995 resultados para OXIDATION PROCESSES


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Wastewater and soil treatment processes based on Fenton's reagent have gained great attention in recent years due to its high oxidation power. This review describes the fundaments of the Fenton and photo-Fenton processes and discusses the main aspects related to the degradation of organic contaminants in water such as the complexation of iron, the use of solar light as the source of irradiation and the most important reactor types used. An overview of the main applications of the process to a variety of industrial wastewater and soil remediations is presented.

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Today, environmental impact associated with pollution treatment is a matter of great concern. A method is proposed for evaluating environmental risk associated with Advanced Oxidation Processes (AOPs) applied to wastewater treatment. The method is based on the type of pollution (wastewater, solids, air or soil) and on materials and energy consumption. An Environmental Risk Index (E), constructed from numerical criteria provided, is presented for environmental comparison of processes and/or operations. The Operation Environmental Risk Index (EOi) for each of the unit operations involved in the process and the Aspects Environmental Risk Index (EAj) for process conditions were also estimated. Relative indexes were calculated to evaluate the risk of each operation (E/NOP) or aspect (E/NAS) involved in the process, and the percentage of the maximum achievable for each operation and aspect was found. A practical application of the method is presented for two AOPs: photo-Fenton and heterogeneous photocatalysis with suspended TiO2 in Solarbox. The results report the environmental risks associated with each process, so that AOPs tested and the operations involved with them can be compared.

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In this work, the efficiency of some homogeneous advanced oxidation processes (UVC/H2O2, Fe2+/H2O2, UVC/Fe2+/H2O2, UVA/Fe2+/H2O2, solar/Fe2+/H2O2) was investigated toward the degradation of geosmin and 2-methylisoborneol (2-MIB). The effect of relevant experimental parameters (ie. pH, Fe2+ and H2O2 concentration) was first investigated by factorial design, using camphor as a model substrate. In the geosmin and 2-MIB degradation studies the Fenton processes assisted by solar and UVA radiation offered the most promising results, mainly on account of high degradation capacity (higher than 80% at a reaction time of 60 min), high operational simplicity and low cost.

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Three technologies were tested (TiO2/UV, H2O2/UV, and TiO2/H2O2/UV) for the degradation and color removal of a 25 mg L-1 mixture of three acid dyes: Blue 9, Red 18, and Yellow 23. A low speed rotating disc reactor (20 rpm) and a H2O2 concentration of 2.5 mmol L-1 were used. The dyes did not significantly undergo photolysis, although they were all degraded by the studied advanced oxidation processes. With the TiO2/H2O2/UV process, a strong synergism was observed (color removal reached 100%). Pseudo first order kinetic constants were estimated for all processes, as well as the respective apparent photonic efficiencies.

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The concern about aquatic ecosystems and the potential risk of drinking water contamination by pharmaceuticals have stimulated the study of processes for the efficient degradation of these contaminants, since the conventional treatment have been inefficient on that purpose. The advanced oxidation processes (AOPs) appear as viable alternatives due to their efficiency on the degradation of different classes of organic contaminants. This review presents an overview of the main AOP (O3, H2O2/UV, TiO2/UV, Fenton and photo-Fenton) which have been applied to the degradation of different pharmaceuticals. The main results obtained, intermediates identified and toxicity data are presented.

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An alternative for landfill leachate treatment are advanced oxidation processes by Fenton's reagent (AOP/Fenton). In this context, the aim of this paper was to evaluate, in a bench scale, the treatability of leachate pós-AOP/Fenton characterizing the supernatant and the sludge generated separately. Observed in optimal conditions, high removal efficiency of COD (76.7%), real color (76.4%) and humic substances (50%). Organic compounds were detected in the sludge (2.465 mg COD L-1) and high concentration of iron (1.757 mg L-1) as was expected. Finally, the sludge generated showed low settling hindering their separation by sedimentation (SVI = 321 mL g-1).

