Abrasion resistance of direct and indirect resins as a function of a sealant veneer

Abrasive wear is one of the most common type of wear that not only affect teeth, as also dental restorations. Thus to investigate one of the etiological factors as tooth brushing procedure is clinical relevant in order to select the best material combination that may prevent damage of resin dental restoration's abrasion. This study evaluated the influence of tooth brushing on mass loss and surface roughness of direct Venus (Vs) and indirect Signum (Sg) resin composites, with and without a surface sealant, Fortify (F). Twenty-four specimens were prepared with each resin composite, using their proprietary curing units, according to manufacturer's instructions. All the specimens were polished and ultrasonically cleaned in distilled water for 5 minutes. Half of the specimens of each resin (n = 12) were covered with F (Vs F and Sg F ), except for the control (C) specimens (Vs C and Sg C ), which were not sealed. Mass loss (ML) as well as surface roughness (Ra ) was measured for all the specimens. Then, the specimens were subjected to toothbrush-dentifrice abrasion, using a testing machine for 67.000 brushing strokes, in an abrasive slurry. After brushing simulation, the specimens were removed from the holder, rinsed thoroughly and blot dried with soft absorbent paper. The abrasion of the material was quantitatively determined with final measurements of ML and surface roughness, using the method described above. ML data were analyzed by two-way analysis of variance (ANOVA) and the analysis indicated that resin composites were not statistically different; however, the specimens sealed with F showed higher ML. Ra mean values of the groups Vs F and Sg F significantly increased. Tooth brushing affects mainly the roughness of the direct and indirect resin composites veneered with a sealant.

Métodos geoelétricos aplicados ao diagnóstico ambiental subsuperficial do Cemitério Municipal de Rio Claro, SP

Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)

Fertilizantes e sistemas de irrigação: emissões de gases de efeito estufa no cultivo do milho

Conselho Nacional de Desenvolvimento Científico e Tecnológico (CNPq)

Desenvolvimento e aceitabilidade de compota de figo convencional e diet

Fundação de Amparo à Pesquisa do Estado de São Paulo (FAPESP)

Estudo e desenvolvimento de filmes espessos de CeO2 obtidos por tape casting

Tape Casting proved to be an effective method for the production of thick films of CeO2 pure and doped with La. For this study, the nanoparticles used to form the slurry were synthesizes by the H-M method, at 100°C for 8 minutes, using KOH mineralizer. The slurry was made in aqueous solvent, requiring optimal control of surroundings conditions so that the produced tape has conditions to be studied. However, there's no toxicity or flammability in the film made by such solvent, being pleasing to the environment. The structural, optical and electrical properties of the films obtained by the Tape Casting process were studied by the methods of X-ray diffraction, scanning electron microscopy, specific surface area, Ultraviolet-visible spectroscopy and voltage-current measures, varying the electric field and frequency. From the results obtained by laboratory experiments, based on the literature, it was possible to reveal and understand some CeO2 features pure and doped with La

Estudo e desenvolvimento de filmes espessos de CeO2 obtidos por tape casting

Tape Casting proved to be an effective method for the production of thick films of CeO2 pure and doped with La. For this study, the nanoparticles used to form the slurry were synthesizes by the H-M method, at 100°C for 8 minutes, using KOH mineralizer. The slurry was made in aqueous solvent, requiring optimal control of surroundings conditions so that the produced tape has conditions to be studied. However, there's no toxicity or flammability in the film made by such solvent, being pleasing to the environment. The structural, optical and electrical properties of the films obtained by the Tape Casting process were studied by the methods of X-ray diffraction, scanning electron microscopy, specific surface area, Ultraviolet-visible spectroscopy and voltage-current measures, varying the electric field and frequency. From the results obtained by laboratory experiments, based on the literature, it was possible to reveal and understand some CeO2 features pure and doped with La

