Qualité de l'air intérieur dans les écoles et toxicité potentielle des particules en suspension

Les collectivités d'enfants, comme les écoles, mettent en contact de nombreuses personnes dans un espace restreint. Cette proximité peut favoriser la transmission croisée de micro-organismes infectieux. Les épidémies de varicelle, conjonctivite virale, rougeole et gastro-entérite, et la transmission de parasites comme les poux sont fréquentes dans les établissements scolaires et affectent les enfants et le personnel encadrant dont les enseignants. Ce risque professionnel est souvent négligé car considéré comme inévitable. À côté des risques infectieux, d'autres risques liés à des micro-organismes environnementaux et à leurs constituants comme les endotoxines peuvent exister. Ainsi, des études ont montré que les concentrations aéroportées de particules à l'intérieur des classes d'école étaient plus élevées qu'à l'extérieur (1) et que leur composition chimique était différente (2). Plusieurs études épidémiologiques ont montré un lien clair entre l'exposition à des particules et différents problèmes de santé notamment des problèmes respiratoires et cardiaques. Cette exposition à des particules en suspension dans l'air peut avoir des effets toxiques sur les cellules épithéliales des voies respiratoires. Deux études récentes menées dans des écoles et portant sur les particules aéroportées sont analysées ci-dessous. La première étude a évalué les effets biologiques in vitro de particules collectées dans des classes d'écoles en Allemagne et la seconde étude a mesuré les concentrations aéroportées de différents indicateurs de la qualité de l'air dont les micro-organismes dans des écoles au Portugal.

APROS code benchmarking inboiling water reactor accident analyses

Diplomityö käsittelee kiehutusvesilaitosten transienttien ja onnettomuuksien analysointia APROS-ohjelmiston avulla. Työ on tehty Teollisuuden Voima Oy:n (TVO) Olkiluoto 1 ja 2 laitosyksiköiden mallin pohjalta. Raportissa esitetään ohjelmiston käyttämiä yhtälöitäja laskentamalleja yleisellä tasolla. Työssä esitellään laitoksen yleispiirteet turvallisuustoimintoineen ja kuvataan ohjelmaan suureksi osaksi aiemmin luotua laskentamallia. Työssä on luetteloitu voimassa olevatlisensiointianalyysit, joiden joukosta on valittu laskentatapauksia ohjelmiston suorituskyvyn arviointia varten. Lisäksi työhön on valittu laskentatapauksia muilla kuin lisensointiin käytetyillä ohjelmilla lasketuista analyyseistä. Lisäksi on suoritettu vertailulaskuja konservatiivisen ja realistisen mallin erojen esille saamiseksi. Laskentatapauksia ovat mm. ylipainetransientti, jäähdytteen menetysonnettomuus ja oletettavissa oleva käyttöhäiriö, jossa pikasulku ei toimi (ATWS). Diplomityön edetessä laitosmallia on kehitetty edelleen lisäämällä joitakin järjestelmiä ja tarkentamalla joidenkin komponenttien kuvausta. Työssä ilmeni, että APROS soveltuu jäähdytteenmenetysonnettomuuden ja suojarakennuksen yhtäaikaiseen analyysiin. APROS.n vaste nopeisiin transientteihin jäi kuitenkin vertailutasosta. Tämän työn perusteella APROS-mallia kehitys jatkuu edelleen siten, että se soveltuisi entistä paremmin myös nopeiden transienttien ja ATWS-tilanteiden kuvaamiseen. Työssä olevaa lisensointianalyysien kuvausta tullaan käyttämään hyväksi selvitettäessä laitoksen turvallisuuden väliarviossa tarvittavien analyysien määrää ja laatua. Nyt saatuja kokemuksia voidaan hyödyntää myös mahdollisen kolmiulotteisen sydänmallin hankinnassa APROS-ohjelmistoon. Tässä diplomityössä esitettyjä parannuksia voidaan käyttää hyväksi SAFIRtutkimusohjelman hankkeiden suunnittelussa.

