986 resultados para Mo-ni Alloy


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Ceramic/metal interfaces were studied that fail by atomistic separation accompanied by plastic dissipation in the metal. The macroscopic toughness of the specific Ni alloy/Al2O3 interface considered is typically on the order of ten times the atomistic work of separation in mode I and even higher if combinations of mode I and mode II act on the interface. Inputs to the computational model of interface toughness are: (i) strain gradient plasticity applied to the Ni alloy with a length parameter determined by an indentation test, and (ii) a potential characterizing mixed mode separation of the interface fit to atomistic results. The roles of the several length parameters in the strain gradient plasticity are determined for indentation and crack growth. One of the parameters is shown to be of dominant importance, thus establishing that indentation can be used to measure the relevant length parameter. Recent results for separation of Ni/Al2O3 interfaces computed by atomistic methods are reviewed, including a set of results computed for mixed mode separation. An approximate potential fit to these results is characterized by the work of separation, the peak separation stress for normal separation and the traction-displacement relation in pure shearing of the interface. With these inputs, the model for steady-state crack growth is used to compute the toughness of the interface under mode I and under the full range of mode mix. The effect of interface strength and the work of separation on macroscopic toughness is computed. Fundamental implications for plasticity-enhanced toughness emerge.

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We carried out quantum mechanics (QM) studies aimed at improving the performance of hydrogen fuel cells. This led to predictions of improved materials, some of which were subsequently validated with experiments by our collaborators.

In part I, the challenge was to find a replacement for the Pt cathode that would lead to improved performance for the Oxygen Reduction Reaction (ORR) while remaining stable under operational conditions and decreasing cost. Our design strategy was to find an alloy with composition Pt3M that would lead to surface segregation such that the top layer would be pure Pt, with the second and subsequent layers richer in M. Under operating conditions we expect the surface to have significant O and/or OH chemisorbed on the surface, and hence we searched for M that would remain segregated under these conditions. Using QM we examined surface segregation for 28 Pt3M alloys, where M is a transition metal. We found that only Pt3Os and Pt3Ir showed significant surface segregation when O and OH are chemisorbed on the catalyst surfaces. This result indicates that Pt3Os and Pt3Ir favor formation of a Pt-skin surface layer structure that would resist the acidic electrolyte corrosion during fuel cell operation environments. We chose to focus on Os because the phase diagram for Pt-Ir indicated that Pt-Ir could not form a homogeneous alloy at lower temperature. To determine the performance for ORR, we used QM to examine all intermediates, reaction pathways, and reaction barriers involved in the processes for which protons from the anode reactions react with O2 to form H2O. These QM calculations used our Poisson-Boltzmann implicit solvation model include the effects of the solvent (water with dielectric constant 78 with pH 7 at 298K). We found that the rate determination step (RDS) was the Oad hydration reaction (Oad + H2Oad -> OHad + OHad) in both cases, but that the barrier for pure Pt of 0.50 eV is reduced to 0.48 eV for Pt3Os, which at 80 degrees C would increase the rate by 218%. We collaborated with the Pu-Wei Wu’s group to carry out experiments, where we found that the dealloying process-treated Pt2Os catalyst showed two-fold higher activity at 25 degrees C than pure Pt and that the alloy had 272% improved stability, validating our theoretical predictions.

We also carried out similar QM studies followed by experimental validation for the Os/Pt core-shell catalyst fabricated by the underpotential deposition (UPD) method. The QM results indicated that the RDS for ORR is a compromise between the OOH formation step (0.37 eV for Pt, 0.23 eV for Pt2ML/Os core-shell) and H2O formation steps (0.32 eV for Pt, 0.22 eV for Pt2ML/Os core-shell). We found that Pt2ML/Os has the highest activity (compared to pure Pt and to the Pt3Os alloy) because the 0.37 eV barrier decreases to 0.23 eV. To understand what aspects of the core shell structure lead to this improved performance, we considered the effect on ORR of compressing the alloy slab to the dimensions of pure Pt. However this had little effect, with the same RDS barrier 0.37 eV. This shows that the ligand effect (the electronic structure modification resulting from the Os substrate) plays a more important role than the strain effect, and is responsible for the improved activity of the core- shell catalyst. Experimental materials characterization proves the core-shell feature of our catalyst. The electrochemical experiment for Pt2ML/Os/C showed 3.5 to 5 times better ORR activity at 0.9V (vs. NHE) in 0.1M HClO4 solution at 25 degrees C as compared to those of commercially available Pt/C. The excellent correlation between experimental half potential and the OH binding energies and RDS barriers validate the feasibility of predicting catalyst activity using QM calculation and a simple Langmuir–Hinshelwood model.

