第1章数据库原理及基本概念 1.填空题 (1)数据及数据之间的联系 (2) DBMS (3)数据库 (4)记录 (5)概念设计、逻辑设计 2.选择题 (1)A(2)A、C、D(3)A

介绍了杨炳儒教授独立提出的知识发现系统内在机理中的3个机制——双库协同机制、双基融合机制、信息扩张机制,及在其上构建的KDD*,KDK*,KD(D&K),ESKD结构模型,并介绍了在知识表示方法、发现算法与自动评价方法等方面的创新性成果

研究了钛酸锶（SrTiO3a）固化体浸出性能的影响因素.采用MCC-1浸出法,分析了钛酸锶的浸出率.实验结果表明：SrTiO3a中各种元素的浸出率随时间延长而减小,且都小于0.1g·m-2·d-1,比玻璃固化体浸出率要低2～3个数量级;钛酸锶的化学稳定性好,是比较好的高放废物固化体

For general applications in 3D, often need to perform 3 separate rotations to relate our inertial frame to our body frame Especially true for aircraft problems There are many ways to do this set of rotations -with the variations be based on the order of the rotations All would be acceptable

矿山采场路面喷洒YCH抑尘剂后,逐日测定了路面粉尘含湿量、路面粉尘粒径分布、汽车行驶后瞬时扬尘浓度.路面喷洒抑尘剂10d后,瞬时扬尘浓度仅为4.9mg·m-3,降尘效率可达98.4%.与矿山路面每天喷洒4次水相比,路面喷洒YCH抑尘剂时节水率98%,降尘成本降低31%

介绍了利用光谱仪分析钢中夹杂物技术的原理.通过对光谱仪原始脉冲强度的研究,建立了Al2O3光谱强度与化学分析含量的工作曲线,确定了光谱强度与夹杂物粒径的关系,实现了Al2O3含量和粒径分布的快速分析.与化学分析相比,分析误差平均为3×10-6,夹杂物含量和粒径的分析时间由2~5d缩短到5min,为炼钢及精炼过程夹杂物控制提供了有效技术手段

3.1 Voltage and Current Laws Kirchhoff's Current Law. Kirchhoff's Current Law in the Complex Domain.Kirchhoff's Voltage Law. Kirchhoff's Voltage Law in the Complex Domain. Importance of KVL and KCI Michael D. Ciletti 3.2 Node and Mesh Analysis University of Colorado Node Analysis. Mesh Analysis. Summary 3.3 Network Theorems J. David Irwin

Eugene F Fama. James D. Mac Beth The Journal of political Economy, Volume 81, Issue 3(May -Jun, 1973),607-636 Stable url: http://links.jstor.org/sici?sici=0022-3808%28197305%2f197306%2981%03a3%03c607%3arraeett3e2.0.c0%03b2-c Your use of the JSTOR archive indicates your acceptance of jSTOR's Terms and Conditions of Use, available at http://www.jstor.org/about/terms.htmlJstOr'sTermsandConditionsofUseprovidesinpartthatunlessyou

Images removed due to copyright considerations See Fig. 2 in David J. Katzmann, Greg Odorizzi Scott D. Emr RECEPTOR DOWNREGULATION AND MULTIVESICULAR-BODY SORTING Nature Reviews Molecular Cell Biology 3, 893-905(2002); doi: 10.1038/nrm973 See Fig. 7 in: Katzmann DJ, Stefan CJ, Babst M, Emr SD

确定局部损失系数的实验方法 例用U形压差计测量水平放置弯管的局部损 失系数。已知d=0.25m,Q=0.04m3/s,U 形管工作液体的密度P=1600kg/m3。如果 测得△h=70mm,试计算5 解忽略沿程损失,对1和2断面列出伯努利方程