Au/Cu/FLA催化剂在不同气氛中CO低温氧化性能研究

采用等体积浸渍法制备系列Au/Cu/FLA催化剂,考察了催化剂在干、湿气氛及高浓度CO_2气氛下对CO低温氧化的催化能力,并采用N_2物理吸脱附、透射电子显微镜、 X射线粉末衍射、红外光谱等表征手段对催化剂进行表征.实验结果表明:Au/Cu/FLA系列催化剂都具有较好的初始活性;与干气氛相比,湿气氛下催化剂的稳定性较好;表征结果初步判断引起本系列催化剂失活的可能的主要因素是碳酸盐产生覆盖活性位点与催化剂表面-OH丢失共同作用的结果.     

Effects of sintering atmospheres on sintering behavior, electrical conductivity and oxygen permeability of mixed-conducting membranes

Effects of sintering atmospheres on properties of SrCo_0.4Fe_0.5Zr_0.1O_3−δ mixed-conducting membranes were in detail studied in terms of sintering behavior, electrical conductivity and oxygen permeability. The sintering atmospheres were 100% N₂, 79% N₂–21% O₂, 60% N₂–40% O₂, 40% N₂–60% O₂, 20% N₂–80% O₂ and 100% O₂ (in vol.%), and the prepared membranes were correspondingly denoted as S-0, S-21, S-40, S-60, S-80 and S-100, respectively. It was found that the properties of membranes were strongly dependent on the sintering atmosphere. As the oxygen partial pressure in the sintering atmosphere (P_O2) increased, sintering ability, electrical conductivity and oxygen permeability decreased at first, which was in the order of S-0 > S-21 > S-40. However, as P_O2 increased further, sintering ability, electrical conductivity and oxygen permeability increased gradually: S-40 < S-60 < S-80 < S-100. And the S-100 membrane had the best sintering ability, electrical conductivity and oxygen permeability in all membranes.     

Studies on the structure and catalytic performance of Cu-Zn-Al catalyst prepared by liquid-phase preparation technology under different heat treatment atmosphere

Cu-Zn-Al slurry catalysts were prepared using a complete liquid-phase preparation technology under different heat treatment atmospheres. The catalysts were characterized using X-ray diffraction, X-ray photoelectron spectroscope, and N2 adsorption-desorption. Their application in the single-step synthesis of dimethyl ether from syngas was also investigated. The results indicate that the type of heat treatment atmosphere has an influence on the Cu species and the Cu⁰/Cu⁺ ratio on the catalyst surface. Moreover, the final Cu/Zn ratio on the catalyst surface is mainly dependent on the composition and reaction environment of the catalyst and little on the type of heat treatment atmosphere. The prepared catalysts can suppress sintering of active sites at high temperatures, and the type of heat treatment atmosphere mainly affects the capability of the catalyst for methanol synthesis. The catalysts perform best using N2 as the heat treatment atmosphere.     

环境气氛作用下煤灰在刚玉质耐火板上的表面结渣行为

采用了扫描电镜、能谱分析仪、X射线衍射等方法对不同环境气氛下熔融煤灰在刚玉耐火板上煅烧渣样进行了测试,并就渣样的形貌、成分分布及与刚玉质耐火板之间的高温烧结特性进行了分析研究。研究结果表明,氧化性气氛下,碱性氧化物促进了煤灰在刚玉耐火板上的黏结作用,特别是Al含量较高的耐火板更有利于促进其发生共晶反应。还原性条件下,煤灰中生成的FeO具有很强的助熔效果,促使矿物之间产生低熔点的共熔物,同时Fe、Cr、Ti的扩散偏析减弱,加强了熔融煤灰对耐火板的黏结作用。     

Coal pyrolysis in a fluidized bed reactor simulating the process conditions of coal topping in CFB boiler

Simulating the conditions of pyrolytic topping in a fluidized bed reactor integrated into a CFB boiler, the study was devoted to the reaction fundamentals of coal pyrolysis in terms of the production characteristics of pyrolysis oil in fluidized bed reactors, including pyrolysis oil yield, required reaction time and the chemical species presented in the pyrolysis oil. The results demonstrated that the maximal pyrolysis oil yield occurred on conditions of 873 K, with a reaction time of 3 min and in a reaction atmosphere gas simulating the composition of pyrolysis gas. Adding H₂ and CO₂ into the reaction atmosphere decreased the pyrolysis oil yield, while the oil yield increased with increasing the CO and CH₄ contents in the atmosphere. TG-FTIR analysis was conducted to reveal the effects of reaction atmosphere on the chemical species present in the pyrolysis oil. The results clarified that the pyrolysis oil yield reached its maximum when the simulated pyrolysis gas was the reaction atmosphere, but there were slightly fewer volatile matters in the pyrolysis oil than the oil generated in the N₂ atmosphere. All of these results are expected not only to reveal the composition characteristics of the pyrolysis oil from different conditions of the coal topping process but also to optimize the pyrolysis conditions in terms of maximizing the light pyrolysis oil yield and quality.     

