Surface Segregation in Chromium-Doped Nanocrystalline Tin Dioxide Pigments

Surface properties play an important role in understanding and controlling nanocrystalline materials. The accumulation of dopants on the surface, caused by surface segregation, can therefore significantly affect nanomaterials properties at low doping levels, offering a way to intentionally control nanoparticles features. In this work, we studied the distribution of chromium ions in SnO2 nanoparticles prepared by a liquid precursor route at moderate temperatures (500 degrees C). The powders were characterized by infrared spectroscopy, X-ray diffraction, (scanning) transmission electron microscopy, Electron Energy Loss Spectroscopy, and Mossbauer spectroscopy. We showed that this synthesis method induces a limited solid solution of chromium into SnO2 and a segregation of chromium to the surface. The s-electron density and symmetry of Sn located on the surface were significantly affected by the doping, while Sn located in the bulk remained unchanged. Chromium ions located on the surface and in the bulk showed distinct oxidation states, giving rise to the intense violet color of the nanoparticles suitable for pigment application.

Evaluation of Chemical Treatment on Zirconia Surface with Two Primer Agents and an Alkaline Solution on Bond Strength

Objectives: This study evaluated the effect of an alkaline solution and two 10-methacryloyloxydecyl dihydrogen phosphate (MDP)-based primer agents on bond strength to zirconia (yttria-stabilized tetragonal zirconium polycrystal [Y-TZP]) through the shear bond strength (SBS) test. Materials and Methods: Sixty square-shaped Y-TZP samples were embedded in an acrylic resin mold, polished, and randomly assigned to one of six groups (n=10) according to treatment surface: group CR, no treatment (control); group NaOH, 0.5 M NaOH; group AP, Alloy Primer; group ZP, Z-Primer Plus; group NaOH-AP, 0.5 M NaOH + Alloy Primer; and group NaOH-ZP, 0.5 M NaOH + Z-Primer Plus. The resin cement (Rely X U100) was applied inside a matrix directly onto the Y-TZP surface, and it was light-cured for 40 seconds. The samples were stored in distilled water at 37 C for 24 hours prior to the test, which was performed in a universal machine at a crosshead-speed of 0.5 mm/min. The data were analyzed by one-way analysis of variance and Tukey tests (p<0.05). Light stereomicroscopy and scanning electron microscopy were used to assess the surface topography and failure mode. Results: The SBS was significantly affected by the chemical treatment (p<0.0001). The AP group displayed the best results, and the use of NaOH did not improve SBS results relative to either AP or ZP. The samples treated with Alloy Primer displayed mainly mixed failures, whereas those conditioned with Z-Primer Plus or with 0.5 M NaOH presented a balanced distribution of adhesive and mixed failure modes. Conclusions: The use of a NaOH solution may have modified the reactivity of the Y-TZP surface, whereas the employment of a MDP/6-4-vinylbenzyl-n-propyl amino-1,3,5-triazine2,4-dithione-based primer enhanced the Y-TZP bond strength.

Residual stresses in Y-TZP crowns due to changes in the thermal contraction coefficient of veneers

Objective. To test the hypothesis that the difference in the coefficient of thermal contraction of the veneering porcelain above (˛liquid) and below (˛solid) its Tg plays an important role in stress development during a fast cooling protocol of Y-TZP crowns. Methods. Three-dimensional finite element models of veneered Y-TZP crowns were developed. Heat transfer analyses were conducted with two cooling protocols: slow (group A) and fast (groups B–F). Calculated temperatures as a function of time were used to determine the thermal stresses. Porcelain ˛solid was kept constant while its ˛liquid was varied, creating different ˛/˛solid conditions: 0, 1, 1.5, 2 and 3 (groups B–F, respectively). Maximum ( 1) and minimum ( 3) residual principal stress distributions in the porcelain layer were compared. Results. For the slowly cooled crown, positive 1 were observed in the porcelain, orientated perpendicular to the core–veneer interface (“radial” orientation). Simultaneously, negative 3 were observed within the porcelain, mostly in a hoop orientation (“hoop–arch”). For rapidly cooled crowns, stress patterns varied depending on ˛/˛solid ratios. For groups B and C, the patterns were similar to those found in group A for 1 (“radial”) and 3 (“hoop–arch”). For groups D–F, stress distribution changed significantly, with 1 forming a “hoop-arch” pattern while 3 developed a “radial” pattern. Significance. Hoop tensile stresses generated in the veneering layer during fast cooling protocols due to porcelain high ˛/˛solid ratio will facilitate flaw propagation from the surface toward the core, which negatively affects the potential clinical longevity of a crown.