In part II, we used QM calculations to study methane stream reforming on a Ni-alloy catalyst surfaces for solid oxide fuel cell (SOFC) application. SOFC has wide fuel adaptability but the coking and sulfur poisoning will reduce its stability. Experimental results suggested that the Ni4Fe alloy improves both its activity and stability compared to pure Ni. To understand the atomistic origin of this, we carried out QM calculations on surface segregation and found that the most stable configuration for Ni4Fe has a Fe atom distribution of (0%, 50%, 25%, 25%, 0%) starting at the bottom layer. We calculated that the binding of C atoms on the Ni4Fe surface is 142.9 Kcal/mol, which is about 10 Kcal/mol weaker compared to the pure Ni surface. This weaker C binding energy is expected to make coke formation less favorable, explaining why Ni4Fe has better coking resistance. This result confirms the experimental observation. The reaction energy barriers for CHx decomposition and C binding on various alloy surface, Ni4X (X=Fe, Co, Mn, and Mo), showed Ni4Fe, Ni4Co, and Fe4Mn all have better coking resistance than pure Ni, but that only Ni4Fe and Fe4Mn have (slightly) improved activity compared to pure Ni.

In part III, we used QM to examine the proton transport in doped perovskite-ceramics. Here we used a 2x2x2 supercell of perovskite with composition Ba8X7M1(OH)1O23 where X=Ce or Zr and M=Y, Gd, or Dy. Thus in each case a 4+ X is replace by a 3+ M plus a proton on one O. Here we predicted the barriers for proton diffusion allowing both includes intra-octahedron and inter-octahedra proton transfer. Without any restriction, we only observed the inter-octahedra proton transfer with similar energy barrier as previous computational work but 0.2 eV higher than experimental result for Y doped zirconate. For one restriction in our calculations is that the Odonor-Oacceptor atoms were kept at fixed distances, we found that the barrier difference between cerates/zirconates with various dopants are only 0.02~0.03 eV. To fully address performance one would need to examine proton transfer at grain boundaries, which will require larger scale ReaxFF reactive dynamics for systems with millions of atoms. The QM calculations used here will be used to train the ReaxFF force field.

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The catalytic partial oxidation of methane to syngas over Ni/Al2O3, Pt/Al2O3 and a series of Pt - Ni/Al2O3 catalysts was investigated. It was found that Pt - Ni/Al2O3 catalysts exhibit higher activity and stability than Ni/Al2O3 and Pt/Al2O3. TPR and TPD methods were used to characterize Pt - Ni bimetallic interactions in the catalysts. A series of Pt - Ni/Al2O3 catalysts and unsupported Pt - Ni samples were studied by XRD and XPS. It was found the formation of Pt - Ni alloy in the Pt - Ni/Al2O3 catalysts and the enrichment of platinum on the surface of the catalysts. It is concluded that the higher activity and stability of Pt - Ni/Al2O3 catalysts were caused by Pt - Ni bimetallic interactions.

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In recent years, Mg-Ni-based metastable alloys have been attracting attention due to their large hydrogen sorption capacities, low weight, low cost, and high availability. Despite the large discharge capacity and high activity of these alloys, the accelerated degradation of the discharge capacity after only few cycles of charge and discharge is the main shortcoming against their commercial use in batteries. The addition of alloying elements showed to be an effective way of improving the electrode performance of Mg-Ni-based alloys. In the present work, the effect of Ti and Pt alloying elements on the structure and electrode performance of a binary Mg-Ni alloy was investigated. The XRD and HRTEM revealed that all the investigated alloy compositions had multi-phase nanostructures, with crystallite size in the range of 6 nm. Moreover, the investigated alloying elements demonstrated remarkable improvements of both maximum discharge capacity and cycling life. Simultaneous addition of Ti and Pd demonstrated a synergetic effect on the electrochemical properties of the alloy electrodes. Among the investigated alloys, the best electrochemical performance was obtained for the Mg(51)Ti(4)Ni(43)Pt(2) composition (in at.%), which achieved 448 mAh g(-1) of maximum discharge capacity and retained almost 66% of this capacity after 10 cycles. In contrast, the binary Mg(55)Ni(45) alloy achieved only 248 mAh g(-1) and retained 11% of this capacity after 10 cycles. (C) 2010 Elsevier By. All rights reserved.

