APCI5000电气自动化成套装置设计

电气自动化成套装置种类繁多，并广泛应用于电力系统．结合现场实际商业运行期所积累的经验，并根据市场预测以及目前工控机发展动态，提出了采用APCI5000工业控制计算机实现电气自动化成套装置设计的最佳方案．     

The Development of Materials for the Production of Hydrogen from Bio-ethanol

1 Results There is an increased interest in the hydrogen production from renewable sources. In this context, recently, numerous studies which use ethanol for hydrogen production have appeared. Ethanol is easily handled, non-toxic, and it can be obtained from biomass. The steam-reforming of bioethanol has been shown to beeffective for hydrogen production:C2H5OH 3 H2O  6 H2 2 CO2. Six moles of hydrogen can be yielded for each mole of ethanol reacted. However, depending on the catalyst used, other und...     

大洋多金属结核中五氧化二磷分析方法

试样经ＮａＯＨ溶融,水浸取后,使Ｆｅ、Ｍｎ、Ｃｕ、Ｃｏ、Ｎｉ等共存元素形成氢氧化物沉淀与磷分离,滤液中的磷用磷钼黄光度法测定。方法简便、快速、精密度好、准确度高。经对标准物质ＧＢＷ０７２４９测定,结果与推荐值吻合,ＲＳＤ（ｎ＝１０）〈１．４％。     

前驱体溶液pH值对溶胶凝胶制备钛酸铋薄膜的影响

采用溶胶凝胶技术在石英玻璃基片上制备钛酸铋薄膜,讨论了前驱体溶液的酸碱度（ｐＨ值）对薄膜结构和结晶性的影响．ｐＨ＜２和ｐＨ＞３５的前驱体溶液所制备的薄膜在晶化过程中出现Ｂｉ２Ｔｉ２Ｏ７和Ｂｉ２Ｔｉ４Ｏ１１杂相．ｐＨ＝２５～３５的前驱体溶液制备的薄膜是钙钛矿Ｂｉ４Ｔｉ３Ｏ１２结构的取向薄膜     

Bi4Ti3O12铁电薄膜溶胶—凝胶法制备过程中Bi—Ti溶胶的匀胶规律研究

介绍了Ｓｏｌｇｅｌ法制备Ｂｉ４Ｔｉ３Ｏ１２薄膜的工艺过程,研究了ＢｉＴｉ溶胶在Ｓｉ基片上的匀胶规律;用ＴＧＤＴＡ和ＴＥＭ技术研究了ＢｉＴｉ干凝胶的形态,并成功地在Ｐｔ／Ｔｉ／Ｓｉ基片上制备了ｃ轴取向的Ｂｉ４Ｔｉ３Ｏ１２薄膜．     

大肠杆菌O157:H7基因组研究进展

对大肠杆菌O157：H7基因组的结构、特点等近年来的研究进展进行了综述。     

纳米Fe3O4/BaTiO3复合体系的微波吸收特性

研究了纳米Fe3O4和BaTiO4及其复合体系在2～18GHz频率范围内的微波吸收性能，并分析了其吸收机制以及复合组分对吸波性能的影响。研究结果表明，通过调节材料组分可调节电磁参数及吸收峰的位置，复合体系的有效吸收频带较单一材料的吸附频带变宽。单一组分的纳米Fe3O4和PaTiO3都有2个吸收峰。在复合体系中，多个吸收峰发生重叠。这2种材料的微波吸收能力随电磁波频率的变化而规律不同，当频率低于14GHz时，PaTiO3的吸收能力大于Fe3O4的吸收能力；当频率高于14GHz时，Fe3O4的吸收能力大于BaTiO3的吸收能力。因此，将这2种材料复合，产生协同效应，材料的整体吸收能办提高，有效吸收频带拓宽。当样品的厚度为2mm，Fe3O4与BaTiO3的质量比为3：2时，反射率为10dB的有效频宽可达2．7GHz；当Fe3O4与BaTiO3的质量比为2：3时，反射率为10dB的有效频宽可达4GHz。     

纳米催化剂KF/Al2O3制备条件的正交设计与优化

采用正交设计法优化了浸渍法制备固体超强碱KF/Al2O3催化剂工艺参数.以丙烯腈和丙二酸二乙酯的Michael加成反应收率为考察指标,对催化剂制备工艺进行优化,并采用SPSS统计软件包对制备工艺参数进行多元回归统计,并根据回归拟合的多项式数学模型,讨论了浸渍法制备的较佳工艺.     

SO42-/ZrO2系列固体超强酸的制备与应用

本文对采用不同方法制备了两种SO4^2-/ZrO2系列的SO4^2-/ZrO2-TiO2和SO4^2-/ZrO2-Al2O3固体超强酸催化剂，并以顺丁烯二酸酐和正丁醇的酯化反应为探针反应，考察了Zr：A1，Zr：Ti的原于配比，焙烧温度，焙烧时间以及浸渍液硫酸的浓度对催化剂活性的影响。     

Review on aggregation of acid extractants in solvent extraction of metal ions: remark on the general model

The aggregation behavior of various acid extractants in the solvent extraction systems of metal ions is re-examined and explained according to knowledge obtained in recent work. The conclusions are as follows. (1) Complexes formed by the extractants and metal ions can form reversed micelles in organic diluents, depending on the microstructures of the complexes. The dimers of the acid extractant cannot percolate to the metal-extractant aggregates, and the acid-salt complexes are always formed in the aggregates. The reversed micelles or the W/O microemulsions formed by different species cannot be associated with each other to form a unified aggregate. (2) In solvent extraction systems, hydration of the extractants and metal ions can be considered as the driving force of forming reversed micelles. (3) Information of the first approach to the insight of the bicontinuous microemulsion of NaDEHP shows that various components in the aqueous phase behave confined and very similar to the typical AOT/n-heptane W/O microemulsions. (4) In the extraction of lanthanide ions by the W/O microemulsion of sodium naphthenate, the saponification is a process of forming reversed micelle or W/O microemulsion, while the extraction step is a process of destroying reversed micelles or W/O microemulsion droplets.