In-situ XANES experiments on Ni K-edge in mesoporous ZrO2-CeO2:Ni.

Ordered mesoporous ZrO2-CeO2 mixed oxides are potential candidates for catalytic applications. These systems, used as anodes in solid oxide fuel cells (SOFC), may lead to better performance of SOFCs, due to an enhancement on surface area, aiming to achieve a lower working temperature. The aim of this studies is to evaluate the reduction capacity of Ni2+ to Ni in ZrO2-x(mol)%CeO2 (x=50 and 90) samples impregnated with 60(wt.)%NiO. The synthesis was made with Zr and Ce chloride precursors, HCl aqueous solution, Pluronic P123, NH4OH to adjust the pH (3-4) and a teflon autoclave to perform a hydrothermal treatment (80oC/48h). The samples were dried and calcined, until 540oC in N2 and 4 hours in air. The NiO impregnation was made with an ethanol dispersion of Ni(NO3)£6H2O. The powder was calcinated in air until 350oC for 2 hours. Temperature-resolved XANES data at the Ni K-edge were collected at the DXAS beam line of the LNLS in transmission mode, using a Si(111) monochromator and a CCD detector. Sample preparation consisted of mixing »6mg of the powder samples with boron nitride and pressing into pellets. The data were acquired during an experiment of temperature programmed reduction (TPR) under a 5% H2/He until 600oC and mixtures of 20%CH4:5%O2/He, at temperatures from 400 to 600oC. All the reactions were monitored with a mass spectrometer. The data was analyzed with a linear combination fit of 2 standards for each valence number using Athena software. The Ni K-edge experiments demonstrated that for both contents of CeO2, NiO embedded in the porous zirconia-ceria matrix reduces at lower temperatures than pure NiO, revealing that the ZrO2-CeO2 support improves the reduction of impregnated NiO. Ni was oxidized to NiO after all reactions with methane and oxygen. Hydrogenated carbonaceous species were detected, but under reducing conditions, the hydrocarbon compounds are removed. The reaction of total oxidation of methane CH4:O2 (1:2 ratio) was observed at lower temperatures (around 400oC) for both samples.

Structural and textural studies of NiO impregnation in mesoporous ZrO2-CeO2 for catalysis applications.

The synthesis of zirconia-based ordered mesoporous structures for catalytic applications is a research area under development. These systems are also potential candidates as anodes in intermediate temperature solid oxide fuel cells (it-SOFC) due to an enhancement on their surface area [1-4]. The structural features of mesoporous zirconia-ceria materials in combination with oxygen storage/release capacity (OSC) are crucial for various catalytic reactions. The direct use of hydrocarbons as fuel for the SOFC (instead of pure H2), without the necessity of reforming and purification reactors can improve global efficiency of these systems [4]. The X-ray diffraction data showed that ZrO2-x%CeO2 samples with x>50 are formed by a larger fraction of the cubic phase (spatial group Fm3m), while for x<50 the major crystalline structure is the tetragonal phase (spatial group P42/nmc). The crystallite size of the cubic phase increases with increase in ceria content. The tetragonal crystallite size decreases when ceria content increases. After impregnation, the Rietveld analysis showed a NiO content around 60wt.% for all samples. The lattice parameters for the ZrO2 tetragonal phase are lower for higher ZrO2 contents, while for all samples the cubic NiO and CeO2 parameters do not present changes. The calculated densities are higher for higher ceria content, as expected. The crystallite size of NiO are similar (~20nm) for all samples and 55nm for the NiO standard. Nitrogen adsorption experiments revealed a broader particle size distribution for higher CeO2 content. The superficial area values were around 35m2/g for all samples, the average pore diameter and pore volumes were higher when increasing ceria content. After NiO impregnation the particle size distribution was the same for all samples, with two pore sizes, the first around 3nm and a broader peak around 10nm. The superficial area increased to approximately 45m2/g for all samples, and the pore volume was also higher after impregnation and increased when ceria content increased. These results point up that the impregnation of NiO improves the textural characteristics of the pristine material. The complementary TEM/EDS images present a homogeneous coating of NiO particles over the ZrO2-x%CeO2 support, showing that these samples are excellent for catalysis applications. [1] D. Y. Zhao, J. Feng, Q. Huo, N. Melosh, G. H. Fredrickson, B. F. Chmelka, G. D. Stucky, Science 279, 548-552 (1998). [2] C. Yu, Y. Yu, D. Zhao, Chem. Comm. 575-576 (2000). [3] A. Trovarelli, M. Boaro, E. Rocchini, C. de Leitenburg, G. Dolcetti, J. Alloys Compd. 323-324 (2001) 584-591. [4] S. Larrondo, M. A. Vidal, B. Irigoyen, A. F. Craievich, D. G. Lamas, I. O. Fábregas, et al. Catal. Today 107–108 (2005) 53-59.

