Wet Oxidation of Paper Mill Evaporation Concentrates

Tämän työn tarkoituksena oli tutkia lämpötilan pH:n ja vetyperoksidin vaikutusta kuorimoveden haihdutuskonsentraatin märkähapetuksessa. Kirjallisuusosassa esitellään massan ja paperin valmistusta sekä kuorintaprosessi. Lisäksi tarkastellaan kuoren kemiallista koostumusta, jäteveden ja prosessiveden käsittelymenetelmiä sekä märkähapetuksen periaatteita. Kokeellinen osa käsittää erään suomalaisen paperitehtaan kuorimoveden haihdutuskonsentraatin märkähapetuskokeet. Hapetuskokeet tehtiin useammassa eri lämpötilassa, pH:ssa ja vetyperoksidikonsentraatiossa. Em. muuttujien vaikutusta tutkittiin kemialliseen hapenkulutukseen (COD), biologiseen hapenkulutukseen (BOD), välittömästi saatavana olevan biologiseen hapenkulutukseen (IABOD), orgaaniseen kokonaishiileen (TOC) ja tanniini/ligniini pitoisuuteen. Koetulokset osoittivat, että korkeimmat COD- ja TOC-reduktiot saavutettiin H2O2-katalysoidulla märkähapetuksella jäteveden alkuperäisessä pH:ssa (60 % reduktio COD:lla ja 45 % reduktio TOC:lla lämpötilassa 170 °C ja 0.2 g H2O2/g COD). Toisaalta, parhaat tulokset biohajoavuuden paranemisen suhteen saavutettiin emäksisissä olosuhteissa, jossa 170 °C:ssa saavutettiin BOD/COD-arvo 76 %. Emäksisissä olosuhteissa saavutettiin lähes täydellinen tanniinin reduktio lämpötila-alueella 130-170 °C, mutta näissä lämpötiloissa orgaanisen kuorman alenemista ei havaittu.

Wet Oxidation of TMP Concentrated Paper Mill Process Water. Kinetics of the reaction

Työn tarkoituksena oli tutkia lämpötilan, paineen, pH:n ja katalyytin vaikutusta paperitehtaan TMP-konsentroidun prosessiveden märkähapetuksessa. Teoriaosio sisältää katsauksen sellu- ja paperiteollisuuteen, jätevesien käsittelyyn, nanosuodatuksen ja märkähapetusprosessin toimintaperiaatteet ja sovellukset hybriditeknologialle nanosuodatus-märkähapetuksessa. Empiirinen osa koostuu märkähapetuskokeista eri lämpötiloissa, paineissa, pH:ssa ja eri katalyyseillä. Työssä tutkittiin näiden vaikutusta kemialliseen hapenkulutukseen (COD), Biologiseen hapenkulutukseen (BOD), Välittömästi saatavana olevan biologisen hapenkulutukseen (IABOD), ligniiniin, täysin orgaanisen hiileen (TOC) ja rasvaliukoisten uuteaineiden (LWEs) pitoisuuteen. Tuloksina kokeellisesta työstä saatiin korkeimmat COD:n alenemat ja BOD/COD (biohajoavuus) suurimmilla lämpötilaolosuhteilla (COD:n alenema 70 % ja BOD/COD 97 % 200 °C:ssa ja hapen 10 bar osapaineella). Tutkimuksessa, jossa selvitettiin hapen osapaineen vaikutusta saatiin tuloksena, että hapen osapaineen kasvu parantaa orgaanisen kuormituksen poistoa: COD poisto oli olosuhteilla130°C, 5bar 5 %, olosuhteilla 130 °C, 15bar 15 %, olosuhteilla 170 °C, 5bar 20 % ja olosuhteilla 170 °C, 15bar 50 %. Lähes täydellinen LWEs –poisto saavutettiin 150 °C ja 10bar olosuhteilla, vaikka tässä lämpötilassa ei saavutettu korkeata orgaanisen kuormituksen poistoa. Emäksinen pH vaikutti suosivan hapettavia reaktioita, koska korkein COD:n poisto saavutettiin näissä olosuhteilla; kuitenkin alkalisen väliaineen tehokkuudelle löydettiin tärkeä lämpötilariippuvuus.

