高压管汇磁致伸缩导波缺陷检测模拟研究

针对高压管汇导波缺陷检测问题,基于磁致伸缩效应,借助COMSOL有限元仿真软件,建立高压管汇直管段的导波缺陷检测模型,探究导波的激励条件及缺陷检测效果,分析不同参数对缺陷附近磁感应强度分布的影响。研究结果表明:在频率为10 kHz的正弦电流信号激励下,可产生沿管道轴向传播的T（0,1）模态导波,并能辨别缺陷处的回波信号。改变缺陷的尺寸参数时,缺陷附近的磁感应强度随着缺陷深度增加呈增大趋势,随轴向宽度增加呈减小趋势,不同形状的缺陷对应的磁感应强度存在一定的差异;改变激励条件,磁感应强度均随激励电流、激励频率的增加呈不断增加趋势。     

Numerical and experimental study on the generation and propagation of negative wave in high-pressure gas pipeline leakage

Negative-wave-based leakage detection and localization technology has been widely used in the pipeline system to diminish leak loss and enhance environmental protection from hazardous leak events. However, the fluid mechanics behind the negative wave method has yet been disclosed. The objective of this paper is to investigate the generation and propagation of negative wave in high-pressure pipeline leakage. A three-dimensional computational fluid dynamic (CFD) study on the negative wave was carried out with large eddy simulation (LES) method. Experimentally validated simulation presented the transient wave generation at the leak onset and the comprehensive wave evolution afterwards. Negative wave was proven to be a kind of rarefaction acoustic waves induced by transient mass loss at the onset of leakage. Diffusion due to the density difference at wave fronts drives the negative wave propagation. Propagation of negative wave can be categorized into three states – semi-spherical wave, wave superposition and plane wave, based on different wave forms. The wave characteristics at different states were elucidated and the attenuation effects were discussed respectively. Finally, a non-dimensional correlation was proposed to predict the negative wave amplitude based on pipeline pressure and leak diameter.     

Inhibiting effects of gas–particle mixtures containing CO2, Mg(OH)2 particles,and NH4H2PO4 particles on methane explosion in a 20-L closed vessel

The main risk factors from methane explosion are the associated shock waves, flames, and harmful gases. Inert gases and inhibiting powders are commonly used to prevent and mitigate the damage caused by an explosion. In this study, three inhibitors (inert gas with 8.0 vol% CO₂, 0.25 g/L Mg(OH)₂ particles, and 0.25 g/L NH₄H₂PO₄ particles) were prepared. Their inhibiting effects on methane explosions with various concentrations of methane were tested in a nearly spherical 20-L explosion vessel. Both single-component inhibitors and gas–particle mixtures can substantially suppress methane explosions with varying degrees of success. However, various inhibitors exhibited distinct reaction mechanisms for methane gas, which indicated that their inhibiting effects for methane explosion varied. To alleviate amplitude, the ranking of single-component inhibitors for both explosion pressure (P_ex) and the rate of explosion pressure rise [(dP/dt)_ex] was as follows: CO₂, NH₄H₂PO₄ particles, and Mg(OH)₂ particles. In order of decreasing amplitude, the ranking of gas‒particle mixtures for both P_ex and (dP/dt)_ex was as follows: CO₂–NH₄H₂PO₄ mixture, CO₂‒Mg(OH)₂ mixture, and pure CO₂. Overall, the optimal suppression effect was observed in the system with the CO₂–NH₄H₂PO₄ mixture, which exhibited an eminent synergistic effect on methane explosions. The amplitudes of P_ex with methane concentrations of 7.0, 9.5, and 11.0 vol% decreased by 37.1%, 42.5%, and 98.6%, respectively, when using the CO₂–NH₄H₂PO₄ mixture. In addition, an antagonistic effect was observed with CO₂‒Mg(OH)₂ mixtures because MgO, which was generated by the thermal decomposition of Mg(OH)₂, can chemically react with water vapor and CO₂ to produce basic magnesium carbonate (xMgCO₃·yMg(OH)₂·zH₂O), thereby reducing the CO₂ concentration in a reaction system. This research revealed the inhibiting effects of gas‒particle mixtures (including CO₂, Mg(OH)₂ particles, and NH₄H₂PO₄ particles) on methane explosions and provided primary experimental data.     