Etude de la toxicité hépatique de la cocaïne associée à de l'alcool: Effets de l'éthanol sur le métabolisme de la cocaïne dan les hépatocytes de rat en suspension et dans un modèle enzymatique humain

Le but essentiel de notre travail a été d?étudier la capacité du foie, premier organe de métabolisation des xénobiotiques, à dégrader la cocaïne en présence d?éthanol, à l?aide de deux modèles expérimentaux, à savoir un modèle cellulaire (les hépatocytes de rat en suspension) et un modèle acellulaire (modèle reconstitué in vitro à partir d?enzymes purifiées de foie humain). La première partie a pour objectifs de rechercher les voies de métabolisation de la cocaïne qui sont inhibées et / ou stimulées en présence d?éthanol, sur hépatocytes isolés de rat. Dans ce but, une méthode originale permettant de séparer et de quantifier simultanément la cocaïne, le cocaéthylène et huit de leurs métabolites respectifs a été développée par Chromatographie Phase Gazeuse couplée à la Spectrométrie de Masse (CPG / SM). Nos résultats préliminaires indiquent que l?éthanol aux trois concentrations testées (20, 40 et 80 mM) n?a aucun effet sur la cinétique de métabolisation de la cocaïne. Notre étude confirme que l?addition d?éthanol à des cellules hépatiques de rat en suspension supplémentées en cocaïne résulte en la formation précoce de benzoylecgonine et de cocaéthylène. L?apparition retardée d?ecgonine méthyl ester démontre l?activation d?une deuxième voie de détoxification. La production tardive d?ecgonine indique une dégradation de la benzoylecgonine et de l?ecgonine méthyl ester. De plus, la voie d?oxydation intervenant dans l?induction du stress oxydant en produisant de la norcocaïne est tardivement stimulée. Enfin, notre étude montre une métabolisation complète de la concentration initiale en éthanol par les hépatocytes de rat en suspension. La deuxième partie a pour but de déterminer s?il existe d?autres enzymes que les carboxylesterases formes 1 et 2 humaines ayant une capacité à métaboliser la cocaïne seule ou associée à de l?éthanol. Pour ce faire, une méthode de micropurification par chromatographie liquide (Smart System®) a été mise au point. Dans le cadre de nos dosages in situ de la cocaïne, du cocaéthylène, de la benzoylecgonine, de l?acide benzoïque et de la lidocaïne, une technique par Chromatographie Liquide Haute Performance couplée à une Détection par Barrette de Diode (CLHP / DBD) et une méthode de dosage de l?éthanol par Chromatographie Phase Gazeuse couplée à une Détection par Ionisation de Flamme équipée d?un injecteur à espace de tête (espace de tête CPG / DIF) ont été développées. La procédure de purification nous a permis de suspecter la présence d?autres enzymes que les carboxylesterases formes 1 et 2 de foie humain impliquées dans le métabolisme de la cocaïne et déjà isolées. A partir d?un modèle enzymatique reconstitué in vitro, nos résultats préliminaires indiquent que d?autres esterases que les formes 1 et 2 de foie humain sont impliquées dans l?élimination de la cocaïne, produisant benzoylecgonine et ecgonine méthyl ester. De plus, nous avons montré que les sensibilités de ces enzymes à l?éthanol sont variables.<br/><br/>The main purpose of our work was to study the ability of the liver, as the first organ to metabolise xenobiotic substances, to degrade cocaine in the presence of ethanol. In order to do this, we used two experimental models, namely a cellular model (rat liver cells in suspension) and an a-cellular model (model reconstructed in vitro from purified human liver enzymes). The purpose of the first part of our study was to look for cocaine metabolising processes which were inhibited and / or stimulated by the presence of ethanol, in isolated rat liver cells. With this aim in mind, an original method for simultaneously separating and quantifying cocaine, cocaethylene and eight of their respective metabolites was developed by Vapour Phase Chromatography coupled with Mass Spectrometry (VPC / MS). Our preliminary results point out that ethanol at three tested concentrations (20, 40 et 80 mM) have no effect on the kinetic of metabolisation of cocaine. Our study confirms that the addition of alcohol to rat liver cells in suspension, supplemented with cocaine, results in the premature formation of ecgonine benzoyl ester and cocaethylene. The delayed appearance of ecgonine methyl ester shows that a second detoxification process is activated. The delayed production of ecgonine indicates a degradation of the ecgonine benzoyl ester and the ecgonine methyl ester. Moreover, the oxidising process which occurs during the induction of the oxidising stress, producing norcocaine, is stimulated at a late stage. Finally, our study shows the complete metabolisation of the initial alcohol concentration by the rat liver cells in suspension. The second part consisted in determining if enzymes other than human carboxylesterases 1 and 2, able to metabolise cocaine on its own or with alcohol, existed. To do this, a micropurification method us ing liquid phase chromatography (Smart System®) was developed. A technique based on High Performance Liquid Chromatography coupled with a Diode Array Detection (HPLC / DAD) in the in situ proportioning of cocaine, cocaethylene, ecgonine benzoyl ester, benzoic acid and lidocaine, and a method for proportioning alcohol by quantifying the head space using Vapour Phase Chromatography coupled with a Flame Ionisation Detection (head space VPC / FID) were used. The purification procedure pointed to the presence of enzymes other than the human liver carboxylesterases, forms 1 and 2, involved in the metabolism of cocaine and already isolated. The preliminary results drawn from an enzymatic model reconstructed in vitro indicate that human liver carboxylesterases, other than forms 1 and 2, are involved in the elimination of cocaine, producing ecgonine benzoyl ester and ecgonine methyl ester. Moreover, we have shown that the sensitivity of these enzymes to alcohol is variable.