Sistema de injeção em fluxo espectrofotométrico para monitorar peróxido de hidrogênio em processo de fotodegradação por reação foto-Fenton

A flow injection spectrophotometric system was projected for monitoring hydrogen peroxide during photodegradation of organic contaminants in photo-Fenton processes (Fe2+/H2O2/UV). Sample is injected manually in a carrier stream and then receives by confluence a 0.1 mol L-1 NH4VO3 solution in 0.5 mol L-1 H2SO4 medium. The product formed shows absorption at 446 nm which is recorded as a peak with height proportional to H2O2 concentration. The performance of the proposed system was evaluated by monitoring the consumption of H2O2 during the photodegradation of dichloroacetic acid solution by foto-Fenton reaction.

Avaliação de contaminantes inorgânicos e orgânicos em álcool combustível utilizando eletroforese capilar

This work reports the analysis of inorganic and organic contaminants in alcohol fuel samples using capillary electrophoresis. Chloride and sulfate were analyzed in nitrate/ monochloroacetic acid at 10 mmol L-1 concentration each under indirect UV detection (210 nm). The analysis of aldehydes is based on the 216 nm detection of 3-methyl-2-benzothiazoline hydrazone adducts. The running buffer consisted of 20 mmol L-1 tetraborate , 40 mmol L-1 sodium dodecyl sufate and 12 mmol L-1 beta-ciclodextrin. Both methodologies were applied to real samples indicating inorganic ion concentrations from 0.15 to 6.64 mg kg-1 and aldehydes from 32.0 to 91.3 mg L-1.

Fundamentos e aplicações ambientais dos processos fenton e foto-fenton

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.

Predição da demanda química de oxigênio em chorume maduro contendo reagente de Fenton, por meio de modelo matemático empírico gerado com planejamento fatorial completo

COD is an important parameter to estimate the concentration of organic contaminants. The closed system technique with the use of K2Cr2O7 is the most important one, however, it has the inconvenience to suffer positive chemical interferences from inorganic compounds such as Fe2+ and H2O2 (not enough reported in the literature). This paper considers a statistical-experimental set capable to validate a empirical mathematical model generated from a 23 experimental design, in the presence of Fe2+ and H2O2. The t test shows that mathematical model has 99,99999% confidence degree and the experimental validation test indicates absolute mean error of 4,70%.

Degradação de fármacos residuais por processos oxidativos avançados

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.

VALIDAÇÃO INTRALABORATORIAL DA DETERMINAÇÃO DE METILTESTOSTERONA EM ÁGUAS NATURAIS POR VOLTAMETRIA USANDO ELETRODO DE GOTA PENDENTE DE MERCÚRIO

17α-methyltestosterone (17α-MT) is a hormone used in medicine and aquaculture which can be found in natural waters. It is considered an emerging organic pollutant and its accurate and precise analysis is required. Therefore, this study presents the in-house validation of a new voltammetric methodology for 17α-MT analysis in natural waters. A hanging mercury drop electrode and NaOH 5.0×10-3 mol L-1 solution as the electrolyte were employed in the voltammetric determinations. To confirm the presence of 17α-MT in water samples quantitative analysis was performed by ESI-MS/MS. The methodology exhibited good selectivity, linearity, accuracy (recovery of between 100.4 and 108.8%) and precision (RSDs for repeatability of 2.85% and for intermediate precision of 14.10%, with n = 5, respectively). LOD and LOQ were 3.07 µg L-1 and 10.78 µg L-1, respectively. The methodology was suitable for determination of 17α-MT in natural waters due to low-cost, good performance and no sample pre-treatment required.

Electro-Oxidation Treatment of Pulp and Paper Mill Circulating Waters and Wastewaters

