Objetivo: Comparar in vitro la resistencia adhesiva a dentina de tres sistemas adhesivos universales con y sin aplicación de una sustancia neutralizadora de la capa inhibida de oxígeno. Materiales y métodos: La muestra estuvo conformada por 90 dientes bovinos, distribuidos aleatoriamente en 6 grupos (n=15): G1-Ambar™ Universal, G2-Tetric® N-bond, G3-Scotchbond™ Universal sin aplicación de sustancia inhibidora: alcohol Isopropílico y G4-Ambar™ Universal, G5-Tetric® N-bond, G6-Scotchbond™ Universal con aplicación de sustancia inhibidora. Los procedimientos adhesivos se realizaron según las indicaciones de cada fabricante y los procedimientos restauradores con cilindros (matrices tipo Tygon 4 x 2 mm) de resina compuesta Filtek™ Z350XT-A2. Las muestras fueron almacenadas en una estufa a 37°C (+/- 5°C) por 24 horas. Se evaluó la resistencia al cizallamiento a dentina en una máquina de ensayos universal Instrom (velocidad 0.5 mm/min/500N). Los resultados fueron analizados mediante estadística descriptiva (Media y desviación estándar) e inferencial (U Mann Whitney, Kruskal Wallis). Resultados: La media y desviación estándar registrada para los grupos con y sin aplicación de alcohol Isopropílico fue; Ambar™ Universal (13.7±5.7) (14.0±5.2), Tetric® N-Bond Universal (16.5±7.2) (14.2±3.9) y Scotchbond™ Universal (13.6±4.5) (18.3±7.5) respectivamente. No se encontraron diferencias estadísticamente significativas en la resistencia adhesiva a dentina de los adhesivos universales con (p=0.528) y sin (p=0.193) aplicación de la sustancia neutralizadora. Conclusión: Los valores de resistencia adhesiva a dentina de los sistemas adhesivos universales con y sin aplicación de alcohol Isopropílico como sustancia neutralizadora de la capa inhibida de oxígeno no presentaron diferencias estadísticamente significativas. / Objective: Compare in vitro bond strength to dentin of three universal adhesive systems with and without application of an oxygen-inhibited layer neutralizing substance. Materials and methods: The sample was composed by 90 bovine teeth, randomly distributed in 6 groups (n=15): G1-Ambar™ Universal, G2-Tetric® N-bond, G3-Scotchbond™ Universal without application of inhibiting substance: Isopropyl alcohol and G4-Ambar™ Universal, G5-Tetric® N-bond, G6-Scotchbond™ Universal with application of inhibiting substance. Then, the adhesive phase was made according to each group and restorative procedures with composite resin Filtek™ Z350XT-A2, according to the manufacturer´s instructions. It was made of tygon composite resin (4 x 2 mm). The samples were stored in an incubator at 37°C (+/- 5°C) for 24 hours. Subsequently, dentin shear strength was evaluated on an Instrom universal testing machine (speed 0.5 mm/min/500N load). The results were analyzed using descriptive (mean and standard deviation) and inferential (U Mann Whitney, Kruskal Wallis) statistics. Results: Mean and standard deviation registered for the groups with and without application of Isopropyl alcohol was; Ambar™ Universal (13.7±5.7) (14.0±5.2), Tetric® N-Bond Universal (16.5±7.2) (14.2±3.9) and Scotchbond™ Universal (13.6±4.5) (18.3±7.5) respectively. No found statistical significant differences between bond strength in dentin of the universal adhesives with (p=0.528) and without (p=0.193) application of the neutralizing substance. Conclusion: The values of bond strength in dentin of the universal adhesive systems with and without application of Isopropyl alcohol as neutralizing substance of the oxygen inhibited layer did not show statistically significant differences. / Tesis

The design of heterogeneous catalysts for selective chemical conversions is a critical factor in developing a more sustainable and efficient chemical industry. In particular, there is significant interest in developing catalysts for the production and valorization of C₂‒C₄ oxygenates, which are versatile platform chemicals, especially from alternative sources of carbon. Promising catalysts for such transformations have been identified, but fundamental understanding of the reaction mechanisms and active sites on these catalytic materials is still lacking. This work utilized three representative reactions to develop this fundamental understanding through the use of model surfaces, probe molecules, in-situ characterization, and reactor evaluation. The three classes of reactions that were investigated are alcohol dehydration and