951 resultados para Air-flow Rate


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Natural ventilation is an efficient bioclimatic strategy, one that provides thermal comfort, healthful and cooling to the edification. However, the disregard for quality environment, the uncertainties involved in the phenomenon and the popularization of artificial climate systems are held as an excuse for those who neglect the benefits of passive cooling. The unfamiliarity with the concept may be lessened if ventilation is observed in every step of the project, especially in the initial phase in which decisions bear a great impact in the construction process. The tools available in order to quantify the impact of projected decisions consist basically of the renovation rate calculations or computer simulations of fluids, commonly dubbed CFD, which stands for Computational Fluid Dynamics , both somewhat apart from the project s execution and unable to adapt for use in parametric studies. Thus, we chose to verify, through computer simulation, the representativeness of the results with a method of simplified air reconditioning rate calculation, as well as making it more compatible with the questions relevant to the first phases of the project s process. The case object consists of a model resulting from the recommendations of the Código de Obras de Natal/ RN, customized according to the NBR 15220. The study has shown the complexity in aggregating a CFD tool to the process and the need for a method capable of generating data at the compatible rate to the flow of ideas and are discarded during the project s development. At the end of our study, we discuss the necessary concessions for the realization of simulations, the applicability and the limitations of both the tools used and the method adopted, as well as the representativeness of the results obtained

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Os oceanos representam um dos maiores recursos naturais, possuindo expressivo potencial energético, podendo suprir parte da demanda energética mundial. Nas últimas décadas, alguns dispositivos destinados à conversão da energia das ondas dos oceanos em energia elétrica têm sido estudados. No presente trabalho, o princípio de funcionamento do conversor do tipo Coluna de Água Oscilante, do inglês Oscillating Water Colum, (OWC) foi analisado numericamente. As ondas incidentes na câmara hidro-pneumática da OWC, causam um movimento alternado da coluna de água no interior da câmara, o qual produz um fluxo alternado de ar que passa pela chaminé. O ar passa e aciona uma turbina a qual transmite energia para um gerador elétrico. O objetivo do presente estudo foi investigar a influência de diferentes formas geométricas da câmara sobre o fluxo resultante de ar que passa pela turbina, que influencia no desempenho do dispositivo. Para isso, geometrias diferentes para o conversor foram analisadas empregando modelos computacionais 2D e 3D. Um modelo computacional desenvolvido nos softwares GAMBIT e FLUENT foi utilizado, em que o conversor OWC foi acoplado a um tanque de ondas. O método Volume of Fluid (VOF) e a teoria de 2ª ordem Stokes foram utilizados para gerar ondas regulares, permitindo uma interação mais realista entre o conversor, água, ar e OWC. O Método dos Volumes Finitos (MVF) foi utilizado para a discretização das equações governantes. Neste trabalho o Contructal Design (baseado na Teoria Constructal) foi aplicado pela primeira vez em estudos numéricos tridimensionais de OWC para fim de encontrar uma geometria que mais favorece o desempenho do dispositivo. A função objetivo foi a maximização da vazão mássica de ar que passa através da chaminé do dispositivo OWC, analisado através do método mínimos quadrados, do inglês Root Mean Square (RMS). Os resultados indicaram que a forma geométrica da câmara influencia na transformação da energia das ondas em energia elétrica. As geometrias das câmaras analisadas que apresentaram maior área da face de incidência das ondas (sendo altura constante), apresentaram também maior desempenho do conversor OWC. A melhor geometria, entre os casos desse estudo, ofereceu um ganho no desempenho do dispositivo em torno de 30% maior.

