleo lubrificante usado, grande parte do mesmo ainda é despejado diretamente no meio ambiente, sem qualquer tratamento, sendo de grande importância estudos que visem o entendimento dos processos e o desenvolvimento de tecnologias de remediação de áreas contaminadas por esse resíduo. O objetivo geral do presente trabalho foi conduzir estudos de tratabilidade de solo arenoso contaminado experimentalmente com 5% (m m-1 seco) de óleo lubrificante usado, através de duas diferentes estratégias de biorremediação: bioestímulo e bioaumento. Foram conduzidos dois experimentos. No primeiro, foi avaliada a atividade microbiana aeróbia na biodegradação do OLU através do método respirométrico de Bartha. No segundo, foram montados três biorreatores de fase sólida simulando biopilhas estáticas com aeração forçada, cada um contendo 125 kg de solo e 5% (m m-1 seco) de óleo lubrificante automotivo usado, os quais receberam como tratamento: bioestímulo por ajuste de pH e umidade (BIOSca); bioestímulo por ajuste de pH e umidade associado ao bioaumento com a adição de composto maduro (BIOA1ca) ; e bioestímulo por ajuste de pH e umidade associado ao bioaumento com a adição de composto jovem (BIOA2ca). Foram também montados três biorreatores de bancada simulando biopilhas estáticas sem aeração forçada, cada um contendo 3 kg de solo e 5% (m m-1) do mesmo contaminante, sendo que o primeiro continha solo sem contaminação - CONTsa, o segundo, solo contaminado com ajuste de pH BIOSsa e o terceiro, solo contaminado com adição de 0,3% de azida sódica - ABIOsa. Os tratamentos foram avaliados pela remoção de hidrocarbonetos totais de petróleo (HTPs) e após 120 dias de experimento obteve-se remoções de HTPs de 84,75%, 99,99% e 99,99%, com BIOS, BIOA1 e BIOA2, respectivamente, demonstrando que a estratégia de bioestímulo associada ao bioaumento foram promissoras na remediação do solo contaminado pelo óleo lubrificante usado. Os tratamentos que receberam composto (BIOA1 e BIOA2) não apresentaram diferenças quanto à remoção de HTPs, evidenciando que a fase de maturação dos compostos não apresentou influência na eficiência do processo. No entanto, verificou-se uma eficiência nos tratamentos que receberam composto quando comparado ao tratamento sem adição de composto / Lubricating oil is worldwide in machinery and motors. The life-cycle of this petroleum-based product generates a waste, the spent lubricating oil SLO, which is hazardous to the environment when inappropriately disposed. In Brazil, regardless the norms that establish rules for storage, collection, recycling and final disposal of spent-lubricating oil, a large part of it ends up in different environment compartments, causing among others, soil contamination. Therefore, it is important to carry out studies focusing on processes and technology development for remediation of sites contaminated by SLO. The objective of this work was to carry out two experiments of treatability studies for sandy soil contaminated experimentally with 5% (weight/dry weight) of SLO, through two different bioremediation strategies: biostimulation and bioaugmentation. During the first experiment, the aerobic microbial activity in SLO-contaminated soil was assessed through Barthas respirometry (CO2 productino). During the second experiment, three reactors simulating static biopiles with forced (up-flow) aeration received 125 kg of soil contaminated with 5% (w/dw) SLO, which received the following treatments: pH and moisture adjustment-BIOSca; pH and moisture adjustment associated to bioaugmentation through addition of mature compost from urban solid waste-BIOA1ca and pH and moisture adjustment associated to bioaugmentation with non-mature compost-BIOA2ca. Another group of three bench reactors with no forced aeration, each one containing 3 kg of soil also contaminated with 5% (w/dw) of SLO were filled as following: the first received non-contaminated soil-CONTsa; the second received contaminated soil with pH adjustment-BIOSsa; the third one received contaminated soil with addition of 0.3% (w/dry w) of sodium azide-ABIOsa. The treatments were compared based on removal of total petroleum hydrocarbons (TPHs) and its fractions. After 120 days, the TPH removal was about 75%, 99.99% and 99.99% in BIOS, BIOA1 and BIOA2 respectively, suggesting that optimization of conditions associated to bioaugmentation were the most promising strategy to treat SLO contaminated soils. The fact that after 120 days BIOA1 e BIOA2 did not present differences regarding TPH removal shows that giving time enough, the degree of the compost maturation does not influence the TPH removal. However, treatments that received compost were more efficient than biostimulation alone