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The development of reliable, high powered plasma generators has resulted in many plasma processes being proposed as alternatives to existing pyrometallurgical technologies. This work evaluates the advantages and disadvantages of plasma systems by reviewing plasma generators, their integration with reactors and the process economics. Many plasma systems were shown to be technically and economically superior to existing technologies, but some of the plasma system advantages quoted in the literature were found to be impractical because of other system constraints. Process applications were limited by the power inputs available from plasma generators compared to AC electric furnaces. A series of trials were conducted where chromite and steelplant baghouse dusts were smelted in the Tetronics' 2.0 MW transferred arc/open bath reactor to confirm the operating characteristics of the plasma system and its economics. Chromite smelting was technical superior to submerged arc furnace technology, but the economics were unfavourable because of the limited power available from the water-cooled plasma torch and the high electrical energy consumption. A DC graphite electrode plasma furnace using preheated and prereduced chromite concentrates will compete economically with the submerged arc furnace. Ni, Cr and Mo were economically recovered from high alloy content steelplant dusts for recycling. Five Electric Arc Furnace dusts were smelted to produce a non-toxic residue and recover the contained zinc to an enriched zinc oxide product for recycling. It should be possible to condense the zinc vapour directly in a zinc splash condenser to increase the value of the product. Because of the limited power available from plasma generators, plasma processes will be most suitable for treating high and medium value materials such as Au, Pt, Mo, Ni, Ti, V, Cr etc at small production rates, heating metals in tundishes and ladles and remelting superalloy scrap. The treatment of environmentally hazardous waste materials is a particularly interesting application because of the additional financial incentives. Non-transferred arc plasma generators will be used for air and gas preheating in blast furnaces to reduce metallurgical coke consumptions.

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Mossbauer effect and X-ray measurements are carried out on product samples of the thermogravimetric analysis (TGA) and isothermal decomposition in hydrogen of homogeneously mixed ferrous nickel oxalates with different iron to nickel ratios. The formation of Fe-Ni alloy is obtained at considerably lower temperatures (z 300 "C) in each case. The Fe-Ni alloys obtained shift from iron-rich to nickel-rich composition as the nickel ratio in the mixed metal oxalates is increased. The formation of Pe-Ni Invar from mixed metal oxalate with Fe:Ni = 1:l is indicated in the early stages but not from those with Fe:Ni = 2: 1 or 64:36. An Produktproben von homogen verteilten Eisen-Nickeloxalaten mit unterschiedlichem Eisen- Nickel-Verhaltnis nach thermogravimetrischer Analyse (TGA) und isothermem Zerfall in Wasserst off werden Mollbauereffekt- und Rontgenmessnngen durchgefuhrt. In allen Fiillen wird die Bildung der Fe-Ni-Legierung bei betriichtlich niedrigeren Temperaturen (= 300 "C) erhalten. Die erhaltenen Fe-Ni-Legierungen verschieben sich von der eisenreichen zur nickelreichen Zusrtmmensetzung, wenn das Nickelverhaltnis in dem BIetall-Mischoxalat erhoht wird. Die Bildung der Fe-Ni-lnvar-Legierung aus dem Metall-Mischoxalat mit Fe:Ni = 1 : 1 wird in fruhen Zu Zustanden beobachtet, iedoch nicht aus Oxalaten mit Fe:Ni = 2:1 oder 64:36.

