Blast wave clearing behavior for positive and negative phases

The purpose of the research was to improve prediction of response of buildings to blast waves by including the negative phase and considering clearing of both positive and negative phases. Commonly used structural design practices, which trace their origins to military design manuals, often ignore the negative phase as well as positive phase clearing. For high explosive threats, this approach is conservative in most circumstances. However, negative phase clearing had not previously been studied for blast waves, and the implications for structural response had not been evaluated. This paper presents results of modeling negative phase blast clearing behavior for a typical blast wave and discusses the differences from positive phase clearing. The implications of including positive and negative phase clearing in building blast damage analysis are also investigated through single-degree-of-freedom (SDOF) analyses.Blast waves from explosion sources like a vapor cloud explosion (VCE), pressure vessel burst or high explosive exhibit both positive and negative phases, and the relative magnitude of the positive and negative phases varies among explosion sources and the specific circumstances of each source. A fully reflected blast wave is produced if an incident blast wave were to strike an infinitely tall and wide wall in a normal orientation. Both the positive and negative phases of the blast wave are enhanced by the reflection process. However, when an incident blast wave strikes a wall of finite size in a normal orientation, rarefaction waves are created at the edges of the wall, and the rarefactions sweep down from the roof and inward from sides. The rarefaction waves result in a clearing effect for both the positive and negative phases.Clearing relieves some of the applied blast load on the reflected wall for the positive phase. However, this is not always the case for the negative phase. As shown by the results presented in this paper, clearing may either relieve or enhance the applied negative phase blast load, depending on the duration of the blast wave and the wall dimensions.The impact of negative phase clearing on structural response for generic building components was also investigated. Nonlinear SDOF methods were used to characterize response in terms of peak positive and negative displacements. It was found that the influence of the negative phase is significant and the peak structural response can occur during negative (outward) displacement.     

铬渣中铬的浸出行为

采用BCR法连续浸提研究铬渣中铬的存在形态,结果表明:铬渣中总铬和六价铬主要以残渣态和可氧化态形式存在;通过铬渣动态连续浸提实验与静态浸提实验研究了浸提剂和活性炭对铬渣中铬浸出行为的影响,研究发现p H值为3.1的醋酸浸提剂浸出液中铬浓度最低,且添加活性炭后的静态浸出液中铬的浓度有不同程度降低。     

油田井场废水配制压裂液处理技术实验研究

针对油田井场废水高悬浮物、高色度、高金属离子浓度的特征,以处理后配制压裂液为目标,通过p H值调节及无机高分子絮凝法对井场废水进行了处理实验。结果表明,碳酸钠作为优选的p H值调节剂,可以在较低的p H值条件下有效去除废水中的高价金属离子;无机絮凝剂聚合硫酸铁在强碱性条件下对于悬浮物、色度的去除效果明显优于聚合氯化铝。聚合硫酸铁絮凝法可以使井场废水达到配制压裂液用水的要求。     

超高“Z型”中庭高度对自燃排烟特性影响的数值模拟研究

超过12m的超高中庭发生火灾时,常规排烟方法不能完全满足实际需求。通过FDS软件对某超高"Z型"中庭进行数值模拟,研究中庭高度对自然排烟特性的影响。该"Z型"中庭底层南面是自然进风口,顶层北面是自然排烟口,以烟气最先到达指定楼层人员危险时间值为到达危险时间。实验条件下模拟结果表明:无风情况下,中庭高度增加,到达危险时间增加,自然排烟效果增强。到达危险时间t与中庭高度h之间满足一定指数增长关系:t=y0+Aexp(h/α),中庭火源位置和中庭宽度对y0、A和α有一定影响。有风情况下,外界风向与进风口方向一致时,中庭自然排烟效果优于无风状况,中庭越高效果越强。在外界风向与排烟口方向相反时,烟气倒灌进中庭,自然排烟效果较弱。     

基于探采对比的煤层瓦斯含量分析及预测

针对新建矿井地勘瓦斯含量测值偏低和井下实测瓦斯含量较少的特点,结合工程和科研实践,提出了利用大量的工作面瓦斯涌出量反演煤层原始瓦斯含量技术和基于探采对比的煤层瓦斯含量预测方法。以邹庄井田32煤层为研究对象,在考虑瓦斯抽采情况下计算3204工作面瓦斯涌出量,并反演该工作面煤层原始瓦斯含量。通过对比采掘过程中获得的瓦斯含量和地勘瓦斯含量,得到不同钻孔深度时的地勘瓦斯含量修正系数,并采用瓦斯地质研究方法对32煤层分3个单元进行瓦斯含量预测。结果表明:32煤层瓦斯含量整体呈现"东部大于西部,北部大于南部"的规律,与临近矿井具有相似的瓦斯赋存规律。这表明利用探采对比的方法预测煤层瓦斯含量是可靠的。     

本煤层瓦斯抽采渗流模型及数值模拟

在研究煤层瓦斯抽采时,假定煤岩为具有孔隙裂隙的双重介质,在运动方程、连续性方程和辅助方程基础上,以煤岩体应变为耦合媒介建立了考虑裂隙瓦斯渗流、微孔隙吸附瓦斯解吸扩散和煤岩变形的渗流模型.借助多物理场分析软件COMSOL Multiphysics,将模型转化为偏微分方程组,结合沙曲矿24305工作面瓦斯赋存条件进行分析求解.结果表明,进行煤层瓦斯预抽时,抽采初期瓦斯压力下降较快,抽采孔间距对抽采效果影响比较显著,距离抽采孔越远瓦斯压力下降越慢,抽采时瓦斯渗流速度变化可分3个阶段.参考模拟结果现场布置孔距为6m的顺层钻孔,抽采稳定时瓦斯纯量达5～7 m3/min,抽采效果比较理想.     

