Thèses sur le sujet « Procédé d'oxydation avancée (POA) »
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Coque, Yves. « Proposition d'outils d'optimisation de procédé d'oxydation avancée (POA) par UV/H2O2 ». Pau, 2002. http://www.theses.fr/2002PAUU3012.
Texte intégralMerouani, Djillali Reda. « Traitement de colorants azoïque et anthraquinonique par procédés d'oxydation avancée (POA) ». Thesis, Lille 1, 2011. http://www.theses.fr/2011LIL10185/document.
Texte intégralDyes used and production generate a persistent, biorefractory, no biodegradable, toxic, carcinogenic and mutagenic effluents. Their treatment before release into the wild is necessary. Physical and biological conventional treatments ineffective due to high number of benzene cycles generated, high stability and resistance of new output molecule; they are non-destructive and transfer organic pollution from aqueous to another phase, causing a secondary pollution. It is in this context that the advanced oxidation processes (AOP) have emerged, they treat dyes solution because they generate highly reactive, no selective species as hydroxyl radicals (•OH). In this work, an azo dye (Orange G), an anthraquinonic dye (Alizarin Red S) and their mixture, were treated by plasma Glidarc, homogeneous photocatalysis (Fenton and photo-Fenton) and heterogeneous photocatalysis (TiO2- and ZnO). The results showed that there is no POA completely suitable for the degradation of all organic dyes types because of their different chemical structures. This study opens the way to other combined treatments as AOP-Physico-chemical or biological AOP-treatment which can be more effective and economical
Castillo, Rivera Luis Antonio (1970. « Etude d'effluents difficilement biodégradables : caractérisation et traitement par procédés d'oxydation avancée (POA) ». Aix-Marseille 1, 1999. http://www.theses.fr/1999AIX11060.
Texte intégralMuranaka, Cínthia Tiemi. « Combinação de adsorção por carvão ativado com Processo Oxidativo Avançado (POA) para tratamento de efluentes contendo fenol ». Thesis, Toulouse, INPT, 2010. http://www.theses.fr/2010INPT0089/document.
Texte intégralAdsorption on activated carbon (AC) is a technique extensively applied for wastewater treatment. However adsorption alone is not an ultimate solution, since the pollutants are just immobilized on the carbon surface. There is thus a need for efficient regeneration techniques. In this context, Fenton and photo-Fenton oxidations, which are promising technologies to destroy organic pollution, have been tested to regenerate the AC. The purposes of this study are the adsorption of phenol on activated carbons and the consecutive in-situ regeneration of carbon by (photo-) Fenton oxidation. Two different operations have been carried out: 1) batch procedure in order to investigate the influence of Fe2+ and H2O2 concentrations; 2) continuous fixed bed adsorption, followed by a batch circulation of the Fenton’s reagent through the saturated AC bed, to examine the efficiency of the real process. Two different activated carbons have been also studied: a both micro- and mesoporous AC (PICA L27) and an only microporous one (PICA S23). In the batch reactor the best conditions found for pollutant mineralization in the homogeneous Fenton system are not the best for AC regeneration: a continuous reduction of adsorption capacity of L27 is observed after 3 oxidations, due to the decrease of both AC weight and surface area. Higher concentration of Fe2+ and lower concentration of H2O2 (2 times the stoechiometry) lead to a 50% recovery of the initial adsorption capacity during at least 4 consecutive cycles for L27, while about 20% for S23. In the consecutive continuous adsorption/batch Fenton oxidation process, the regeneration efficiency reaches 30% to 40% for L27 after two cycles whatever the feed concentration and less than 10% for S23. A photo-Fenton test performed on L27 shows almost complete mineralization (contrary to dark Fenton) and further improves recovery of AC adsorption capacity although not complete (56% after two cycles)
Korichi, Noussaiba. « Epuration d'effluents pharmaceutiques par plasmas non thermiques couplés à des procédés catalytiques ». Electronic Thesis or Diss., Orléans, 2023. http://www.theses.fr/2023ORLE1057.