As indústrias químicas são consideradas como o segmento industrial que gera os efluentes mais perigosos ao meio ambiente. Em virtude das concentrações expressivas de poluentes, tanto orgânicos quanto inorgânicos, os efluentes dessas indústrias podem interferir na atividade da biomassa de estações de tratamento de efluentes (E.T.E.), diminuindo sua eficiência e gerando efluentes tratados, porém em desacordo com a legislação pertinente. Para prevenir tais efeitos, o recebimento de efluentes industriais em E.T.E.s pode ser precedido por pré-tratamento, dentre os quais, o biológico, otimizado pela adição de microrganismos com capacidade de degradar poluentes. Foram isolados microrganismos com capacidade de degradar os compostos identificados como responsáveis pela toxicidade do efluente final da E.T.E.: benzeno, clorofórmio, 1,2-dicloroetano, pentaclorofenol, tricloroeteno, tolueno e p-xileno. Foram realizados testes de bioaumentação para pré tratar o efluente industrial, que foram avaliados através de ensaios físico-químicos e de toxicidade aguda para Vibrio fischeri e Daphnia similis. Os resultados obtidos demonstraram que o pré tratamento reduziu a toxicidade do efluente final da estação de tratamento. / Chemical industries are considered the industrial sector that generates the most dangerous effluents to the environment. Due to the high pollutant concentration, either organics or inorganics, the chemical industries effluents may interferer in the biomass activity in wastewater treatment plants (WWTP), what may reduce its efficiency and generate treated effluents in disagreement to the concerned law. In order to prevent such effects, the industrial effluents disposal in WWTPs can be preceded by biological pretreatment, which can be optimized by adding microorganisms capable of pollutants degradation. Microorganism strains that are able to degrade the compounds identified as the responsible for toxicity levels in the WWTP final effluent: benzene, chloroform, 1,2-dichloroethane, pentachlorophenol, trichloroethene, tolune and p-xylene were isolated. Bioaugmentation tests aiming the chemical effluent pretreatment were performed and they were evaluated through physical-chemical analysis and acute toxicity tests for Vibrio fischeri and Daphnia similis. The results showed that the industrial effluent pretreatment reduced the toxicity levels in the WWTP final effluent.

This study was done to determine the effectiveness of a commercially available bioaugmentation product, BiOWiSHTM-Aqua FOG, for remediating petroleum-contaminated sandy soil. Biodegradation enhancement by BiOWiSHTM-Aqua FOG was evaluated in laboratory microcosms by directly measuring total petroleum hydrocarbon (TPH) and indirectly using respirometry. Attempts were made to enrich hydrocarbon-degrading bacteria in BiOWiSHTM-Aqua FOG, and the resulting enrichment cultures were screened using respirometry as well. Potential hydrocarbon-degrading bacteria in BiOWiSHTM-Aqua FOG were isolated. Experiments were performed at bench-scale using microcosm bottles containing sand contaminated with either motor oil or No. 2 diesel fuel. The microcosms were incubated at 25oC under aerobic conditions. TPH measurements of soil in the microcosms at 0, 25 and 56 days indicated that the addition of 500-ppm BiOWiSHTM-Aqua FOG improved biodegradation of the motor oil-contaminated soil by 45%. However, BiOWiSHTM-Aqua FOG did not have a measurable effect on biodegradation in the diesel-contaminated soil. In the respirometry experiments, BiOWiSHTM-Aqua FOG and two hydrocarbon-enriched BiOWiSHTM-Aqua FOG cultures were evaluated indirectly by the measurement of microbial carbon dioxide production and oxygen uptake using a MicroOxymaxTM respirometer. The respirometry experiments showed that in the six-day period following motor oil-contamination of soil, the addition of BiOWiSHTM-Aqua FOG substantially improves biodegradation rates. The added organisms in the product out-performed the indigenous organisms in the 5-6 days following contamination of the soil. The CO2 production observed in the BiOWiSHTM microcosms contaminated with motor oil was much greater than CO2 production without motor oil, which confirms that the observed metabolism can be attributed to motor oil biodegradation rather than metabolism of other organic material in the soil. Enriched consortia consistently generated far less CO2 than microcosms with the 500 ppm BiOWiSHTM-Aqua FOG. Stoichiometric calculations suggested that BiOWiSHTM-Aqua FOG removed approximately 1400 ppm TPH (14%) from the soil in 6.5 days, while an enrichment culture of BiOWiSHTM-Aqua FOG only reduced TPH levels by 459 ppm (5%). This result suggests that increased biodegradation rate in bioaugmented soil is aided by biodiversity in the augmenting inoculum. A potential hydrocarbon-degrading candidate organism was isolated from the product and cultured on Bushnell-Haas agar and plate-count agar (PCA). While at least two distinct colony types were successfully grown on media with motor oil, these same colonies appeared on Bushnell-Haas agar with no apparent carbon source, and survived repeated transfers onto this same medium. Therefore, their status as hydrocarbon-degraders is inconclusive. More thorough enrichment work could be pursued, especially using soil samples collected from petroleum-contaminated sites.