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Mossbauer effect and X-ray measurements are carried out on product samples of the thermogravimetric analysis (TGA) and isothermal decomposition in hydrogen of homogeneously mixed ferrous nickel oxalates with different iron to nickel ratios. The formation of Fe-Ni alloy is obtained at considerably lower temperatures (z 300 "C) in each case. The Fe-Ni alloys obtained shift from iron-rich to nickel-rich composition as the nickel ratio in the mixed metal oxalates is increased. The formation of Pe-Ni Invar from mixed metal oxalate with Fe:Ni = 1:l is indicated in the early stages but not from those with Fe:Ni = 2: 1 or 64:36. An Produktproben von homogen verteilten Eisen-Nickeloxalaten mit unterschiedlichem Eisen- Nickel-Verhaltnis nach thermogravimetrischer Analyse (TGA) und isothermem Zerfall in Wasserstoff werden Mollbauereffekt- und Rontgenmessnngen durchgefuhrt. In allen Fiillen wird die Bildung der Fe-Ni-Legierung bei betriichtlich niedrigeren Temperaturen (= 300 "C) erhalten. Die erhaltenen Fe-Ni-Legierungen verschieben sich von der eisenreichen zur nickelreichen Zusrtmmensetzung, wenn das Nickelverhaltnis in dem BIetall-Mischoxalat erhoht wird. Die Bildung der Fe-Ni-lnvar-Legierung aus dem Metall-Mischoxalat mit Fe:Ni = 1 : 1 wird in fruhen Zustanden beobachtet, iedoch nicht aus Oxalaten mit Fe:Ni = 2:1 oder 64:36.

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Rapid solidification of Ti-7.3wt.%Cu (near-eutectoid composition), Ti-36.2wt.%Ni and Ti-34.3wt.% Ni-5.8wt.%Si alloys has been carried out by electron beam melting and splat quenching on a water-cooled rotating copper disc. The product obtained was in the form of thin ribbons 60–100 μm thick. Transmission electron microscopy studies of Ti---Cu alloy splats showed that the microstructure consisted of a mixture of martensite and a lamellar eutectoid product. The formation of the intermetallic compound Ti2Cu involved a diffusionless ω transformation and spinodal clustering. In the case of Ti---Ni alloy the as-quenched microstructure is complex, consisting of α, transformed β and intermetallic phases. This could have arisen possibly as a result of local variation in cooling rates. Rapid solidification of Ti---Ni---Si alloy resulted in partial quenching of an amorphous phase. The amorphous phase was seen to be extremely hard (a Vickers hardness of about 800 HV).

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In this paper we derive an approach for the effective utilization of thermodynamic data in phase-field simulations. While the most widely used methodology for multi-component alloys is following the work by Eiken et al. (2006), wherein, an extrapolative scheme is utilized in conjunction with the TQ interface for deriving the driving force for phase transformation, a corresponding simplistic method based on the formulation of a parabolic free-energy model incorporating all the thermodynamics has been laid out for binary alloys in the work by Folch and Plapp (2005). In the following, we extend this latter approach for multi-component alloys in the framework of the grand-potential formalism. The coupling is applied for the case of the binary eutectic solidification in the Cr-Ni alloy and two-phase solidification in the ternary eutectic alloy (Al-Cr-Ni). A thermodynamic justification entails the basis of the formulation and places it in context of the bigger picture of Integrated Computational Materials Engineering. (C) 2015 Elsevier Ltd. All rights reserved.

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We analyzed the effects of both natural convection and forced flows on solid–liquid interface morphology during upward Bridgman solidification of metallic alloys. Experiments were carried out on Al–3.5wt% Ni alloy, for a cylindrical sample. The influence of natural convection induced by radial thermal gradient on solidified microstructure was first analyzed as a function of the pulling rate. Then, the influence of axial vibration on solidification microstructure was experimentally investigated by varying vibration parameters (frequency and amplitude). Experimental results demonstrated that vibrations could be used to either attenuate fluid flow in the melt and obtain a uniform dendritic pattern or to promote a fragmented dendritic microstructure. However, no marked effect was observed for cellular growth. This pointed out the critical role of the mushy zone in the interaction between fluid flow and solidification microstructure.