Gas-liquid mass transfer in bubbly flow: Estimation of mass transfer, bubble size and reactor performance in various applications

Gas-liquid mass transfer is an important issue in the design and operation of many chemical unit operations. Despite its importance, the evaluation of gas-liquid mass transfer is not straightforward due to the complex nature of the phenomena involved. In this thesis gas-liquid mass transfer was evaluated in three different gas-liquid reactors in a traditional way by measuring the volumetric mass transfer coefficient (kLa). The studied reactors were a bubble column with a T-junction two-phase nozzle for gas dispersion, an industrial scale bubble column reactor for the oxidation of tetrahydroanthrahydroquinone and a concurrent downflow structured bed.The main drawback of this approach is that the obtained correlations give only the average volumetric mass transfer coefficient, which is dependent on average conditions. Moreover, the obtained correlations are valid only for the studied geometry and for the chemical system used in the measurements. In principle, a more fundamental approach is to estimate the interfacial area available for mass transfer from bubble size distributions obtained by solution of population balance equations. This approach has been used in this thesis by developing a population balance model for a bubble column together with phenomenological models for bubble breakage and coalescence. The parameters of the bubble breakage rate and coalescence rate models were estimated by comparing the measured and calculated bubble sizes. The coalescence models always have at least one experimental parameter. This is because the bubble coalescence depends on liquid composition in a way which is difficult to evaluate using known physical properties. The coalescence properties of some model solutions were evaluated by measuring the time that a bubble rests at the free liquid-gas interface before coalescing (the so-calledpersistence time or rest time). The measured persistence times range from 10 msup to 15 s depending on the solution. The coalescence was never found to be instantaneous. The bubble oscillates up and down at the interface at least a coupleof times before coalescence takes place. The measured persistence times were compared to coalescence times obtained by parameter fitting using measured bubble size distributions in a bubble column and a bubble column population balance model. For short persistence times, the persistence and coalescence times are in good agreement. For longer persistence times, however, the persistence times are at least an order of magnitude longer than the corresponding coalescence times from parameter fitting. This discrepancy may be attributed to the uncertainties concerning the estimation of energy dissipation rates, collision rates and mechanisms and contact times of the bubbles.

Mass transfer and particleinteractions in granular systems and suspension flows

The purpose of this study was to investigate some important features of granular flows and suspension flows by computational simulation methods. Granular materials have been considered as an independent state ofmatter because of their complex behaviors. They sometimes behave like a solid, sometimes like a fluid, and sometimes can contain both phases in equilibrium. The computer simulation of dense shear granular flows of monodisperse, spherical particles shows that the collisional model of contacts yields the coexistence of solid and fluid phases while the frictional model represents a uniform flow of fluid phase. However, a comparison between the stress signals from the simulations and experiments revealed that the collisional model would result a proper match with the experimental evidences. Although the effect of gravity is found to beimportant in sedimentation of solid part, the stick-slip behavior associated with the collisional model looks more similar to that of experiments. The mathematical formulations based on the kinetic theory have been derived for the moderatesolid volume fractions with the assumption of the homogeneity of flow. In orderto make some simulations which can provide such an ideal flow, the simulation of unbounded granular shear flows was performed. Therefore, the homogeneous flow properties could be achieved in the moderate solid volume fractions. A new algorithm, namely the nonequilibrium approach was introduced to show the features of self-diffusion in the granular flows. Using this algorithm a one way flow can beextracted from the entire flow, which not only provides a straightforward calculation of self-diffusion coefficient but also can qualitatively determine the deviation of self-diffusion from the linear law at some regions nearby the wall inbounded flows. Anyhow, the average lateral self-diffusion coefficient, which was calculated by the aforementioned method, showed a desirable agreement with thepredictions of kinetic theory formulation. In the continuation of computer simulation of shear granular flows, some numerical and theoretical investigations were carried out on mass transfer and particle interactions in particulate flows. In this context, the boundary element method and its combination with the spectral method using the special capabilities of wavelets have been introduced as theefficient numerical methods to solve the governing equations of mass transfer in particulate flows. A theoretical formulation of fluid dispersivity in suspension flows revealed that the fluid dispersivity depends upon the fluid properties and particle parameters as well as the fluid-particle and particle-particle interactions.