Texte intégralThe work of this PhD thesis aims at studying a hybrid process for the treatment of organic molecules in water. It consists of the Non Thermal Plasma (NTP) process coupled with heterogeneous catalysis (Fenton-like type). Paracetamol is used as the target molecule for this study. Two different configurations of Dielectric Barrier Discharge (DBD) plasma reactor were used: (i) a multi-needles-to-plane reactor in static mode; (ii) a coaxial tubular reactor with flow of the solution to be treated. In order to evaluate the synergy between the two processes (plasma and catalysis), the treatments were applied separately and then coupled. The synergistic effects of the coupled plasma-catalysis process were demonstrated in terms of degradation rate, energy yield, and also in terms of pollutant mineralization, corresponding to a decrease of the organic molecules load in the solution with the conversion of organic carbon into inorganic carbon. The first part of the work carried out with the multi-needles-to-plane reactor allowed to establish the effective role of the plasma-catalysis coupling in comparison with the plasma process alone. Indeed, in coupling, a mineralization of 54% was reached after the 60 minutes of treatment and the energy yield was increased by a factor of two, thus reducing the cost of treatment. The work carried out on the coaxial reactor allowed us to study the effect of many parameters on plasma-catalysis coupling efficiency such as the composition of the injected gas, the gas and liquid flow rate, the position of the catalyst in relation to the plasma discharge, etc. We were thus able to show the interest of working in an oxygen-rich gas on kinetics of degradation and mineralization as well as the role of applied electrical power on the oxidation mechanisms. As an example, it was possible to obtain a mineralization of 70 % after 90 minutes under air, whereas under O₂/N₂ (80/20 sccm), the mineralization reached 95 %. The stability of the catalyst was also studied in terms of mineralization after several reuses of the catalyst. We also demonstrated the role of the hydroxyl radical (·OH) on the treatment with the use of radical scavengers. Indeed, the presence of methanol, known as a scavenger of hydroxyl radicals, a decrease of the degradation of nearly 50% was obtained and no mineralization was observed
Olya, Mohammad Ebrahim. « Contribution à l'étude du procédé de dégradation des colorants synthétiques par les méthodes d'oxydation chimique et d'oxydation avancée UV/H2O2 ». Thesis, Mulhouse, 2009. http://www.theses.fr/2009MULH3057.
Texte intégralThis work is about the degradation of some synthetic dyes by the chemical oxidation method using KMnO4 and UV/H2O2 advanced oxidation process. Decolourisation of the dyes by potassium permanganate under optimal condition is very rapid but a complete dye mineralization is not obtained. The results show that despite of its high cost; UV/H2O2 is an effective method to achieve the dyes mineralization. So, an appropriate combination of these two methods could granite high amount of mineralization with a reasonable cost. The operational conditions and hydrodynamic behaviour of the reactors are very important to optimise the process. Efficiency study of the combined method KMnO4/UV/H2O2, as well as the economic calculations show, this process can be used to increase the rate of dyes degradation and reduce notably the cost of electrical energy consumed for the process. Response surface methodology (RSM) was used as a modelling and optimizing method
Mahdi, ahmed Moussa. « Elimination de substances pharmaceutiques d'effluents urbains par un procédé d'oxydation avancée basé sur le radical sulfate ». Thesis, Aix-Marseille, 2013. http://www.theses.fr/2013AIXM4746.
Texte intégralThis work is devoted to the study of an alternative advanced oxidation process (AOP) generating sulfate radical (SO4•-) for the removal of pharmaceuticals in municipal wastewater effluents. Four nitrogen containing pharmaceuticals (carbamazepine, diclofenac, sulfamethoxazole and ciprofloxacin) belonging to different therapeutic classes were chosen as model contaminants. The evaluation of the kinetic performance of processes based on the generation of HO• (H2O2/Fe(II) and UV-C/H2O2 ) and SO4•- (HSO5-/Co2+, UV-C/S2O82- and UV-C/HSO5- ) was conducted in biologically treated effluent. Comparison of photochemical and non- photochemical processes performed under the same optimal conditions showed that the processes generating SO4•- are less inhibited by the environmental matrix than processes producing HO•. This electron transfer reaction is demonstrated by the identification of transformation products using liquid chromatography coupled to high resolution mass spectrometer. Oxidation of parent compounds starts by an electron transfer reaction on the nitrogen groups thereby generating a cation radical which further reacts with water or O2. The sulfamethoxazole degradation pathway gives more insights into this mechanism due to the primary amine moiety (aniline) which is converted into nitro function. This treatment system can be regarded as a new strategy for the treatment of urban wastewater contaminated by pharmaceutical residues through the generation of SO4•-
Esmilaire, Roseline. « Matériaux membranaires en TiO₂ sous-stœchiométrique pour le traitement de l'eau par procédé électrochimique d'oxydation avancée ». Thesis, Montpellier, 2017. http://www.theses.fr/2017MONTT182.