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An in situ method was developed to produce an Ni alloy composite coating reinforced by in situ reacted TiC particles with a gradient distribution, using one-step laser cladding with a pre-placed powder mixture on a 5CrMnMo steel substrate. Dispersed and ultra-fine TIC particles were formed in situ in the coating. Most. of the TiC particles, with a marked gradient distribution, were uniformly distributed within interdendritic regions because of the trapping effect of the advancing solid-liquid interface. In addition, the TiC-gamma-Ni interfaces generated in situ were found to be free from any deleterious surface reaction. Finally, the microhardness also showed a gradient variation, with the highest value of 1250 Hv0.2 and the wear properties of the coating were significantly enhanced.

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贮氢合金是镍一金属氢化物电池的核心材料,其综合性能的改善是提高镍一金属氢化物电池性能的关键。本研究以探索镍一金属氢化物电池新型负极材料为目的,以非ABS型贮氢合金为研究对象,采用X射线衍射、Rietveld分析、恒电流充/放电、P-C-T曲线及线性微极化等方法,从基础和潜在应用等方面详细研究了非ABS型合金的结构与电化学性能。对La-Ni体系中非ABS型二元合金的结构和电化学性能的研究表明,LaNi_(228)具有最优异的高倍率充电性能;La_2Ni_7合金电极的高倍率放电性能最佳;La_7Ni_3在低温条件下表现出较好的放电性能。然而,所有得到的La-Ni合金电极容量远低于其理论容量。因此,必须通过进一步研究,如元素取代、热处理、表面处理等来提高其电化学容量。对RENi_3(RE=La,Ce,Pr,Nd,Sm,Gd,Th,Dy,Ho,Er,Y)研究表明:YNi_3合金因其具有最大的晶胞体积,最小的密度,而表现出最好的高倍率充/放电性能及低温放电性能,但其高温放电性能需要进一步提高,以满足实际应用的要求。用Al、Mn、Ti、Fe、Sn、Si、Cr、M。、Cu和Co十种元素取代Ni进行了大量的配方筛选工作。得到了大量的实验数据,并发现LaNi_(3.7)Al_(0.3)合金电极电化学放电容量最高,达290.8mAh/g;LaNi_(3.7)Mo_(0.3)合金电极的高倍率放电性能最好,在以4200mA/g的电流密度下进行放电时,其放电容量仍达到145.8mA/g;而I镍一金属氢化物电池新型负极材料研究镍一金属氢化物电池新型负极材料的研究Al的取代会使合金电极性能对温度不敏感。以我们的实验为基础,进一步进行合金配方的微调,具有可能开发出具有实用价值的贮氢合金的潜力。在Ar保护下用真空电弧炉熔炼合成了四种Lal一xMg:(NICoAI)3.6体系贮氢合金,制成姐卜Ni电池负极,通过恒电流充/放电方法研究了其电化学性能。结果表明:Lal一xMg:(NiCoAI)3.6体系金属氢化物电极较容易活化,室温下具有优异的高倍率放电性能,在以4200mA/g电流放电时,La卜汉gx(NICoAI)36合金电极的放电容量是ABS型合金电极的3倍,达152hah/g,显示出良好的动力学特性。R,入1兮Ni(R:raree田劝,Ca,Y)型合金因能吸引/释放1.8一1.87%质量的HZ而被认为是种很有希望的贮氢合金。但其吸/放氢平台过高,循环寿命短。如何提高Rh厦g剑19循环稳定性是这类合金能否成功商业化的关键。研究发现,Co能够显著提高ABS型合金电极的循环寿命,但其价格太贵。人们发现Al在提高电极寿命方面与C。有类似的作用,但Al元素的添加因其在碱性电解质的作用下在电极表面易生成致密的氧化膜而不利于氢的扩散,进而对高倍率放电性能不利。入物在提高电极表面活性,改善其高倍率放电性方面作用明显。本工作在前面的基础上用Al和MO联合取代Ni,以期待同时改善La一Mg一Ni一Co合金的循环稳定性和高倍率放电性能。详细研究了La07Mg03Ni切一(A105Mo05)x(x:o,0.2,0.4,0.6,0.8)系列贮氢合金的晶体结构和电化学性能。X射线衍射及Rietveld分析发现:所有La07Mg03Ni4D一x(A105Mo05)x合金均为包含PuNi3结构的六方LaZMgNig相、CaCus结构的LaNis主相及L匆Ni7,LaN儿和LaNi杂相的多相结构。合金中La(La,Mg)剑19相及LaNis相的晶格参数及晶胞体积均随合金中Al和Mo含量的增加而增大。用电化学方法测得的RC一T曲线显示:Al和'fo部分取代Ni降低了氢的平台压力。随合金中Al和Mo含量的增加,电极的电化学容量从329.7(x=0)、徽橇毓孺鑫盆一11瀚加至365.物A吨(=0.6)后又降低到351.3毗吨(x=0.8)。当以1200m刀g的电流密度进行放电时,其I{RD从62.0%沁0)增加到82.1%沁0.8)。线性微极化结果显示:Al和Mo的添加增大了合金表面的交换电流密度,因而也改善了合金电极的高倍率放电性能。另外,Al和M。取代合金中的Ni增大了氢在电极合金中的扩散系数(D),改善了La07Mgo3Ni4。一x(Alo5M。。5)x(X=o,0.2,0.4,0.6,0.8)合金电极的低温放电性能(LTD)。