Structural and reduction studies of ZrO2-CeO2:Ni for application in SOFC anodes.

Zirconia-ceria solid-solutions are extensively used as promoters for three-way catalysts, which are applied in the control of NOx, CO and hydrocarbons emission from automotive exhausts. In addition, thesematerials can be used as anodes in solid oxide fuel cells (SOFCs) operated with hydrocarbons. There areonly few works on ZrO2-CeO2 ordered mesoporous materials for catalytic applications and for anodes inSOFCs. The interest in these anodes relies on the fact that ZrO2-CeO2materials are mixed ionic/electronic conductors in reducing atmosphere and, therefore, fuel oxidation is produced on its entire surface, while it only occurs in the [anode/electrolyte/gas] interface (triple-phase boundaries) for electronic conductors. In this work, a synthesis method was developed usingZr and Ce chloride precursors, HCl aqueous solution, Pluronic P123 as the structure directing agent, NH4OH to adjust the pH (3-4) and a Teflon autoclave to perform hydrothermal treatment (80ºC/48 hours). The samples were dried and calcined, until 540ºC in N2and 4 hours in air. The X-ray diffraction data showed that powders with higher CeO2 content are formed by a larger fraction of the cubic CeO2 phase, while for a lower CeO2content the major crystalline structure is the tetragonal ZrO2 phase. The NiO impregnation was made with an ethanol dispersion of Ni(NO3)×6H2O. The resulting powder was calcinated in air until 350ºC for 2 hours. Temperature-programmed reduction (TPR) data were collected in order to evaluate the reduction profiles of ZrO2-x%CeO2:Ni samples in H2/Ar atmosphere. Results showed lower reduction temperatures for all ceria content in samples comparing to a NiO standard.

Photoluminescence of core-shell nanoparticles made from yttrium stabilized zirconia powder grain coated with alumina

A YSZ@Al2O3 nanocomposite was obtained by Al2O3 coating on the surface of yttrium stabilized zirconia via a polymeric precursor method. The resulting core–shell structures were characterized by X-ray diffraction, scanning electron microscopy, transmission electronic microscopy and PL spectra. The TEM micrographs clearly show a homogeneous Al2O3 shell around the ZrO2 core. The observed PL is related to surface–interface defects. Such novel technologies can, in principle, explore materials which are not available in the bulk single crystal form but their figure-of-merit is dramatically dependent on the surface–interface defect states.