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To gain a better understanding of the fluid–structure interaction and especially when dealing with a flow around an arbitrarily moving body, it is essential to develop measurement tools enabling the instantaneous detection of moving deformable interface during the flow measurements. A particularly useful application is the determination of unsteady turbulent flow velocity field around a moving porous fishing net structure which is of great interest for selectivity and also for the numerical code validation which needs a realistic database. To do this, a representative piece of fishing net structure is used to investigate both the Turbulent Boundary Layer (TBL) developing over the horizontal porous moving fishing net structure and the turbulent flow passing through the moving porous structure. For such an investigation, Time Resolved PIV measurements are carried out and combined with a motion tracking technique allowing the measurement of the instantaneous motion of the deformable fishing net during PIV measurements. Once the two-dimensional motion of the porous structure is accessed, PIV velocity measurements are analyzed in connection with the detected motion. Finally, the TBL is characterized and the effect of the structure motion on the volumetric flow rate passing though the moving porous structure is clearly demonstrated.

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Study developed in order to know the carpet influence when used in the floor of a hotel room. Twelve air samples of 250L (six in a room with carpet and six more in a room with wood floor) were collected through an impaction method with a flow rate of 140 L/min onto malt extract agar (MEA) supplemented with chloramphenicol (0.05%), using the Millipore air Tester (Millipore), during cleaning activities. Outdoor sample was also performed to be used as a reference. Surface samples from floor and desks, taken at the same time, were collected by the swabbing method. to 7 days. Besides fungal contamination, we also assessed particulate matter contamination in both rooms during the same cleaning tasks. In the analyzed sur- faces, isolates belonging to Aspergillus fumigatus complex were the only fungi found in the carpeted room, whereas in the other room we found Penicllium sp. (63.6%) and Aspergillus sp. (13.6%) as the most frequent genera. In the case of particles the room with carpet obtained significant higher values for both metrics (PMC and PNC), showing that carpet may has influence on particles’ contamination of the room.

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The off-cycle refrigerant mass migration has a direct influence on the on-cycle performance since compressor energy is necessary to redistribute the refrigerant mass. No studies, as of today, are available in the open literature which experimentally measured the lubricant migration within a refrigeration system during cycling or stop/start transients. Therefore, experimental procedures measuring the refrigerant and lubricant migration through the major components of a refrigeration system during stop/start transients were developed and implemented. Results identifying the underlying physics are presented. The refrigerant and lubricant migration of an R134a automotive A/C system-utilizing a fixed orifice tube, minichannel condenser, plate and fin evaporator, U-tube type accumulator and fixed displacement compressor-was measured across five sections divided by ball valves. Using the Quick-Closing Valve Technique (QCVT) combined with the Remove and Weigh Technique (RWT) using liquid nitrogen as the condensing agent resulted in a measurement uncertainty of 0.4 percent regarding the total refrigerant mass in the system. The determination of the lubricant mass distribution was achieved by employing three different techniques-Remove and Weigh, Mix and Sample, and Flushing. To employ the Mix and Sample Technique a device-called the Mix and Sample Device-was built. A method to separate the refrigerant and lubricant was developed with an accuracy-after separation-of 0.04 grams of refrigerant left in the lubricant. When applying the three techniques, the total amount of lubricant mass in the system was determined to within two percent. The combination of measurement results-infrared photography and high speed and real time videography-provide unprecedented insight into the mechanisms of refrigerant and lubricant migration during stop-start operation. During the compressor stop period, the primary refrigerant mass migration is caused by, and follows, the diminishing pressure difference across the expansion device. The secondary refrigerant migration is caused by a pressure gradient as a result of thermal nonequilibrium within the system and causes only vapor phase refrigerant migration. Lubricant migration is proportional to the refrigerant mass during the primary refrigerant mass migration. During the secondary refrigerant mass migration lubricant is not migrating. The start-up refrigerant mass migration is caused by an imbalance of the refrigerant mass flow rates across the compressor and expansion device. The higher compressor refrigerant mass flow rate was a result of the entrainment of foam into the U-tube of the accumulator. The lubricant mass migration during the start-up was not proportional to the refrigerant mass migration. The presence of water condensate on the evaporator affected the refrigerant mass migration during the compressor stop period. Caused by an evaporative cooling effect the evaporator held 56 percent of the total refrigerant mass in the system after three minutes of compressor stop time-compared to 25 percent when no water condensate was present on the evaporator coil. Foam entrainment led to a faster lubricant and refrigerant mass migration out of the accumulator than liquid entrainment through the hole at the bottom of the U-tube. The latter was observed for when water condensate was present on the evaporator coil because-as a result of the higher amount of refrigerant mass in the evaporator before start-up-the entrainment of foam into the U-tube of the accumulator ceased before the steady state refrigerant mass distribution was reached.

