Quando as wetlands alcançam a máxima capacidade de tratamento para remover metais pesados, a remoção ainda pode ocorrer por precipitação na forma de sulfetos devido a redução biológica de sulfato. Para alcançar este objetivo, devem ser promovidas condições anaeróbias, uma fonte de sulfato deve existir e uma fonte adequada de carbono/energia deve estar presente. No presente trabalho, a macroalga Sargassum filipendula e bagaço de cana-de-açúcar (materiais lígneo-celulósicos) foram selecionados como fontes de carbono, devido ao seu acentuado conteúdo de compostos orgânicos de degradação lenta e serem resíduos de alta disponibilidade. Experimentos foram simultaneamente conduzidos em operação contínua em duas colunas (0,5 L cada), uma contendo a macroalga e/ou bagaço de cana-de-açúcar e a outra contendo os materiais inoculados com um lodo anaeróbio. Neste trabalho, foi estudada a remoção de cádmio e zinco, devido à presença deles em efluentes de operações de mineração/metalurgia. Os ensaios foram realizados sob três diferentes condições experimentais no que se refere à quantidade de lodo anaeróbio inoculado no reator e o material empregado como fonte de carbono/energia. Os resultados indicaram que o reator inoculado foi capaz de tratar o efluente mais eficientemente que o reator não inoculado, considerando o período dos testes / When wetlands reach maximum treatment capacity to remove heavy metals, removal can still take place through precipitation as sulphides, due to biological reduction of sulphate. To achieve this goal, anaerobic conditions must be attained, a sulphate source must exist, and an adequate carbon/energy source must be present. In the present work, the seaweed Sargassum filipendula and sugarcane bagasse (ligneous-cellulosic materials) have been selected as carbon sources, due to their high content of slow degradation organic compounds and high availability as waste materials. Experiments were simultaneously conducted in continuous operation in two columns (0.5 L each), one containing the seaweed and/or sugarcane bagasse and another containing the materials inoculated with an anaerobic sludge. In this work, the removal of cadmium and zinc was studied, due to their presence in effluents from mining/metallurgy operations. The rehearsals were accomplished under three different experimental conditions in what refers to the amount of anaerobic mud inoculated in the reactor and employed material as carbon/energy source. The results obtained indicated that the inoculated reactor was able to treat the effluent more efficiently than the non inoculated reactor, considering the time-course of the tests

This project was compiled in co-operation with the Royal Institute of Technology, Stockholm and Veolia Environmental Services (Australia) at the Woodlawn Bioreactor in NSW, Australia. Hydrogen sulphide is an unwanted component of landfill gas, raising occupational health and safety concerns, whilst leading to acid gas corrosion of power generation equipment and increased emissions of SOx, a primary constituent of acidification. Australian governmental requirements to place a periodic cover over the unused proportion of the tipping surface of landfills and bioreactors create an interesting opportunity for the removal of the hydrogen sulphide component of landfill gas. Using waste materials containing a high concentration of metals as waste cover can enhance the precipitation of sulphur in the form of metal sulphides. The reduction of sulphate via sulphate reducing bacteria is prevalent in sites that have a sizeable inflow of sulphate. The Woodlawn Bioreactor is located in an area where the influence of sulphate has a critical influence of bioreactor performance and production of hydrogen sulphide. Through a series of experimental bioreactors it was established that from the use of metalliferous periodic waste covers, the hydrogen sulphide component of landfill gas was maintained at an extremely low level when compared to the levels of hydrogen sulphide produced in waste under the influence of high sulphate loads with no waste cover. / www.ima.kth.se