Sviluppi di catalizzatori per l'abbattimento di NOx in presenza di ossigeno

Il traffico veicolare è la principale fonte antropogenica di NOx, idrocarburi (HC) e CO e, dato che la sostituzione dei motori a combustione interna con sistemi alternativi appare ancora lontana nel tempo, lo sviluppo di sistemi in grado di limitare al massimo le emissioni di questi mezzi di trasporto riveste un’importanza fondamentale. Sfortunatamente non esiste un rapporto ottimale aria/combustibile che permetta di avere basse emissioni, mentre la massima potenza ottenibile dal motore corrisponde alle condizioni di elevata formazione di CO e HC. Gli attuali sistemi di abbattimento permettono il controllo delle emissioni da sorgenti mobili tramite una centralina che collega il sistema di iniezione del motore e la concentrazione di ossigeno del sistema catalitico (posto nella marmitta) in modo da controllare il rapporto aria/combustibile (Fig. 1). Le marmitte catalitiche per motori a benzina utilizzano catalizzatori “three way” a base di Pt/Rh supportati su ossidi (allumina, zirconia e ceria), che, dovendo operare con un rapporto quasi stechiometrico combustibile/comburente, comportano una minore efficienza del motore e consumi maggiori del 20-30% rispetto alla combustione in eccesso di ossigeno. Inoltre, questa tecnologia non può essere utilizzata nei motori diesel, che lavorano in eccesso di ossigeno ed utilizzano carburanti con un tenore di zolfo relativamente elevato. In questi ultimi anni è cresciuto l’interesse per il controllo delle emissioni di NOx da fonti veicolari, con particolare attenzione alla riduzione catalitica in presenza di un eccesso di ossigeno, cioè in condizioni di combustione magra. Uno sviluppo recente è rappresentato dai catalizzatori tipo “Toyota” che sono basati sul concetto di accumulo e riduzione (storage/reduction), nei quali l’NO viene ossidato ed accumulato sul catalizzatore come nitrato in condizioni di eccesso di ossigeno. Modificando poi per brevi periodi di tempo le condizioni di alimentazione da ossidanti (aria/combustibile > 14,7 p/p) a riducenti (aria/combustibile < 14,7 p/p) il nitrato immagazzinato viene ridotto a N2 e H2O. Questi catalizzatori sono però molto sensibili alla presenza di zolfo e non possono essere utilizzati con i carburanti diesel attualmente in commercio. Obiettivo di questo lavoro di tesi è stato quello di ottimizzare e migliorare la comprensione del meccanismo di reazione dei catalizzatori “storage-reduction” per l’abbattimento degli NOx nelle emissioni di autoveicoli in presenza di un eccesso di ossigeno. In particolare lo studio è stato focalizzato dapprima sulle proprietà del Pt, fase attiva nei processi di storage-reduction, in funzione del tipo di precursore e sulle proprietà e composizione della fase di accumulo (Ba, Mg ed una loro miscela equimolare) e del supporto (γ-Al2O3 o Mg(Al)O). Lo studio è stato inizialmente focalizzato sulle proprietà dei precursori del Pt, fase attiva nei processi di storage-reduction, sulla composizione della fase di accumulo (Ba, Mg ed una loro miscela equimolare) e del supporto (γ-Al2O3 o Mg(Al)O). E’ stata effettuata una dettagliata caratterizzazione chimico-fisica dei materiali preparati tramite analisi a raggi X (XRD), area superficiale, porosimetria, analisi di dispersione metallica, analisi in riduzione e/o ossidazione in programmata di temperatura (TPR-O), che ha permesso una migliore comprensione delle proprietà dei catalizzatori. Vista la complessità delle miscele gassose reali, sono state utilizzate, nelle prove catalitiche di laboratorio, alcune miscele più semplici, che tuttavia potessero rappresentare in maniera significativa le condizioni reali di esercizio. Il comportamento dei catalizzatori è stato studiato utilizzando differenti miscele sintetiche, con composizioni che permettessero di comprendere meglio il meccanismo. L’intervallo di temperatura in cui si è operato è compreso tra 200-450°C. Al fine di migliorare i catalizzatori, per aumentarne la resistenza alla disattivazione da zolfo, sono state effettuate prove alimentando in continuo SO2 per verificare la resistenza alla disattivazione in funzione della composizione del catalizzatore. I principali risultati conseguiti possono essere così