dehydrogenation, ethylene hydroformylation, and olefin epoxidation. This work elucidates how interactions between active species, surface intermediates, and catalyst/support interfaces influence the catalytic performance of catalysts based on bimetallic and transition metal nitride materials. The first part of this dissertation used ethanol and isopropanol as biomass model compounds to probe the active sites of metal-modified molybdenum nitride catalysts. The non-oxidative dehydrogenation of alcohols is a route to synthesize aldehydes from biomass-derived alcohols while simultaneously producing hydrogen. Comparing the reaction pathways of ethanol, the simplest molecule containing O−H, C−H, C−O and C−C bonds that are present in biomass-derived molecules, with isopropanol, the simplest secondary alcohol, provided useful insights into the upgrading of more complex biomass. Chapter 3 compared the two alcohols on Cu-modified molybdenum nitride, and Chapter 4 focused solely on the reaction of isopropanol over Fe- and Pt-modified molybdenum nitride. This work showed how the orientation of intermediates, chemical state of active centers, and metal d-band structures influenced the bond scission preference. In addition, this work demonstrated effective strategies for promoting dehydrogenation over molybdenum nitride-based catalysts, as well as the feasibility of using model surface experiments to guide the design of practical powder catalysts. Following the investigations of the selective bond scission of oxygenates, Chapter 5 of the dissertation was focused on the production of C₃ oxygenate molecules through ethylene hydroformylation, a C−C coupling reaction. The influence of a mesoporous silica support on bimetallic interactions between Rh and Co for ethylene hydroformylation was elucidated through a systematic study of monometallic and bimetallic catalysts. In-situ vibrational studies suggested that the mesoporous silica-supported bimetallic catalyst facilitated moderate binding of important gem-dicarbonyl species that enabled facile co-adsorption of CO and ethylene, ultimately leading to improved hydroformylation performance. Kinetic measurements revealed a lower hydroformylation barrier for the Rh-Co bimetallic compared to the Rh monometallic catalyst. Then, Chapter 6 investigated another class of reaction, olefin epoxidation, focusing on the direct epoxidation of propylene with oxygen. The critical challenge of this reaction is facilitating the formation of the oxametallacycle intermediate and minimizing the abstraction of allylic hydrogen atoms. In this work, propylene oxide and 1-epoxy-3-butene were used to study the interaction between the epoxide ring and Ag(111) and Pt(111) model surfaces. Cu modification of Ag(111) was shown to lead to improved stabilization of the oxametallacycle. Following this, Pt(111) was used to identify the factors that influence the undesirable complete oxidation pathway. Chapter 7 outlined potential future avenues of research, which include the use molybdenum nitride-based catalysts for reactions of CO₂ and ethane, and propylene epoxidation with in-situ generated H₂O₂ as the oxidant.

Bioprocesses for air pollution control can generally be categorized as bioscrubber, biofilter, and biotrickling filter systems. These processes have been proven to be economical and effective for control of volatile organic compounds (VOCs) with concentrations of <1,000 mg C m-3 in gas streams. First, an activated sludge aeration tank (W x L x H = 40 x 40 x 300 cm) with a set of 2 mm orifice air spargers was utilized to treat gas-borne VOCs (toluene, p-xylene, and dichloromethane) in air streams. The effects of liquid depth (Z), aeration intensity (G/A), the overall mass transfer rate of oxygen in clean water (KLaO2), the Henry¡¦s law constant of the tested VOC (H), and the influent gaseous VOC concentration (C0) on the efficiency of removal of VOCs were examined and compared with a literature-cited model. Results show that the measured VOC removal efficiencies and those predicted by the model were comparable at a G/A of 3.75 ¡V 11.25 m3 m-2 hr-1 and C0 of around 1,000 ¡V 6,000 mg m-3. Experimental data also indicate that the designed gas treatment reactor with KLaO2 = 5 ¡V 15 hr-1, could achieve > 85% removal of VOCs with H = 0.24 ¡V 0.25 at an aerated liquid depth of 1 m, and > 95% removal of dichloromethane with H = 0.13 at a 1 m liquid