No description available.

Le traitement des déchets alimentaires (FW) par digestion anaérobie peut conduire à une production d'énergie couplée à une réduction des émissions de volume et de gaz à effet de serre à partir de ce type de déchets. Néanmoins, l'obtention de la récupération du méthane la plus élevée possible dans un temps plus court avec un fonctionnement stable est difficile. Pour surmonter les obstacles de la MA de divers procédés de pré-traitement FW, la supplémentation en oligo-éléments, bioaugmentation utilisant la bouse des animaux de zoo et la comparaison des configurations de réacteurs, y compris une étape ou en deux réacteurs à cuve agités en continu (CSTR) et un réacteur à membrane anaérobie (AnMBR ) ont été étudiées dans le cadre de la présente recherche. Sur la base des résultats des expériences de traitement par lots, de pré-traitement thermique à 80 ° C pendant 1,5 heure cédés> 50% augmentation de la production de biométhane, et il a été trouvé à être plus économe en énergie que l'ozonation ou prétraitements de choc thermophiles. Parmi les différentes concentrations testées et les oligo-éléments, Fe (II) et Se (VI) des concentrations de 25 à 50 ug / L ont donné lieu à 39 et 35% d'augmentation de la production de biométhane, respectivement. Une meilleure solubilisation des protéines (6,96 ± 2,76% de plus) et de glucides récalcitrants (344,85 ± 54,31 mg / L par rapport à zéro) pourrait être obtenue avec bioaugmentation de girafe fumier (30% en volume), qui a donné un 11,24 ± 4,51% de plus production de biométhane. Un CSTR à deux étages avec digestat re-circulation de meilleurs résultats que d'un stade en raison de sa (i) une meilleure capacité d'auto-ajustement du pH; (ii) une plus grande résistance aux chocs de charge organique; (iii) de près de 100% de matières solides volatiles a été destryoed par rapport à 71% en CSTR une étape; (iv) 50 à 60% de teneur en méthane a été obtenu, alors qu'il était de 40 à 50% en une seule étape CSTR; (c) une petite quantité d'hydrogène a également été détectée à partir de la première étape du réacteur à deux étages qui en fait un système attrayant pour la production de biohythane. Bien que la séparation physique des méthanogènes rendus plus sensibles à des facteurs inhibiteurs, tels que l'ammonium et l'acide propionique. En outre, le temps de rétention hydraulique (HRT) est encore une chute de ces systèmes, d'où une AnMBR équipé d'une membrane de fluorure de vinylidène courant latéral a été proposé et exploité avec succès pour 100 d. Merci de membranes HRT a pu être réduite de 20 d à 1d, tout en conservant un rendement global d'élimination de> 97% de la demande en oxygène influent chimique (COD) et a abouti à une production de biogaz supérieure à 70% de teneur en méthane / Treatment of food waste by anaerobic digestion can lead to an energy production coupled to a reduction of the volume and greenhouse gas emissions from this waste type. Nevertheless, obtaining the highest possible methane recovery in a shorter time with a stable operation is challenging. To overcome the hurdles of AD of FW various pretreatment methods, supplementation of trace elements, bioaugmentation using zoo animals' dung and comparison of reactor configurations including one-stage and two-stage continuously stirred tank reactors (CSTR) as well as anaerobic membrane reactor (AnMBR) were studied in the scope of this research. Based on the results of the batch experiments, thermal pretreatment at 80°C for 1.5 hours yielded 46 – 52% higher biomethane production, and it is more energy efficient than ozonation or thermophilic shock pretreatments. Among the various tested concentrations and trace elements Fe (II) and Se (VI) concentrations of 25-50 ug/L resulted in 39 and 35% increase of biomethane production, respectively. A better solubilization of proteins (6.96 ± 2.76% more) and recalcitrant carbohydrates (344.85 ± 54.31 mg/L as compared to