AMMONIA LOSSES ESTIMATED BY AN OPEN COLLECTOR FROM UREA APPLIED TO SUGARCANE STRAW

The quantification of ammonia (NH3) losses from sugarcane straw fertilized with urea can be performed with collectors that recover the NH3 in acid-treated absorbers. Thus, the use of an open NH3 collector with a polytetrafluoroethylene (PTFE)-wrapped absorber is an interesting option since its cost is low, handling easy and microclimatic conditions irrelevant. The aim of this study was to evaluate the efficiency of an open collector for quantifying NH3-N volatilized from urea applied over the sugarcane straw. The experiment was carried out in a sugarcane field located near Piracicaba, Sao Paulo, Brazil. The NH3-N losses were estimated using a semi-open static collector calibrated with N-15 (reference method) and an open collector with an absorber wrapped in PTFE film. Urea was applied to the soil surface in treatments corresponding to rates of 50, 100, 150 and 200 kg ha(-1) N. Applying urea-N fertilizer on sugarcane straw resulted in losses NH3-N up to 24 % of the applied rate. The amount of volatile NH3-N measured in the open and the semi-open static collector did not differ. The effectiveness of the collection system varied non-linearly, with an average value of 58.4 % for the range of 100 to 200 kg ha(-1) of urea-N. The open collector showed significant potential for use; however, further research is needed to verify the suitability of the proposed method.

EX-SITU BIOREMEDIATION OF BRAZILIAN SOIL CONTAMINATED WITH PLASTICIZERS PROCESS WASTES

The aim of this research was to evaluate the bioremediation of a soil contaminated with wastes from a plasticizers industry, located in Sao Paulo, Brazil. A 100-kg soil sample containing alcohols, adipates and phthalates was treated in an aerobic slurry-phase reactor using indigenous and acclimated microorganisms from the sludge of a wastewater treatment plant of the plasticizers industry (11gVSS kg(-1) dry soil), during 120 days. The soil pH and temperature were not corrected during bioremediation; soil humidity was corrected weekly to maintain 40%. The biodegradation of the pollutants followed first-order kinetics; the removal efficiencies were above 61% and, among the analyzed plasticizers, adipate was removed to below the detection limit. Biological molecular analysis during bioremediation revealed a significant change in the dominant populations initially present in the reactor.

In Situ Effect of Dentifrices Associated to CO2 Laser in the Permeability of Eroded Root Dentin

Objective: The aim of this study was to evaluate, through a crossover 2 x 2 in situ trial, the effect of a desensitizing dentifrice associated with CO2 laser irradiation to control the permeability of eroded root dentin. Background data: Facing the increased prevalence of erosive lesion and the need for preventive means to control painful symptoms related to them. Methods: Eighty slabs of bovine root dentin were subjected to initial erosive challenge (citric acid 0.3%, 2 h), followed by a remineralizing period in artificial saliva (24 h). Specimens were then divided according to dentin treatment: desensitizing dentifrice, desensitizing dentifrice + CO2 laser, fluoride anticavity dentifrice. and fluoride anticavity dentifrice + CO2 laser. After a 2-day lead-in period, 10 volunteers wore an intraoral palatal appliance containing four root dentin slabs, in two phases of 5 days each. During the intraoral phase, one side of the appliance was immersed in 0.3% citric acid, and the opposite side was immersed in deionized water, four times a day. One hour after the immersions, all specimens were brushed with dentifrice slurry provided by the researcher. After a 7-day washout period, volunteers were crossed over on the different dentifrice group. Each phase having been completed, the specimens were evaluated for permeability through an optical microscope. Results: Data were analyzed using ANOVA and no significant difference (p = 0.272) was found between the surface treatments performed on bovine root dentin. Conclusions: It can be concluded that fluoride anticavity or desensitizing dentifrice, regardless of the association with the CO2 laser irradiation, was able to control the permeability of eroded root dentin.

