部分信息下的最优投资选择模型研究

在部分信息下研究了均值方差投资选择模型.投资者只能观察到风险资产的价格,漂移过程用一个高斯过程来刻画.本文的目的是使最终财富期望最大化,而使得最终财富的方差最小.本文模型中有一个债券及股票资产,在部分信息下推导出了最优策略及均值方差有效前沿.     

混合装配线过程平衡研究与仿真

生产过程的混合装配线平衡问题,分为在确定条件下的最小生产循环单元的静态平衡问题和不确定条件修正过后的动平衡问题.针对确定工位条件下的混装生产线,构建其静态平衡模型,分析不确定因素,并以操作工人的操作时间不确定性为例,研究时间不确定性动态平衡.利用Flexsim软件,通过仿真进行了验证.相关实验验证了上述方法和结论的正确性.     

动态批次主元分析在化工过程中的应用研究

本文研究了批次动态主元分析(BDPCA)及其在化工过程中的应用.批次动态主元分析是主元分析的一种延伸,通过把三维矩阵转化成二维矩阵,结合时滞变量算法捕捉批次过程中的动态特性完成过程的监视并给出了确定时滞变量的算法.以TE过程为例,与多向主元分析法相比,仿真结果表明,BDPCA算法实现了考虑过程中的批次动态特性并提高了对过程变化的故障检测能力.     

Fault-Diagnosis Method Based on Support Vector Machine and Artificial Immune for Batch Process

A new fault-diagnosis method to be used in batch processes based on multi-phase regression is presented to overcome the difficulty arising in the processes due to non-uniform sample data in each phase. Support vector machine is first used for phase identification, and for each phase, improved artificial immune network is developed to analyze and recognize fault patterns. A new cell elimination role is proposed to enhance the incremental clustering capability of the immune network. The proposed method has been applied to glutamic acid fermentation, comparison results have indicated that the proposed approach can better classify fault samples and yield higher diagnosis precision.     

Characteristics of oxygen consumption of coal at programmed temperatures

Oxygen consumption is an important index of coal oxidation.In order to explore the coal-oxygen reaction,we developed an experimental system of coal spontaneous combustion and tested oxygen consumption of differently ranked coals at programmed temperatures.The size of coal samples ranged from 0.18~0.42 mm and the system heat-rate was 0.8℃/min.The results show that,for high ranked coals,oxygen consumption rises with coal temperature as a piecewise non-linear process.The critical coal temperature is about 50%.Below this temperature,oxygen consumption decreases with rising coal temperatures and reached a minimum at 50℃,approximately.Subsequently,it begins to increase and the rate of growth clearly increased with temperature.For low ranked coals,this characteristic is inconspicuous or even non-existent.The difference in oxygen consumption at the same temperatures varies for differently ranked coals.The results show the difference in oxygen consumption of the coals tested in our study reached 78.6% at 100 ℃.Based on the theory of coal-oxygen reaction,these phenomena were analyzed from the point of view of physical and chemical characteristics,as well as the appearance of the coal-oxygen complex.From theoretical analyses and our experiments,we conclude that the oxygen consumption at programmed temperatures reflects the oxidation ability of coals perfectly.     

1-氯甲基杂氮硅三环的合成

以甲基三氯硅烷为原料,采用氯化、醇解和酯交换等反应,合成了1-氯甲基杂氮硅三环,并通过单因素实验方法对合成工艺条件进行了优化。在最佳条件下,1-氯甲基杂氮硅三环的总产率可达到54.5%,与文献报道的比较,具有产率高、能耗低等优点。并对反应过程中的副产物氯化氢气体进行了回收,减少了环境污染。     

3D Modeling of the preparation process of metal rubber material

Based on the analysis of the preparation of metal rubber (MR) and two pivotal hypotheses,the uniform distribution and the unaltered topological structure of wires in the radial direction of columns in the punch process,a 3D parametrical model was established based on four approaches:helix-making,planar roughcast-weaving,planar roughcast-rolling,and 3D roughcast punching.In the modeling process,5 lattice types of weave patterns in planar roughcast were put forward,and 10 quantificational modeling parameters ...     

Treatment of methanol wastewater with two-stage and two-phase anaerobic process

The two-stage and two-phase anaerobic process (TSTP) composed of hydrolytic acidification reactor,first-order and second-order external circulation anaerobic reactors (EC) was taken to treat methanol wastewater. Test results show that TSTP process is quick start-up in 51 d, and the maximum VFA of hydrolytic acidification reactor effluent reaches 876 mg/L. Under the condition of volume loading of 6.56 kgCOD/m3·d, COD removal rate of the first-order EC reactor is about 85%, and under the condition of volume loading of 1.02 kgCOD/m3·d, COD removal rate of the second-order EC reactor is about 50%. When the inflow COD of TSTP process is between 7000-11000 mg/L, its effluent COD is lower than 600 mg/L. In the biological conversion process of methanol into methane,the production of acetic acids as an intermediate product can be ignored and the direct production of methane from methanol is predominant.     

基于工作过程的《异步电动机运行与维护》课程改革与实践

本文按照基于工作过程的系统化课程开发方法,对《异步电动机运行与维护》课程进行了教学设计。文中系统提出了该课程的构建方法、学习情境、学习内容、实施方案和考评方法等,简要分析了改革试点实践的初步成效与不足。     

充水比对UniFed SBR 工艺脱氮的影响

为了考察充水比对新型UniFed SBR工艺脱氮的影响,试验采用充水比分别为25%和42%的2个并行的UniFed SBR反应器,并以实际生活污水为处理对象,通过比较在6组相同的进水ρ(C)/ρ(N)比,TN在2个充水比条件下1个完整周期中的降解规律及出水TN质量浓度,分析了充水比对进水/排水阶段和曝气阶段TN去除的影响.试验结果表明,UniFed SBR工艺在任意一个充水比下运行时,都存在一个与之相对应的进水/排水阶段最大脱氮率η_(1max),η_(1max)只与充水比有关,而与进水ρ(C)/ρ(N)比无关,且在进水碳源充足时,充水比越大,η_(1max)越低;在相同进水ρ(C)/ρ(N)比时,充水比越大,曝气阶段由SND产生的脱氮率η_2越高.由于进水/排水阶段对UniFed SBR工艺TN的去除贡献更大,因此采用较小的充水比,更有利于工艺整体对TN的去除.