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Flumequine degradation by electrochemical and photo-electrochemical processes was evaluated in this study. The antimicrobial activity of the solutions subjected to the electrochemical processes was monitored during the assays. The experiments were carried out using DSA® (dimensionally stable anode) electrode. The influence of current density was investigated for the 7.5 to 45 mA cm-2 range. The photo-electrochemical process was more efficient for degrading flumequine (85%) and reducing solution antimicrobial activity. For both processes, the residual antimicrobial activity decreased as flumequine degradation increased. The reaction intermediate m/z 244 (5-methyl-1-oxo-6,7-dihydro-1H,5H-pyrido[3,2,1-ij]quinoline-2-carboxylic acid) was identified.

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Kirjallisuustyössä tutkittiin tehostetun hapetuksen menetelmiä (engl. Advanced Oxidation Processes, AOPs) kloorifenolien käsittelyssä. Tutkittava aine valittiin US EPA:n (United States Environmental Protection Agency) ympäristölle haitallisten aineiden listalta. Työssä tutkitut AOP-menetelmät olivat otsonointi kasvatetussa pH:ssa, O3/H2O2-prosessi, fotolyyttinen otsonointi (O3/UV), H2O2/UV-prosessi ja Fenton-prosessi (H2O2+Fe2+). AOP-käsittelyssä OH-radikaalien oletetaan pääosin aiheuttavan epäpuhtauksien hapettumisen. Kirjallisuustyössä tutkittiin OH-radikaaleihin vaikuttavien parametrien, kuten pH:n, lämpötilan sekä hapettimien ja hapetettavan aineen konsentraatioiden vaikutusta kloorifenolien hapetusprosessissa. Työn tarkoituksena oli selvittää tehokkain AOP-käsittely kloorifenoleja sisältävien jätevesien käsittelylle. AOP-käsittelyjen tehokkuutta verrattiin hajoamisnopeusvakioiden, puoliintumisaikojen sekä hapettimen kemikaalikulutuksen ja kustannuksen perusteella. Fenton-prosessin ja otsonoinnin pH:ssa 9 todettiin olevan tehokkaimpia menetelmiä kloorifenolien hapetuksessa. Fenton-prosessin hapetusnopeus oli tehokkaampaa 4-CP:n ja 2,4-DCP:n hapetuksessa, kun taas otsonointi pH:ssa 9 hapetti nopeammin 2,3,4,6-TeCP:n ja 2,4,6-TCP:n. Kustannustehokkuuden perusteella Fenton-prosessi oli otsonointia tehokkaampi. Parhaan menetelmän valinta kloorifenoleiden poistamiseksi oli vaikeaa, sillä useissa tutkimuksissa oli tutkittu vain yhtä menetelmää. Lisäksi eri tutkimuksissa käytetyt prosessiolosuhteet olivat erilaiset, joka hankaloitti tutkimusten vertailua. Lopullinen AOP-menetelmän valinta tulisikin suorittaa vasta laboratoriotutkimusten jälkeen.

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Teoriaosassa tutkittiin mäskin muodostumista oluentuotantoprosessissa, ligniiniä ja sen pilkkoutumista hapetuksella, eri kehittyneitä hapetusmenetelmiä ja hapetuksella saatavia potentiaalisia pääkomponentteja. Kehittyneissä hapetusmenetelmissä keskityttiin pääasiassa pulssitettuun koronapurkaukseen perustuvaan PCD-menetelmään (Pulsed Corona Discharge). Tutkittavana pääkomponenttina toimi glyoksyylihappo. Työn kokeellisessa osassa tutkittiin mäskistä erotetun ligniinin pilkkoutumista PCD-hapetuksella. Tässä menetelmässä hapetus perustuu sähköpurkauksen aikana syntyvien hydroksyyliradikaalien ja otsonin muodostumiseen, jotka voivat toimia hapettimina. Kokeissa käytettiin oluentuotannosta saatua mäskiä, josta ligniiniä liuotettiin natriumhydroksidi-vesi-liuoksen avulla uuttamalla.. Tämän jälkeen liuosta käsiteltiin PCD laitteistossa. PCD-käsiteltyä tuotetta analysoitiin mittaamalla ligniinin ja aldehydien pitoisuudet siitä spektrofotometrin avulla. Työn tarkoituksena on tutkia PCD hapetusmenetelmän soveltuvuutta mäskin sisältämän ligniinin muokkaamiseen siten, että siitä syntyvää tuotetta voitaisiin käyttää jossakin muussa sovelluksessa, kuten esimerkiksi lääkkeiden raaka-aineena lääketeollisuudessa. PCD hapetusmenetelmä on koronasähköpurkauksiin perustuva laite, jota käytetään pääasiassa vedenpuhdistuksessa hajoittamaan haitallisia orgaanisia yhdisteitä. Tämän työn perusteella ligniiniä hajosi, aldehydejä muodostui ja hapetusnäytteiden pH laski hapetusajan kasvaessa. Tämä viittasi vahvasti glyoksyylihapon muodostumiseen PCD-laitteistossa.