riassunti: A. Caratteristiche Fisiche. Dall’analisi XRD si osserva che l’impregnazione con Pt(NH3)2(NO2)2 o con la sospensione nanoparticellare in DEG, non modifica le proprietà chimico-fisiche del supporto, con l’eccezione del campione con sospensione nanoparticellare impregnata su ossido misto per il quale si è osservata sia la segregazione del Pt, sia la presenza di composti carboniosi sulla superficie. Viceversa l’impregnazione con Ba porta ad una significativa diminuzione dell’area superficiale e della porosità. B. Caratteristiche Chimiche. L’analisi di dispersione metallica, tramite il chemiassorbimento di H2, mostra per i catalizzatori impregnati con Pt nanoparticellare, una bassa dispersione metallica e di conseguenza elevate dimensioni delle particelle di Pt. I campioni impregnati con Pt(NH3)2(NO2)2 presentano una migliore dispersione. Infine dalle analisi TPR-O si è osservato che: Maggiore è la dispersione del metallo nobile maggiore è la sua interazione con il supporto, L’aumento della temperatura di riduzione del PtOx è proporzionale alla quantità dei metalli alcalino terrosi, C. Precursore Metallo Nobile. Nelle prove di attività catalitica, con cicli ossidanti e riducenti continui in presenza ed in assenza di CO2, i catalizzatori con Pt nanoparticellare mostrano una minore attività catalitica, specie in presenza di un competitore come la CO2. Al contrario i catalizzatori ottenuti per impregnazione con la soluzione acquosa di Pt(NH3)2(NO2)2 presentano un’ottima attività catalitica, stabile nel tempo, e sono meno influenzabili dalla presenza di CO2. D. Resistenza all’avvelenamento da SO2. Il catalizzatore di riferimento, 17Ba1Pt/γAl2O3, mostra un effetto di avvelenamento con formazione di solfati più stabili che sul sistema Ba-Mg; difatti il campione non recupera i valori iniziali di attività se non dopo molti cicli di rigenerazione e temperature superiori ai 300°C. Per questi catalizzatori l’avvelenamento da SO2 sembra essere di tipo reversibile, anche se a temperature e condizioni più favorevoli per il 1.5Mg8.5Ba-1Pt/γAl2O3. E. Capacità di Accumulo e Rigenerabilità. Tramite questo tipo di prova è stato possibile ipotizzare e verificare il meccanismo della riduzione. I catalizzatori ottenuti per impregnazione con la soluzione acquosa di Pt(NH3)2(NO2)2 hanno mostrato un’elevata capacità di accumulo. Questa è maggiore per il campione bimetallico (Ba-Mg) a T < 300°C, mentre per il riferimento è maggiore per T > 300°C. Per ambedue i catalizzatori è evidente la formazione di ammoniaca, che potrebbe essere utilizzata come un indice che la riduzione dei nitrati accumulati è arrivata al termine e che il tempo ottimale per la riduzione è stato raggiunto o superato. Per evitare la formazione di NH3, sul catalizzatore di riferimento, è stata variata la concentrazione del riducente e la temperatura in modo da permettere alle specie adsorbite sulla superficie e nel bulk di poter raggiungere il Pt prima che l’ambiente diventi troppo riducente e quindi meno selettivo. La presenza di CO2 riduce fortemente la formazione di NH3; probabilmente perché la CO2, occupando i siti degli elementi alcalino-terrosi lontani dal Pt, impedisce ai nitriti/nitrati o all’H2 attivato di percorrere “elevate” distanze prima di reagire, aumentando così le possibilità di una riduzione più breve e più selettiva. F. Tempo di Riduzione. Si è migliorata la comprensione del ruolo svolto dalla concentrazione dell’agente riducente e dell’effetto della durata della fase riducente. Una durata troppo breve porta, nel lungo periodo, alla saturazione dei siti attivi, un eccesso alla formazione di NH3 Attraverso queste ultime prove è stato possibile formulare un meccanismo di reazione, in particolare della fase riducente. G. Meccanismo di Riduzione. La mobilità dei reagenti, nitriti/nitrati o H2 attivato è un elemento fondamentale nel meccanismo della riduzione. La vicinanza tra i siti di accumulo e quelli redox è determinante per il tipo di prodotti che si possono ottenere. La diminuzione della concentrazione del riducente o l’aumento della temperatura concede maggiore tempo o energia alle specie adsorbite sulla superficie o nel bulk per migrare e reagire prima che l’ambiente diventi troppo riducente e quindi meno selettivo.