Acid mine drainage (AMD) is a worldwide environmental problem associated with the mining wastes, generated from active and inactive mining sites from mineral processing activities. AMD is defined as the drainage that occurs as a result of oxidation of sulphide minerals/wastes/tailings when exposed to air and water in the presence of chemolithotrophs namely the Acidithiobacillus sp. AMD is characterised by low pH and increased acidity due to elevated heavy metals and sulphate concentration. The acid production potential was carried out for sulphide minerals such as pyrite and chalcopyrite and copper tailings sample in the absence and presence of bacteria namely Acidithiobacillus ferrooxidans and Acidithiobacillus thiooxidans. Acidity was generated in all the cases due to the oxidation of the mineral samples. The oxidation was found to occur at a higher rate in the presence of the bacteria compared to the control samples. Bioremediation experiments were conducted on acid mine water collected from the Ingaldahl Mines, Chitradurga, Karnataka, India, using organic and inorganic substrates. In the experiments with rice husk, complete removal of metal ions from the acid mine water was achieved with an attendant increase in the pH of the acid mine water from 2.3 to 5.5. About 21% of sulphate could be removed using Dsm. nigrificans from acid mine water pretreated with rice husk at pH 5.5 and this was further increased to 40% by the supplementation of organic components. The rice husk filtrate was found to serve as a good growth medium for Dsm. nigrificans. About 96 % of Fe, 75 % of Zn, 92 % of Cu and 41 % of sulphate removal was achieved from the acid mine water of pH 2.4 with a concomitant increase in the pH value by two units after interaction with the tree bark. About 56 % and 71 % of sulphate reduction could be achieved at initial pH values of 4.1 and 5.5 respectively of the acid mine water pretreated with E. tereticornis (Sm) bark, after inoculation with Dsm. nigrificans. The complete removal of Fe2+ and Fe3+, 80% of Zn, 83% of Cu and 62% of sulphate could be removed from acid mine water using fly ash as the substrate with an increase in pH of acid mine water from 2.3 to 7. About 68% of sulphate reduction at pH 6.8 could be achieved in acid mine water pretreated with fly ash in the presence of Dsm. nigrificans. With red mud as the substrate, complete removal of all the metal ions namely Fe2+, Fe3+, Zn, and Cu from acid mine water was achieved with a concomitant increase in the pH from 2.3 to 8. The sulphate reduction was increased to about 51% at pH 7.2 when the acid mine water pretreated with red mud was inoculated with Dsm. nigrificans. The adsorption experiments carried out on the acid mine water using either organic or inorganic substrates indicated that the free energy of adsorption was negative for all the chosen metal ions attesting to favorable interaction. The adsorption isotherms of the metal ions for rice husk exhibited Langmuirian behaviour, while those for the other substrates adhered to both Langmuir and Freundlich relationships. The adsorption process was found to be endothermic in nature for rice husk, fly ash and red mud. On the contrary, the adsorption onto tree bark showed exothermic behaviour. The adsorption kinetics of the metal ions onto the various substrates adhered to the first order Lagergren equation. The metal uptake processes by the organic and inorganic substrates chosen for this study involve ionic, chemical and physical forces of adsorption. The different types of functional groups present on the surface of the substrates such as carboxyl, hydroxyl and carbonyl, as revealed by FTIR spectroscopic studies, partake in metal binding. The metal ions will also be adsorbed by complexing with the negatively charged reaction sites on the substrate surfaces. Furthermore, the complex solution chemistry of the metals as a function of pH has also to be taken into consideration. The mechanism of sulphate reduction by Dsm. nigrificans in the presence of organic carbon can be illustrated as: 2CH2O + SO42- + 2H+  2CO2 + 2H2O + H2S M2 + H2S  MS  + 2H+ where, CH2O represents the organic matter and M represents the metal ion.