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A fixação biológica de dióxido de carbono por microalgas é considerada a melhor forma de fixar CO2. Dentre os microrganismos utilizados destaca-se Spirulina platensis devido às suas altas taxas de fixação de CO2 e variedade de aplicações da biomassa gerada. A aplicação de modelos e simulações pode auxiliar na previsão de custos e na escolha das condições ideais de cultivo. Este trabalho teve como objetivo etsabelecer um modelo cinético no qual a iluminância é o fator limitante para o crescimento da microalga Spirulina platensis. A fim de validar o modelo proposto foi utilizada a microalga S. platensis, cultivada em meio Zarrouk modificado (NaHCO3 1,0 g.L-1 ), em biorreator aberto tipo raceway de 200L, mantido a 30°C, sob iluminação natural. A concentração celular variou de 0,19 a 0,34 g.L-1 e a velocidade específica de crescimento celular obtida a partir da regressão exponencial das curvas de crescimento de cada período iluminado variou de 0,55 a 0,59 d-1 . O modelo proposto gerou dados estimados satisfatórios (r2 =0,97). De acordo com os dados obtidos 16,2% da biomassa é consumida durante o período não iluminado.

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A reduzida informação e o pouco trabalho científico desenvolvido na área de sistemas de combustão de biomassa de média potência, faz dos objectivos propostos neste trabalho elementos importantes. O trabalho científico a seguir apresentado, vai permitir obter as bases para o desenvolvimento de condições apropriadas de operação de sistemas de combustão a biomassa, aumentando a eficiência e a rentabilidade económica deste tipo de sistema energético. O principal objetivo do presente trabalho consistiu na aplicação de metodologias de monitorização que permitam caracterizar e melhorar a eficiência do sistema de combustão, na implementação dos métodos escolhidos e na monitorização das condições de operação de uma caldeira industrial de combustão de biomassa, destacando-se: (i) monitorização dos caudais de alimentação de biomassa à caldeira realizada por sistemas de alimentação sem-fim; (ii) análise e monitorização de temperaturas e pressão; (iii) monitorização do caudal de ar de combustão; (iv) monitorização do caudal de gases de exaustão; (v) monitorização da potência térmica; (vi) monitorização da composição do efluente gasoso. A caracterização físicas de amostras de biomassa, o teste a diferentes tipos de biomassa com diferentes condições de operação e a recolha de amostras de cinzas de combustão para a caracterização físico-química são outros métodos de monitorização e caracterização aplicados. Também foi desenvolvido e aplicado um ensaio de controlo do sistema de alimentação em modo de operação manual e comparado com o sistema de controlo do sistema de alimentação em modo de operação automático. O estudo realizado permite concluir que deve ser desenvolvido e implementado um algoritmo de controlo e operação da fornalha que permita um doseamento mais adequado dos caudais de combustível e ar de combustão com vista a melhorar o desempenho do sistema combustão.