depth. The model predicts that, for gas treatment in common activated sludge tanks, with KLaO2 = 5 ¡V 10 hr-1, depth = 3 ¡V 4.5 m, G/A = 9 ¡V 18 m3 m-2 hr-1, > 92% VOC removal can be achieved with operating parameters of Z of 3.0 m and KLaVOC/(G/A) of about 0.28 m-1, for VOCs with H < 0.3, such as most oxygen-containing hydrocarbons with low molecular weights, and benzene, toluene, ethylbenzene, and dichloromethane. Second, an activated sludge aeration tank and a sieve-plate column with six sieve plates were utilized to treat gas-borne VOCs in air streams. The tank was used for the biodegradation of the absorbed VOCs from the column which utilized the activated mixed liquor drawn from the tank as a scrubbing liquor. This research proposed a model for VOC absorption to a down-flow activated sludge liquor in a sieve-plate column. The experimental setup consisted of a pilot-scale activated-sludge tank and a sieve-plate tower, as demonstrated. The sieve-plate tower was constructed from a 25 x 25 x 162 cm (W x L x H) acrylic column with six custom-made sieve plates. Each plate has 382 holes which are 3 mm in diameter arranged on a square pitch. The holes give an open area of 3.82% of the whole plate area for gas flow. Two 25 mm-i.d. down-comer pipes were also equipped to allow for the downflow of the activated sludge liquor. Ports were provided at the column inlet, outlet, and each plate for gas and liquid sampling. Experiments were conducted and the model verified based on the results of tests on the removal efficiencies of isopropyl alcohol (IPA), toluene and p-xylene in the system operated at a range of influent VOC concentrations, air application rates, and liquid/gas flow ratios (L/G). The model developed by a material balance for the gaseous- and liquid-VOC over each plate of the column was developed and experimentally verified in this study. Superficial gas velocity over the column plate (U), number of plates (N), volumetric liquid-phase VOC-transfer coefficient (KLaVOC), aerated liquid depth over the plate (Z), volumetric liquid/gas flow-rate ratio (L/G), dimensionless Henry¡¦s law coefficient of the VOC to be absorbed (H), VOC content of the influent scrubbing liquor (xN+1), and the biodegradation rate constant of the VOC in the activated sludge mixed liquor (k) are among the affecting parameters to the effectiveness of the VOC removal. Model application by the model for effects of affecting parameters on the VOC removal effectiveness indicates that L/G, plate number N, biodegradation rate constant k, Henry¡¦s law constant of VOC H are among the important ones. A L/GH of greater than 2 and N of around 6 are enough for the effective (>90%) removal of the influent VOCs with H < 0.01 if no biodegradation occurred in the column. However, a N of over 16 is required for the influent VOCs with H of around 0.2. Biodegradation with a rate constant of around 100 hr-1 in the column greatly improves the column performance.

Abstract Isopropyl alcohol¡]IPA¡^and toluene are extensively used in industry as solvents. They are all highly toxic to animals and humans. Accordingly, IPA and toluene are strongly associated with problems of VOCs. In first step catalytic incineration was adopted to decompose IPA and toluene in laboratory, and the second step for a pilot-scale regenerative catalytic oxidizer ¡]RCO¡^were adopted to decompose mixture VOCs in real soil herein. The screening test of catalytic activity and the influences of the operational parameters on IPA and toluene removal efficiencies were widely discussed through catalytic incinerations of IPA and toluene in laboratory. The more effective and cheaper catalysts through above discussions of catalytic incineration were selected. And they were utilized in an pilot scale RCO as follows to investigate their performance in VOCs oxidation and RCO operations in THC removal of contamination soils. The achievements of this study are summarized as follows: ¡]1¡^Cu/Mn and Cu/Co gravel catalytic incinerations of isopropyl alcohol The results demonstrated that 10 wt% Cu0.6Co0.4 catalyst was the most effective because the CO2 yield reached 95 % under the following operating conditions; a temperature of 425oC, an inlet IPA concentration of 2500 ppm, an oxygen concentration of 21%, and a space velocity of 13500 hr-1. Additionally, the stability test results indicated that the 10 wt% Cu0.6Co0.4 catalyst exhibited excellent