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1.
Al 2O 3–SiC composites containing up to 30 wt.% of dispersed SiC particles (280 nm) were fabricated via hot-pressing and machined as cutting tools. The Al 2O 3–SiC particulate composites exhibit higher hardness than their unreinforced matrix because of the inhibited grain growth by adding SiC and the presence of hard secondary phase (SiC). The fracture toughness of the composites remains constant up to 10 wt.% loading of SiC. For machining heat-treated AISI 4144140 steel, the Al 2O 3–10 wt.% SiC composite tool showed the longest tool life, seven times longer than a commercial tool made of Al 2O 3–TiC composite, while the composite tool with 5 wt.% SiC showed the longest tool life for machining gray cast iron. The improved performance of the Al 2O 3–SiC composite tools attributes to the transformation of fracture mode from intergranular fracture for Al 2O 3 to intragranular fracture for Al 2O 3–SiC composites. 相似文献
2.
Al 2O 3/TiCN composites have been fabricated by gas pressure sintering, which overcomes the limitations of hot pressing. The densification behavior and mechanical properties of the Al 2O 3 gas pressure sintered with 30 wt.% TiCN at different temperatures have been investigated. The gas pressure sintered Al 2O 3–30 wt.%TiCN composite achieved a relative density of 99.5%, a bending strength of 772 MPa, a hardness of 19.6 GPa, and a fracture toughness of 5.82 MPa·M 1/2. 相似文献
3.
In situ growth of needlelike LaAl 11O 18 grains reinforcing Al 2O 3 composites can be fabricated by a coprecipitation method using La(NO 3) 3√6H 2O and Al(NO 3) 3√9H 2O as starting materials. The new two-step process involved firstly preparing needlelike LaAl 11O 18 grains distributed homogeneously in Al 2O 3 powder and then pressureless sintering the composite powders. The Al 2O 3/25 vol.%LaAl 11O 18 samples pressureless sintered at 1550°C for 4 h achieve relative density up to 96.5% and exhibit a bending strength of 420±30 MPa and a fracture toughness of 4.3±0.4 MPa m 1/2. 相似文献
4.
The effect of Al 2O 3 on mechanical properties of Ti 3SiC 2/Al 2O 3 composite fabricated by SPS was studied systematically. The results show that the hardness of the Ti 3SiC 2/Al 2O 3 composite can reach 10.28 GPa, 50% higher than that of pure Ti 3SiC 2. However, slight decrease in the other mechanical properties was observed with Al 2O 3 addition higher than 5–10 vol.%, which is believed to be due to the agglomeration of Al 2O 3 in the composite. 相似文献
5.
Al 2O 3–30 wt.%TiCN composites have been fabricated successfully by a two-stage gas pressure sintering schedule. The gas pressure sintered Al 2O 3–30 wt.%TiCN composite achieved a relative density of 99.5%, a bending strength of 772 MPa, a hardness of 19.6 GPa, and a fracture toughness of 5.82 MPa m 1/2. The fabrication procedure involves solid state sintering of two phases without solubility to prepare Al 2O 3–TiCN composite. Little grain growth occurred for TiCN during sintering while Al 2O 3 grains grew about three times to an average size of 3–5 μm. The interface microstress arising during cooling from the processing temperature because of the thermal and/or mechanical properties mismatch between the Al 2O 3 and TiCN phase is about 50 MPa. Such a compressive microstress is not high enough to cause grain boundary cracking that may weaken the composite but it can introduce dislocations within grains, which is very good to enhance the composite properties. 相似文献
6.
以Si、Al 2O 3、MoSi 2微粉和生物竹材为原料,采用包埋烧结法分别制备出SiC多孔材料、Al 2O 3/SiC、MoSi 2/SiC复合材料。采用XRD、SEM及波导法测试其物相组成、显微结构及吸波性能。结果表明:MoSi 2/SiC复合材料的厚度为2 mm时有明显的吸波特性,有效吸收带宽在X波段的9.65~12.4 GHz频率范围内达2.75 GHz,且最低反射损耗为-38.27 dB。Al 2O 3/SiC复合材料孔道内的Al 2O 3与SiC晶须交缠,形成大量电偶极矩,产生介电损耗;MoSi 2/SiC复合材料除介电损耗外还存在电阻损耗,使得复合材料电磁损耗增加,是较有前途的结构功能吸波材料。 相似文献
7.
