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研究了在不同的激光扫描速度下对45^#钢表面进行Ni/Cr3C2激光熔覆,工对合金组织,显微硬度和物相进行了分析,结果表明,激光扫描度对Ni/Cr3C2合金层的组织和显微硬度有很大的影响。 相似文献
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使用2kw连续波CO2激光器在45^#钢表面进行激光熔敷Ni合金中添加50wt%Ni Cr包敷的Cr3C2复合粉的复合少层,并对激光熔敷层的晶体生长形态、物相和硬度进行了分析。结果表明:熔敷层由下至上可分为平面前沿生长区,胸状晶区及枝晶:熔敷区的近表层由高度细小的奥氏体枝晶和C7C3、Cr3C2等物组成,熔敷层的硬度平均高达HV0.2950-1200。添加Cr3C2粒子的激光熔敷层的显微硬度比镍基合金的显微硬度平均提高了HV0.2300。 相似文献
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通过对等离子喷涂涂层在Nd-YAG激光处理前和处理后的磨损量对比,研究了激光处理对等离子喷涂Cr2O3陶瓷薄涂层的影响,为此,用陶瓷/SAE4620钢以线接触配对进行了环形试样磨损试验,还讨论了磨损机制和因激光处理引起的涂层中有关孔隙率,显微结构和涂层结合情况的变化。 相似文献
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引进型的电站泵平衡鼓等零件采用1Cr17Ni2钢制造。国产的1Cr17Ni2钢的含镍量低,导致金相组织有大量的铁素体,从而影响力学性能,通过调整热处理工艺使材料达到了设计规定的技术要求。表7参2 相似文献
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《International Journal of Hydrogen Energy》2022,47(5):2958-2966
Exploring cost-efficient electrocatalysts for oxygen evolution reaction (OER) is still a huge challenge in the electrochemical energy conversion technology. In this work, Gallium (Ga)-doped Ni3S2 nanosheet arrays grown on Ti3C2-MXene/nickel foam (Ga–Ni3S2/Ti3C2/NF) have been synthesized by a successive hydrothermal and sulfidization process. The Ga doping modulates the electronic structure of Ni3S2, so tuning the adsorption energies of oxygen intermediate (1OOH). The Ga–Ni3S2/Ti3C2/NF delivers outstanding catalytic activities toward OER with an overpotential of 340 mV at 100 mA cm?2, and exhibits superior electrochemical durability. The excellent OER performance of Ga–Ni3S2/Ti3C2/NF can be ascribed to the 3D sheet arrays morphology and optimized electronic structure. Density functional theory (DFT) calculations also demonstrate that electronic disturbance attributed to Ga doping effectively improves the activity of Ni sites, leading to stronger binding strength of 1OOH intermediate at Ni sites nearby Ga. This study provides insights into the fabrication of advanced electrocatalysts for application. 相似文献
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三维激光雷达扫描技术以精度高、测量速度快的特点被应用于多个行业。为快速获取河道流场结构,开展60°弯道动床模型试验,探索采用激光雷达扫描技术获得河床数字地形,以激光扫描数字地形和水准测量地形为边界开展水流数值模拟,并将模拟值与试验测量值进行对比分析。结果表明,流场数值模拟结果与试验值吻合较好。沙波地形的精度对纵向时均流速、水深平均流速影响有限,但对河床切应力及断面流场结构影响明显。将激光雷达扫描技术和数值模拟技术相结合,既能获得高精度的河床数字高程和精细水流流动结构,又可大大缩短试验流场测量周期。 相似文献
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The aqueous-phase reforming (APR) of n-butanol (n-BuOH) over Ni(20 wt%) loaded Al2O3 and CeO2 catalysts has been studied in this paper. Over 100 h of run time, the Ni/Al2O3 catalyst showed significant deactivation compared to the Ni/CeO2 catalyst, both in terms of production rates and the selectivity to H2 and CO2. The Ni/CeO2 catalyst demonstrated higher selectivity for H2 and CO2, lower selectivity to alkanes, and a lower amount of C in the liquid phase compared to the Ni/Al2O3 sample. For the Ni/Al2O3 catalyst, the selectivity to CO increased with temperature, while the Ni/CeO2 catalyst produced no CO. For the Ni/CeO2 catalyst, the activation energies for H2 and CO2 production were 146 and 169 kJ mol−1, while for the Ni/Al2O3 catalyst these activation energies were 158 and 175 kJ mol−1, respectively. The difference of the active metal dispersion on Al2O3 and CeO2 supports, as measured from H2-pulse chemisorption was not significant. This indicates deposition of carbon on the catalyst as a likely cause of lower activity