stability at both low and high conversion of IPA. ¡]2¡^20% Cu/Mn aluminum oxide catalytic incinerations of toluene The conversion for toluene reached 95% when the Cu/Mn catalyst was used with a metal ratio of 1:1 and 20% loading at 350¢XC, an influent toluene concentration of 1000 ppm, oxygen concentration of 21%, a space velocity of 12000 hr-1, and relative humidity of 26%. The long-term test was proceeded for seven days at a constant influent toluene concentration of 1000 ppm, constant oxygen concentration of 21%, constant space velocity of 12000 hr-1 and constant relative humidity of 26%. The SEM results indicated the Cu/Mn catalyst was quite stable at 350¢J. ¡]3¡^RCO testing for a copper/manganese catalyst of gaseous toluene The Cu/Mn (20wt%) catalyst was selected as the best one, because it converted 95% of the toluene at 400¢J. The results also indicating that the Cu/Mn catalyst was quite stable at 400¢J. (4) RTO treatment of VOCs with SVE system The conversion for VOCs reached 80% at 900¢XC, an influent VOCs concentration of 450-2000 ppm and a gas flow rate of 0.5 m3/min.The Thermal Recovery Efficiency¡]TRE¡^was approximately 86-90% in a RTO operated at 800-900¢J. (5)RCO treatment of VOCs with SVE system¡]10 wt% Cu0.6Co0.4 gravel catalyst¡^ The 10 wt% Cu0.6Co0.4 gravel catalyst was the poverty active, because it converted 65% of the VOCs by SVE system operated at 650¢J. (6)RCO treatment of VOCs with SVE system¡]20% Cu/Mn aluminum oxide catalytst¡^ The 20% Cu/Mn aluminum oxide catalytic was the best choice, because it converted 95% of the VOCs at 650¢J, an influent VOCs concentration of 450-10000 ppm and a gas flow rate of 0.5-1.5 m3/min. The SEM results indicated that the conversion of VOCs decay did not clearly vary at 650¢J, also indicating that the Cu/Mn catalyst selected was quite stable. The TRE was approximately 90% in a RCO¡]20% Cu/Mn aluminum oxide catalytic¡^operated at 650¢J. (7)RCO treatment of VOCs with SVE system¡]20% Cu/Mn gravel catalytst¡^ The 20% Cu/Mn gravel catalytst was the best selection , because it converted 95% of the VOCs at 600¢J, an influent VOCs concentration of 450-10000 ppm and a gas flow rate of 0.5-1.5 m3/min. The SEM results indicated that the conversion of VOCs decay did not clearly vary at 600¢J, also indicating that the Cu/Mn catalyst selected was quite stable. The TRE was approximately 90% in a RCO¡]20% Cu/Mn gravel catalytic¡^operated at 600¢J.

Esta investigação objetivou a eficácia antimicrobiana de agentes desinfetantes utilizados na desinfecção dos instrumentos endodônticos, durante o período transoperatório do tratamento endodôntico. A atividade antimicrobiana dos desinfetantes álcool isopropílico, acetona e ácido peracético (PAA) foi avaliada sobre microrganismos planctônicos através de teste de contato (time kill assay), utilizando inóculo de 9,9 X 109 a 1,2 X 1012 unidades formadoras de colônia (UFC) e por determinação da concentração bactericida mínima (CBM), usando inóculo de aproximadamente 106 UFC. Os agentes químicos também foram avaliados sobre Enterococcus faecalis (E. faecalis) ATCC 29212 cultivada em matriz de dentina (ex vivo) visando a formação de biofilme. O biofilme (organismos sésseis) microbiano foi removido com limas tipo Kerr (LK), até as lâminas estarem visualmente preenchidas. As LK contaminadas foram usadas como carreadores (logo após a contaminação ou secas dentro de uma câmara de fluxo laminar por 10 minutos). As LK carreadoras foram imersas em álcool isopropílico ou acetona ambos a 80%, ou em Ácido peracético 2%, por 30 ou 60 segundos. As limas foram posteriormente colocadas em tubos de ensaio contendo caldo Enterococcosel para observar o crescimento dos enterococos viáveis. Depois, os experimentos in vivo foram realizados com LK contaminadas por material necrótico pulpar da região cervical de dentes indicados para tratamento endodôntico. As LK contaminadas foram imersas, por 30 ou 60 segundos, em 80% de acetona ou 80% de álcool isopropílico ou 2% de PAA. As limas foram então inoculadas em tubos de ensaio contendo meio tioglicolato. Os organismos que cresceram, foram identificados após o tratamento com PAA. A corrosão mediada pelos agentes químicos também foi testada, após a incubação de LK de aço inoxidável e de NiTi por 60 minutos, medindo o peso das LK antes e depois da imersão e por microscopia eletrônica de varredura (MEV). Todos os agentes químicos foram capazes de eliminar