Texte intégralThis project aims to contribute to the sustainable management of water as an essential natural resource, through the development of an innovative technology based on the coupling of a baromembranar filtration process and electrochemical advanced oxidation processes (EAOP) in order to mineralize very stable organic molecules.Since these bio-refractory pollutants cannot be totally degraded by common oxidants (biological, O3, Cl2, H2O2), advanced oxidation processes (AOP) are thus considered. In electrochemistry, these hydroxyl radicals can be generated by water oxidation on carbon cathodes by the electro-Fenton process or on anode showing high oxygen evolution overvoltage like sub-stoichiometric titanium oxide and Boron Doped Diamond (BDD).This work deals with the development and characterization of tubular filtration membranes composed of the most conductive Magnéli phases: Ti4O7 and Ti5O9. These materials can be used in anodic oxidation process with lower manufacturing cost compared to BDD. Microfiltration tubular membranes composed of these phases were prepared with the support of CREE (Research Group of Saint-Gobain). They were elaborated by carbothermal reduction of TiO2, which is very innovative compared to dihydrogen reduction. TinO2n-1 powders (with 3 ≤ n ≤ 5) of controlled grain size were elaborated by electrofusion of TiO2 powder and coke followed by grinding. These powders were further used at the European Institute of Membranes to formulate stable suspensions of particles to prepare thin solid films of low microfiltration, by dip-coating or slip-casting. We also propose an original method for the production of thin layers of TinO2n-1 (n to be defined) by sol-gel route followed by a thermal treatment to obtain ultra or nanofiltration active layers. After optimization, those materials have shown their efficiency towards the degradation of bio-refractory compounds such as pharmaceutics (Paracetamol) when used as electrochemical reactive membranes either in static (beaker) or in dynamic mode (filtration pilot). The next step will focus on the coupling of the anodic oxidation and the baromembranar filtration processes using the reactive developed membranes. From first results, this technology appears really promising for the treatment of bio-refractory pollutants in water. This thesis was financially supported by the National Research Agency (NRA) within the framework of the ECO-TS program, the CElectrON project
Mahdi, Ahmed Moussa. « Elimination de substances pharmaceutiques d'effluents urbains par un procédé d'oxydation avancée basé sur le radical sulfate ». Electronic Thesis or Diss., Aix-Marseille, 2013. http://www.theses.fr/2013AIXM4746.
Texte intégralThis work is devoted to the study of an alternative advanced oxidation process (AOP) generating sulfate radical (SO4•-) for the removal of pharmaceuticals in municipal wastewater effluents. Four nitrogen containing pharmaceuticals (carbamazepine, diclofenac, sulfamethoxazole and ciprofloxacin) belonging to different therapeutic classes were chosen as model contaminants. The evaluation of the kinetic performance of processes based on the generation of HO• (H2O2/Fe(II) and UV-C/H2O2 ) and SO4•- (HSO5-/Co2+, UV-C/S2O82- and UV-C/HSO5- ) was conducted in biologically treated effluent. Comparison of photochemical and non- photochemical processes performed under the same optimal conditions showed that the processes generating SO4•- are less inhibited by the environmental matrix than processes producing HO•. This electron transfer reaction is demonstrated by the identification of transformation products using liquid chromatography coupled to high resolution mass spectrometer. Oxidation of parent compounds starts by an electron transfer reaction on the nitrogen groups thereby generating a cation radical which further reacts with water or O2. The sulfamethoxazole degradation pathway gives more insights into this mechanism due to the primary amine moiety (aniline) which is converted into nitro function. This treatment system can be regarded as a new strategy for the treatment of urban wastewater contaminated by pharmaceutical residues through the generation of SO4•-
Kesraoui-Abdessalem, Aïda. « Dégradation des pesticides chlortoluron, carbofurane et bentazone en milieux aqueux par les procédés d'oxydation avancée ». Thesis, Paris Est, 2008. http://www.theses.fr/2008PEST0228/document.