Sintesi e caratterizzazione di nanopolveri composite allumina-zirconia

Il presente lavoro di tesi riguarda la sintesi di nanopolveri allumina-zirconia, seguendo tre differenti metodologie (sintesi per coprecipitazione, sintesi con il metodo dei citrati, sintesi idrotermale assistita da microonde) e il trattamento termico (calcinazione) delle polveri ottenute, mediante tecniche di riscaldamento convenzionali ed alternative (microonde). Lo scopo del lavoro è consistito nell’individuare, tra le tecniche esaminate, quella più idonea e conveniente, per la preparazione di nanopolveri cristalline 95 mol% Al2O3 – 5 mol% ZrO2 e nell’esaminare gli effetti che la calcinazione condotta con le microonde, ha sulle caratteristiche finali delle polveri, rispetto ai trattamenti termici convenzionali. I risultati ottenuti al termine del lavoro hanno evidenziato che, tra le tecniche di sintesi esaminate, la sintesi idrotermale assistita da microonde, risulta il metodo più indicato e che, il trattamento termico eseguito con le microonde, risulta di gran lunga vantaggioso rispetto a quello convenzionale. La sintesi idrotermale assistita da microonde consente di ottenere polveri nano cristalline poco agglomerate, che possono essere facilmente disaggregate e con caratteristiche microstrutturali del tutto peculiari. L’utilizzo di tale tecnica permette, già dopo la sintesi a 200°C/2ore, di avere ossido di zirconio, mentre per ottenere gli ossidi di alluminio, è sufficiente un ulteriore trattamento termico a basse temperature e di breve durata (400°C/ 5 min). Si è osservato, inoltre, che il trattamento termico condotto con le microonde comporta la formazione delle fasi cristalline desiderate (ossidi di alluminio e zirconio), impiegando (come per la sintesi) tempi e temperature significativamente ridotti. L’esposizione delle polveri per tempi ridotti e a temperature più basse consente di evitare la formazione di aggregati duri nelle nanopolveri finali e di contrastare il manifestarsi di fenomeni di accrescimento di grani, preservando così la “nanostruttura” delle polveri e le sue caratteristiche proprietà.

Idrolisi diretta di cellulosa e lignocellulosa in catalisi eterogenea

This work deals with a comparison of the catalytic behavior of several heterogeneous acid catalysts in the direct hydrolysis of an untreated softwood dust. Amongst the various catalysts investigated, some were characterized by relatively high yield to monosaccharides, such as a Zirconium phosphate and the reference Amberlyst 15. Conversely, some catalyst types, ie, Sn/W mixed oxide and Zirconia-grafted trifluoromethanesulphonic acid, were selective into glucose, since sugars derived from hemicellulose dissolution and hydrolysis were rapidly degraded. A detailed analysis of the reactivity of Zr/P/O was pursued, in the hydrolysis of both untreated and ball-milled microcrystalline cellulose; at 150°C and 3h reaction time, the catalyst gave high selectivity to glucose, with negligible formation of 5-hydroxymethylfurfural, and moderate cellulose conversion. After ball-milling of the cellulose, a remarkable increase of conversion was achieved, still with a high selectivity to glucose and very low formation of degradation compounds. The catalyst showed high affinity for β-1,4-glucans, as demonstrated by the activity in cellobiose hydrolysis into glucose.

Influence of curing rate on softening in ethanol, degree of conversion, and wear of resin composite

PURPOSE: To investigate the effect of curing rate on softening in ethanol, degree of conversion, and wear of resin composites. METHOD: With a given energy density and for each of two different light-curing units (QTH or LED), the curing rate was reduced by modulating the curing mode. Thus, the irradiation of resin composite specimens (Filtek Z250, Tetric Ceram, Esthet-X) was performed in a continuous curing mode and in a pulse-delay curing mode. Wallace hardness was used to determine the softening of resin composite after storage in ethanol. Degree of conversion was determined by infrared spectroscopy (FTIR). Wear was assessed by a three-body test. Data were submitted to Levene's test, one and three-way ANOVA, and Tukey HSD test (alpha = 0.05). Results: Immersion in ethanol, curing mode, and material all had significant effects on Wallace hardness. After ethanol storage, resin composites exposed to the pulse-delay curing mode were softer than resin composites exposed to continuous cure (P< 0.0001). Tetric Ceram was the softest material followed by Esthet-X and Filtek Z250 (P< 0.001). Only the restorative material had a significant effect on degree of conversion (P< 0.001): Esthet-X had the lowest degree of conversion followed by Filtek Z250 and Tetric Ceram. Curing mode (P= 0.007) and material (P< 0.001) had significant effect on wear. Higher wear resulted from the pulse-delay curing mode when compared to continuous curing, and Filtek Z250 showed the lowest wear followed by Esthet-X and Tetric Ceram.