ou reduzir a viabilidade das bactérias de espécies planctônicas Gram-negativas e Gram-positivas, embora a atividade dos produtos químicos sobre E. faecalis sésseis em testes de carreadores de LK demonstrou que o álcool isopropílico ou acetona foram incapazes de eliminar a contaminação bacteriana, especialmente, quando as limas foram secas previamente à exposição aos produtos químicos, por 15 ou 30 segundos. O PAA demonstrou a melhor atividade antimicrobiana e eliminou a viabilidade das células sésseis E. faecalis de ambas as limas endodônticas tipo K úmidas ou secas, após exposição por 15 segundos (100% de eliminação). Os experimentos desenvolvidos in vivo demonstraram que o PAA foi o agente mais eficaz (p<0,05), capaz de eliminar a viabilidade dos organismos em 92% das LK imersas depois de 60 segundos, quando comparado com acetona (64%) ou com álcool isopropílico (50%). O crescimento microbiano após o contato com o PAA demonstrou que somente o grupo dos Lactobacillus sp foi resistente a essa substância química. Os agentes químicos não demonstraram ser corrosivos, após a imersão por 1 hora, tanto por pesagem quanto por MEV. Foi observado que o PAA foi o agente mais eficaz para ser utilizado como desinfetante de instrumentos, durante o período transoperatório do tratamento endodôntico. / This investigation aimed to evaluate the antimicrobial efficacy of disinfectant agents used to maintain the disinfection of endodontic instruments during the transoperatory period in endodontic treatment. The antimicrobial activity of disinfectants isopropyl alcohol, acetone and peracetic acid were evaluated upon planktonic micro-organisms by time kill assay (contact test) using inoculums from 9,9 X 109 to 1,2 X 1012 colony forming units (CFU) and determination of minimal bactericidal concentration (MBC), using inoculums of 106 CFU. Chemical agents were also evaluated upon Enterococcus faecalis (E. faecalis) ATCC 29212 strain grown on matrix dentin (ex vivo) for biofilm formation. Biofilm (sessile organisms) were removed with Kerr files until the blades were visually filled and contaminated K files used as carriers (shortly after contamination or dried inside a flow chamber for 10 minutes). K files carriers were immersed in 80% isopropyl alcohol, 80% acetone or in 2% peracetic acid for 30 or 60 seconds. The files were subsequently dispensed into test tubes containing Enterococcosel broth to observe the growth of viable enterococci. Thereafter, in vivo experiments were performed with K files contaminated with pulp necrotic material from cervical region of teeth indicated to endodontic treatment. The contaminated K files were immersed for 30 or 60 seconds in 80% acetone, 80% isopropyl alcohol and 2% peracetic acid. The files were then inoculated into test tubes containing tioglycolate medium. The organisms that grew after peracetic acid treatment were identified. The corrosion mediated by the chemical agents was also tested after incubation of stainless steel and NiTi K files for 60 minutes, by measuring the weight of K-files before and after immersion, and by scanning electron microscopy (SEM). All chemical agents were capable to eliminate or reduce bacterial viability of planktonic Gram-negative and Gram-positive species, though the activity of chemicals upon sessile E. faecalis in K-file carrier tests demonstrated that isopropyl alcohol or acetone were incapable to eliminate bacterial contamination, especially when the files were dried previously to the exposition to the chemicals for 15 or 30 seconds. Peracetic acid demonstrated the best antimicrobial activity, and eliminated the viability of sessile E. faecalis cells from both wet and dried K-endodontic files after exposition for 15 seconds (100% elimination). The experiments developed in vivo demonstrated that peracetic acid was the most effective agent (p<0,05), capable of eliminating the viability of organisms in 92% of K files immersed after 60 seconds, when compared to acetone (64%) or isopropyl alcohol (50%). The microbial grown after contact with peracetic acid demonstrated that only Lactobacillus sp group was resistant to this chemical. The chemical agents demonstrated to be non-corrosive after immersion for 1 hour, by both weighing and SEM. The results indicated that peracetic acid was the most effective agent to be used as disinfectant of instruments during transoperatory period of endodontic treatment.