Texte intégralThe use of advanced oxidation electrochemical process: Electro-Fenton is an easy and economical way to obtain hydroxyl radical (•OH) strongly oxidizing. During this work radicals were used for the degradation of chlortoluron, carbofuran and bentazon in aqueous medium. The methodology of experimental research has been used to study the influence of some parameters (initial concentration, current intensity and processing time) on the rate of degradation and to determine the optimum conditions for mineralization. The evolution of chlortoluron concentration with processing time shows a pseudo first order kinetics ( (4.92 × 109, 109 × 3.24 × 2.63 and 109 M-1 S-1 respectively for the chlortoluron, and Carbofuran bentazon). In our optimal conditions (pH = 3, I = 300 mA, [pesticide]0 = 0.125 mM and t = 8 h), we obtain a TOC removal ratio more than 90% for the three pesticides. In the case of molecules studied, it was shown that the rate of mineralization by the photo-Fenton (UV/Fe3+/H2O2) is a function of doses of reagents used and the initial concentration of pesticides treaty. A comparison of the performance of mineralization by the different processes studied (Electro-Fenton (BDD), Electro-Fenton (PT), anodic oxidation and photo-Fenton) has shown that more than 90% of TOC removal was obtained after only 2 hours of photo-Fenton and electro-Fenton (BDD) process. Nevertheless, a comparison of the cost treatment shows that photo-Fenton process is more expensive than electro-Fenton (BDD). The plasma humid air was used for chlortoluron degradation. Different catalysers (Fe2+, Fe3+ and TiO2) were studied to improve the glidarc performances. The combination of TiO2 and Fe2+ can reach 96% of chlortoluron degradation after 3h
Loukou, Affoue. « Couplage adsorption-procédés d'oxydation avancée pour l'élimination de polluants biorécalcitrants en milieu aqueux ». Thesis, Toulouse, INPT, 2019. http://www.theses.fr/2019INPT0083.
Texte intégralThis study is part of the development of new economically viable methods of treating water pollution that is refractory to conventional (biological) processes. Advanced oxidation technologies integrating a heterogeneous phase such as catalytic ozonation or photocatalysis are among the most effective techniques. The ozonation was coupled with a material resulting from the recycling and the valorization of waste of Côte d’Ivoire. The objective of this study was to develop hybrid methods coupling adsorption and these advanced oxidation methods to remove phenol organic micropollutants. The 2,4-dimethylphenol molecule (2,4-DMP) was chosen as a model pollutant and the tests were carried out on a synthetic aqueous solution of 2,4-DMP and on a real wastewater containing this micropollutant. The first part of the work involved the development of the innovative material, under varying operating conditions. Activated carbons were prepared from branches of rônier and bamboo stems. The textural, structural and physicochemical characterization of the adsorbents has been carried out using conventional techniques, showing excellent properties, especially BET surfaces greater than 840 m2.g-1. The materials developed were tested in a 2,4-DMP adsorption process, showing good removal abilities, both with the synthetic aqueous solution and with the actual effluent. These tests made it possible to select an activated carbon based on rônier branches (ACR) for the oxidation process tests. The effectiveness of the input of this activated carbon was tested on a treatment pilot, coupling ozonation and adsorption. Two coupling modes were tested, simultaneous ozonation/adsorption treatment and sequential ozonation treatment followed by adsorption and comparisons with a simple ozonation process were analyzed. In both cases, the addition of activated carbon had a positive effect on the overall degradation kinetics of the 2,4-dimethylphenol molecule, with, however, a TOC residual difficult to remove. This activated carbon has been shown to be a promoter of free radicals, active in both homogeneous and heterogeneous phases. Four mechanisms have thus been demonstrated in the micropollutant elimination phenomenon: adsorption, molecular oxidation and homogeneous and heterogeneous radical oxidation. Finally, photocatalytic degradation tests were conducted with a composite catalyst, TiO2/activated carbon (fibers) and with TiO2 powder and deposited on a glass plate. The irradiation was carried out with a UV lamp in a conventional batch reactor, giving good efficiencies then with a LEDs panel at 365 nm in a closed-loop reactor. Two modes of operation were tested: a simultaneous adsorption/photocatalysis mode which did not make it possible to highlight the contribution of the irradiation and a sequential mode. This second procedure made it possible to demonstrate the photocatalytic effect of the deposit for a sufficiently long duration of irradiation
Gumuchian, Diane. « Développement et étude d'un procédé d'oxydation avancée de traitement de l'eau pour composés organiques résistants par couplage plasma/catalyse ». Thesis, Paris 6, 2014. http://www.theses.fr/2014PA066577/document.