突发事件情景演化及关键要素提取方法

针对突发事件应急处置难度大的特点,突发事件应急管理模式必须向"情景-应对"转变。从系统复杂性、开放式预先设想以及序贯性三个主要原则的角度理解突发事件情景演化的机理,构建了突发事件情景演化系统模型,并以此为基础设计了突发事件情景网络关键要素的提取方法。该方法以危险源形成、突发事件演化以及应急响应三方面主要内容为情景网络的主体,以三方面主要内容所涉及的影响因素为分支,适当的选取情景网络关键要素并将关键要素分为四类。该方法的提出弥补了情景网络关键要素提取方法理论的空白,为突发事件情景构建提供了理论支持。     

Application of CFD on the sensitivity analyses of some parameters of the modified Hartmann tube

The aim of this work is to determine the influence of operating parameters such as the dispersion pressure, the ignition delay and height on the dust flammability. A Computational Fluid Dynamics (CFD) simulation, based on an Euler–Lagrange approach, was developed with Ansys Fluent™ and validated experimentally. Such analysis will facilitate the choice of the most conservative conditions for a flammability test. This paper is focused on a case study performed on wheat starch with the modified Hartmann tube. The dispersion process of the powder was studied with granulometric analyses performed in situ and high speed videos. Tests were performed with injections at gas pressure ranging from 3 to 6 bars and the evolution of the particle size distribution (PSD) was recorded at different ignition heights (5, 10 and 15 cm over the dispersion nozzle). The observations highlighted the presence of agglomeration/deagglomeration processes and dust segregation. Besides, a CFD simulation analysis was aimed at evaluating the impact of a set of parameters on the PSD and the local turbulence, which are closely linked to some flammability parameters. For this computational analysis, the CFD simulation was coupled with a collision treatment based on a Discrete Element Method (DEM) in order to consider the cohesive behavior of the combustible dust. Thus the results suggest performing the injection of the gases at approximately 5 bars for the flammability tests of wheat starch in order to obtain the finest PSD at a given ignition height. It is also shown that the finest PSD are obtained at 5 cm over the dispersion nozzle. However, the local instabilities and turbulence levels are so high during the first stages of the dispersion that the flame growth can be disturbed for short ignition delays. Moreover, the stabilization of the bulk of the dust cloud requires longer periods of time when the ignition sources are located at 15 cm. As a result, the recommended height to perform a flammability test is 10 cm in this case. Finally, this study proposes some tools that might improve the procedure of dust flammability testing.     

Application of a hydroxylamine nitrate stability model to plutonium purification process equipment

A mathematical model that predicts hydroxylamine nitrate (HAN) (NH₂OH·HNO₃) stability is applied to aqueous solutions containing HAN, nitric acid and plutonium that are used in plutonium purification processes. The model estimates the stability of these solutions with respect to the rapid, hazardous, autocatalytic reaction of HAN with nitric acid that generates heat and gas. It also accounts for reaction kinetics, temperature changes, gas generation rates, solution volumes and flow rates, and distribution of plutonium and nitric acid between aqueous and organic phases. The model is applied to three typical process vessels used in solvent extraction purification of plutonium – a countercurrent aqueous/organic plutonium stripping column, an oxidation column used for HAN and hydrazine destruction, and a plutonium rework tank. Both normal and off-normal process scenarios are modeled. Two of the off-normal scenarios lead to the rapid autocatalytic reaction of HAN with nitric acid where heat and gas are generated and that could lead to damage of the process equipment and/or release of hazardous plutonium solution from the vessel. In these two cases, stationary aqueous solutions containing HAN, Pu(III), and nitric acid were allowed to slowly react until conditions for the autocatalytic reaction were reached.     

中和-络合萃取-双极膜电渗析处理金刚烷胺制药废水

采用中和沉淀-络合萃取-双极膜电渗析组合工艺协同处理金刚烷胺制药胺化废水与溴化废水.结果表明,通过胺化废水与溴化废水的中和反应,可以大幅消减废水中溶解性固体和有机污染物,避免后续萃取过程中的乳化现象.在pH值为8.0、油/水相比为1∶1的条件下,P204∶正辛醇=3∶2的复配萃取剂对废水中TOC和TN的萃取效率分别为56.9%和20.6%,金刚烷胺及其衍生物几乎被完全萃取.以2.0 mol·L-1的HCl溶液为反萃取剂,可以将47.5%的金刚烷胺从负载有机相中反萃分离,再生后的萃取剂可以多次重复使用.对萃余液采用双极膜电渗析进行处理,可以去除64.2%的无机盐和部分有机物,同时还能回收到较高浓度的酸,但由于氢离子的渗漏难以回收高浓度的碱.