Interest in water treatment by electrochemical methods has grown in recent years. Electrochemical oxidation has been applied particularly successfully to degrade different organic pollutants and disinfect drinking water. This study summarizes the effectiveness of the electrochemical oxidation technique in inactivating different primary biofilm forming paper mill bacteria as well as sulphide and organic material in pulp and paper mill wastewater in laboratory scale batch experiments. Three different electrodes, borondoped diamond (BDD), mixed metal oxide (MMO) and PbO2, were employed as anodes. The impact on inactivation efficiency of parameters such as current density and initial pH or chloride concentration of synthetic paper machine water was studied. The electrochemical behaviour of the electrodes was investigated by cyclic voltammetry with MMO, BDD and PbO2 electrodes in synthetic paper mill water as also with MMO and stainless steel electrodes with biocides. Some suggestions on the formation of different oxidants and oxidation mechanisms were also presented during the treatment. Aerobic paper mill bacteria species (Deinococcus geothermalis, Pseudoxanthomonas taiwanensis and Meiothermus silvanus) were inactivated effectively (>2 log) at MMO electrodes by current density of 50 mA/cm2 and the time taken three minutes. Increasing current density and initial chloride concentration of paper mill water increased the inactivation rate of Deinococcus geothermalis. The inactivation order of different bacteria species was Meiothermus silvanus > Pseudoxanthomonas taiwanensis > Deinococcus geothermalis. It was observed that inactivation was mainly due to the electrochemically generated chlorine/hypochlorite from chloride present in the water and also residual disinfection by chlorine/hypochlorite occurred. In real paper mill effluent treatment sulphide oxidation was effective with all the different initial concentrations (almost 100% reduction, current density 42.9 mA/cm2) and also anaerobic bacteria inactivation was observed (almost 90% reduction by chloride concentration of 164 mg/L and current density of 42.9 mA/cm2 in five minutes). Organic material removal was not as effective when comparing with other tested techniques, probably due to the relatively low treatment times. Cyclic voltammograms in synthetic paper mill water with stainless steel electrode showed that H2O2 could be degraded to radicals during the cathodic runs. This emphasises strong potential of combined electrochemical treatment with this biocide in bacteria inactivation in paper mill environments.

Lämpötilan vaikutus oksaalihapon hapetukseen pulssitetulla koronapurkauksella

Tutkimuksen tarkoituksena oli kartoittaa lämpötilan vaikutusta veden orgaanisten haitta-aineiden hapetuksessa PCD-menetelmällä. Kokeita tehtiin näytteiden eri alkulämpötiloilla. Malliyhdisteenä kokeissa käytettiin oksaalihappoa. Teoriaosuudessa käsiteltiin pulssittaista koronapurkausta ilmiönä. Lisäksi tarkasteltiin, kuinka PCD-menetelmällä muodostuu hapettimia neste-kaasufaasissa. Syntyvistä hapettimista keskityttiin otsoniin ja hydroksyyliradikaaliin. Kokeellisessa osuudessa esiteltiin käytetty PCD-laitteisto. Esittelyn jälkeen siirryttiin hapetuskokeiden kuvaamiseen ja analyysin suorittamiseen titrauksella. Lopuksi koottiin tulokset. Tutkimuksissa prosessin hapetustehon havaittiin heikentyvän lämpötilan noustessa tutkitulla lämpötila-alueella, mikä voi selittyä kaasufaasissa muodostuvan otsonin heikentyvällä liukoisuudella. Tuloksia voidaan pitää viitteellisinä, ja selkeän mallin muodostamiseksi tarvitaan jatkotutkimuksia laajemmalla lämpötila-alueella tarkasti toistettavilla koejärjestelyillä.

Développement de méthodes analytiques pour la détection et la quantification de traces de produits pharmaceutiques dans les eaux du fleuve Saint Laurent

