基于交换机技术的网络安全策略研究

本文对交换机及其作用进行了简单的概述,并对基于交换机技术的网络安全策略进行了详细的分析和探究,以期为保障网络的安全流畅运行提供借鉴意义.     

有机硅改性无皂丙烯酸酯类水分散体的合成技术及其产业化实践

介绍了以特殊结构的纳米无机体材料为骨架,采用无皂工艺合成的以有机硅材料进行改性的具有LIPN结构的丙烯酸酯类水分散体的性能及其产业化实践的情况,并对以该水分散体开发的水性木器涂料的性能作了对比说明。实践表明,以该丙烯酸水分散体开发的水性木器涂料较好地解决了目前水性木器涂料在硬度、光泽度、丰满度、回粘温度等方面不如溶剂型涂料的弱点,且该分散体的合成工艺独特、成本低廉,利于产业化和下游厂家开发使用。     

科技创新与钢铁科技进步

建设创新型国家是我们中华民族的历史责任。“自主创新、重点突破、支撑发展、引领未来”的16字方针应当成为我们未来创新活动的指南。建设创新型国家把自主创新放在首位,并提出了引领未来的高标准要求。钢铁科技创新必须突出重点,抓住创新成果产业化这个关键,支撑起行业和国民经济的发展。     

尿素合成气的取样技术

介绍了我国尿素合成在线分析的现状及在取样技术上遇到的困难，针对这一难点，研究设计了旋液分离器及成套系统，经实际应用，效果较好。     

哌嗪的生产应用和市场

综述了哌嗪的合成技术和应用开发现状,分析了哌嗪的市场前景。     

旋转注射式反应注射成型技术混合方式剖析

为了克服反应注射成型技术混合方式存在的缺点，新近出现了一种旋转注射式－ＲＩＭ技术。该技术采用低速旋转注射剪切层流混合方式，具有能耗低，混合效果好，应用广泛等特点，是一种很有应用潜力的新技术，文内对该技术的混合方式进行了简要剖析。     

NGF型生料均化库装备技术的开发及应用

南京院开发的小型NGF型系列连续重力充气搅拌式生料均化库，已成功用于多条2500—10000t／d水泥熟料生产线。文章介绍了该库的均化工作原主要由三部分完成：一是库顶多点下料生料分配器；二是内、外充气系统；三是库底卸料装置及充气计量仓系统。同时详细分析了该库的结构组成和结构特点；还作了其中的二个应用实例及其效果。运行结果表明，该库的装备技术安全可靠，造价合理寿命长，均化原理先进，运行电耗低，均化效果好，达到国内外同类产品的先进水平。     

Transport processes during electrowashing of filter cakes

Applications of electric fields during washing of filter cakes increases the removal rate of ions from the cake mother liquor, and under appropriate conditions the field also increases the wash flow rate by electroosmosis. Experimental data that show the key effects of the fields on the rates of ion mass transfer are presented: with the downstream electrode acting as a cathode, cation removal rates are increased whilst the removal rate of the anions is decreased. The concentration profile of the cations with washing time shows an increase in concentration to a value above that of the mother liquor, before it decreases due to displacement by the fresh wash liquor. A model is formulated that describes the advection, dispersion, ion migration and electroosmosis transport processes in the cake. Numerical solution of the model gives cation concentration profiles at the exit of the cake that are in qualitative agreement with the experimental observations. Experimentally measured wash liquor flow rates tend to be lower than what traditional colloid science principles predict by a factor of 5-10: reasons for this difference, supported by experimental work from other researchers, are discussed.     

国外聚甲醛生产技术现状与发展

综述了国外主要甲醛生产厂商的工艺技术，树脂生产技术的发展和品种开发情况。     

Dynamic modeling of drainage through three-dimensional porous materials

The interplay of viscous, gravity and capillary forces determines the flow behavior of two or more phases through porous materials. In this study, a rule-based dynamic network model is developed to simulate two-phase flow in three-dimensional porous media. A cubic network analog of porous medium is used with cubic bodies and square cross-section throats. The rules for phase movement and redistribution are devised to honor the imbibition and drainage physics at pore scale. These rules are based on the pressure field within the porous medium that is solved for by applying mass conservation at each node. The pressure field governs the movement and flow rates of the fluids within the porous medium. Film flow has been incorporated in a novel way. A pseudo-percolation model is proposed for low but non-zero capillary number (ratio of viscous to capillary forces). The model is used to study primary drainage with constant inlet flow rate and constant inlet pressure boundary conditions. Non-wetting phase front dynamics, apparent wetting residuals (S_wr), and relative permeability are computed as a function of capillary number (N_ca), viscosity ratio (M), and pore-throat size distribution. The simulation results are compared with experimental results from the literature. Depending upon the flow rate and viscosity ratio, the displacement front shows three distinct flow patterns—stable, viscous fingering and capillary fingering. Capillary desaturation curves (S_wr vs. N_ca) depend on the viscosity ratio. It is shown that at high flow rates (or high N_ca), relative permeability assumes a linear dependence upon saturation. Pseudo-static capillary pressure curve is also estimated (by using an invasion percolation model) and is compared with the dynamic capillary pressure obtained from the model.