不同塔型交流输电线路的电磁环境分析

选择500 kV同杆双回紧凑型线路、500 kV同杆双回常规线路、500 kV单回紧凑型线路、500 kV单回常规线路、220 kV同杆双回线路和220 kV/110 kV同杆4回线路进行不同塔型交流线路的电磁环境测量.通过测试和计算分析,给出了被测试线路的电磁环境水平.     

区域开发战略环境影响评价总体思路与技术要点

以内蒙古"十一五"规划战略环境影响评价为例,分析了战略环境影响评价与建设项目环境影响评价的差异,提出了战略环境影响评价是从"决策-源头-过程-末端"的全过程评价;其技术要点是突出区域环境和经济社会协调发展为核心的总体思路,重点把握战略环境影响评价6大特性即整体性、区域性、特色性、科学性、前瞻性和可操作性;其技术方法主要包括战略决策失灵分析法、战略决策灰色分析法、环境影响矩阵识别法、产业关联和物流分析等定性方法,以及GIS技术平台的图层叠置法、承载压力度分析、情景分析和模拟分析等定量方法.     

印度夏季风降水周期性研究

印度夏季风降水(ISMR)在南亚气候系统中是一个非常重要的内容,近年来对它的研究日益受到人们的重视。为了深入认识ISMR的变化特征,主要利用Scargle周期图和小波变换研究了1871-2004年间ISMR变化的周期性。结果表明,ISMR的周期性波动非常复杂,相应的周期参数具有明显的时变特征。文中还简单讨论了ISMR周期时变的可能原因。     

实际烟气生成量计算方法的商榷

火灾烟气是火灾时所产生的气体和悬浮在其中的烟粒子的总称，是燃烧和热解产物的混合物。烟气量的大小取决于可燃物本身的燃烧性能、空气供给量等。火灾烟气具有缺氧、毒害、尘害、高温的特点，加上火场火灾烟气的减光性和恐怖性，使火灾烟气成为火灾人员伤亡的最主要原因，为此防排烟工程的设计对建筑消防安全非常重要，实际烟气生成量计算是防排烟工程设计的理论基础，就目前一些文献对实际烟气量计算方法存在的不足进行了探讨，并提出了一个新的计算方法，对两种方法的计算结果进行了对比，得出结论认为，计算实际烟气量应从实际空气供给量是否过剩或不足两种情况分别进行考虑计算。     

北京山区公路地质灾害应急与防治对策

北京是地质灾害较严重的城市之一,具有灾种多、活动频繁、群发性强的特征。北京山区公路所遭受的地质灾害主要有滑坡、滑(崩)塌、泥石流、岩溶、采空地面塌陷等。为了防止山区公路地质灾害可能造成的危害,笔者通过对北京山区公路所遭受的地质灾害类型、发育特征、分布规律等特点及其所造成的危害进行分析、研究,提出了山区公路地质灾害应急与防治对策,以提高北京市的防灾减灾能力,减少和避免地质灾害造成的损失。     

化学事故救援方舱舱室环境安全性模拟研究

运用计算流体动力学(CFD)方法,对具有超压防护功能的某化学事故应急救援手术方舱室内气体污染物运动扩散的规律以及对人员安全的影响进行了数值模拟,其研究结果表明:当大气环境中氢氰酸(HCN)浓度为5mg/L时,前10s从常规进风口进入舱室的HCN在滤毒通风装置开启后,随气流运动逐渐向整个舱室扩散,经净化空气的混合稀释作用,绝大部分通过舱体缝隙排出舱室,30min内舱室HCN浓度的总量下降了95.1%,说明超压防护很好地保证了舱室环境的安全性。     

地铁轨道区火灾场景特性研究

在考虑人为恐怖袭击行为情况下，采用地铁轨道区模型实体火灾试验研究了地铁轨道区的火灾场景。得出了模拟地铁轨道区在火灾中的热释放速率，烟气浓度，温度，烟密度的变化规律。通电模拟短路以致引燃方式着火的最大热释放速率为9．66kW。浇洒煤油方式点火，轨道区最大热释放速率达到了204kW。随着电缆的点燃，燃烧进行的较为缓慢，烟气上升至隧道顶，沿着顶部向开口外扩散。C02的浓度变化较为缓慢。至10’41″达到c02释放峰值5027．7ppm；至10’41″时C0浓度达到最大354．0ppm。在轨道区问燃烧过程中，高温烟气始终沿着隧道顶部扩散，低于1．5m的空间是相对安全的；高于1．7m的空间是相对危险区域。火灾中烟气是首先弥漫整个房顶，然后再往下漫延的。     