Esta investigação objetivou a eficácia antimicrobiana de agentes desinfetantes utilizados na desinfecção dos instrumentos endodônticos, durante o período transoperatório do tratamento endodôntico. A atividade antimicrobiana dos desinfetantes álcool isopropílico, acetona e ácido peracético (PAA) foi avaliada sobre microrganismos planctônicos através de teste de contato (time kill assay), utilizando inóculo de 9,9 X 109 a 1,2 X 1012 unidades formadoras de colônia (UFC) e por determinação da concentração bactericida mínima (CBM), usando inóculo de aproximadamente 106 UFC. Os agentes químicos também foram avaliados sobre Enterococcus faecalis (E. faecalis) ATCC 29212 cultivada em matriz de dentina (ex vivo) visando a formação de biofilme. O biofilme (organismos sésseis) microbiano foi removido com limas tipo Kerr (LK), até as lâminas estarem visualmente preenchidas. As LK contaminadas foram usadas como carreadores (logo após a contaminação ou secas dentro de uma câmara de fluxo laminar por 10 minutos). As LK carreadoras foram imersas em álcool isopropílico ou acetona ambos a 80%, ou em Ácido peracético 2%, por 30 ou 60 segundos. As limas foram posteriormente colocadas em tubos de ensaio contendo caldo Enterococcosel para observar o crescimento dos enterococos viáveis. Depois, os experimentos in vivo foram realizados com LK contaminadas por material necrótico pulpar da região cervical de dentes indicados para tratamento endodôntico. As LK contaminadas foram imersas, por 30 ou 60 segundos, em 80% de acetona ou 80% de álcool isopropílico ou 2% de PAA. As limas foram então inoculadas em tubos de ensaio contendo meio tioglicolato. Os organismos que cresceram, foram identificados após o tratamento com PAA. A corrosão mediada pelos agentes químicos também foi testada, após a incubação de LK de aço inoxidável e de NiTi por 60 minutos, medindo o peso das LK antes e depois da imersão e por microscopia eletrônica de varredura (MEV). Todos os agentes químicos foram capazes de eliminar ou reduzir a viabilidade das bactérias de espécies planctônicas Gram-negativas e Gram-positivas, embora a atividade dos produtos químicos sobre E. faecalis sésseis em testes de carreadores de LK demonstrou que o álcool isopropílico ou acetona foram incapazes de eliminar a contaminação bacteriana, especialmente, quando as limas foram secas previamente à exposição aos produtos químicos, por 15 ou 30 segundos. O PAA demonstrou a melhor atividade antimicrobiana e eliminou a viabilidade das células sésseis E. faecalis de ambas as limas endodônticas tipo K úmidas ou secas, após exposição por 15 segundos (100% de eliminação). Os experimentos desenvolvidos in vivo demonstraram que o PAA foi o agente mais eficaz (p<0,05), capaz de eliminar a viabilidade dos organismos em 92% das LK imersas depois de 60 segundos, quando comparado com acetona (64%) ou com álcool isopropílico (50%). O crescimento microbiano após o contato com o PAA demonstrou que somente o grupo dos Lactobacillus sp foi resistente a essa substância química. Os agentes químicos não demonstraram ser corrosivos, após a imersão por 1 hora, tanto por pesagem quanto por MEV. Foi observado que o PAA foi o agente mais eficaz para ser utilizado como desinfetante de instrumentos, durante o período transoperatório do tratamento endodôntico. / This investigation aimed to evaluate the antimicrobial efficacy of disinfectant agents used to maintain the disinfection of endodontic instruments during the transoperatory period in endodontic treatment. The antimicrobial activity of disinfectants isopropyl alcohol, acetone and peracetic acid were evaluated upon planktonic micro-organisms by time kill assay (contact test) using inoculums from 9,9 X 109 to 1,2 X 1012 colony forming units (CFU) and determination of minimal bactericidal concentration (MBC), using inoculums of 106 CFU. Chemical agents were also evaluated upon Enterococcus faecalis (E. faecalis) ATCC 29212 strain grown on matrix dentin (ex vivo) for biofilm formation. Biofilm (sessile organisms) were removed with Kerr files until the blades were visually filled and contaminated K files used as carriers (shortly after contamination or dried inside a flow chamber for 10 minutes). K files carriers were immersed in 80% isopropyl alcohol, 80% acetone or in 2% peracetic acid for 30 or 60 seconds. The files were subsequently dispensed into test tubes containing Enterococcosel