The effect of Al 2O 3 levels on the properties of NiO in coprecipitated NiO–Al 2O 3 samples were investigated, using samples with up to 60.7 wt.% Al 2O 3 that had been calcined in the range 300–700°C. Characterization techniques included BET surface area of fresh and reduced catalysts, X-ray diffraction analysis of structure and crystallite size, magnetic susceptibility measurements, oxidizing power, and reducibility in H 2. Only NiO was detected in samples with up to 4.1 wt.% Al 2O 3 for all sample calcination temperatures. Surface areas were similar for all fresh samples but decreased rapidly after calcination at high temperatures. The surface area loss was less for the higher Al 2O 3-containing samples. Nickel oxide crystallite sizes increased at higher calcination temperatures, but remained approximately the same for each Al 2O 3 level. The NiO was nonstoichiometric (NiO1+x), with x decreasing at higher calcination temperatures and increasing with small amounts of added Al2O3 through a maximum at about 3 wt.% Al2O3. However, this did not correlate well with microstrain in the NiO crystallites nor with reducibility, which decreased with Al2O3 addition. At higher levels of Al2O3 (13.6 wt.% and above), surface areas increased with higher Al2O3 loadings, but NiO crystallite sizes remained approximately the same, independent of both Al2O3 content and calcination temperature. X-ray diffraction patterns were very diffuse, and it was not possible to rule out the presence of pseudo-spinel combinations of NiO and Al2O3. Reducibility was more difficult than with low Al2O3 levels, and nonstoichiometry was low and independent of Al2O3 content. Reducibilities of all samples calcined at 300°C correlated well with the final BET surface area of the reduced samples, indicating that more dispersed NiO crystallites are more difficult to reduce, a conclusion that supports a model for reduction proposed previously. 相似文献
8.
A process using metal-organic chemical vapor infiltration (MOCVI) conducted in fluidized bed was employed for the preparation of nano-sized ceramic composites. The Cr-species was infiltrated into Al 2O 3 granules by the pyrolysis of chromium carbonyl (Cr(CO) 6) at 300–450 °C. The granulated powder was pressureless sintered or hot-pressed to achieve high density. The results showed that the dominant factors influencing the Cr-carbide phases formation, either Cr 3C 2 or Cr 7C 3, in the composite powders during the sintering process were the temperature and oxygen partial pressure in the furnace. The coated Cr-phase either in agglomerated or dispersive condition was controlled by the use of colloidal dispersion. The microstructures showed that fine (20 –600 nm) Cr xC y grains (≤8 vol.%) located at Al 2O 3 grain boundaries hardly retarded the densification of Al 2O 3 matrix in sintering process. The tests on hardness, strength and toughness appeared that the composites with the inclusions (Cr 3C 2) had gained the advantages over those by the rule of mixture. Even 8 vol.% ultrafine inclusions have greatly improved the mechanical properties. The strengthening and toughening mechanisms of the composites were due to grain-size reduction, homogenous dispersion of hard inclusions, and crack deflection. 相似文献
9.
A multi-component NO x-trap catalyst consisting of Pt and K supported on γ-Al 2O 3 was studied at 250 °C to determine the roles of the individual catalyst components, to identify the adsorbing species during the lean capture cycle, and to assess the effects of H 2O and CO 2 on NO x storage. The Al 2O 3 support was shown to have NO x trapping capability with and without Pt present (at 250 °C Pt/Al 2O 3 adsorbs 2.3 μmols NO x/m 2). NO x is primarily trapped on Al 2O 3 in the form of nitrates with monodentate, chelating and bridged forms apparent in Diffuse Reflectance mid-Infrared Fourier Transform Spectroscopy (DRIFTS) analysis. The addition of K to the catalyst increases the adsorption capacity to 6.2 μmols NO x/m 2, and the primary storage form on K is a free nitrate ion. Quantitative DRIFTS analysis shows that 12% of the nitrates on a Pt/K/Al 2O 3 catalyst are coordinated on the Al 2O 3 support at saturation. When 5% CO2 was included in a feed stream with 300 ppm NO and 12% O2, the amount of K-based nitrate storage decreased by 45% after 1 h on stream due to the competition of adsorbed free nitrates with carboxylates for adsorption sites. When 5% H2O was included in a feed stream with 300 ppm NO and 12% O2, the amount of K-based nitrate storage decreased by only 16% after 1 h, but the Al2O3-based nitrates decreased by 92%. Interestingly, with both 5% CO2 and 5% H2O in the feed, the total storage only decreased by 11%, as the hydroxyl groups generated on Al2O3 destabilized the K–CO2 bond; specifically, H2O mitigates the NOx storage capacity losses associated with carboxylate competition. 相似文献
10.