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In tumor-bearing rats, most of the serum amino acids are used for synthesis and oxidation processes by the neoplastic tissue. In the present study, the effect of Walker 256 carcinoma growth on the intestinal absorption of leucine, methionine and glucose was investigated in newly weaned and mature rats. Food intake and carcass weight were decreased in newly weaned (NT) and mature (MT) rats bearing Walker 256 tumor in comparison with control animals (NC and MC). The tumor/carcass weight ratio was higher in NT than in MT rats, whereas nitrogen balance was significantly decreased in both as compared to control animals. Glucose absorption was significantly reduced in MT rats (MT = 47.3 ± 4.9 vs MC = 99.8 ± 5.3 nmol min-1 cm-1, Kruskal-Wallis test, P<0.05) but this fact did not hamper the evolution of cancer. There was a significant increase in methionine absorption in both groups (NT = 4.2 ± 0.3 and MT = 2.0 ± 0.1 vs NC = 3.7 ± 0.1 and MC = 1.2 ± 0.2 nmol min-1 cm-1, Kruskal-Wallis test, P<0.05), whereas leucine absorption was increased only in young tumor-bearing rats (NT = 8.6 ± 0.2 vs NC = 7.7 ± 0.4 nmol min-1 cm-1, Kruskal-Wallis test, P<0.05), suggesting that these metabolites are being used for synthesis and oxidation processes by the neoplastic cells, which might ensure their rapid proliferation especially in NT rats.

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Tavallisten hapetusmenetelmien sijasta kehittyneitä hapetusmenetelmiä (AOP) on kehitetty yhä enemmän, jotta hapetusprosessista tulisi kannattavampi, tehokkaampi, ympäristöystävällisempi ja sitä voitaisiin hyödyntää laajalti eri paikoissa. Uusi teknologia, joka käyttää otsonia ja hydroksyyliradikaalia sähköimpulssien kanssa, on yksi mahdollinen tehokkaampi vedenkäsittelymentelmä. Kyseistä menetelmää kutsutaa pulsed corona discharge (PCD) -menetelmäksi, joka käyttää prosessissa muodostuvia otsonia ja hydroksyyliradikaalia hapettavina tekijöinä. Tässä työssä tutkittiin nitraatin muodostumista vedessä, kun vettä käsiteltiin PCD-laitteessa ja, kun oksalaatti- ja formaatti-ioneja oli sekoittuneina veteen. Nitraatteja muodostuu PCD–laitteessa veteen, kun ilman typpi reagoi hapettimina toimivien otsonin ja hydroksyyliradikaalin kanssa. Aiemmissa tutkimuksissa nitraatin muodostumisen on todistettu parantuvan, kun karboksyylihapot muurahais- ja oksaalihappo ovat sekoittuneina veteen. Tässä tutkimuksessa tarkoituksena oli tutkia, miten formaatti- ja oksalaatti-ionien, joiden pitoisuudet olivat 0 ppm, 50 ppm ja 100 ppm, läsnäolo vedessä vaikuttaa nitraatin muodostumiseen. PCD-kokeista saadut näytteet analysoitiin ionikromatografilla. Kyseisessä tutkimuksessa nitraatin muodostuminen oli samansuuruista jokaisessa kokeessa hapetusajan kasvaessa samalla, kun otettujen näytteiden pH-arvot laskivat. Tuloksena voitiin pitää sitä, ettei formaatti- tai oksalaatti-ioneilla ollut vaikutusta nitraatti-ionien muodostumiseen.