broth to observe the growth of viable enterococci. Thereafter, in vivo experiments were performed with K files contaminated with pulp necrotic material from cervical region of teeth indicated to endodontic treatment. The contaminated K files were immersed for 30 or 60 seconds in 80% acetone, 80% isopropyl alcohol and 2% peracetic acid. The files were then inoculated into test tubes containing tioglycolate medium. The organisms that grew after peracetic acid treatment were identified. The corrosion mediated by the chemical agents was also tested after incubation of stainless steel and NiTi K files for 60 minutes, by measuring the weight of K-files before and after immersion, and by scanning electron microscopy (SEM). All chemical agents were capable to eliminate or reduce bacterial viability of planktonic Gram-negative and Gram-positive species, though the activity of chemicals upon sessile E. faecalis in K-file carrier tests demonstrated that isopropyl alcohol or acetone were incapable to eliminate bacterial contamination, especially when the files were dried previously to the exposition to the chemicals for 15 or 30 seconds. Peracetic acid demonstrated the best antimicrobial activity, and eliminated the viability of sessile E. faecalis cells from both wet and dried K-endodontic files after exposition for 15 seconds (100% elimination). The experiments developed in vivo demonstrated that peracetic acid was the most effective agent (p<0,05), capable of eliminating the viability of organisms in 92% of K files immersed after 60 seconds, when compared to acetone (64%) or isopropyl alcohol (50%). The microbial grown after contact with peracetic acid demonstrated that only Lactobacillus sp group was resistant to this chemical. The chemical agents demonstrated to be non-corrosive after immersion for 1 hour, by both weighing and SEM. The results indicated that peracetic acid was the most effective agent to be used as disinfectant of instruments during transoperatory period of endodontic treatment.

Objetivo: Comparar in vitro la resistencia adhesiva a dentina de tres sistemas adhesivos universales con y sin aplicación de una sustancia neutralizadora de la capa inhibida de oxígeno. Materiales y métodos: La muestra estuvo conformada por 90 dientes bovinos, distribuidos aleatoriamente en 6 grupos (n=15): G1-Ambar™ Universal, G2-Tetric® N-bond, G3-Scotchbond™ Universal sin aplicación de sustancia inhibidora: alcohol Isopropílico y G4-Ambar™ Universal, G5-Tetric® N-bond, G6-Scotchbond™ Universal con aplicación de sustancia inhibidora. Los procedimientos adhesivos se realizaron según las indicaciones de cada fabricante y los procedimientos restauradores con cilindros (matrices tipo Tygon 4 x 2 mm) de resina compuesta Filtek™ Z350XT-A2. Las muestras fueron almacenadas en una estufa a 37°C (+/- 5°C) por 24 horas. Se evaluó la resistencia al cizallamiento a dentina en una máquina de ensayos universal Instrom (velocidad 0.5 mm/min/500N). Los resultados fueron analizados mediante estadística descriptiva (Media y desviación estándar) e inferencial (U Mann Whitney, Kruskal Wallis). Resultados: La media y desviación estándar registrada para los grupos con y sin aplicación de alcohol Isopropílico fue; Ambar™ Universal (13.7±5.7) (14.0±5.2), Tetric® N-Bond Universal (16.5±7.2) (14.2±3.9) y Scotchbond™ Universal (13.6±4.5) (18.3±7.5) respectivamente. No se encontraron diferencias estadísticamente significativas en la resistencia adhesiva a dentina de los adhesivos universales con (p=0.528) y sin (p=0.193) aplicación de la sustancia neutralizadora. Conclusión: Los valores de resistencia adhesiva a dentina de los sistemas adhesivos universales con y sin aplicación de alcohol Isopropílico como sustancia neutralizadora de la capa inhibida de oxígeno no presentaron diferencias estadísticamente significativas. / Objective: Compare in vitro bond strength to dentin of three universal adhesive systems with and without application of an oxygen-inhibited layer neutralizing substance. Materials and methods: The sample was composed by 90 bovine teeth, randomly distributed in 6 groups (n=15): G1-Ambar™ Universal, G2-Tetric® N-bond, G3-Scotchbond™ Universal without application of inhibiting substance: Isopropyl alcohol and G4-Ambar™ Universal, G5-Tetric® N-bond, G6-Scotchbond™ Universal with application of inhibiting substance. Then, the adhesive phase was made