The system Al 2O 3–ZrO 2 was studied by differential thermal analysis in inert atmosphere and in vacuum. The eutectic was located at 1866°C and 40% mass of ZrO 2. Zirconia solid solution at the eutectic temperature is up to 1.1±0.3% mass of Al 2O 3. Enthalpy of melting of this eutectic is 1080±90 J/g. Pure ZrO 2 transforms from monoclinic to tetragonal at 1162±7°C, but the saturated solid solution of ZrO 2, with 0.7±0.2% mass Al 2O 3 at this temperature, transforms at 1085±5°C. Inverse transitions occur with hysteresis correspondingly at 1055±5 and 995±5°C. Enthalpy of transformation of pure ZrO 2 from monoclinic to tetragonal phase is 42±5 J/g (5.2±0.6 J/mol) but only 30±5 J/g for a ZrO 2 saturated solid solution. 相似文献
11.
Supported molybdenum and tungsten carbides were synthesized by temperature-programmed reactions. These materials were characterized by XRD, EDS analysis, HRTEM and CO chemisorption. Hydrogenation of tetralin was carried out at a total pressure of 4 MPa (3.06 MPa of H 2), at 573 K, without or with sulfur (200 ppm of sulfur as DMDS). The resulting activities were compared with those of MoS 2/Al 2O 3 and Pt (1% (w/w) metal loading) supported on Al 2O 3 or SiO 2. In the absence of sulfur, WC/Al 2O 3 showed an initial activity similar to that of Pt/SiO 2, higher than that of MoS 2/Al 2O 3 but lower than that of Pt/Al 2O 3. In the presence of H 2S, WC/Al 2O 3 showed a steady-state activity similar to that of Pt/Al 2O 3 (which suffered a marked deactivation). Post-reaction characterization did not show any sulfur poisoning of the supported carbides. Therefore the supported carbides are sulfur-tolerant and promising catalysts for the hydrogenation of aromatics in diesel fuels in the presence of small amounts of S-containing compounds. 相似文献
12.
Previous studies demonstrated that the strength of alumina could be enhanced by incorporating >5 vol.% nano-sized nickel particles. In the present study, the possibility of using a much smaller amount, <0.5 vol.%, of nano-sized Ni particles to improve the mechanical properties of Al 2O 3 is explored. As the Ni content is low, the densification of Al 2O 3 is affected little and the Ni inclusions remain small after pressureless sintering at 1600 °C. The presence of Ni inclusions can refine the matrix grains; the strength of Al 2O 3 matrix is consequently enhanced. 相似文献
13.
Co 3O 4/CeO 2 composite oxides with different cobalt loading (5, 15, 30, 50, 70 wt.% as Co 3O 4) were prepared by co-precipitation method and investigated for the oxidation of methane under stoichiometric conditions. Pure oxides, Co 3O 4 and CeO 2 were used as reference. Characterization studies by X-ray diffraction (XRD), BET, temperature programmed reduction/oxidation (TPR/TPO) and X-ray photoelectron spectroscopy (XPS) were carried out. An improvement of the catalytic activity and thermal stability of the composite oxides was observed with respect to pure Co3O4 in correspondence of Co3O4–CeO2 containing 30% by weight of Co3O4. The combined effect of cobalt oxide and ceria, at this composition, strongly influences the morphological and redox properties of the composite oxides, by dispersing the Co3O4 phase and promoting the efficiency of the Co3+–Co2+ redox couple. The presence in the sample Co3O4(30 wt.%)–CeO2 of a high relative amount of Ce3+/(Ce4+ + Ce3+) as detected by XPS confirms the enhanced oxygen mobility. The catalysts stability under reaction conditions was investigated by XRD and XPS analysis of the used samples, paying particular attention to the Co3O4 phase decomposition. Methane oxidation tests were performed over fresh (as prepared) and thermal aged samples (after ageing at 750 °C for 7 h, in furnace). The resistance to water vapour poisoning was evaluated for pure Co3O4 and Co3O4(30 wt.%)–CeO2, performing the tests in the presence of 5 vol.% H2O. A methane oxidation test upon hydrothermal ageing (flowing at 600 °C for 16 h a mixture 5 vol.% H2O + 5 vol.%O2 in He) of the Co3O4(30 wt.%)–CeO2 sample was also performed. All the results confirm the superiority of this composite oxide. 相似文献
14.