Texte intégralThis work enabled the development of a method of water treatment by plasma/catalysis coupling.The plasma treatments were carried out in two different reactors: a point/plane reactor and a dynamic reactor.Both reactors allow to control the gas atmosphere of the treatment. The feasibility of the degradation of aceticacid has been proven. Some processing parameters in the point/plane reactor (treatment gas, gas flow rate andfrequency of discharge) and the dynamic reactor (liquid phase flow, concentration of the pollutant and injectedpower) were studied.A modeling of the process using Comsol Multiphysics and Scilab softwares was conducted. It was possible toobserve the importance of the way active species (mainly hydroxyl radicals) are brought to the solution.A Co3O4 powder catalyst was studied in order to couple the plasma treatment with a catalytic treatment. Thus,manipulations of catalytic ozonation were conducted. They highlighted the efficiency of the catalyst for thedecomposition of pollutants.Finally, the plasma/catalysis coupling produced promising results, since it improved the decomposition ofpollutants.Possible improvements of the process could be to maximize the amount of high voltage electrodes and toredesign their shape (electrodes in parallel, plane geometry, etc.). Depositing a thin layer of catalyst on thegrounded electrode by PECVD (Plasma Enhanced Chemical Vapor Deposition) technique has to be performed
Guivarch, Elodie. « Traitement des polluants organiques en milieux aqueux par procédé électrochimique d'oxydation avancée "Electro-Fenton" : application à la minéralisation des colorants synthétiques ». Université de Marne-la-Vallée, 2004. http://www.theses.fr/2004MARN0201.
Texte intégralThis reports deals with a new electrochemical advanced oxidation process development and applicability, called "Electro-Fenton process", for waters contaminated by synthetic colorant treatment. In this study, we highlight that degradation kinetic and mineralization rate could be significantly increased by experimental parameters variation (pH, kind and catalyst concentration, imposed current value, temperature…. ). We have also determined in this work that hydroxyl radical oxidation kinetic constant rate to organic dyes was about 109 M-1s-1. Oxidation by-products identification permitted to establish plausible reactional mechanism for azobenzene and malachite green mineralization. For all compounds studied, COD analyses demonstrated mineralization exceed 90% for Electro-Fenton process
Kesraoui-Abdessalem, Aida. « Dégradation des pesticides chlortoluron, carbofurane et bentazone en milieux aqueux par les procédés d'oxydation avancée ». Phd thesis, Université de Marne la Vallée, 2008. http://tel.archives-ouvertes.fr/tel-00742462.
Texte intégralLesage, Olivier. « Développement d'un procédé d'oxydation avancée pour le traitement d'effluents aqueux contaminés par des polluants réfractaires : étude d'un procédé de décharge plasma à pression atmosphérique couplé à un catalyseur supporté ». Phd thesis, Université Pierre et Marie Curie - Paris VI, 2014. http://tel.archives-ouvertes.fr/tel-01069381.
Texte intégralLesage, Olivier, et Olivier Lesage. « Développement d'un procédé d'oxydation avancée pour le traitement d'effluents aqueux contaminés par des polluants réfractaires : étude d'un procédé de décharge plasma à pression atmosphérique couplé à un catalyseur supporté ». Doctoral thesis, Université Laval, 2014. http://hdl.handle.net/20.500.11794/25272.
Texte intégralDans ces travaux de recherche nous avons cherché à développer et optimiser un procédé d’oxydation avancée dédié au traitement de l’eau. Pour cela, Nous avons développé un procédé combinant la génération de radicaux hydroxyles par décharge plasma à pression atmosphérique et un catalyseur fixe. L’originalité de ce travail a été d’utiliser un système d’écoulement permettant l’obtention d’un film liquide (épaisseur < 1mm) afin de permettre une interaction entre le plasma, le liquide et la surface catalytique. Les résultats ont montré que la décharge de type DBD était préférable au Glidarc, plus thermique, plus énergétique et produisant trop de NOx. Les valeurs d’efficacités respectives ont été de 0,67 g.kWh-1 (DBD) et 0,23 g.kWh-1 (Glidarc). Les résultats ont également montré que le matériau de la surface d’écoulement pouvait influencer l’efficacité du procédé. Ainsi dans le cas du laiton, la présence de réactions de corrosion produisant des NO2- réduit l’efficacité de moitié comparée à une plaque d’acier. Le développement d’un modèle CFD 1D du procédé a également été effectué. Celui-ci a permis d’estimer que l’efficacité énergétique de production des HO⋅ est de 4,4.10-9 molHO.J-1 pour la décharge DBD. Il a également permis de montrer que les facteurs majoritairement limitants étaient la présence de réactions parasites telles que la recombinaison des HO⋅. Le modèle a également montré que les réactions chimiques ne durent pas plus de 1µs après l’impact du streamer et n’ont lieu que dans les premiers 5% d’épaisseur de liquide. Enfin, un dépôt catalytique de DLC dopé à l’argent et réalisé par rf-PECVD a permis d’améliorer de près de 10% l’efficacité maximale du procédé. Mots clés : Procédé d’Oxydation Avancée, décharge à barrière diélectrique, Glidarc, dépollution, rf-PECVD, Diamond-Like Carbon, catalyseur, argent, modélisation CFD.