zero) could be obtained with bioaugmentation of giraffe dung (30% by volume), which yielded a 11.24 ± 4.51% higher biomethane production. A two-stage CSTR with digestate re-circulation performed better than one-stage with (i) a better pH self-adjusting capacity; (ii) a higher resistance to organic loading shocks; (iii) almost 100% volatile solids was destroyed as compared to 71% in one-stage CSTR; (iv) 50-60% methane content was obtained, while it was 40-50% in one-stage CSTR; (v) a small amount of hydrogen was also detected from the first stage of the two-stage reactor making it an attractive biohythane production system. Although physically separating the methanogens made them more sensitive to inhibitory factors, such as ammonium and propionic acid. Moreover, the long hydraulic retention time (HRT) is still the problem with these systems, hence an AnMBR equipped with a side-stream polyvinylidene fluoride membrane was proposed and a successful operation was achieved. Thanks to the membranes the HRT was able to be reduced from 20 d to 1d, while maintaining an overall removal efficiency of >97% of the influent chemical oxygen demand (COD) and yielded a higher biogas production with 70% methane content

No Brasil, a contaminação do solo por derramamentos de combustíveis representa um dos mais graves problemas ambientais e o impacto da introdução de novas misturas como diesel/biodiesel na matriz energética requer investigação quanto a tecnologias apropriadas de remediação. O presente estudo teve por objetivo avaliar diferentes estratégias de biorremediação no tratamento de solo contaminado experimentalmente com óleo diesel B5. Foram conduzidos três experimentos. No primeiro, quatro microcosmos em duplicata, contendo 500 g de solo e 5% (p/p) de óleo diesel B5, todos suplementados com oxigênio através de revolvimento manual e com ajuste de umidade, tiveram como tratamentos: bioestímulo com ajuste de pH (BE1); bioestímulo com ajuste de pH e nutrientes (BE2); bioaumento com ajuste de pH, nutrientes e adição de consórcio microbiano comercial KMA (BAM) e; controle abiótico, com ajuste de pH e solo esterilizado em autoclave (PA). Paralelamente, foi conduzido tratamento por bioaumento com ajuste de pH e nutrientes, suplementação de oxigênio e consórcio KMA, em solo contaminado apenas por diesel a 5% (BAD). A população microbiana foi monitorada através da contagem de UFC e os tratamentos, avaliados pela remoção de carbono orgânico e de hidrocarbonetos de petróleo (n-alcanos C10-C36). No segundo experimento, o metabolismo microbiano aeróbio foi avaliado através da produção de CO2 em respirômetros de Bartha (triplicatas), em solo contaminado com 5% (p/p) de óleo diesel B5, ajustado para pH e umidade, nas seguintes condições: solo com adição do consórcio KMA; solo com adição de cultura microbiana obtida a partir de outro solo proveniente de um posto de combustível com histórico de vazamento de tanques (RES) e; solo esterilizado por adição de azida de sódio a 0,3% (p/p). Como controle, solo sem contaminação, com sua população microbiana autóctone. No terceiro experimento, a capacidade da microbiota autóctone (EX), assim como do consórcio KMA e da cultura RES, em biodegradar óleo diesel B5, diesel e biodiesel de soja foi testada através do uso de indicadores de oxirredução DCPIP e TTC. Os experimentos em microcosmos indicam que houve uma complementaridade metabólica entre a população nativa e o consórcio comercial de microorganismos KMA, cuja presença promoveu um decaimento mais rápido de n-alcanos nas primeiras semanas do experimento. No entanto, após 63 dias de experimento, os tratamentos BAM, BAD e BE2 apresentaram, respectivamente, em média, 92,7%, 89,4% e 81,7% de remoção dos hidrocarbonetos n-alcanos C10-C36, sendo tais diferenças, sem significância estatística. Nos respirômetros, o bioaumento com cultura microbiana RES apresentou a maior produção de CO2 e a maior remoção de