Impact of filler size and distribution on roughness and wear of composite resin after simulated toothbrushing

Objectives: Nanofilled composite resins are claimed to provide superior mechanical properties compared with microhybrid resins. Thus, the aim of this study was to compare nanofilled with microhybrid composite resins. The null hypothesis was that the size and the distribution of fillers do not influence the mechanical properties of surface roughness and wear after simulated toothbrushing test. Material and methods: Ten rectangular specimens (15 mm x 5 mm x 4 mm) of Filtek Z250 (FZ2), Admira (A), TPH3 (T), Esthet-X (EX), Estelite Sigma (ES), Concept Advanced (C), Grandio (G) and Filtek Z350 (F) were prepared according to manufacturer's instructions. Half of each top surface was protected with nail polish as control surface (not brushed) while the other half was assessed with five random readings using a roughness tester (Ra). Following, the specimens were abraded by simulated toothbrushing with soft toothbrushes and slurry comprised of 2: 1 water and dentifrice (w/w). 100,000 strokes were performed and the brushed surfaces were re-analyzed. Nail polish layers were removed from the specimens so that the roughness (Ra) and the wear could be assessed with three random readings (mu m). Data were analyzed by ANOVA and Tukey's multiple-comparison test (alpha = 0.05). Results: Overall outcomes indicated that composite resins showed a significant increase in roughness after simulated toothbrushing, except for Grandio, which presented a smoother surface. Generally, wear of nanofilled resins was significantly lower compared with microhybrid resins. Conclusions: As restorative materials suffer alterations under mechanical challenges, such as toothbrushing, the use of nanofilled materials seem to be more resistant than microhybrid composite resins, being less prone to be rougher and worn.

Interaction of p-cymene with beta-cyclodextrin

In this investigation, the study of inclusion complexes formation between p-cymene and beta-cyclodextrin using the methods of physical mixture, paste (PC) and slurry (SC), was evaluated. The results of DSC and TG/DTG showed that the products prepared by PC and SC methods were able to incorporate greater amounts of p-cymene, as evidenced by the weight loss of 7.15 and 3.97%, respectively, which occurred between 120 and 270 A degrees C. SEM images showed decreased size of the household, especially in the SC product. The absorption bands in the IR spectrum, characteristic of p-cymene, were also identified in the preparations, indicating the presence of the compound in the complex.

Biorremediação de solo contaminado por isobutanol, Bis-2-etil-hexilftalato e Di-isodecilftalato

Embora os ftalatos sejam um dos poluentes mais frequentemente encontrados no meio ambiente, há escassez de dados na literatura sobre biorremediação de solos tropicais contaminados por esses compostos. Por esse motivo, este estudo avaliou a biorremediação de um solo contaminado com os plastificantes DEHP (Bis-2-etilhexilftalato), DIDP (Di-isodecilftalato) e álcool isobutílico, por uma indústria no Estado de São Paulo. A biorremediação ocorreu pela utilização de microrganismos presentes no solo e pela adição de inóculo adaptado em reator em fase de lama. O reator foi monitorado durante 120 dias, sendo corrigida apenas a umidade do solo. Os resultados indicaram que a biodegradação dos ftalatos seguiu uma cinética de primeira ordem e a biorremediação ocorreu na faixa de pH entre 7,4 e 8,4 e temperaturas entre 17 e 25 ºC, com eficiência de remoção de contaminantes acima de 70 %. Após 120 dias, o teor de DEHP estava abaixo de 4 mg kg-1, limite estipulado pela legislação brasileira para solo de uso residencial.

Degradation of the resin-dentin bonds after simulated and inhibited cariogenic challenge in an in situ model