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As metas da União Europeia para 2020 em termos de biocombustíveis e biolíquidos traduziram-se, na última década, num destaque da indústria de biodiesel em Portugal. Inerente ao processo de produção biodiesel está um subproduto, o glicerol bruto, cujo estudo tem vindo a ser alvo de interesse na comunidade científica. O objetivo principal deste trabalho consistiu no estudo da gasificação do glicerol técnico e do glicerol bruto, usando vapor como agente oxidante. Pretendeu-se avaliar a composição do gás de produção obtido e os parâmetros de gasificação, como a percentagem de conversão de carbono e de hidrogénio, o rendimento de gás seco, a eficiência de gás frio e o poder calorífico do gás produzido. No estudo da gasificação do glicerol técnico avaliou-se o efeito da temperatura na performance do processo, entre 750 – 1000 ºC, e estudou-se ainda o efeito do caudal de alimentação ao reator (3,8 mL/min, 6,5 mL/min e 10,0 mL/min). Para o caudal mais baixo, estudou-se o efeito da razão de mistura glicerol/água (25/75, 40/60, 60/40 e 75/25) e para a razão de mistura 60/40 foi avaliada a influência da adição de ar como agente gasificante. O estudo da gasificação do glicerol bruto foi feito realizando ensaios de gasificação numa gama de temperaturas de 750 ºC a 1000 ºC, para uma razão de mistura glicerol/água (60/40) com o caudal de 3,8 mL/min e usando apenas vapor de água como agente de gasificação. Os ensaios foram realizados num reator de leito fixo de 500 mm de comprimento e 90 mm de diâmetro interno, composto por um leito de alumina com partículas de 5 mm de diâmetro. O aquecimento foi realizado com um forno elétrico de 4 kW. A amostra de gás de produção recolhida foi analisada por cromatografia gasosa com detector de termocondutividade. Os resultados obtidos na gasificação do glicerol técnico, revelaram que a temperatura é uma variável preponderante no desempenho do processo de gasificação. À exceção do poder calorífico superior, para o qual se obteve uma ligeira diminuição de valores com o aumento da temperatura, os valores mais elevados dos parâmetros de gasificação foram obtidos para temperaturas superiores a 900 ºC. Esta temperatura parece ser determinante no modelo cinético de gasificação do glicerol, condicionando a composição do gás de produção obtido. Concluiu-se ainda que, na gama de caudais testada, o caudal de alimentação ao reator não teve influência no processo de gasificação. Os ensaios realizados para avaliar o efeito da razão de mistura permitiram verificar que, o aumento da adição de água à alimentação se traduz na redução do teor de CO e de CH4 e no aumento do teor de H2 e CO2, no gás de produção. Para a razão de mistura 25/75 foram obtidos valores de 1,3 para o rácio H2/CO para temperaturas superiores a 900 ºC. A influência da adição de água tornou-se mais evidente nos ensaios de gasificação realizados a temperaturas superiores a 900 ºC. Verificou-se um aumento da conversão de carbono, do rendimento de gás seco e da eficiência do gás frio e uma ligeira diminuição do poder calorífico e da potência disponível, no gás de produção. Para as razões de misturas 60/40 e 40/60 obtiveram-se resultados, para os parâmetros de gasificação, da mesma ordem de grandeza e com valores intermédios entre os obtidos para as razões de mistura 25/75 e 75/25. Porém, quanto maior o teor de água alimentado maior o consumo de energia associado à vaporização da água. Assim, o aumento do teor de água na mistura só apresentará interesse industrial se o objetivo passar pela produção de hidrogénio. Quanto ao efeito da adição de ar como agente de gasificação, os resultados obtidos dão indicação que se poderão potenciar algumas reações exotérmicas que contribuirão para a redução do consumo energético global do processo. Por outro lado, o gás de produção apresentou um rácio H2/CO interessante do ponto de vista da sua aplicação industrial, superior em 35 % ao verificado para a gasificação efetuada apenas na presença de vapor. À exceção do decréscimo no valor do poder calorífico superior do gás de produção, os restantes parâmetros estudados apresentaram a mesma ordem de grandeza, dos obtidos para o estudo da mesma razão de mistura na ausência de ar. Relativamente ao estudo da gasificação do glicerol bruto, obtiveram-se valores de rácio H2/CO e eficiência de gás frio mais elevados que os valores obtidos para a mesma razão de mistura usando glicerol técnico. Os demais parâmetros de gasificação avaliados mostraram-se semelhantes entre as duas matérias-primas, verificando-se apenas uma ligeira diminuição no valor do poder calorífico superior do gás produzido com glicerol bruto. Os resultados obtidos demonstram a possibilidade de valorização energética do glicerol bruto resultante da produção de biodiesel.