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Electron paramagnetic resonance (EPR) spectroscopy of spin labels was used to monitor membrane dynamic changes in erythrocytes subjected to oxidative stress with hydrogen peroxide (H2O2). The lipid spin label, 5-doxyl stearic acid, responded to dramatic reductions in membrane fluidity, which was correlated with increases in the protein content of the membrane. Membrane rigidity, associated with the binding of hemoglobin (Hb) to the erythrocyte membrane, was also indicated by a spin-labeled maleimide, 5-MSL, covalently bound to the sulfhydryl groups of membrane proteins. At 2% hematocrit, these alterations in membrane occurred at very low concentrations of H2O2 (50 µM) after only 5 min of incubation at 37°C in azide phosphate buffer, pH 7.4. Lipid peroxidation, suggested by oxidative hemolysis and malondialdehyde formation, started at 300 µM H2O2 (for incubation of 3 h), which is a concentration about six times higher than those detected with the probes. Ascorbic acid and α-tocopherol protected the membrane against lipoperoxidation, but did not prevent the binding of proteins to the erythrocyte membrane. Moreover, the antioxidant (+)-catechin, which also failed to prevent the cross-linking of cytoskeletal proteins with Hb, was very effective in protecting erythrocyte ghosts from lipid peroxidation induced by the Fenton reaction. This study also showed that EPR spectroscopy can be useful to assess the molecular dynamics of red blood cell membranes in both the lipid and protein domains and examine oxidation processes in a system that is so vulnerable to oxidation.

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L’objectif général de cette thèse est de développer une plateforme d’immobilisation d’enzymes efficace pour application en biopile. Grâce à la microencapsulation ainsi qu’au choix judicieux des matériaux polymériques pour la fabrication de la plateforme d’immobilisation, l’efficacité du transfert électronique entre l’enzyme encapsulée et l’électrode serait amélioré. Du même coup, les biopiles employant cette plateforme d’immobilisation d’enzymes pourrait voir leur puissance délivrée être grandement augmentée et atteindre les niveaux nécessaires à l’alimentation d’implants artificiels pouvant remplacer des organes telque le pancréas, les reins, le sphincter urinaire et le coeur. Dans un premier temps, le p-phénylènediamine a été employé comme substrat pour la caractérisation de la laccase encapsulée dans des microcapsules de poly(éthylèneimine). La diffusion de ce substrat à travers les microcapsules a été étudiée sous diverses conditions par l’entremise de son oxidation électrochimique et enzymatique afin d’en évaluer sa réversibilité et sa stabilité. La voltampérométrie cyclique, l’électrode à disque tournante (rotating disk electrode - RDE) et l’électrode à O2 ont été les techniques employées pour cette étude. Par la suite, la famille des poly(aminocarbazoles) et leurs dérivés a été identifée pour remplacer le poly(éthylèneimine) dans la conception de microcapsules. Ces polymères possèdent sur leurs unités de répétition (mono- ou diamino) des amines primaires qui seraient disponibles lors de la polymérisation interfaciale avec un agent réticulant tel qu’un chlorure de diacide. De plus, le 1,8-diaminocarbazole (unité de répétition) possède, une fois polymérisé, les propriétés électrochimiques recherchées pour un transfert d’électrons efficace entre l’enzyme et l’électrode. Il a toutefois été nécessaire de développer une route de synthèse afin d’obtenir le 1,8-diaminocarbazole puisque le protocole de synthèse disponible dans la littérature a été jugé non viable pour être utilisé à grande échelle. De plus, aucun protocole de synthèse pour obtenir du poly(1,8-diaminocarbazole) directement n’a été trouvé. Ainsi, deux isomères de structure (1,6 et 1,8-diaminocarbazole) ont pu être synthétisés en deux étapes. La première étape consistait en une substitution électrophile du 3,6-dibromocarbazole en positions 1,8 et/ou 1,6 par des groupements nitro. Par la suite, une réaction de déhalogénation réductive à été réalisée en utilisant le Et3N et 10% Pd/C comme catalyseur dans le méthanol sous atmosphère d’hydrogène. De plus, lors de la première étape de synthèse, le composé 3,6-dibromo-1-nitro-carbazole a été obtenu; un monomère clé pour la synthèse du copolymère conducteur employé. Finalement, la fabrication de microcapsules conductrices a été réalisée en incorporant le copolymère poly[(9H-octylcarbazol-3,6-diyl)-alt-co-(2-amino-9H-carbazol-3,6-diyl)] au PEI. Ce copolymère a pu être synthétisé en grande quantité pour en permettre son utilisation lors de la fabrication de microcapsules. Son comportement électrochimique s’apparentait à celui du poly(1,8-diaminocarbazole). Ces microcapsules, avec laccase encapsulée, sont suffisamment perméables au PPD pour permettre une activité enzymatique détectable par électrode à O2. Par la suite, la modification de la surface d’une électrode de platine a pu être réalisée en utilisant ces microcapsules pour l’obtention d’une bioélectrode. Ainsi, la validité de cette plateforme d’immobilisation d’enzymes développée, au cours de cette thèse, a été démontrée par le biais de l’augmentation de l’efficacité du transfert électronique entre l’enzyme encapsulée et l’électrode.