The aim of this research lies in the development and optimization of an advanced oxidation process dedicated to wastewater treatment. This process combines an atmospheric plasma discharge with an immobilized catalyst (Ag-DLC) in order to generate hydroxyl radicals. The novelty of this work relies in the use of a falling thin film system (thickness < 1mm) to promote the interaction between plasma discharge, the solution and the catalytic surface. The results demonstrate the interest of employing a Dielectric Barrier Discharge configuration instead of a Glidarc system. Indeed, the Glidarc system leads to a too high production level of NOx. The efficiencies of these two processes were respectively 0,67 g.kWh-1 and 0,23 g.kWh-1 for the DBD and the Glidarc system. Moreover, the influence of the counter-electrode / flowing plate material on the process efficiency was pointed out. Compared to stainless steel, the presence of corrosion reactions on the brass surface produced NO2- and thus, reduced the process efficiency. The production of HO⋅ radicals at the plasma / water interface was estimated to be 4,4.10-9 molHO.J-1 by the use of 1D CFD modeling. Side reactions such as HO⋅ recombinaison appear as the major limiting factors. Futhermore the model demonstrates that the time needed to complete all the chemical reactions was less than 1 µs and these reactions occurred only in the first 5% of the top liquid film. Finally with an Ag-DLC based catalytic coating elaborated by RF-PECVD, the efficiency was increased to 10% compared to the best efficiency observed with the non-catalytic system. Keywords : Advanced Oxidation Process, Dielectric barrier discharge, Glidarc, depollution, rf-PECVD, Diamond-Like Carbon, catalyst, silver, CFD modelling.
The aim of this research lies in the development and optimization of an advanced oxidation process dedicated to wastewater treatment. This process combines an atmospheric plasma discharge with an immobilized catalyst (Ag-DLC) in order to generate hydroxyl radicals. The novelty of this work relies in the use of a falling thin film system (thickness < 1mm) to promote the interaction between plasma discharge, the solution and the catalytic surface. The results demonstrate the interest of employing a Dielectric Barrier Discharge configuration instead of a Glidarc system. Indeed, the Glidarc system leads to a too high production level of NOx. The efficiencies of these two processes were respectively 0,67 g.kWh-1 and 0,23 g.kWh-1 for the DBD and the Glidarc system. Moreover, the influence of the counter-electrode / flowing plate material on the process efficiency was pointed out. Compared to stainless steel, the presence of corrosion reactions on the brass surface produced NO2- and thus, reduced the process efficiency. The production of HO⋅ radicals at the plasma / water interface was estimated to be 4,4.10-9 molHO.J-1 by the use of 1D CFD modeling. Side reactions such as HO⋅ recombinaison appear as the major limiting factors. Futhermore the model demonstrates that the time needed to complete all the chemical reactions was less than 1 µs and these reactions occurred only in the first 5% of the top liquid film. Finally with an Ag-DLC based catalytic coating elaborated by RF-PECVD, the efficiency was increased to 10% compared to the best efficiency observed with the non-catalytic system. Keywords : Advanced Oxidation Process, Dielectric barrier discharge, Glidarc, depollution, rf-PECVD, Diamond-Like Carbon, catalyst, silver, CFD modelling.
Pimentel, Marcio. « Etudes de l'oxydation de phénol et crésols par l'oxydation électrochimique avancée en milieu homogène. Application au traitement d'effluent de l'industrie aéronautique ». Phd thesis, Université Paris-Est, 2008. http://tel.archives-ouvertes.fr/tel-00742470.