according to each group and restorative procedures with composite resin Filtek™ Z350XT-A2, according to the manufacturer´s instructions. It was made of tygon composite resin (4 x 2 mm). The samples were stored in an incubator at 37°C (+/- 5°C) for 24 hours. Subsequently, dentin shear strength was evaluated on an Instrom universal testing machine (speed 0.5 mm/min/500N load). The results were analyzed using descriptive (mean and standard deviation) and inferential (U Mann Whitney, Kruskal Wallis) statistics. Results: Mean and standard deviation registered for the groups with and without application of Isopropyl alcohol was; Ambar™ Universal (13.7±5.7) (14.0±5.2), Tetric® N-Bond Universal (16.5±7.2) (14.2±3.9) and Scotchbond™ Universal (13.6±4.5) (18.3±7.5) respectively. No found statistical significant differences between bond strength in dentin of the universal adhesives with (p=0.528) and without (p=0.193) application of the neutralizing substance. Conclusion: The values of bond strength in dentin of the universal adhesive systems with and without application of Isopropyl alcohol as neutralizing substance of the oxygen inhibited layer did not show statistically significant differences. / Tesis

Ce travail montre la mise en œuvre d'une technique originale pour le chauffage rapide et bien contrôlé de catalyseurs sous forme de films minces déposés sur un structurant métallique. L'utilisation d'un système à induction électromagnétique adapté à un réacteur catalytique de type annulaire nous a permis d'étudier un certain nombre de matériaux catalytiques, déposés sur acier inoxydable, dans une perspective d'oxydation totale en CO2 et H2O de composés organiques volatiles (COV) présents dans l'air. La combustion de l'isopropanol et du toluène par l'oxygène de l'air a été étudiée en utilisant différents catalyseurs déposés sous forme de films minces: 1%Pt/Al2O3, 0,3%Pt/SnO2, 1%Pt/SnO2 et 1%Pt/YSZ. Les solides ont été préparés par imprégnation des oxydes correspondants par H2PtCl6 puis ont été déposés sur le support d'acier inoxydable par électrophorèse. Les principaux paramètres relatifs au mode de chauffage ont été étudiés de même que l'influence sur la conversion des COV de différents facteurs tels que la quantité de catalyseur, le pourcentage de platine ou la nature du support oxyde employé. Les informations fournies par ce système innovant ont également été comparées pour validation à celles obtenues à l'aide d'un système classique (microréacteur en quartz à lit traversé chauffé de manière conventionnelle) pour une réaction de référence qui est l'oxydation de CO en CO2. Le système décrit dans cette étude présente d'une part un intérêt pratique pour le traitement rapide de contaminations accidentelles de l'air ambiant, mais est aussi un très bon moyen d'obtenir des paramètres cinétiques fiables dans le domaine des catalyseurs en films minces utilisés dans de nombreux réacteurs structurés / This study shows the development of an innovative technique for a fast and well-controlled heating of catalysts deposited as thin films on a metallic support. The use of an electromagnetic induction system fitted to an annular catalytic reactor enabled us to study some catalytic materials deposited on stainless steel. The target application was the abatement of volatile organic compounds (VOCs) in the air. Isopropyl alcohol and toluene combustion by the oxygen was studied on various thin films catalysts, i.e. : 1%Pt/Al2O3, 0,3%Pt/SnO2, 1%Pt/SnO2 et 1%Pt/YSZ. Solids were prepared by wet impregnation of the corresponding oxides by H2PtCl6 and were deposited on the stainless steel support using an electrophoretic deposition technique. The main parameters of the heating system were investigated as well as the influence on VOCs abatement of various parameters such as the thickness of catalyst film, the platinum amount and the nature of the oxide. For validation purpose, the data provided by this innovative system were also compared to the ones provided by a classical one (quartz plug-through microreactor heated in a conventional way) in a reference reaction which was CO oxidation into CO2. The system described in this study shows on the one hand a real practical interest for fast remediation of indoor air polluted by VOCs, and on the other hand is a very powerful tool for obtaining kinetic data about thin layer catalysts used in many structured reactors