Fire and explosion risk assessment for large-scale oil export terminal

Now in Russian Federation and other countries large-scale oil terminals (volume of one tank exceeds 100 000 m³, total volume of tanks exceeds 300 000 m³) are designed and constructed. Therefore fire safety of such objects becomes a very important task, solution of which is hardly possible without detail fire risk assessment. This study is aimed to a solution of this problem. Potential, individual and social risks were calculated. The potential risk was defined as a frequency of occurrence of hazardous factors of fires and explosions in a given point of space (the so-called risk contours). The individual risk was defined as a frequency of injuring a given person by hazardous factors of fires and explosions. Time of presence of this person in hazardous zones (near the hazardous installation) is taken into account during calculations of the individual risk. Social risk was defined as a dependence of frequency of injuring a given number of people by hazardous factors of fires and explosions on this number. In practice the social risk is usually determined on injuring not less than 10 people.

The oil terminal under consideration includes the following main parts: crude oil storage consisting of three tanks of volume 100 000 m³ each, input crude oil pipeline of diameter 0.6 m, crude oil pumps, output crude oil pipeline of diameter 0.8 m, auxiliary buildings and facilities. The following main scenarios of tank fires have been considered: rim seal fire, pool fire on a surface of a floating roof, pool fire on a total cross-section surface of the tank, pool fire in a dyke, explosions in closed or semiclosed volumes. Fires and explosions in other parts of the terminal are also taken into account. Effects of escalation of accidents are considered.

Risk contours have been calculated both for the territory of the terminal and for the neighbouring space. The potential risk for the storage zone is near 10⁻⁴–10⁻⁵ year⁻¹, and at a distance 500 m from the terminal the potential risk values do not exceed 10⁻⁶ year⁻¹. The values of the individual risk for various categories of workers are in the range of 10⁻⁵–10⁻⁶ year⁻¹. Because of low number of the workers on the terminal and large distances to towns and villages the social risk value is negligible. These risk values are consistent with practice of the best oil companies, and fire hazard level of the terminal can be accepted as tolerable.     

Comparison of different liquid anaerobic digestion effluents as inocula and nitrogen sources for solid-state batch anaerobic digestion of corn stover

Effluents from three liquid anaerobic digesters, fed with municipal sewage sludge, food waste, or dairy waste, were evaluated as inocula and nitrogen sources for solid-state batch anaerobic digestion of corn stover in mesophilic reactors. Three feedstock-to-effluent (F/E) ratios (i.e., 2, 4, and 6) were tested for each effluent. At an F/E ratio of 2, the reactor inoculated by dairy waste effluent achieved the highest methane yield of 238.5 L/kgVS_feed, while at an F/E ratio of 4, the reactor inoculated by food waste effluent achieved the highest methane yield of 199.6 L/kgVS_feed. The microbial population and chemical composition of the three effluents were substantially different. Food waste effluent had the largest population of acetoclastic methanogens, while dairy waste effluent had the largest populations of cellulolytic and xylanolytic bacteria. Dairy waste also had the highest C/N ratio of 8.5 and the highest alkalinity of 19.3 g CaCO₃/kg. The performance of solid-state batch anaerobic digestion reactors was closely related to the microbial status in the liquid anaerobic digestion effluents.     

基于CFD分析的呼吸防护面具罩体设计

分析呼吸防护面具研究领域在呼吸阻力方面的研究情况,提出基于计算流体力学分析的呼吸防护面具罩体设计方案,在设计过程中添加以计算流体力学分析为手段的有限元模拟仿真模块。通过ANSYS产品ICEM CFD与CFX对设计模型进行网格划分与流体分析,根据仿真结果对初步设计的模型进行结构优化再设计。