hidrocarbonetos (46,2%) após 29 dias. Tanto nos ensaios em microcosmos quanto nos respirométricos, não foi possível estimar a contribuição dos processos abióticos, tendo em vista evidências da existência de atividade microbiana no solo esterilizado térmica ou quimicamente. Os ensaios com os dois indicadores redox mostraram que apenas a microbiota nativa do solo em estudo e a cultura microbiana RES apresentaram potencial para degradar óleo diesel B5, biodiesel de soja ou diesel, quando colocadas em meio mineral contendo tais combustíveis como única fonte de carbono. / In Brazil, the contamination of soils due to spill of fuels is one of the most serious environmental problems. The impact of introducing new fuel mixtures in the energy matrix, such as diesel/biodiesel requires investigation regarding appropriate remediation technologies. The objective of this study was to assess different bioremediation strategies for treatment of soil spiked with diesel B5 (diesel plus 5% of biodiesel w/w). Three experiments were carried out. In the first, four microcosms (in duplicate), with 500g of soil and 5% (w/w) of diesel B5 each, being all of them supplied with oxygen by manual stirring and with moisture, performed the following treatments: bio-stimulation with pH adjustment (BE1); bio-stimulation with pH and nutrients (N, P) adjustment (BE2); bio-augmentation with pH and nutrients adjustment and addition of a commercial consortium of microorganisms KMA (BAM); abiotic processes control with pH adjustment and soil that underwent thermal sterilization (PA). As a control of the effect of biodiesel, a bio-augmentation treatment was carried out with pH and nutrients adjustment, oxygen supply and addition of KMA consortium, in soil contaminated only with diesel at 5% (w/w) (BAD). The microorganisms populations were monitored through colony-forming units CFU, and the treatment efficiency was estimated based on removal of total organic carbon (TOC) and petroleum hydrocarbon (n-alkanes C10-C36). In the second experiment, the microorganisms aerobic metabolism was assessed through measurement of the CO2 production in Barthas respirometers in triplicates, pH and moisture adjustment, under the following conditions: Contaminated soil inoculated with KMA consortium; contaminated soil inoculated with a microorganisms culture obtained from another soil excavated from a gas station with leaking from the tanks (RES); contaminated soil sterilized with sodium azide 0.3% (w/w) (PA). As a control, soil with no contamination and its indigenous microbiota was monitored. In the third experiment, the capacity of the indigenous microbiota (EX), as well as the consortia KMA and RES in biodegrading diesel B5 and pure biodiesel from soil-beans were assessed by using the oxi-reduction indicators DCPIP and TTC. The experiments in microcosms showed a higher percentage of decay in n-alkanes C10-C36 during the first weeks, in those microcosms where commercial consortium KMA was added, suggesting metabolic complementation between the indigenous and the KMA microbiota. However, after 63 days, the treatments BAM, BAD and BE2 showed respectively the average removal of 92.7%, 89.4% and 81.7% of n-alkanes C10-C36, been the differences statistically not significant. In both experiments (microcosms and Bartha respirometers) it was not possible to estimate the contribution of the abiotic processes alone, due to clear indication of microbiological activity in the soils that underwent thermal or chemical sterilization. In the Bartha respirometers, bio-augmentation with the RES culture presented higher CO2 production and the highest hydrocarbons removal (46.2%) after 29 days. The assays with the redox indicators showed that both the native microbiota of the soil and the RES microbial culture presented potential to degrade diesel B5, biodiesel and diesel, when placed in mineral media with these fuels as the only carbon source.