Le présent projet vise à documenter la nécessité d’augmenter notre connaissance de la présence des contaminants organiques tels que les médicaments dans l’environnement et d’évaluer leur devenir environnemental. On a étudié la présence de composés pharmaceutiques dans différents échantillons d'eau. On a focalisé nos efforts spécialement sur les échantillons d'eau de l'usine d'épuration de la Ville de Montréal et ses effluents, les eaux de surface avoisinantes et l’eau du robinet dans la région de Montréal. Pour ce faire, on a tout d’abord développé deux méthodes analytiques automatisées basées sur la chromatographie liquide avec extraction en phase solide (SPE) couplée à la chromatographie liquide couplée à la spectrométrie de masse en tandem (LC-MS/MS). On a également étudié les performances des trois techniques d'ionisation à pression atmosphérique (API), pour ensuite les utiliser dans la méthode analytique développée. On a démontré que l'ionisation par électronébulisation (ESI) est une méthode d'ionisation plus efficace pour l'analyse des contaminants pharmaceutiques dans des échantillons de matrices très complexes comme les eaux usées. Une première méthode analytique SPE couplée à la LC-MS/MS a été développée et validée pour l'étude des échantillons complexes provenant de l'usine d'épuration de la Ville de Montréal et des eaux de surface près de l'usine. Cinq médicaments de prescription ont été étudiés: le bézafibrate (un régulateur de lipides), le cyclophosphamide et le méthotrexate (deux agents anticancéreux), l'orlistat (un agent anti-obésité) et l’énalapril (utilisé dans le traitement de l'hypertension). La plupart de ces drogues sont excrétées par le corps humain et rejetées dans les eaux usées domestiques en faisant par la suite leur chemin vers les usines municipales de traitement des eaux usées. On a pu démontrer qu'il y a un faible taux d’élimination à l'usine d'épuration pour le bézafibrate et l'énalapril. Ces deux composés ont aussi été détectés dans les eaux de surface sur un site à proximité immédiate de la décharge de l’effluent de la station d'épuration. i En observant la nécessité de l'amélioration des limites de détection de la première méthode analytique, une deuxième méthode a été développée. Pour la deuxième méthode, un total de 14 contaminants organiques, incluant trois agents anti-infectieux (clarithromycin, sulfaméthoxazole et triméthoprime), un anticonvulsant (carbamazépine) et son produit de dégradation (10,11-dihydrocarbamazépine), l'agent antihypertensif (enalapril), deux antinéoplastiques utilisés en chimiothérapie (cyclophosphamide et méthotrexate), des herbicides (atrazine, cyanazine, et simazine) et deux produits de transformation de l’atrazine (deséthylatrazine et déisopropylatrazine) ainsi qu’un agent antiseptique (triclocarban). Ces produits ont été quantifiés dans les eaux de surface ainsi que dans l’eau du robinet. L'amélioration des limites de détection pour cette méthode a été possible grâce à la charge d'un volume d'échantillon supérieur à celui utilisé dans la première méthode (10 mL vs 1 mL). D'autres techniques de confirmation, telles que les spectres des ions produits utilisant une pente d’énergie de collision inverse dans un spectromètre de masse à triple quadripôle et la mesure des masses exactes par spectrométrie de masse à temps d’envol, ont été explorées. L'utilisation d'un analyseur de masse à temps d’envol a permis la confirmation de 6 des 14 analytes. Finalement, étant donné leur haute toxicité et pour évaluer leur persistance et leur transformation au niveau du traitement des eaux potables, la cinétique d'oxydation du cyclophosphamide et de méthotrexate avec l'ozone moléculaire et des radicaux OH a été étudiée. Les constantes de dégradation avec l'ozone moléculaire ont été calculées et la qualité de l'eau après traitement a pu être évaluée. Le rendement du processus d'ozonation a été amélioré pour la cyclophosphamide dans les eaux naturelles, en raison de la combinaison de réactions directes et indirectes. Cette étude a montré que l'ozone est très efficace pour oxyder le méthotrexate mais que le cyclophosphamide serait trop lent à s’oxyder pour un traitement efficace aux conditions usuelles de traitement de l’eau potable.

Studies on Catalysis by Nano Titania Modified with Metals and Nonmetals

Semiconductor photocatalysis has received much attention during last three decades as a promising solution for both energy generation and environmental problems. Heterogeneous photocatalytic oxidation allows the degradation of organic compounds into carbon dioxide and water in the presence of a semiconductor catalyst and UV light source. The •OH radicals formed during the photocatalytic processes are powerful oxidizing agents and can mineralise a number of organic contaminants. Titanium dioxide (TiO2), due to its chemical stability, non-toxicity and low cost represents one of the most efficient photocatalyst. However, only the ultraviolet fraction of the solar radiation is active in the photoexcitation processes using pure TiO2 and although, TiO2 can treat a wide range of organic pollutants the effectiveness of the process for pollution abatement is still low. A more effective and efficient catalyst therefore must be formulated. Doping of TiO2 was considered with the aim of improving photocatalytic properties. In this study TiO2 catalyst was prepared using the sol-gel method. Metal and nonmetal doped TiO2 catalysts were prepared. The photoactivity of the catalyst was evaluated by the photodegradation of different dyes and pesticides in aqueous solution. High photocatalytic degradation of all the pollutants was observed with doped TiO2. Structural and optical properties of the catalysts were characterized using XRD, BET surface area, UV-Vis. DRS, CHNS analysis, SEM, EDX, TEM, XPS, FTIR and TG. All the catalysts showed the anatase phase. The presence of dopants shifts the absorption of TiO2 into the visible region indicating the possibility of using visible light for photocatalytic processes.