Under de senaste 30 åren så har antalet massa- och pappersbruk minskat medan den totala produktionen av massa och papper har ökat. En högre produktion per bruk tillsammans med en hårdare miljölagstiftning, sätter ett högre tryck på vattenreningen på varje bruk. I flera massa- och pappersbruk så är vattenreningen en av faktorerna som begränsar produktionen av massa och papper. Dessutom så renas oftast restvattnet från massa- och pappersbruken med aerob rening som kräver mycket elektricitet och som producerar slam. För att minska kostnaden av vattenreningen och för att öka kapaciteten, så kan en anaerob vattenrening användas före den aeroba reningen. Fördelar med att ha en anaerob rening före den aeroba reningen är att den minskar belastningen av organiskt material på den aeroba reningen, värdefull biogas produceras, anaerob rening producerar mindre slam och kräver mindre elektricitet. Däremot så innehåller restvattnet från massa- och pappersbruk en hög halt av sulfat, vilket har orsakat en instabil biogasproduktion på flera existerande anläggningar. En potentiell lösning på detta är att använda en ytterligare anaerob reaktor före den biogasproducerande reaktorn, med syftet att reducera sulfat. Syftet med detta projekt var att optimera en anaerob två-stegs process för att få en effektiv biogasproduktion och för en stabil process. I projektet har två upp-flöde anaerob packad bädd (UAPB) reaktorer använts. Den första reaktorn var anrikad med sulfatreducerande bakterier före starten av projektet och den andra reaktorn innehöll metanogener. Processvatten från ett massa- och pappersbruk som använder barrträd som råmaterial och gör termomekanisk massa, användes i projektet. Den anaeroba två-stegs processen optimerades genom att minska retentionstiden i båda reaktorerna; genom att undersöka alternativ för att minska sulfidkoncentrationen i inflödet till biogasreaktorn; och genom att minska tillsatsen av näringsämnen till processvattnet. Stabiliteten av två-stegsprocessen mättes genom att analysera sulfat, sulfid och COD innehållet med spektrofotometri; genom att analysera pH; genom att analysera innehållet av metan i biogasen med gaskromatografi; och genom att analysera flyktiga fettsyror i utflödet med högtrycksvätskekromatografi. Resultaten visade att processen var stabil när retentionstiden för den sulfatreducerande reaktorn och biogasreaktorn var 0.3 dagar respektive 1.5 dagar. Effektiviteten av borttagningen av sulfat och COD i den sulfatreducerande reaktorn var 82% respektive 31%. Innehållet av metan i biogasen i den sulfatreducerande reaktorn var 53% i genomsnitt. I biogasreaktorn var borttagningen av COD 32% och metanhalten i biogasen var 31% i genomsnitt. Den totala borttagningen av COD för tvåstegsprocessen var 61%, när reaktorerna var kopplade via en uppsamlingsflaska. Biometanpotentialen i processvattnet och i utflödet från den sulfatreducerande reaktorn var 147 NmL CH4/g VS respektive 47 NmL CH4/g VS. Slutsatsen av projektet är att processen var stabil när retentionstiden för den sulfatreducerande reaktorn och biogasreaktorn var 0.3 dagar respektive 1.5 dagar, motiverat med stabiliteten av borttagning av sulfat och COD. Däremot var metanpotentialen för utflödet från den sulfatreducerande reaktorn bara 32% jämfört med processvattnet och nedbrytbarheten av COD var lägre i utflödet än i processvattnet. Eftersom den sulfatreducerande reaktorn var stabil vid de testade förhållandena så skulle det vara intressant att testa en enstegsprocess i en UAPB reaktorpilot i framtiden. Det skulle även vara intressant att minska retentionstiden i biogasreaktorn för att se om metanhalten i biogasen ökar. / In the past 30 years, the number of P&P mills have decreased while the total production of pulp and paper have increased. A higher production per mill together with a stringent environmental legislation puts a high pressure on the wastewater treatment of P&P mills. In several P&P mills the wastewater treatment is one of the factors limiting the production of pulp and paper. In addition, the wastewater is usually treated with aerobic treatment that consumes a high amount of electricity and produces sludge. To decrease the cost of the wastewater treatment and to increase the treatment efficiency, an anaerobic treatment can be used before the aerobic treatment. Advantages of having an anaerobic treatment before the aerobic treatment is that it reduces the organic loading of the aerobic treatment, valuable biogas is produced, anaerobic treatment produce less sludge and requires less electricity. However, the wastewater of P&P mills is rich in sulphate, which have resulted in an unstable biogas production. A potential solution for this to have another anaerobic reactor before the biogas producing reactor, with the purpose to remove sulphate. The aim of this project was to optimize a two-step anaerobic treatment for an effective biogas production and for a stable process. In the project, two UAPB reactors were used. The first bioreactor (hereafter pretreatment reactor) was enriched with sulphate reducing bacteria before the start of the project while the second reactor contained methanogens (hereafter biogas