Texte intégralAbouzlam, Manhal. « Optimisation d'un procédé de traitement des eaux par ozonation catalytique ». Thesis, Poitiers, 2014. http://www.theses.fr/2014POIT2251/document.
Texte intégralThe main goal of the PhD thesis focuses on the optimization of an advanced oxidation process by implementing the modern control tools.The considered process is a lab-scale pilot of industrial wastewater treatment by catalytic ozonation. The optimization of this process is achieved by controlling the pollutant abatement while minimizing the high operating costs. The online measurement of the pollutant concentration is provided by the absorbance which is correlated with COD. Therefore, the process is considered as a system with one input, the ozone generator power, and two outputs, the ozone gas concentration at the top of the reactor and the absorbance.A linear model of the process was identified. It allowed calculating the control laws. And a nonlinear model, with a so-called Wiener model structure, was also identified to test the controllers in simulation before the experiments.The three control methods applied, the internal model control, the optimal control and the H∞ control, allow rejecting disturbance on the pollutant concentration of the effluent to be treated.The stability of closed-loop system with delayed control input was analyzed.The experimental results show the significant benefits provided by this closed-loop system.The methodology developed for this application can be extended to other processes to facilitate the industrial development of advanced oxidation processes
Trellu, Clément. « Mise en place des procédés électrochimiques d'oxydation avancée pour le traitement de solutions de lavage de sols contaminés par des hydrocarbures aromatiques polycycliques ». Thesis, Paris Est, 2016. http://www.theses.fr/2016PESC1161/document.
Texte intégralRemediation of soil contaminated by polycyclic aromatic hydrocarbons (PAHs) is an important societal, environmental, economical and technological challenge, due to the high number of sites contaminated by these persistent and toxic compounds. Environmental engineering companies using conventional bioremediation processes often fails to reach sufficient PAH removal rates from historically contaminated soils. Therefore, there is a real need for the development of innovative solutions.In the present work, the characterization of 6 historically tar oil-contaminated soils showed that 42 to 86% of PAH are located in the sand fraction, either adsorbed on various coal/coke/wood particles or integrated in resinified and weathered tar oil particles. Thus, either selective separation of the most contaminated fraction or surfactant-enhanced soil washing (SW) appears to be promising alternatives to bioremediation, according to the level of sequestration of PAHs. Further investigations were performed on the surfactant-enhanced SW process, which is based on the transfer of PAHs from the soil-sorbed fraction to the washing solution. This process generates SW solutions containing a large amount of surfactant and pollutant. They have to be treated in order to avoid environmental contamination and ensure the cost-effectiveness of the whole process.Anodic oxidation (AO) was identified as a suitable and promising process for the treatment of SW solutions containing PAHs and Tween® 80 as extracting agent. The detailed understanding of mechanisms involved in the removal of organic compounds from SW solutions during AO allowed the implementation of two different treatment strategies:• First, it was emphasized that the use of AO at low current intensity during long treatment times (23 h) allows the selective degradation of target pollutants (PAHs) and the reuse of the SW solution for additional SW steps. Thus, the large amount of Tween® 80 saved strongly improves the cost-effectiveness and ecological footprint of SW processes, particularly when the high sequestration of pollutants requires several SW steps using high surfactant concentrations.• In contrast, high removal rates of organic compounds and production of more biodegradable by-products was observed during short treatment times (3 h) by AO at high current intensity. Thus, synergistic effects were observed for the combination of AO with a biological post-treatment. High removal rates with optimized operating costs can be achieved. Moreover, AO can also be used as a post-treatment (polishing step) for the removal of hardly-biodegradable compounds. This treatment strategy aims at avoiding environmental contamination by SW solutions.Both treatment strategies have to be considered for a suitable management of SW solutions. In view of promising results obtained, scientific challenges related to the scale-up of this process were discussed
González-Labrada, Katia. « Dégradation du paracétamol et de la ciprofloxacine par des procédés d'oxydation avancés dans des eaux usées ». Thesis, Toulouse, INPT, 2018. http://www.theses.fr/2018INPT0150/document.