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Natural ventilation is an efficient bioclimatic strategy, one that provides thermal comfort, healthful and cooling to the edification. However, the disregard for quality environment, the uncertainties involved in the phenomenon and the popularization of artificial climate systems are held as an excuse for those who neglect the benefits of passive cooling. The unfamiliarity with the concept may be lessened if ventilation is observed in every step of the project, especially in the initial phase in which decisions bear a great impact in the construction process. The tools available in order to quantify the impact of projected decisions consist basically of the renovation rate calculations or computer simulations of fluids, commonly dubbed CFD, which stands for Computational Fluid Dynamics , both somewhat apart from the project s execution and unable to adapt for use in parametric studies. Thus, we chose to verify, through computer simulation, the representativeness of the results with a method of simplified air reconditioning rate calculation, as well as making it more compatible with the questions relevant to the first phases of the project s process. The case object consists of a model resulting from the recommendations of the Código de Obras de Natal/ RN, customized according to the NBR 15220. The study has shown the complexity in aggregating a CFD tool to the process and the need for a method capable of generating data at the compatible rate to the flow of ideas and are discarded during the project s development. At the end of our study, we discuss the necessary concessions for the realization of simulations, the applicability and the limitations of both the tools used and the method adopted, as well as the representativeness of the results obtained

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Nearly 3 x 1011 m3 of medium and light oils will remain in reservoirs worldwide after conventional recovery methods have been exhausted and much of this volume would be recovered by Enhanced Oil Recovery (EOR) methods. The in-situ combustion (ISC) is an EOR method in which an oxygen-containing gas is injected into a reservoir where it reacts with the crude oil to create a high-temperature combustion front that is propagated through the reservoir. The High Pressure Air Injection (HPAI) method is a particular denomination of the air injection process applied in light oil reservoirs, for which the combustion reactions are dominant between 150 and 300°C and the generation of flue gas is the main factor to the oil displacement. A simulation model of a homogeneous reservoir was built to study, which was initially undergone to primary production, for 3 years, next by a waterflooding process for 21 more years. At this point, with the mature condition established into the reservoir, three variations of this model were selected, according to the recovery factors (RF) reached, for study the in-situ combustion (HPAI) technique. Next to this, a sensitivity analysis on the RF of characteristic operational parameters of the method was carried out: air injection rate per well, oxygen concentration into the injected gas, patterns of air injection and wells perforations configuration. This analysis, for 10 more years of production time, was performed with assistance of the central composite design. The reservoir behavior and the impacts of chemical reactions parameters and of reservoir particularities on the RF were also evaluated. An economic analysis and a study to maximize the RF of the process were also carried out. The simulation runs were performed in the simulator of thermal processes in reservoirs STARS (Steam, Thermal, and Advanced Processes Reservoir Simulator) from CMG (Computer Modelling Group). The results showed the incremental RF were small and the net present value (NPV) is affected by high initial investments to compress the air. It was noticed that the adoption of high oxygen concentration into the injected gas and of the five spot pattern tends to improve the RF, and the wells perforations configuration has more influence with the increase of the oil thickness. Simulated cases relating to the reservoir particularities showed that smaller residual oil saturations to gas lead to greater RF and the presence of heterogeneities results in important variations on the RF and on the production curves