reactor). Wastewater from a P&P mill using the TMP process and soft wood as raw material was used in this project. The anaerobic two-step process was optimized by decreasing the HRT of both reactors, by investing alternatives to decrease the sulphide in the influent to the biogas reactor and by decreasing the addition of nutrients to the process water. The stability of the two-step process was measured by analysing the sulphate, sulphide and COD content spectrophotometrically; by analysing pH; by analysing the methane content in the headspace of the reactors with GC and by analysing the VFA content in the effluents using HPLC. The results showed that the process was stable when the HRT of the pretreatment reactor and biogas reactor was 0.3 days and 1.5 days, respectively. The removal efficiency of sulphate and COD in the pretreatment reactor was 82% and 31%, respectively. The methane content in the biogas of the PT reactor was 53% in average. The COD removal efficiency of the biogas reactor was 32% and there was in average 31% methane in the biogas. The average total COD removal efficiency of the two-step process was 61% when the reactors were coupled via a collection tank. The biomethane potential of the process water and the effluent of the pretreatment reactor was 147 NmL CH4/g VS and 47 NmL CH4/g VS, respectively. The process was stable when the HRT of the pretreatment reactor and biogas reactor was 0.3 days and 1.5 days, respectively, considering the stability of the sulphate and COD removal efficiency. However, the BMP of the effluent of the PT reactor was only 32% of the BMP of the process water and the degradability of the COD was lower in the effluent. Since the PT reactor exhibited stability at the tested conditions, it would be interesting to try it as a one-step process in a pilot UAPB reactor in the future. In the future, research is needed to investigate if the methane content in the headspace of the biogas reactor can be increased by decreasing the HRT of the reactor.

Aquesta tesi tracta sobre l'efecte de la contaminació per cru de petroli sobre l'ecosistema costaner mediterrani i sobre el paper fonamental dels sediments marins en la regulació i el manteniment dels processos biogeoquímics. L'estudi presta especial atenció a les comunitats bacterianes reductores de sulfat i la seva implicació en la degradació de contaminants orgànics. La diversitat, abundància i fisiologia dels bacteris reductors de sulfat que habiten el sediment arenós del nord de Mallorca (Illes Balears), van ser analitzades mitjançant un enfocament polifàsic, basat en la combinació d'experiments in situ i in vitro, biologia molecular clàssica i d’última generació, cultius i determinació d'activitats metabòliques. Els resultats obtinguts durant aquesta tesi demostren que el sediment mediterrani alberga una microbiota autòctona que podria prosperar després d'un vessament de cru de petroli i el paper de la qual podria ser crucial per a la transformació i l'eliminació de compostos orgànics xenobiòtics en aquest ambient. / Esta tesis trata sobre el efecto de la contaminación por crudo de petróleo en el ecosistema costero mediterráneo y sobre el papel fundamental de los sedimentos marinos en la regulación y el mantenimiento de los procesos biogeoquímicos. El estudio presta especial atención a las comunidades bacterianas reductoras de sulfato y a su implicación en la degradación de contaminantes orgánicos. La diversidad, abundancia y fisiología de las bacterias reductoras de sulfato que habitan el sedimento arenoso del norte de Mallorca (Islas Baleares), fueron analizadas mediante un enfoque polifásico, basado en la combinación de experimentos in situ e in vitro, biología molecular clásica y de última generación, cultivos y determinación de actividades metabólicas. Los resultados obtenidos durante esta tesis demuestran que el sedimento mediterráneo alberga una microbiota autóctona que podría prosperar después de un derrame de crudo de petróleo y cuyo papel podría ser crucial para la transformación y la eliminación de compuestos orgánicos xenobióticos en este ambiente. / This thesis discusses the fate and behave of crude oil contamination in the Mediterranean coastal ecosystem, and the essential role of the marine sediments in the regulation and maintenance of biogeochemical processes. The study pays particular attention to the role of sulphate reducing bacterial communities in the degradation of organic matter and pollutants entering the Mediterranean environment. A polyphasic approach based in the combination of in situ and in vitro experiments, next generation and classical molecular biology, cultivation, and the determination of metabolic activities, provided first insights into the diversity, abundance and physiology of sulphate reducing bacteria inhabiting the undisturbed sandy sediment at the north of Mallorca (Balearic Islands). The results obtained during the thesis demonstrate that the undisturbed Mediterranean sediment harbours an autochthonous microbiota that could prosper after a crude oil spill and which role might be crucial for the transformation and removal of hazardous organic compounds in this environment.