Characterisation of Hydrophobic Nonfibrous Material and Its Removal From Pulp Suspension

Paperin ja kartongin kierrätys lisääntyy taloudellisten intressien ja ympäristöhygieenisten tavoitteiden takia jatkuvasti. Lisääntyvän kierrätyksen myötä myös paperin ja kartongin epäpuhtauksien määrä kasvaa, mikä huonontaa kierrätysraaka-aineen laatua. Tämän työn tarkoituksena on antaa perustietoa eräästä kartongin päällystyksessä käytettävästä hydrofobisesta materiaalista, epäpuhtaan kartongin kierrätyksestä sekä ongelmista, joita epäpuhtaan kartongin kierrätyksestä syntyy. Kierrätyskuidun fraktiointi on yksinkertainen prosessi aallotuskartongin, testilainerin ja taivekartongin valmistuksessa. Kierrätysprosessin ensisijaisia tehtäviä ovat kuidutus ja epäpuhtauksien poisto sekä näiden epäpuhtauksien vaikutusten eliminointi, jotta kierrätysmassan laatuvaatimukset täyttyvät. Lisääntynyt epäpuhtauksien määrä raaka-aineessa asettaa vaatimuksia lajitteluprosessin kehittämiseksi. Nykyaikaisilla kierrätyslaitoksilla ei pystytä käsittelemään ylettömiä määriä epäpuhtauksia. Epäpuhtaudet aiheuttavat ongelmia ajettavuuteen ja heikentävät tuotteen laatua kierrätysprosessissa. Epäpuhtauksien poistoon on olemassa useita teknisiä ratkaisuja, mutta minkään niistä ei ole todettu täysin poistavan kaikkia ongelmia. Työn kokeellisessa osassa kartongin päällystykseen käytettävää hydrofobista materiaalia analysoitiin erilaisin menetelmin. Tutkittiin myös erilaisten olosuhteiden vaikutusta tämän materiaalin poistoon.

Hydrodynamics and Heat Transfer in an Airlift Reactor

Työn teoriaosassa esitetään kirjallisuudessa esiintyviä teoreettisia ja kokeellisia yhtälöitä nesteen nopeuden, kaasun tilavuusosuuden, painehäviön ja lämmönsiirron laskemiseksi. Lisäksi käsitellään airlift-reaktoreiden toimintaa, rakennetta ja teollisia sovelluksia, sekä sekoitusta ja geometrian vaikutusta airlift-reaktoreiden hydrodynaamisiin ominaisuuksiin. Kokeellisessa osassa kuvataan käytetty koelaitteisto ja mittausmenetelmät sekä esitetään saadut koetulokset. Koelaitteisto on viidellä nousuputkella varustettu ulkoisen kierron airlift-reaktori. Kokeellisessa osassa pyritään ratkaisemaan tällaisessa reaktorissa mahdollisesti esiintyviä ongelmia, kuten "slug flown" muodostuminen nousuputkissa sekä fluidien epätasainen jakautuminen nousuputkiin. Lisäksi tutkitaan erilaisten muuttujien, kuten kaasun tilavuusvirran, nesteen viskositeetin, suutinkoon ja nesteen jakoputken rakenteen, vaikutusta kaasun tilavuusosuuteen ja nesteen nopeuteen nousuputkissa. Nesteen nopeudet mitataan merkkiainemenetelmällä ja kaasun tilavuusosuudet manometrimenetelmällä. Lämmönsiirtoa tutkitaan mittaamalla lämpötilaeroja nousuputkissa NiCr-Ni –termoelementeillä. Mittaustulosten perusteella muokataan korrelaatiot kaasun tilavuusosuudelle ja nesteen tyhjäputkinopeudelle. Korrelaatioista lasketut tulokset sopivat kohtuullisen hyvin yhteen mitattujen tulosten kanssa. "Slug flown" ei todettu muodostuvan ongelmaksi 2.5 mPa s pienemmillä viskositeetin arvoilla 2 metriä pitkissä ja 19 mm halkaisijaltaan olevissa putkissa. Lisäksi todettiin, että kaasu- ja nestefaasien jakautumisongelmat voidaan ratkaista rakenteellisesti.