Catalytic properties of supported gallium oxides have been examined for the selective reduction of NO by CH 4 in excess oxygen. The activity was greatly affected by the support; Ga 2O 3/Al 2O 3 (Al 2O 3 supported Ga 2O 3) and Ga 2O 3–Al 2O 3 mixed oxide exhibited high activity and selectivity as comparable to Ga-ZSM-5, while unsupported Ga 2O 3 and the other supported Ga 2O 3 were ineffective. For Ga 2O 3/Al 2O 3, the activity changed with Ga 2O 3 content, and was highest at about 30 wt% Ga 2O 3, which corresponds to a theoretical monolayer coverage. Gallium oxide highly dispersed on Al 2O 3 is considered to be responsible for the high activity and selectivity. The reaction characteristics of Ga 2O 3/Al 2O 3 were studied and compared with Ga-ZSM-5 and Co-ZSM-5. Ga 2O 3/Al 2O 3 exhibited the highest activity and selectivity at high temperature. In addition, Ga 2O 3/Al 2O 3 showed higher tolerance against water than Ga-ZSM-5. C 3H 8 and C 3H 6 were also evaluated as reducing agents, and Ga 2O 3/Al 2O 3 showed higher activity than Ga-ZSM-5 above 723 K achieving almost complete reduction of NO to N 2. 相似文献
15.
The flexure creep behaviour of monolithic Al 2O 3 and 10 vol% SiC-particle reinforced Al 2O 3 matrix composites was investigated in air atmosphere at 1160 to 1400 °C and under a stress of 40 to 125 MPa. Two kinds of SiC particles with different particle sizes and oxygen contents were used in the composites, one having an average size of 0.6 μm with 1.7 vol% SiO 2 impurities and the other of average size 2.7 μm with 3.4 vol% SiO 2 impurities. Compared with the creep behaviour of monolithic Al 2O 3 the strain rate of the composites with 0.6 μm SiC particles did not decrease; however, the composites with 2.7 μm SiC particles exhibited excellent creep resistance. Microstructure analysis showed that the Al 2O 3 grains in the composites with 0.6 μm SiC particles were mainly equiaxed with most of the SiC particles lying at the grain boundaries or triplegrain junctions, whereas the grain features of the composites with 2.7 μm SiC particles were irregular and elongated and most of the SiC particles were entrapped into Al 2O 3 matrix grains. It was revealed that the entrapment of 2.7 μm SiC particles into Al 2O 3 matrix grains was related to the high SiO 2 impurity content on SiC particle surfaces, and the change of grain morphology and the good high-temperature oxidation resistance were responsible for the creep resistance increase of the composites with 2.7 μm SiC particles. 相似文献
16.
The effectiveness of Ag/Al 2O 3 catalyst depends greatly on the alumina source used for preparation. A series of alumina-supported catalysts derived from AlOOH, Al 2O 3, and Al(OH) 3 was studied by means of X-ray diffraction (XRD), scanning electron microscopy (SEM), ultraviolet–visible (UV–vis) spectroscopy, diffuse reflectance infrared Fourier transform (DRIFT) spectroscopy, O 2, NO + O 2-temperature programmed desorption (TPD), H 2-temperature programmed reduction (TPR), thermal gravimetric analysis (TGA) and activity test, with a focus on the correlation between their redox properties and catalytic behavior towards C 3H 6-selective catalytic reduction (SCR) of NO reaction. The best SCR activity along with a moderated C 3H 6 conversion was achieved over Ag/Al 2O 3 (I) employing AlOOH source. The high density of Ag–O–Al species in Ag/Al 2O 3 (I) is deemed to be crucial for NO selective reduction into N 2. By contrast, a high C 3H 6 conversion simultaneously with a moderate N 2 yield was observed over Ag/Al 2O 3 (II) prepared from a γ-Al 2O 3 source. The larger particles of Ag mO ( m > 2) crystallites were believed to facilitate the propene oxidation therefore leading to a scarcity of reductant for SCR of NO. An amorphous Ag/Al 2O 3 (III) was obtained via employing a Al(OH) 3 source and 500 °C calcination exhibiting a poor SCR performance similar to that for Ag-free Al 2O 3 (I). A subsequent calcination of Ag/Al 2O 3 (III) at 800 °C led to the generation of Ag/Al 2O 3 (IV) catalyst yielding a significant enhancement in both N 2 yield and C 3H 6 conversion, which was attributed to the appearance of γ-phase structure and an increase in surface area. Further thermo treatment at 950 °C for the preparation of Ag/Al 2O 3 (V) accelerated the sintering of Ag clusters resulting in a severe unselective combustion, which competes with SCR of NO reaction. In view of the transient studies, the redox properties of the prepared catalysts were investigated showing an oxidation capability of Ag/Al 2O 3 (II and V) > Ag/Al 2O 3 (IV) > Ag/Al 2O 3 (I) > Ag/Al 2O 3 (III) and Al 2O 3 (I). The formation of nitrate species is an important step for the deNO x process, which can be promoted by increasing O 2 feed concentration as evidenced by NO + O 2-TPD study for Ag/Al 2O 3 (I), achieving a better catalytic performance. 相似文献
17.