Texte intégralIn this work, the feasibility of paracetamol and ciprofloxacin degradation by different advanced oxidation processes (AOPs) was investigated. These molecules are representative of pharmaceutical pollutants found in wastewater. The used processes were the ozonation, the high frequency ultrasound, the gamma radiation and the ultraviolet radiation, alone or in combination with oxidizers and/or catalysts (hydrogen peroxide, Fenton’s reagent and zeolite Fe/MFI). The influence of different operations parameters (pH, oxidant concentration, catalyst concentration, gamma radiation dose and ultrasonic power and frequency) for each processes were studied, in order to determine the optimal operating ranges for the degradation and mineralization of the pharmaceuticals pollutants. Results showed marked synergistic effects by combining individual processes with hydrogen peroxide or Fenton’s reagent, being the most important synergy factors those corresponding to the heterogeneous catalytic ozonation and photo-Fenton processes. Taking into account the energy consumption, the mineralization and the synergy factor, the most effective treatments were radio-Fenton oxidation and photo-Fenton oxidation. Optimal conditions for photo-Fenton oxidation were studied in an open channel reactor at bench scale in tap water and in a real matrix from a municipal wastewater treatment plant. Samples were spiked with a mixture of the pharmaceuticals. In both cases 95% degradation within the first 15 minutes was achieved and its mineralization exceeded 55% in three hours
Biard, Pierre-François. « Contribution au développement d'un procédé de lavage chimique compact. Traitement du sulfure d'hydrogène par le chlore à l'échelle semi-industrielle et de COV odorants par oxydation avancée ozone/peroxyde d'hydrogène à l'échelle du laboratoire ». Phd thesis, Université Rennes 1, 2009. http://tel.archives-ouvertes.fr/tel-00541110.
Texte intégralEuvrard, Élise. « Substances dangereuses dans les effluents de traitement de surface : identification et traitement par des procédés innovants ». Thesis, Besançon, 2016. http://www.theses.fr/2016BESA2027/document.
Texte intégralThe industrial sector of surface treatment (ST), sector of excellence in Bourgogne Franche-Comté, is forced to resort to new methods for water treatment due to European regulations increasingly strict. Indeed, particularly in the context of the Water Framework Directive, industries must continually improve the quality of their discharge waters and reduce the impacts generated by them. This work is part of this. Thus, three types of investigations were conducted: the first has defined qualitative and quantitative composition of hazardous substances (HS) in ST discharge waters and study their temporal variability; the second has approved changes in a physicochemical wastewater decontamination station to decrease HS water flow; the last proposed innovative solutions by biosorption on cyclodextrin materials and advanced oxidation process (AOP) by ozone / UV, or by the use of Pd-Cu catalysts to achieve the same objective.[...]
Daher, Elias. « Conception de nouvelles nanostructures de ZnO pour une dégradation photocatalytique améliorée des polluants organiques ». Electronic Thesis or Diss., Sorbonne université, 2023. http://www.theses.fr/2023SORUS320.
Texte intégralWith a continuously growing global industrialization reaching 6.1% in 2021 and a demographic burden of 8 billion people, today’s world is facing the most extensive energy shortages and environmental pollution in its history. Particularly, loaded effluents with recalcitrant organic toxic molecules from refineries, petrochemicals, pharmaceuticals, plasticizers, and many other industries, are continuously endangering surface and groundwater water sustainability. With the low efficiency of conventional treatment techniques in addressing this issue, advanced oxidation processes have emerged as an efficient, promising, and inexpensive technology, capable of tackling different types of organic molecules in aquatic mediums. Amongst these techniques, heterogeneous photocatalysis has emerged as one of the most efficient and economical methods due to the photocatalyst reusability and lack of secondary disposal requirements. The technique is based on the generating of highly reactive oxygen species (ROS) such as hydroxyl radical and superoxide radical upon the exposure of a photocatalyst material to light, making it a green and sustainable technology. These ROS are well-known for their strong oxidation capacity toward organic matter, leading to their mineralization into harmless molecules such as water and carbon dioxide. For that reason, developing an efficient and eco-friendly photocatalyst is of great importance. In this scope, Zinc oxide (ZnO) has been attracting high attention due to its high conversion efficiency of photonic energy, low production price, low degree of toxicity to marine/human life, and long life span. Nonetheless, one of the main challenges facing this material is the limited photocatalytic efficiency due to the recombination of electron-hole pairs. Therefore, new strategies have been developed to enhance its photocatalytic activity such as designing new micro/nanostructures of ZnO or coupling the photocatalysts with other treatment techniques to produce synergic effects