Emulsification in turbulent flow: 3. Daughter drop-size distribution

Systematic set of experiments is performed to clarify the effects of several factors on the size distribution of the daughter drops, which are formed as a result of drop breakage during emulsification in turbulent flow. The effects of oil viscosity, etaD, interfacial tension, sigma, and rate of energy dissipation in the turbulent flow, epsilon, are studied. As starting oil-water premixes we use emulsions containing monodisperse oil drops, which have been generated by membrane emulsification. By passing these premixes through a narrow-gap homogenizer, working in turbulent regime of emulsification, we monitor the changes in the drop-size distribution with the emulsification time. The experimental data are analyzed by using a new numerical procedure, which is based on the assumption (supported by the experimental data) that the probability for formation of daughter drops with diameter smaller than the maximum diameter of the stable drops, d相似文献   

Ordered porous films based on fluorinated polyimide derived from 2,2′-bis(3,4-dicarboxyphenyl) hexafluoropropane dianhydride and 3,3′-dimethyl-4,4′-diaminodiphenylmethane

One of fluorinated polyimides was synthesized from 2,2′-bis(3,4-dicarboxyphenyl) hexafluoropropane dianhydride (6FDA) and 3,3′-dimethyl-4,4′-diaminodiphenylmethane (DMMDA) by two-steps method, which had good solubility and hydrophilicity. 6FDA-DMMDA polyimide was dissolved in chloroform (CHCl₃) and cast on a glass substrate in a humid atmosphere. It was found that 6FDA-DMMDA/CHCl₃ solution was easy to form ordered porous structure at high concentration, and the reason was discussed in detail. In addition, the influences of solution concentration, the atmosphere humidity, were also tested.     

在线加压溶剂微提取-湍流色谱-高效液相色谱法同时测定管花肉苁蓉中3种苯乙醇苷

建立了在线加压溶剂微提取-湍流色谱-高效液相色谱(online PLME-TFC-HPLC)法,并将其应用于管花肉苁蓉中松果菊苷、毛蕊花糖苷和异毛蕊花糖苷3种苯乙醇苷类成分含量的同时测定。微量样品粉末(0.5 mg)置于空预柱芯中并用正相硅胶填充,得到提取池后装入预柱套(Security Guard^TM)。将预柱套置于70℃柱温箱中,将一根长聚醚醚酮(PEEK)管线(1000 mm×0.13 mm)连于预柱套末端,采用0.1%(v/v)甲酸水为提取溶剂,以2.5 mL/min的速度流经PEEK管线,产生高压,实现管花肉苁蓉的在线加压溶剂微提取,通过TurboFlow cyclone色谱柱在线净化和富集。引入两个电子六通阀,将整个分析过程分为提取阶段和洗脱阶段,并在洗脱阶段将TurboFlow cyclone色谱柱中的分析物反冲至Capcell PAK C₁₈ AQ分析柱上,以0.1%(v/v)甲酸水-乙腈为流动相进行梯度洗脱,以340 nm为检测波长同时定量分析松果菊苷、毛蕊花糖苷和异毛蕊花糖苷3种苯乙醇苷类成分。结果表明,3种苯乙醇苷类在1~200 mg/L范围内线性良好,相关系数r均大于0.999,定量限分别为0.50 mg/L(松果菊苷)、0.25 mg/L(毛蕊花糖苷)和0.38 mg/L(异毛蕊花糖苷),加标回收率为83.13%~114.00%,相对标准偏差为1.89%~13.34%。该方法简便、快速、可靠,不仅节约了药材和溶剂的使用量,而且极大地简化了前处理方法,省时省力,同时显著降低了化学成分在提取过程中降解的几率,适用于管花肉苁蓉中苯乙醇苷类化合物的含量测定。     

钛硅分子筛TS-1合成晶化气氛的影响

考察了不同晶化气氛(N2、H2、A ir、O2)对合成钛硅分子筛TS-1的影响,用XRD、IR和N2吸附/脱附对所合成的钛硅分子筛进行结构表征,发现在H2气氛下合成的TS-1结晶度最高,锐钛矿的含量最少;O2气氛下合成的TS-1中锐钛矿含量最高.以氯丙烯氧化为模型反应,考察了不同晶化气氛下合成的钛硅分子筛的催化活性和双氧水的利用效率.结果表明,在H2气氛下所合成的钛硅分子筛的双氧水的利用效率最高.     

Analysis of t-Butyldimethylsilyl Derivatives of Chlorophenols in the Atmosphere of Urban and Rural Areas in East of France

A method using GC-MS and derivatization with N-(t-butyldimethylsilyl)-N-ethyltrifluoroacetamide (MTBSTFA) was developed for the analysis of 19 chlorophenols compounds in atmospheric samples (gas and particles). Air sampling was carried out using a Hi-Vol sampler with glass fibre filter and XAD-2 resin at a flow rate of 60 m³ h⁻¹. The particle and gas phases were collected separately over a period of 4 h. Samples were Soxhlet extracted, evaporated to dryness under nitrogen and refilled with acetonitrile. 100 mL of these extracts were derivatized with 100 μL of MTBSTFA at 80 °C for 1 h under strong stirring. Sylylated chlorophenols were injected into a GC-MS in splitless mode and quantified as their TBDMS derivatives in the SIM mode. Mass spectral analysis of the derivatives of the 19 compounds studied indicates that the spectra are highly specific showing an ion at [M - 57]⁺ which is useful for structure confirmation or analysis at low levels using selected ion monitoring. Quantification limits varied between 5 μg L⁻¹ and 10 μg L⁻¹ which correspond to 20 pg m⁻³ and 40 pg m⁻³ for 250 m³ of air sampled. This method was successfully applied to atmospheric samples collected simultaneously in winter 2004 in an urban (Strasbourg) and rural (Erstein) areas in east of France.