The aim of this study was to evaluate the resindentin bonds of two simplified etch-and-rinse adhesive after simulated cariogenic and inhibited cariogenic challenge in situ. Dental cavities (4 mm wide, 4 mm long, and 1.5 mm deep) were prepared in 60 bovine teeth with enamel margins. Restorations were bonded with either adhesive Adper Single Bond 2 (3MESPE) or Optibond Solo Plus (Kerr). Forty restorations were included in an intra-oral palatal appliance that was used for 10 adult volunteers while the remaining 20 dental blocks were not submitted to any cariogenic challenge [NC group] and tested immediately. For the simulated cariogenic challenge [C+DA], each volunteer dropped 20% sucrose solution onto all blocks four times a day during 14 days and distilled water twice a day. In the inhibited cariogenic challenge group [C + FA], the same procedure was done, but slurry of fluoride dentifrice (1.100 ppm) was applied instead of water. The restored bovine blocks were sectioned to obtain a slice for cross-sectional Vickers microhardness evaluation and resindentin bonded sticks (0.8 mm2) for resindentin microtensile evaluation. Data were evaluated by two-way ANOVA and Tukey's tests (a = 0.05). Statistically lower microhardness values and degradation of the resindentin bonds were only found in the C + DW group for both adhesives. The in situ model seems to be a suitable short-term methodology to investigate the degradation of the resindentin bonds under a more realistic condition. (c) 2012 Wiley Periodicals, Inc. J Biomed Mater Res Part B: Appl Biomater 100B: 14661471, 2012.

Ex-situ bioremediation of Brazilian soil contaminated with plasticizers process wastes

The aim of this research was to evaluate the bioremediation of a soil contaminated with wastes from a plasticizers industry, located in São Paulo, Brazil. A 100-kg soil sample containing alcohols, adipates and phthalates was treated in an aerobic slurry-phase reactor using indigenous and acclimated microorganisms from the sludge of a wastewater treatment plant of the plasticizers industry (11gVSS kg-1 dry soil), during 120 days. The soil pH and temperature were not corrected during bioremediation; soil humidity was corrected weekly to maintain 40%. The biodegradation of the pollutants followed first-order kinetics; the removal efficiencies were above 61% and, among the analyzed plasticizers, adipate was removed to below the detection limit. Biological molecular analysis during bioremediation revealed a significant change in the dominant populations initially present in the reactor.

Produzione di bioetanolo da scarti lignocellulosici della canna da zucchero: condizioni di saccarificazione e fermentazione simultanee (SSF) e aspetti ambientali del processo