Curing capability of halogen and LED light curing units in deep class II cavities in extracted human molars

Class II cavities were prepared in extracted lower molars filled and cured in three 2-mm increments using a metal matrix. Three composites (Spectrum TPH A4, Ceram X mono M7 and Tetric Ceram A4) were cured with both the SmartLite PS LED LCU and the Spectrum 800 continuous cure halogen LCU using curing cycles of 10, 20 and 40 seconds. Each increment was cured before adding the next. After a seven-day incubation period, the composite specimens were removed from the teeth, embedded in self-curing resin and ground to half the orofacial width. Knoop microhardness was determined 100, 200, 500, 1000, 1500, 2500, 3500, 4500 and 5500 microm from the occlusal surface at a distance of 150 microm and 1000 microm from the metal matrix. The total degree of polymerization of a composite specimen for any given curing time and curing light was determined by calculating the area under the hardness curve. Hardness values 150 microm from the metal matrix never reached maximum values and were generally lower than those 1000 microm from the matrix. The hardest composite was usually encountered between 200 microm and 1000 microm from the occlusal surface. For every composite-curing time combination, there was an increase in microhardness at the top of each increment (measurements at 500, 2500 and 4500 microm) and a decrease towards the bottom of each increment (measurements at 1500, 3500 and 5500 microm). Longer curing times were usually combined with harder composite samples. Spectrum TPH composite was the only composite showing a satisfactory degree of polymerization for all three curing times and both LCUs. Multiple linear regression showed that only the curing time (p < 0.001) and composite material (p < 0.001) had a significant association with the degree of polymerization. The degree of polymerization achieved by the LED LCU was not significantly different from that achieved by the halogen LCU (p = 0.54).

Effect of zirconia surface treatments on the shear strength of zirconia/veneering ceramic composites

Aim of the investigation was to assess the effect of different surface treatments on the bond strength of veneering ceramics to zirconia. In a shear test, the influences of polishing, sandblasting, and silica-coating of the zirconia surface on bonding were assessed with five different veneering ceramics. In addition the effect of liner application was examined. With one veneering ceramic, the impact of regeneration firing of zirconia was also evaluated. Statistical analysis was performed with one-way ANOVA and post hoc Scheffé's test. Failure in every case occurred in the veneering ceramic adjacent to the interface with a thin layer of ceramic remaining on the zirconia surface, indicating that bond strength was higher than the cohesive strength of the veneering ceramic. Shear strength ranged from 23.5 +/- 3.4 MPa to 33.0 +/- 6.8 MPa without explicit correlation to the respective surface treatment. Regeneration firing significantly decreased the shear strength of both polished and sandblasted surfaces. Findings of this study revealed that bonding between veneering ceramics and zirconia might be based on chemical bonds. On this note, sandblasting was not a necessary surface pretreatment to enhance bond strength and that regeneration firing was not recommended.

Zirconia for teeth and implants

This case series reports on the use of nonsilica-based high-strength full ceramics for different prosthetic indications. Fifty-two consecutive patients received tooth- or implant-supported zirconia reconstructions during a 2-year period. The observation period for reexamination was 12 to 30 months. The most frequent indications were single crowns and short-span fixed partial dentures. A few implant superstructures were screw-retained, whereas all remaining restorations were cemented on natural teeth or zirconia implant abutments. Clinical examination included biologic (probing depths, bleeding on probing) and esthetic (Papilla Index) parameters, as well as technical complications. No implant was lost or caused any problems, but two teeth were lost after horizontal fracture. Overall, the periodontal parameters were favorable. Fractures of frameworks or implant abutments were not observed. Abutment-screw loosening occurred once for one premolar single crown. Furthermore, five implant crowns in the posterior region exhibited chipping of the porcelain veneering material. With regard to esthetics, no reconstructions were considered unacceptable, but three crowns were remade shortly after delivery. In this short-term study, it was observed that biologic, esthetic, and mechanical properties of zirconia were favorable, and the material could be used in various prosthetic indications on teeth or implants.

[Zirconia and removable partial dentures]

The present paper deals with the double crown technique in removable prosthodontics. New ceramic materials like zirconia are increasingly used in combination with CAD/CAM technologies for framework fabrication of fixed prosthesis, tooth- or implant-supported. However, zirconia is also a newly accepted material in removable prosthodontics. It replaces gold alloys for the fabrication of primary telescopic crowns. The Galvanoforming technology is preferably used to fabricate the secondary crowns. The combination of both techniques and materials results in a prosthetic reconstruction of high quality, optimum fit and good biocompatibility.