of the Ni/Al2O3 catalyst. It is unlikely that carbon would build up on the Ni/CeO2 catalyst due to higher oxygen mobility in the Ni doped non-stoichiometric CeO2 lattice. Based on the products formed, the proposed primary reaction pathway is the dehydrogenation of n-BuOH to butaldehyde followed by decarbonylation to propane. The propane then partially breaks down to hydrogen and carbon monoxide through steam reforming, while CO converts to CO2 mostly through water gas shift. Ethane and methane are formed via Fischer-Tropsch reactions of CO/CO2 with H2. 相似文献
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Guanyi Chen Junyu Tao Caixia Liu Beibei Yan Wanqing Li Xiangping Li 《International Journal of Hydrogen Energy》2017,42(32):20729-20738
Ni-based catalysts supported on various alumina supports with different crystalline phases (γ-, α-, θ- and δ-Al2O3) were prepared and the effects of crystalline phases on the catalytic performance towards acetic acid steam reforming (AASR) were investigated. An acetic acid conversion of nearly 100% was observed in all the four catalysts, and their hydrogen selectivities were in the following order: Ni/α-Al2O3 (90%) > Ni/γ-Al2O3 (79%) > Ni/δ-Al2O3 (53%) > Ni/θ-Al2O3 (25%). Using different characterization methods, the inner relationship between catalyst crystalline phase and catalytic properties was determined. Through TEM, H2-TPR and XPS characterization, Compared with α-Al2O3, on the surface of other crystalline phases of Al2O3 support were formed NiAl2O4 which indicated stronger interaction intensity between these supports and Ni., and that would reduce the formation of metallic Ni. It was confirmed that metallic Ni played a core role of catalytic AASR. More metallic Ni content caused better CC bonds and CH bonds breaking capability and eventually enhanced the selectivity towards hydrogen. That would be the key reason for Ni/α-Al2O3 showed best hydrogen selectivity among these four catalysts. 相似文献
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将金属有机骨架MIL-101(Cr)-NH2与CaCl2通过浸渍的方法复合得到MIL-101(Cr)-NH2/CaCl2热化学蓄热复合材料。采用X射线衍射分析仪(XRD)、扫描电子显微镜(SEM)、能谱分析(EDS)、全自动比表面积及孔径分析仪以及同步热分析仪(TG-DSC)等分析了复合材料的表观形貌、盐含量、比表面积和蓄热密度等参数。结果显示,复合材料的盐含量为49%,在30℃、32%湿度下的最大吸水量为0.54 g(H2O)/g(样品),蓄热密度达到了1 204 kJ/kg,并且在经历了17次吸附-解吸循环后,其蓄热密度仅降低了6.5%,表现出优异的循环稳定性,出色的吸附性能表明这一新型复合材料在太阳能蓄热领域具有广阔的应用前景。 相似文献
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《International Journal of Hydrogen Energy》2022,47(6):3633-3643
The influence of the addition amount of lanthanum oxide on the activity and coke formation over Ni/SiO2 catalyst for hydrogen production from AcOH steam reforming was studied in the paper. Through the catalyst characterization and experimental research, it was found that with the addition of La2O3 the particle size of the active metal Ni decreased, and the active Ni-support interaction was enhanced. With the optimal addition amount of La2O3 (30 wt %), Ni/30LaSi catalyst displayed the highest activity with the high carbon conversion rate of 98.8%. The surface morphology and thermogravimetric analysis of the spent catalyst revealed that the carbon deposition was mainly in the form of filamentous coke and the diameter of the carbon fiber was related with the Ni particle size. The addition of suitable La2O3 can inhibit the formation of carbon deposition, decrease the content of encapsulating coke, and improve the catalyst stability. 相似文献