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The occurrence of heavy oil reservoirs have increased substantially and, due to the high viscosity characteristic of this type of oil, conventional recovery methods can not be applied. Thermal methods have been studied for the recovery of this type of oil, with a main objective to reduce its viscosity, by increasing the reservoir temperature, favoring the mobility of the oil and allowing an increasing in the productivity rate of the fields. In situ combustion (ISC) is a thermal recovery method in which heat is produced inside the reservoir by the combustion of part of the oil with injected oxygen, contrasting with the injection of fluid that is heated in the surface for subsequent injection, which leads to loss heat during the trajectory to the reservoir. The ISC is a favorable method for recovery of heavy oil, but it is still difficult to be field implemented. This work had as an objective the parametric analysis of ISC process applied to a semi-synthetic reservoir with characteristics of the Brazilian Northeast reservoirs using vertical production and vertical injection wells, as the air flow injection and the wells completions. For the analysis, was used a commercial program for simulation of oil reservoirs using thermal processes, called Steam, Thermal and Advanced Processes Reservoir Simulator (STARS) from Computer Modelling Group (CMG). From the results it was possible to analyze the efficiency of the ISC process in heavy oil reservoirs by increasing the reservoir temperature, providing a large decrease in oil viscosity, increasing its mobility inside the reservoir, as well as the improvement in the quality of this oil and therefore increasing significantly its recovered fraction. Among the analyzed parameters, the flow rate of air injection was the one which had greater influence in ISC, obtaining higher recovery factor the higher is the flow rate of injection, due to the greater amount of oxygen while ensuring the maintenance of the combustion front

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Le nettoyage des systèmes de Chauffage, Ventilation et Climatisation de l’Air est important pour assurer une bonne qualité d’air intérieur. Le déclenchement de leur nettoyage est basé sur une inspection visuelle qui ne tient pas compte du contenu en moisissures, lesquelles ont des effets sur le système respiratoire. Cette recherche vise à proposer une méthode d’évaluation du contenu en moisissures afin d’aider les gestionnaires d’immeuble. Cinq générations de poussières ont été effectuées pour simuler un conduit de ventilation. Une cassette modifiée 37 mm et un filtre CPV pré-pesés ont utilisés pour collecter les poussières déposées avec une pompe calibrée à 15L/min. Les pourcentages de collecte des cassettes et des filtres ont été calculés pour 54 échantillons. Dix générations supplémentaires de poussières ont été effectuées concomitamment avec la génération de spores. Soixante échantillons ont été analysés selon quatre méthodes : culture, comptage direct des spores par microscopie (CDSM), dosage de β-N-acétylhexosaminidase (NAHA), 18S-q-PCR. La limite de détection (LD), la réplicabilité, la répétabilité, le nombre de spores et le coefficient de corrélation (r) ont été déterminés. Les récupérations de poussières étaient supérieures à 84%. Selon la méthode analytique, les concentrations médianes de spores/100 cm² allaient de 10 000 à 815 000. Les LD variaient dépendamment de la méthode de 120 à 218 000 spores/100 cm² et r de -0,08 à 0,83. La réplicabilité et la répétabilité étaient de 1% et 1% pour PCR; 5% et 10% pour CDSM; 6% et 15% pour NAHA; 12% et 11% pour culture. La méthode de collecte a démontré une excellente efficacité de récupération. La PCR est la méthode analytique recommandée pour l’évaluation fongique des systèmes de ventilation. Une validation terrain est en cours.