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电感耦合等离子体发射光谱(ICP-AES)已有20多年的历史,经过20年来的发展,ICP-AES已成为世界各地分析化学实验室制备的分析手段之一。目前ICP-AES已经应用于生物样品、地质样品,合金等各种样品的分析中。虽然ICP-AES已成为溶液分析最理想、最有效的方法之一,但由于样品组成的复杂性,也使分析化学工作者面临着许多困难。如在钢铁及合金分析中,样品主成份的分析需准确度要好于1%,精密度≤0.3%,采用ICP-AES法的非内标法通常是达不到要求的。对于一些较纯的水溶液样品,一般可以采用简单的水样标准化,而含有复杂的、可变的基体成份就不适合于基体匹配。为了使冶金样品主成份分析的精度小于0.3%,准确度好于1%,我们将ICP摄谱法广泛应用的内标法应用到光电直读光谱仪中。内标法的作用达到了这一目的。使用内标法,就是要使内标元素能起到在等离子体激发过程中变动的补偿作用同时,还能起到在样品引入过程中,对样品喷雾量和提升率变动的补偿作用以提高分析方法精度和准确度。在初步的试验中,我们考察了28种元素谱线强度随等离子体操作参数变化的情况。(a)谱线强度与正向功率的关系;(b)谱线强度与观察高度的关系;(c)谱线强度与载气流速的关系。这样各元素在等离子体中的行为就因所给定的条件不同而异。根据上述28种元素在等离子体中的行为进行分类,为选择合适的内标元素奠定了基础。我们还对等离子体的正向功率、载气流量、观察高度、酸度等实验条件做了研究。发现,当各操作参数等主要条件改变时,谱线强度往往改变较大,但选择的内标元素谱线亦有类似的变化。因此,在采用内标法后,可以使这种变动得到一定的补偿,从而提高了分析结果的精度。本工作选用的折衷工作条件为:正向功率:1.30KW;载气流量:0.75 l/min; 观察高度:17 mm; 酸度:10% HNO_3(v/v)。研究了单一酸对分析元素谱线强度的影响。结果表明,单一酸的酸度在20%(v/v)以内,对分析元素与内标元素的谱线净强度的比值无影响。在折衷工作条件下,我们用合成水溶液体系研究了共存元素引起的物理干扰对分析元素谱线强度的影响。实验结果表明,随着试液中共存元素(Cu)浓度的增加,粘度明显增加,并导致提升量的急剧降低,谱线强度相应下降。但是当气溶胶导入量发生变化的时候,同时也引起内标元素和分析元素的原子或离子在等离子体中浓度分布的发迹内标元素与分析元素严格一致,可以较正共存元素引起的物理干扰。当共存元素达到一定的浓度时,由于内标元素与分析元素不严格一致,内标法失去作用。我们又考察了内标元素的浓度对分析元素的影响,内标元素的加入量从5~500μg/ml变化。当内标元素的浓度为200μg/ml时,对Mo, Ni, Pb, Ti及Mg略有影响,对其它元素无影响。我们选定内标元素的浓度为10 PPm。在折衷工作条件下,我们绘制了含有Y作内标的一套工作曲线及相应的不含Y的工作曲线,并分析了BMn40-1.5锰白铜样品。结果表明,当含量大于0.3%时,测定精度均低于0.3%,并得出以下结论:(1)各种元素在等离子体中的行为依测定条件而异,因此内标元素的选择最好是从在等离子体中行为相似的一组内选择。(2)在光电直流光谱仪中动用内标法可以提高样品中主成份元素的精度和准确度。(3)内标法在SBR较高的情况下可以起到较好的效果,但当SBR较小时,内标法就会失去作用。样品分解是样品分析的关键步骤。在现有的分解方法中,常用的有干灰化法和湿灰化法等。然而这些方法各有其缺点。因此,我们试图寻找一种快速的湿法消解技术,微波炉快速样品溶解似乎很具有吸引力。我们利用国产微波炉和全聚器氟乙烯密封溶器结合,系统地考查了微波炉溶解茶叶及茶树叶,利用ICP-AES测定的可行性,并与湿式消解法,加压密封法等进行了比较,获得满意结果。首先,我们选择了微波炉消化处理的最佳条件,确定了最佳溶解方案,已证明HNO_3-HF(5:1)混合酸溶解样品是令人满意的。又研究了微波炉加热对分析无素挥发性的影响。结果表明,微波炉加热与不经微波炉加热样品的浓度没有明显差异。按上述确定的工作条件,我们分析茶叶及茶树叶样品,并与不同的处理方法进行了比较。采用干灰化法处理茶叶(茶树叶)至少需8小时,而且还极易损失和沾污,但干灰化法用的酸量较少,空白较低,对Cr等的测定有利。湿法消解由于使用HClO_4-HF混酸,B大部分损失或完全挥发挥失。然而采用微波炉完全溶解样品只需19分钟即可,而且由于未使用HClO_4,样品溶液最后只需蒸至近干,有效地防止了易挥发元素的损失及某些不溶性高氯酸盐的生成。微波炉混合酸消酸系统是一种合适的溶解各种各样样品的技术,它为分解各种各样样品以进行多元素测定提供了一种快速、准确、经济的方法。该方法对于通常在敞口溶器中分解易于损失的挥发性元素特别有用,而且还特别适用于样品个数多,量少的生物样品等的微量元素的分析测定。