Il presente studio ha avuto l’obiettivo di indagare la produzione di bioetanolo di seconda generazione a partire dagli scarti lignocellulosici della canna da zucchero (bagassa), facendo riscorso al processo enzimatico. L’attività di ricerca è stata svolta presso il Dipartimento di Ingegneria Chimica dell’Università di Lund (Svezia) all’interno di rapporti scambio con l’Università di Bologna. Il principale scopo è consistito nel valutare la produzione di etanolo in funzione delle condizioni operative con cui è stata condotta la saccarificazione e fermentazione enzimatica (SSF) della bagassa, materia prima che è stata sottoposta al pretrattamento di Steam Explosion (STEX) con aggiunta di SO2 come catalizzatore acido. Successivamente, i dati ottenuti in laboratorio dalla SSF sono stati utilizzati per implementare, in ambiente AspenPlus®, il flowsheet di un impianto che simula tutti gli aspetti della produzione di etanolo, al fine di studiarne il rendimento energetico dell’intero processo. La produzione di combustibili alternativi alle fonti fossili oggigiorno riveste primaria importanza sia nella limitazione dell’effetto serra sia nel minimizzare gli effetti di shock geopolitici sulle forniture strategiche di un Paese. Il settore dei trasporti in continua crescita, consuma nei paesi industrializzati circa un terzo del fabbisogno di fonti fossili. In questo contesto la produzione di bioetanolo può portare benefici per sia per l’ambiente che per l’economia qualora valutazioni del ciclo di vita del combustibile ne certifichino l’efficacia energetica e il potenziale di mitigazione dell’effetto serra. Numerosi studi mettono in risalto i pregi ambientali del bioetanolo, tuttavia è opportuno fare distinzioni sul processo di produzione e sul materiale di partenza utilizzato per comprendere appieno le reali potenzialità del sistema well-to-wheel del biocombustibile. Il bioetanolo di prima generazione ottenuto dalla trasformazione dell’amido (mais) e delle melasse (barbabietola e canna da zucchero) ha mostrato diversi svantaggi: primo, per via della competizione tra l’industria alimentare e dei biocarburanti, in secondo luogo poiché le sole piantagioni non hanno la potenzialità di soddisfare domande crescenti di bioetanolo. In aggiunta sono state mostrate forti perplessità in merito alla efficienza energetica e del ciclo di vita del bioetanolo da mais, da cui si ottiene quasi la metà della produzione di mondiale di etanolo (27 G litri/anno). L’utilizzo di materiali lignocellulosici come scarti agricolturali e dell’industria forestale, rifiuti urbani, softwood e hardwood, al contrario delle precedenti colture, non presentano gli svantaggi sopra menzionati e per tale motivo il bioetanolo prodotto dalla lignocellulosa viene denominato di seconda generazione. Tuttavia i metodi per produrlo risultano più complessi rispetto ai precedenti per via della difficoltà di rendere biodisponibili gli zuccheri contenuti nella lignocellulosa; per tale motivo è richiesto sia un pretrattamento che l’idrolisi enzimatica. La bagassa è un substrato ottimale per la produzione di bioetanolo di seconda generazione in quanto è disponibile in grandi quantità e ha già mostrato buone rese in etanolo se sottoposta a SSF. La bagassa tal quale è stata inizialmente essiccata all’aria e il contenuto d’acqua corretto al 60%; successivamente è stata posta a contatto per 30 minuti col catalizzatore acido SO2 (2%), al termine dei quali è stata pretrattata nel reattore STEX (10L, 200°C e 5 minuti) in 6 lotti da 1.638kg su peso umido. Lo slurry ottenuto è stato sottoposto a SSF batch (35°C e pH 5) utilizzando enzimi cellulolitici per l’idrolisi e lievito di birra ordinario (Saccharomyces cerevisiae) come consorzio microbico per la fermentazione. Un obiettivo della indagine è stato studiare il rendimento della SSF variando il medium di nutrienti, la concentrazione dei solidi (WIS 5%, 7.5%, 10%) e il carico di zuccheri. Dai risultati è emersa sia una buona attività enzimatica di depolimerizzazione della cellulosa che un elevato rendimento di fermentazione, anche per via della bassa concentrazione di inibitori prodotti nello stadio di pretrattamento come acido acetico, furfuraldeide e HMF. Tuttavia la concentrazione di etanolo raggiunta non è stata valutata sufficientemente alta per condurre a scala pilota un eventuale distillazione con bassi costi energetici. Pertanto, sono stati condotti ulteriori esperimenti SSF batch con addizione di melassa da barbabietola (Beta vulgaris), studiandone preventivamente i rendimenti attraverso fermentazioni alle stesse condizioni della SSF. I risultati ottenuti hanno suggerito che con ulteriori accorgimenti si potranno raggiungere gli obiettivi preposti. E’ stato inoltre indagato il rendimento energetico del processo di produzione di bioetanolo mediante SSF di bagassa con aggiunta di melassa in funzione delle variabili più significative. Per la modellazione si è fatto ricorso al software AspenPlus®, conducendo l’analisi di sensitività del mix energetico in uscita dall’impianto al variare del rendimento di SSF e dell’addizione di saccarosio. Dalle simulazioni è emerso che, al netto del fabbisogno entalpico di autosostentamento, l’efficienza energetica del processo varia tra 0.20 e 0.53 a seconda delle condizioni; inoltre, è stata costruita la curva dei costi energetici di distillazione per litro di etanolo prodotto in funzione delle concentrazioni di etanolo in uscita dalla fermentazione. Infine sono già stati individuati fattori su cui è possibile agire per ottenere ulteriori miglioramenti sia in laboratorio che nella modellazione di processo e, di conseguenza, produrre con alta efficienza energetica bioetanolo ad elevato potenziale di mitigazione dell’effetto serra.