瓦斯积聚量及爆炸距离对风机和防爆门的影响研究*

为揭示瓦斯积聚量及瓦斯爆炸距离对风机和防爆门的影响机制,利用Fluent模拟软件,结合宁煤集团羊场湾矿的实际情况,在构建三维数学物理模型的基础上,开展不同瓦斯积聚量（56.52,113.04,169.56,226.08 m3）和不同爆炸距离（20,30,50,70 m）条件下的模拟研究。研究结果表明:风机和防爆门处超压峰值随瓦斯积聚量增加而增加,均呈线性关系,瓦斯积聚量为56.52 m3时风机处超压峰值为0.260 MPa,小于风机破坏荷载0.306 MPa;考虑安全系数前提下,当瓦斯积聚量超过56.52 m3时防爆门应开启保护风机;在确定瓦斯积聚量为56.52 m3基础上,分析不同爆炸距离对风机和防爆门影响,由模拟结果可知,风机和防爆门处超压峰值随爆炸距离增加而降低,均呈幂函数关系。研究成果可为瓦斯爆炸对风机和防爆门的影响研究提供指导。     

突出冲击波对防突风门的破坏失效研究*

为了分析煤与瓦斯突出事故中防突风门的安全性,同时降低成本寻求对现有防突风门材料和结构的替代方案,研究不同厚度的Q460钢制防突风门在突出冲击波载荷下的破坏情况。基于能量法得到不同厚度的风门最大挠度数学模型,再根据煤炭行业规定中的对应数据和安全要求,运用LS-DYNA软件对冲击载荷下的风门破坏进行数值模拟,得到Q460钢制防突风门的静力学特征并与能量法结果进行比对。结果表明:长宽分别为1.75 m和1.8 m,厚度为25 mm和30 mm的风门在0.6 MPa的冲击波超压作用下能满足安全要求,能量法计算结果与数值模拟误差在9%以内,基于安全设计余量可以接受;提出挠厚比概念,当挠厚比小于0.84时,风门不会被破坏,在使用Q460钢设计防突风门时,应尽量确保该值小于0.84。     

获取NEBS认证的“3P”阶段

NEBS认证,是电信网络设备进入北美地区电信网络的通行证。本文把获取NEBS认证的全过程划分为三个阶段,即准备阶段、设计阶段和实施阶段,并论述了各阶段的关键要点。首先,在准备阶段对NEBS进行了介绍,简要分析了NEBS认证的主要标准,同时指出运营商的特殊要求的重要性。接着分析了在设计阶段应该注意的技术点,如空间尺寸要求、电源输入、接地、防火、地震等。最后,讨论了认证测试阶段面临的困难,并强调了认证前摸底测试的重要性及必须具备足够的耐心。     

超声波强化γ-Al_2O_3催化臭氧氧化法降解2,4-二硝基苯酚

采用超声波强化γ-Al_2O_3催化臭氧氧化法降解模拟废水中的2,4-二硝基苯酚,考察了超声波对降解反应的强化作用及γ-Al_2O_3加入量、臭氧流量、超声波功率等对2,4-二硝基苯酚降解的影响.实验结果表明:2,4-二硝基苯酚在超声波强化γ-Al_2O_3催化臭氧氧化作用下的降解过程符合一级表观动力学;在2,4-二硝基苯酚质量浓度为20.00 mg/L、γ-Al_2O_3催化剂加入量为1.5g/L、臭氧流量为61 mg/min、超声波功率为300 W、反应时间为60 min时,2,4-二硝基苯酚的降解率达96.4%.     

我国大陆未来几年的地震形势与灾害分析

依据中国大陆的地震活动必将受到全球地震活动的制约,要分析中国大陆未来的地震趋势必须研究全球的地震活动的思路,通过对全球地震活动趋势以及近期大陆和周边地震活动的概况分析,认为大陆第五活跃期已基本结束,但并不意味着地震灾害水平随之降低,防震羊城灾任务依然严峻。     

基于GIS的城市生命线工程地震反应仿真研究——以上海市供水系统为例

探讨了地理信息系统（GIS）在城市生命线地震反应仿真研究中的应用,以上海市内环中心城区为背景,以供水系统为例,运用网络可靠性分析法进行了给水管网的震害预测,在此基础上以GIS功能强大的软件ArcView为开发平台,创建了可视化的上海市水管网地震反应仿真真信息系统。     

我国社会可接受地震人员死亡率的研究

在分析地震的特点及我国目前抗震设防中存在问题的基础上,提出了社会可接受地震人员死亡率的概念,介绍了确定可接受地震人员死亡率的方法及需要考虑的因素。同时通过对其它自然灾害和人为灾害死亡率的统计,以问卷调查的形式咨询了熟悉防震减灾工作的有关专家和政府管理部门等业内人士的意见,在此基础上,给出了较合理的社会可接受地震人员死亡率的建议值,为在抗震设防标准研究中定量考虑和控制地震人员伤亡提供了依据。