Les sols agricoles sont depuis de nombreuses années contaminés directement par apports d'intrants (pesticides, fertilisants) mais également de façon indirecte en raison de la proximité de certaines installations industrielles. Notre étude porte sur des sols agricoles à l'aval de la vallée de la Thur (Haut-Rhin), polycontaminés par du chrome (488 mg/kg), du mercure (13 mg/kg) et du plomb (381 mg/kg). La phytoextraction est une méthode innovante, employée pour ses propriétés respectueuses de la vie biologique du sol et son faible coût. La faible disponibilité des métaux dans le sol (notamment Cr, Hg et Pb), et par conséquent le temps de décontamination, constitue la principale limite de cette technique. La bioaugmentation couplée à la phytoremédiation (rhizoremédiation) est une technique récente qui a été testée pour cette étude de façon à accroître la vitesse de phytoextraction. Les résultats ont montré que les microorganismes producteurs de sidérophores, notamment les Pseudomonas, étaient potentiellement intéressants pour augmenter la mobilité du chrome et du plomb dans le sol. La production de sidérophores par des cellules libres ou immobilisées de Pseudomonas cultivées en présence de divers substrats carbonés a été optimisée. L'immobilisation des microorganismes dans des billes d'alginate de calcium enrichies en lait écrémé a montré que les microorganismes étudiés produisaient plus de sidérophores en présence de métaux et que leur survie dans le sol était accrue. Les billes de Ca-alginate adsorbent plus de 90% de Cr, Fe et Pb ainsi que plus de 40% de Hg, ce qui diminue la toxicité métallique pour les cellules libres ou immobilisées, et crée également un déficit en Fe dans les billes, stimulant ainsi la production de sidérophores par les microorganismes. Les microorganismes sélectionnés ont ensuite été inoculés dans le sol contaminé, cultivé avec du maïs comme plante modèle. La bioaugmentation des pots de sol avec Pseudomonas aeruginosa co-immobilisé dans des billes de Ca-alginate avec du lait écrémé a permis de multiplier le prélèvement de Cr par les feuilles de maïs par 5,4 et celui du Pb par 3,8 par rapport aux pots non bioaugmentés. L'inoculation du sol enrichi en lait écrémé avec des cellules libres de R. metallidurans a permis d'augmenter le rélèvement foliaire de Cr par 5,2.

No Brasil, a contaminação do solo por derramamentos de combustíveis representa um dos mais graves problemas ambientais e o impacto da introdução de novas misturas como diesel/biodiesel na matriz energética requer investigação quanto a tecnologias apropriadas de remediação. O presente estudo teve por objetivo avaliar diferentes estratégias de biorremediação no tratamento de solo contaminado experimentalmente com óleo diesel B5. Foram conduzidos três experimentos. No primeiro, quatro microcosmos em duplicata, contendo 500 g de solo e 5% (p/p) de óleo diesel B5, todos suplementados com oxigênio através de revolvimento manual e com ajuste de umidade, tiveram como tratamentos: bioestímulo com ajuste de pH (BE1); bioestímulo com ajuste de pH e nutrientes (BE2); bioaumento com ajuste de pH, nutrientes e adição de consórcio microbiano comercial KMA (BAM) e; controle abiótico, com ajuste de pH e solo esterilizado em autoclave (PA). Paralelamente, foi conduzido tratamento por bioaumento com ajuste de pH e nutrientes, suplementação de oxigênio e consórcio KMA, em solo contaminado apenas por diesel a 5% (BAD). A população microbiana foi monitorada através da contagem de UFC e os tratamentos, avaliados pela remoção de carbono orgânico e de hidrocarbonetos de petróleo (n-alcanos C10-C36). No segundo experimento, o metabolismo microbiano aeróbio foi avaliado através da produção de CO2 em respirômetros de Bartha (triplicatas), em solo contaminado com 5% (p/p) de óleo diesel B5, ajustado para pH e umidade, nas seguintes condições: solo com adição do consórcio KMA; solo com adição de cultura microbiana obtida a partir de outro solo proveniente de um posto de combustível com histórico de vazamento de tanques (RES) e; solo esterilizado por adição de azida de sódio a 0,3% (p/p). Como controle, solo sem contaminação, com sua população microbiana autóctone. No terceiro experimento, a capacidade da microbiota autóctone (EX), assim como do consórcio KMA e da cultura RES, em biodegradar óleo diesel B5, diesel e biodiesel de soja foi testada através do uso de indicadores de oxirredução DCPIP e TTC. Os experimentos em microcosmos indicam que houve uma