Relative proportions of polycyclic aromatic hydrocarbons differ between accumulation bioassays and chemical methods to predict bioavailability

Chemical methods to predict the bioavailable fraction of organic contaminants are usually validated in the literature by comparison with established bioassays. A soil spiked with polycyclic aromatic hydrocarbons (PAHs) was aged over six months and subjected to butanol, cyclodextrin and tenax extractions as well as an exhaustive extraction to determine total PAH concentrations at several time points. Earthworm (Eisenia fetida) and rye grass root (Lolium multiflorum) accumulation bioassays were conducted in parallel. Butanol extractions gave the best relationship with earthworm accumulation (r2 ≤ 0.54, p ≤ 0.01); cyclodextrin, butanol and acetone–hexane extractions all gave good predictions of accumulation in rye grass roots (r2 ≤ 0.86, p ≤ 0.01). However, the profile of the PAHs extracted by the different chemical methods was significantly different (p < 0.01) to that accumulated in the organisms. Biota accumulated a higher proportion of the heavier 4-ringed PAHs. It is concluded that bioaccumulation is a complex process that cannot be predicted by measuring the bioavailable fraction alone. The ability of chemical methods to predict PAH accumulation in Eisenia fetida and Lolium multiflorum was hindered by the varied metabolic fate of the different PAHs within the organisms.

Diffusion of the synthetic pyrethroid permethrin into bed-sediments

Bed-sediments are a sink for many micro-organic contaminants in aquatic environments. The impact of toxic contaminants on benthic fauna often depends on their spatial distribution, and the fate of the parent compounds and their metabolites. The distribution of a synthetic pyrethroid, permethrin, a compound known to be toxic to aquatic invertebrates, was studied using river bed-sediments in lotic flume channels. trans/cis-Permethrin diagnostic ratios were used to quantify the photoisomerization of the trans isomer in water. Rates were affected by the presence of sediment particles and colloids when compared to distilled water alone. Two experiments in dark/light conditions with replicate channels were undertaken using natural sediment, previously contaminated with permethrin, to examine the effect of the growth of an algal biofilm at the sediment-water interface on diffusive fluxes of permethrin into the sediment. After 42 days, the bulk water was removed, allowing a fine sectioning of the sediment bed (i.e., every mm down to 5 mm and then 5-10 mm, then every 10 mm down to 50 mm). Permethrin was detected in all cases down to a depth of 5-10 mm, in agreement with estimates by the Millington and Quirk model, and measurements of concentrations in pore water produced a distribution coefficient (K-d) for each section, High K-d's were observed for the top layers, mainly as a result of high organic matter and specific surface area. Concentrations in the algal biofilm measured at the end of the experiment under light conditions, and increases in concentration in the top 1 mm of the sediment, demonstrated that algal/bacterial biofilm material was responsible for high K-d's at the sediment surface, and for the retardation of permethrin diffusion. This specific partition of permethrin to fine sediment particles and algae may enhance its threat to benthic invertebrates. In addition,the analysis of trans/cis-permethrin isomer ratios in sediment showed greater losses of trans-permethrin in the experiment under light conditions, which may have also resulted from enhanced biological activity at the sediment surface.

Effect of agitation on the performance of an anaerobic sequencing batch biofilm reactor in the treatment of dairy effluents

Agitation rate is an important parameter in the operation of Anaerobic Sequencing Biofilm Batch Reactors (ASBBRs), and a proper agitation rate guarantees good mixing, improves mass transfer, and enhances the solubility of the particulate organic matter. Dairy effluents have a high amount of particulate organic matter, and their anaerobic digestion presents inhibitory intermediates (e. g., long-chain fatty acids). The importance of studying agitation in such batch systems is clear. The present study aimed to evaluate how agitation frequency influences the anaerobic treatment of dairy effluents. The ASBBR was fed with wastewater from milk pasteurisation process and cheese manufacture with no whey segregation. The organic matter concentration, measured as chemical oxygen demand (COD), was maintained at approximately 8,000 mg/L. The reactor was operated with four agitation frequencies: 500 rpm, 350 rpm, 200 rpm, and no agitation. In terms of COD removal efficiency, similar results were observed for 500 rpm and 350 rpm (around 90%) and for 200 rpm and no agitation (around 80%). Increasing the system`s agitation thus not only improved the global efficiency of organic matter removal but also influenced volatile acid production and consumption and clearly modified this balance in each experimental condition.