Oxidation of propene and propane to CO 2 and H 2O has been studied over Au/Al 2O 3 and two different Au/CuO/Al 2O 3 (4 wt.% Au and 7.4 wt.% Au) catalysts and compared with the catalytic behaviour of Au/Co 3O 4/Al 2O 3 (4.1 wt.% Au) and Pt/Al 2O 3 (4.8 wt.% Pt) catalysts. The various characterization techniques employed (XRD, HRTEM, TPR and DR-UV–vis) revealed the presence of metallic gold, along with a highly dispersed CuO (6 wt.% CuO), or more crystalline CuO phase (12 wt.% CuO). A higher CuO loading does not significantly influence the catalytic performance of the catalyst in propene oxidation, the gold loading appears to be more important. Moreover, it was found that 7.4Au/CuO/Al2O3 is almost as active as Pt/Al2O3, whereas Au/Co3O4/Al2O3 performs less than any of the CuO-containing gold-based catalysts. The light-off temperature for C3H8 oxidation is significantly higher than for C3H6. For this reaction the particle size effect appears to prevail over the effect of gold loading. The most active catalysts are 4Au/CuO/Al2O3 (gold particles less than 3 nm) and 4Au/Co3O4/Al2O3 (gold particles less than 5 nm). 相似文献
18.
(SiC, TiB 2)/B 4C composites were fabricated by reactive hot-pressing B 4C, Si 3N 4, -SiC and TiC powders, with (Al 2O 3 + Y 2O 3) as sintering additives. According to the thermodynamics principles, the possible reaction equations and the reaction products for the system were determined. By means of XRD, SEM of surface thermally etched and TEM the phase composition was determined. It was shown that the phase composition of sintered body was B 4C, -SiC, BN and TiB 2, and the matrix was B 4C and -SiC. The typical values of hardness, bending strength, fracture toughness and the relative density of the composites can reach HRA 88.6, 554 MPa, 5.6 MPa m 1/2 and 95.6%, respectively. Furthermore, the microstructures of the composites were analyzed by TEM, SEM and energy spectrum methods. The results show the presence of laminated structure and a clubbed frame dispersion phase and bunchy dispersion phase among the matrix. Some intragranular structures were also found in the B 4C grains. Microstructural analysis indicates that the new formed phase, uniform and fine grains, and the layered and clubbed structure play an important role in improving the properties of the composites. Fractography and crack propagation suggest that crack deflection and crack bridging are the possible toughening mechanisms. 相似文献
19.
In this study, a novel bifunctional catalyst IrFe/Al 2O 3, which is very active and selective for preferential oxidation of CO under H 2-rich atmosphere, has been developed. When the molar ratio of Fe/Ir was 5/1, the IrFe/Al 2O 3 catalyst performed best, with CO conversion of 68% and oxygen selectivity towards CO 2 formation of 86.8% attained at 100 °C. It has also been found that the impregnation sequence of Ir and Fe species on the Al 2O 3 support had a remarkable effect on the catalytic performance; the activity decreased following the order of IrFe/Al 2O 3 > co-IrFe/Al 2O 3 > FeIr/Al 2O 3. The three catalysts were characterized by XRD, H 2-TPR, FT-IR and microcalorimetry. The results demonstrated that when Ir was supported on the pre-formed Fe/Al 2O 3, the resulting structure (IrFe/Al 2O 3) allowed more metallic Ir sites exposed on the surface and accessible for CO adsorption, while did not interfere with the O 2 activation on the FeO x species. Thus, a bifunctional catalytic mechanism has been proposed where CO adsorbed on Ir sites and O 2 adsorbed on FeO x sites; the reaction may take place at the interface of Ir and FeO x or via a spill-over process. 相似文献
20.
More than 0.22 mmol of isolated VO 4 species of V 2O 5/Al 2O 3 exhibited the highest evolution of the partial oxidation products (alcohol and ketone) in the oxidation of cyclohexane and cyclopentane. The conversion of cyclohexane and the selectivity of the partial oxidation products were achieved to be 0.49% and 85% over 0.8 g of 3.5 wt.% V 2O 5/Al 2O 3, respectively, where the K/A ratio was 6.2. In addition, V 2O 5/Al 2O 3 can selectively oxidize various hydrocarbons in the liquid phase by the one-step oxygen atom insertion to CH bond. The order of priority was tertiary carbon > secondary carbon > primary carbon > benzene ring. 相似文献
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