complementaridade metabólica entre a população nativa e o consórcio comercial de microorganismos KMA, cuja presença promoveu um decaimento mais rápido de n-alcanos nas primeiras semanas do experimento. No entanto, após 63 dias de experimento, os tratamentos BAM, BAD e BE2 apresentaram, respectivamente, em média, 92,7%, 89,4% e 81,7% de remoção dos hidrocarbonetos n-alcanos C10-C36, sendo tais diferenças, sem significância estatística. Nos respirômetros, o bioaumento com cultura microbiana RES apresentou a maior produção de CO2 e a maior remoção de hidrocarbonetos (46,2%) após 29 dias. Tanto nos ensaios em microcosmos quanto nos respirométricos, não foi possível estimar a contribuição dos processos abióticos, tendo em vista evidências da existência de atividade microbiana no solo esterilizado térmica ou quimicamente. Os ensaios com os dois indicadores redox mostraram que apenas a microbiota nativa do solo em estudo e a cultura microbiana RES apresentaram potencial para degradar óleo diesel B5, biodiesel de soja ou diesel, quando colocadas em meio mineral contendo tais combustíveis como única fonte de carbono. / In Brazil, the contamination of soils due to spill of fuels is one of the most serious environmental problems. The impact of introducing new fuel mixtures in the energy matrix, such as diesel/biodiesel requires investigation regarding appropriate remediation technologies. The objective of this study was to assess different bioremediation strategies for treatment of soil spiked with diesel B5 (diesel plus 5% of biodiesel w/w). Three experiments were carried out. In the first, four microcosms (in duplicate), with 500g of soil and 5% (w/w) of diesel B5 each, being all of them supplied with oxygen by manual stirring and with moisture, performed the following treatments: bio-stimulation with pH adjustment (BE1); bio-stimulation with pH and nutrients (N, P) adjustment (BE2); bio-augmentation with pH and nutrients adjustment and addition of a commercial consortium of microorganisms KMA (BAM); abiotic processes control with pH adjustment and soil that underwent thermal sterilization (PA). As a control of the effect of biodiesel, a bio-augmentation treatment was carried out with pH and nutrients adjustment, oxygen supply and addition of KMA consortium, in soil contaminated only with diesel at 5% (w/w) (BAD). The microorganisms populations were monitored through colony-forming units CFU, and the treatment efficiency was estimated based on removal of total organic carbon (TOC) and petroleum hydrocarbon (n-alkanes C10-C36). In the second experiment, the microorganisms aerobic metabolism was assessed through measurement of the CO2 production in Barthas respirometers in triplicates, pH and moisture adjustment, under the following conditions: Contaminated soil inoculated with KMA consortium; contaminated soil inoculated with a microorganisms culture obtained from another soil excavated from a gas station with leaking from the tanks (RES); contaminated soil sterilized with sodium azide 0.3% (w/w) (PA). As a control, soil with no contamination and its indigenous microbiota was monitored. In the third experiment, the capacity of the indigenous microbiota (EX), as well as the consortia KMA and RES in biodegrading diesel B5 and pure biodiesel from soil-beans were assessed by using the oxi-reduction indicators DCPIP and TTC. The experiments in microcosms showed a higher percentage of decay in n-alkanes C10-C36 during the first weeks, in those microcosms where commercial consortium KMA was added, suggesting metabolic complementation between the indigenous and the KMA microbiota. However, after 63 days, the treatments BAM, BAD and BE2 showed respectively the average removal of 92.7%, 89.4% and 81.7% of n-alkanes C10-C36, been the differences statistically not significant. In both experiments (microcosms and Bartha respirometers) it was not possible to estimate the contribution of the abiotic processes alone, due to clear indication of microbiological activity in the soils that underwent thermal or chemical sterilization. In the Bartha respirometers, bio-augmentation with the RES culture presented higher CO2 production and the highest hydrocarbons removal (46.2%) after 29 days. The assays with the redox indicators showed that both the native microbiota of the soil and the RES microbial culture presented potential to degrade diesel B5, biodiesel and diesel, when placed in mineral media with these fuels as the only carbon source.