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Measurement and modeling techniques were developed to improve over-water gaseous air-water exchange measurements for persistent bioaccumulative and toxic chemicals (PBTs). Analytical methods were applied to atmospheric measurements of hexachlorobenzene (HCB), polychlorinated biphenyls (PCBs), and polybrominated diphenyl ethers (PBDEs). Additionally, the sampling and analytical methods are well suited to study semivolatile organic compounds (SOCs) in air with applications related to secondary organic aerosol formation, urban, and indoor air quality. A novel gas-phase cleanup method is described for use with thermal desorption methods for analysis of atmospheric SOCs using multicapillary denuders. The cleanup selectively removed hydrogen-bonding chemicals from samples, including much of the background matrix of oxidized organic compounds in ambient air, and thereby improved precision and method detection limits for nonpolar analytes. A model is presented that predicts gas collection efficiency and particle collection artifact for SOCs in multicapillary denuders using polydimethylsiloxane (PDMS) sorbent. An approach is presented to estimate the equilibrium PDMS-gas partition coefficient (Kpdms) from an Abraham solvation parameter model for any SOC. A high flow rate (300 L min-1) multicapillary denuder was designed for measurement of trace atmospheric SOCs. Overall method precision and detection limits were determined using field duplicates and compared to the conventional high-volume sampler method. The high-flow denuder is an alternative to high-volume or passive samplers when separation of gas and particle-associated SOCs upstream of a filter and short sample collection time are advantageous. A Lagrangian internal boundary layer transport exchange (IBLTE) Model is described. The model predicts the near-surface variation in several quantities with fetch in coastal, offshore flow: 1) modification in potential temperature and gas mixing ratio, 2) surface fluxes of sensible heat, water vapor, and trace gases using the NOAA COARE Bulk Algorithm and Gas Transfer Model, 3) vertical gradients in potential temperature and mixing ratio. The model was applied to interpret micrometeorological measurements of air-water exchange flux of HCB and several PCB congeners in Lake Superior. The IBLTE Model can be applied to any scalar, including water vapor, carbon dioxide, dimethyl sulfide, and other scalar quantities of interest with respect to hydrology, climate, and ecosystem science.

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Le nettoyage des systèmes de Chauffage, Ventilation et Climatisation de l’Air est important pour assurer une bonne qualité d’air intérieur. Le déclenchement de leur nettoyage est basé sur une inspection visuelle qui ne tient pas compte du contenu en moisissures, lesquelles ont des effets sur le système respiratoire. Cette recherche vise à proposer une méthode d’évaluation du contenu en moisissures afin d’aider les gestionnaires d’immeuble. Cinq générations de poussières ont été effectuées pour simuler un conduit de ventilation. Une cassette modifiée 37 mm et un filtre CPV pré-pesés ont utilisés pour collecter les poussières déposées avec une pompe calibrée à 15L/min. Les pourcentages de collecte des cassettes et des filtres ont été calculés pour 54 échantillons. Dix générations supplémentaires de poussières ont été effectuées concomitamment avec la génération de spores. Soixante échantillons ont été analysés selon quatre méthodes : culture, comptage direct des spores par microscopie (CDSM), dosage de β-N-acétylhexosaminidase (NAHA), 18S-q-PCR. La limite de détection (LD), la réplicabilité, la répétabilité, le nombre de spores et le coefficient de corrélation (r) ont été déterminés. Les récupérations de poussières étaient supérieures à 84%. Selon la méthode analytique, les concentrations médianes de spores/100 cm² allaient de 10 000 à 815 000. Les LD variaient dépendamment de la méthode de 120 à 218 000 spores/100 cm² et r de -0,08 à 0,83. La réplicabilité et la répétabilité étaient de 1% et 1% pour PCR; 5% et 10% pour CDSM; 6% et 15% pour NAHA; 12% et 11% pour culture. La méthode de collecte a démontré une excellente efficacité de récupération. La PCR est la méthode analytique recommandée pour l’évaluation fongique des systèmes de ventilation. Une validation terrain est en cours.

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Indoor environmental conditions in classrooms, in particular temperature and indoor air quality, influence students’ health, attitude and performance. In recent years, several studies regarding indoor environmental quality of classrooms were published and natural ventilation proved to have great potential, particularly in southern European climate. This research aimed to evaluate indoor environmental conditions in eight schools and to assess their improvement potential by simple natural ventilation strategies. Temperature, relative humidity and carbon dioxide concentration were measured in 32 classrooms. Ventilation performance of the classrooms was characterized using two techniques, first by fan pressurization measurements of the envelope airtightness and later by tracer gas measurements of the air change rate assuming different envelope conditions. A total of 110 tracer gas measurements were made and the results validated ventilation protocols that were tested afterward. The results of the ventilation protocol implementation were encouraging and, overall, a decrease on the CO2 concentration was observed without modifying the comfort conditions. Nevertheless, additional measurements must be performed for winter conditions.