Identification of Driver Model Parameters

The paper presents a driver model, which can be used in a computer simulation of a curved ride of a car. The identification of the driver parameters consisted in a comparison of the results of computer calculations obtained for the driver-vehicle-environment model with different driver data sets with test results of the double lane-change manoeuvre (Standard No. ISO/TR 3888:1975, International Organization for Standardization [ISO], 1975) and the wind gust manoeuvre. The optimisation method allows to choose for each real driver a set of driver model parameters for which the differences between test and calculation results are smallest. The presented driver model can be used in investigating the driver-vehicle control system, which allows to adapt the car construction to the psychophysical characteristics of a driver.     

Protection Against Dust by Respirators

This article is a brief review of the mechanism of action of fibrous filters and of the performance of respirators; it neglects many of the complications discussed in longer and more detailed articles. An expression is given for the pressure drop across a filter in terms of fibre diameter and filtration velocity. The particle capture mechanisms of interception and diffusional deposition are introduced and the way in which filtration efficiency varies with particle size is discussed. Filters with fibres of small diameter are shown to be the most efficient, but their use can cause problems. Electrically charged materials are widely used in respirators because of their high efficiency and low pressure drop. Types of material, their means of charging, and their method of action are described. An account is given of respirator leakage, the protection factor, and of the way that these may vary in a period of use. The leakage of air and particles through face seal leaks and leaky valves is discussed. The frequent discrepancy in the protection given by respirators in the workplace, on the one hand, and that suggested by laboratory measurements, on the other, is reviewed, and the article ends with an account of the combined effect of aerosol penetration through a filter and through a leak.     

1种抑制巷道信号NLOS的矿井RSSI高精度定位算法*

在RSSI（Received Signal Strength Indication）测距定位技术中,为抑制巷道信号NLOS（Non Line of Sight）传输对定位结果的影响,提出信号指纹定位和几何优化算法。在离线阶段利用高斯滤波最大值加权法和最小二乘法建立符合矿井巷道环境的无线信号测距模型,设计改进卡尔曼滤波器平滑处理离线信号值,抑制巷道信号NLOS传输带来的影响,建立离线信号指纹库;在线定位阶段,利用加权K最近邻法（WKNN）将定位目标接收到的信号值与指纹库中的信号值进行匹配,将匹配到的最优信号值参与测距定位计算,最后通过几何优化算法将定位结果归一化处理,使其符合一维定位分布。结果表明:所提算法的平均定位误差为0.9 m,相比于高斯滤波最大值加权法、经典卡尔曼滤波指纹定位算法和改进卡尔曼滤波指纹定位方法,其平均误差分别减小2.36,1.17,0.35 m。所提算法能够有效抑制巷道信号NLOS传输对RSSI测距定位的影响,可实现RSSI方法在矿井NLOS环境中的有效应用。     

方解石活性覆盖系统抑制底泥磷释放的影响因素研究

通过摇床振荡试验和底泥磷释放控制模拟试验,考察了覆盖系统厚度、上覆水Ca2 浓度、温度、方解石粒径以及人工曝气等对方解石活性覆盖系统抑制底泥磷释放效率的影响.结果表明,方解石覆盖系统可以抑制厌氧状态下底泥磷的释放,且抑制效果受覆盖系统厚度、上覆水Ca2 浓度、温度、方解石粒径及人工曝气等的影响.方解石覆盖系统对底泥磷释放的抑制效率随厚度的增加而明显提高,方解石投加量由12.7 kg/m2增加到38.2 kg/m2,模拟期间覆盖系统对底泥磷释放的抑制率则由56%增加到99%;上覆水的Ca2 会增强方解石覆盖系统对底泥磷释放抑制的效率,上覆水Ca2 浓度由1 mmol/L增加到5mmol/L,模拟期间上覆水的磷浓度下降36%左右;对于方解石投加量较少的情况下,高温条件与低温条件相比,底泥向上覆水释放更多的磷,而通过增加覆盖系统的厚度可以消除高温所带来的不利影响;方解石覆盖系统对底泥磷释放的抑制效率随粒径的减小而明显增强;对方解石覆盖系统表面进行人工曝气,不仅可以降低底泥氨氮的释放速率,而且还可以降低底泥磷的释放速率.     

滤床熟化周期及其主要影响因素的研究

阐述滤床熟化的概念及其形成机理,对影响熟化床层的因素进行了试验研究,结果表明进水浊度、混凝效果及洗砂量是影响熟化床层的主要因素。由于集成型给水处理设备的表面滤层一直处于熟化状态,而滤层水流方向的深处滤料始终处于清洁状态,砂滤器内始终保持一种动态的平衡关系,滤床运行在熟化后的有效过滤期,因而能够保证较高的出水水质。     

袋式除尘器节能降耗途径的探讨

阐述袋式除尘器的阻力组成,从除尘器结构,过滤速度及清灰制度三个方面分析了降低阻力的途径。     

主动脉动气流分选处理废弃催化剂

废弃催化剂重整后含有富集贵金属的海绵体和烧结磁珠,二者的有效分选是提纯贵金属富集体的重要环节。主动脉动气流分选装置能够对此物料进行干法分选,避免了湿法分选对物料的改性,有利于贵金属富集体的后续提纯。介绍了主动脉动气流分选装置的结构,分析主动脉动气流分选机理及其动力学模型。通过实际物料进行分选试验。结果表明,在脉动频率为7/3 Hz,气流流速为2.50~6.00 m/s时,总分选效率Ef高于94.50%;在气流流速为3.33 m/s时,分选效率最高,总分选效率Ef可达97.63%。     

曝气生物滤池在炼油废水处理中的应用

介绍了曝气生物滤池的工艺原理和主要特点,以及在炼油厂废水处理中的应用,分析了曝气生物滤池的主要影响因素温度、pH值和碱度、水力负荷、溶解氧等。曝气生物滤池在废水处理中有较好的应用前景。     

防空干道地下水作为化工工艺用水工程改造实例

防空干道地下水质YD390-400mg／l,TDS750 mg,／l,经强化纤维过滤-OR低压反渗透装置处理后水质达到钛白粉生产工艺用水标准。YD〈200mg/l,TDS〈450mg/l。工艺条件：处理量7000M^3／d,净水荆加入量1501／h,反渗透设计压力2．5Mpa,工作压力1．3Mpa,工作温度10℃-30℃,采用芳香族聚酰胺反渗透膜,设计压力4．0Mpa,工作压力1．5Mpa,工作温度10℃-40℃。同时,该处理系统占地面积小,工艺成熟,简洁、高效,在确保出水达标的同时降低了运行成本。在强化纤维过滤中采用GM多功能净水剂,具有絮凝快,分离速度快,分界清楚,浊度去除高。反渗透工序分离过程不需加热,没有相的变化,具有耗能较少,设备体积小、操作简单、适应性强,应用广泛。