APPLICATION OF OZONE AIMING TO KEEP THE QUALITY OF STRAWBERRIES USING A LOW COST REACTOR

RESUMO O morango é uma fruta de alto valor comercial e tem uma rápida deterioração, como a demanda por produtos saudáveis, seguros sob o ponto de vista microbiológico e livre de produtos químicos aumenta cada vez mais, o método de aplicação do gás ozônio em uma atmosfera controlada foi proposto. O objetivo deste trabalho foi verificar a eficiência do gás ozônio produzido por um reator, a fim de que os pequenos produtores de morangos possam usá-lo, contribuindo, assim, para as economias regionais. Morangos (Fragaria ananassa) variedade Oso Grande, colhidasna região de Minas Gerais foram divididas dois grupos: o primeiro recebeu tratamento com ozônio e o segundo não. No primeiro grupo, o ozônio foi aplicado durante 20 minutos a partir de um reator de Corona. Os frutos foram armazenados a 4 ° C, por períodos de 5, 10 e 15 dias. A qualidade dos frutos foi relata a partir dos níveis de sólidos solúveis totais (SS), acidez titulável (AT ), pH, compostos fenólicos (CF), ácido ascórbico (AA), perda de massa fresca (PM%) e análise microbiológica (AM), em diferentes tempos de armazenamento de frutos ozonizados e não ozonizados. O uso de gás ozônio foi eficiente para a pós-colheita de morango. Os níveis de microrganismos estão dentro dos limites aceitáveis e as propriedades físicas e químicas foram mantidas.

Structure of a-Si:H/a-Si1-xCx:H multilayers deposited in a reactor with automated substrate holder

This paper deals with the structural properties of a-Si:H/a-Si1-xCx: H multilayers deposited by glow-discharge decomposition of SiH4 and SiH4 and CH4 mixtures. The main feature of the rf plasma reactor is an automated substrate holder. The plasma stabilization time and its influence on the multilayer obtained is discussed. A series of a-Si:H/a-Si1-xCx: H multilayers has been deposited and characterized by secondary ion mass spectrometry (SIMS), X-ray diffraction (XRD) and transmission electron microscopy (TEM). No asymmetry between the two types of interface has been observed. The results show that the multilayers present a very good periodicity and low roughness. The difficulty of determining the abruptness of the multilayer at the nanometer scale is discussed.

Fischer-Tropsch Slurry Bubble Column Reactor Modeling

The literature part of the work reviews overall Fischer-Tropsch process, Fischer-Tropsch reactors and catalysts. Fundamentals of Fischer-Tropsch modeling are also presented. The emphasis is on the reactor unit. Comparison of the reactors and the catalysts is carried out to choose the suitable reactor setup for the modeling work. The effects of the operation conditions are also investigated. Slurry bubble column reactor model operating with cobalt catalyst is developed by taking into account the mass transfer of the reacting components (CO and H2) and the consumption of the reactants in the liquid phase. The effect of hydrostatic pressure and the change in total mole flow rate in gas phase are taken into account in calculation of the solubilities. The hydrodynamics, reaction kinetics and product composition are determined according to literature. The cooling system and furthermore the required heat transfer area and number of cooling tubes are also determined. The model is implemented in Matlab software. Commercial scale reactor setup is modeled and the behavior of the model is investigated. The possible inaccuraries are evaluated and the suggestions for the future work are presented. The model is also integrated to Aspen Plus process simulation software, which enables the usage of the model in more extensive Fischer-Tropsch process simulations. Commercial scale reactor of diameter of 7 m and height of 30 m was modeled. The capacity of the reactor was calculated to be about 9 800 barrels/day with CO conversion of 75 %. The behavior of the model was realistic and results were in the right range. The highest uncertainty to model was estimated to be caused by the determination of the kinetic rate.

Coolant Flow and Heat Transfer in Pebble-Bed Reactor Core

This thesis gathers knowledge about ongoing high-temperature reactor projects around the world. Methods for calculating coolant flow and heat transfer inside a pebble-bed reactor core are also developed. The thesis begins with the introduction of high-temperature reactors including the current state of the technology. Process heat applications that could use the heat from a high-temperature reactor are also introduced. A suitable reactor design with data available in literature is selected for the calculation part of the thesis. Commercial computational fluid dynamics software Fluent is used for the calculations. The pebble-bed is approximated as a packed-bed, which causes sink terms to the momentum equations of the gas flowing through it. A position dependent value is used for the packing fraction. Two different models are used to calculate heat transfer. First a local thermal equilibrium is assumed between the gas and solid phases and a single energy equation is used. In the second approach, separate energy equations are used for the phases. Information about steady state flow behavior, pressure loss, and temperature distribution in the core is obtained as results of the calculations. The effect of inlet mass flow rate to pressure loss is also investigated. Data found in literature and the results correspond each other quite well, considered the amount of simplifications in the calculations. The models developed in this thesis can be used to solve coolant flow and heat transfer in a pebble-bed reactor, although additional development and model validation is needed for better accuracy and reliability.