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在本工作中,制备了一系列催化剂样品,其中有K、Ni、Mo单组份催化剂,K-Ni、K-Mo、Ni-Mo双组份催化剂及不同活性组份含量的K-Ni-Mo三组份催化剂。针对水煤气变换反应,对上述催化剂进行反应活性考察,得出如下结果:①催化剂各活性组份的最佳含量大致是NiO(3%), MoO_3(13%), K_2CO_3(6%);②催化剂制备中的最佳焙烧温度在400 ℃左右;③催化剂使用前用H_2S/H_2的混和气进行预处理其效果最佳;④催化剂的催化活性与催化剂表面硫的含量有关,当催化剂表面处于严重缺硫状态时其活性下降;⑤反应的最佳汽:气 = 0.5-1.5;⑥加压有利于催化剂活性的提高,在加压情况下催化剂的活性随着反应温度的增加通过一极大值(在约200 ℃左右),不加压的反应催化剂活性随着反应温度的提高而增加。在催化剂的表征部分,利用XPS、XRD、紫外可见温反射光谱、SEM、ESR、比表面、TPR、酸度测定、TPD、TPS、TPS-TPR等实验对我们所制备的催化剂进行了研究。最后,我们用ESR和XRD实验技术研究了MoO_3、M_2CO_3 (M = Li、Na、K、Cs)-MoO_3加热过程中的固相反应,知道MoO_3在空气中焙烧时可以失去晶格氧,使晶体中的一些Mo~(6+)变成Mo~(5+)。在焙烧过程中,Li、Cs~+的加入将阻止MoO_3晶格氧向气相氧的转变,对Mo~(5+)的生成有抑制作用。加入一定量Na~+、K~+的MoO_3在焙烧过程中,其晶格氧被活化更易失去它们对Mo~(5+)的生成有促进作用,这种作用的大小是Na~+ > K~+。