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Nitrification is the biological oxidation of ammonium, first to nitrite and then to nitrate by two groups of aerobic, chemolithotrophic bacteria belonging to the family Nitrobacteriaceae. The biological nitrification in municipal wastewater treatment is important in those cases were ammonia removal requirement specially exist. In a trickling filter or in an activated sludge system nitrification is rate limiting and thus necessitates longer detention time. The combined carbon oxidation-nitrification processes generally have low population of nitrifiers due to a high ratio of BOD to total nitrogen in the effluent. This necessitates, separate carbon and nitrogen oxidation processes, which thus minimizes wash out ofthe nitrifiers. Therefore, a separate stage nitrification has become essential to achieve faster and efficient removal of ammonia from the wastewater. The present work deals with the development of bio reactor for nitrifying of sewage as the tertiary process so that the treated wastewater can be used for irrigation, algal culture or fish culture

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The term ‘water pollution’ broadly refers to the contamination of water and water bodies (e.g. lakes, rivers, oceans, groundwater etc). Water pollution occurs when pollutants are discharged directly or indirectly into water bodies without adequate treatment to remove the harmful contaminants. This affects not only the plants and organisms living in these bodies of water but also the entire natural biological communities and the biodiversity.Advanced Oxidation Processes (AOPs) have been tested as environment-friendly techniques for the treatment of contaminated water, in view of their ability to convert pollutants into harmless end products. These techniques refer to a set of treatment procedures designed to remove organic or inorganic contaminants in wastewater by oxidation. The contaminants are oxidized by different reagents such as air, oxygen, ozone, and hydrogen peroxide which are introduced in precise, preprogrammed dosages, sequences and combinations under appropriate conditions. The procedure when combined with light in presence of catalyst is known as photocatalysis. When ultrasound (US) is used as the energy source, the process is referred as sonication. Sonication in presence of catalyst is referred as sonocatalysis. Of late, combination of light and sound as energy sources has been tested for the decontamination of wastewater in the presence of suitable catalyst. In this case, the process is referred as sonophotocatalysis. These AOPs are specially advantageous in pollution control and waste water treatment because unlike many other technologies, they do not just transfer the pollutant from one phase to another but completely degrade them into innocuous substances such as CO2 and H2O.