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41.
介绍了城镇燃气管道泄漏爆炸冲击波超压的定量风险分析方法.简要介绍了城镇燃气管道,对城镇燃气管道泄漏的失效概率、泄漏源模型、爆炸冲击波超压模型、超压概率模型、个人风险和社会风险分别作了论述.  相似文献   
42.
目的获取弹药在殉爆情况下发生反应的特征行为,为不敏感弹药的评定以及弹药安全性的评估提供技术支撑。方法参照北约STANAG4396标准,开展某型弹药殉爆试验。采用超压测量、见证板变形破坏情况观测、破片速度测量等传统测试方法,结合先进的激光干涉测速技术(Photonic Doppler Velocimetry—PDV)测量被发弹药及主发弹药反应后壳体膨胀速度。结果被发弹药侧见证板比主发弹药侧见证板产生了更严重的变形。11 m和14 m处超压测量结果分别达到306 kPa和177 kPa,与两枚弹药爆轰后产生的超压相当。被发弹药和主发弹药的壳体膨胀速度相当,达到约3500 m/s。结论在试验条件下,被发弹药发生了爆轰反应,该弹药不属于不敏感弹药。在殉爆试验中,主发弹药和被发弹药的壳体膨胀速度可作为判断被发弹药反应等级的关键参量。  相似文献   
43.
Porous media has a significant effect on flame and overpressure of methane explosion. In this paper, the pore diameter and thickness of porous media are studied. Nine experimental combinations of different pore diameter and thickness on the propagation of flame and overpressure of methane explosion in a tube are analyzed. The results show that the porous media not only can suppress the explosive flame propagation, but the porous media with large pore diameter can cause deflagration and accelerate the transition of flame from laminar to turbulent. The pore diameter of the porous media mainly determines the quenching of the flame. Simply increasing the thickness of porous media may cause the flame to temporarily stop propagating, but the flame is not completely extinguished for larger pore diameter. However, the deflagration propagation speed of flame is affected by the thickness. The attenuation of overpressure by porous media is mainly reflected in reducing the duration of overpressure and the peak value of overpressure. The smaller the pore diameter, the greater the thickness, and the more remarkable the reduction in overpressure duration and peak value. Suitable pore diameter and thickness of porous media can effectively suppress flame propagation and reduce the maximum value and duration of overpressure.  相似文献   
44.
为研究可燃气体爆炸压力场受障碍物布置的影响情况,运用流体动力学软件AutoReaGas建立不同阻塞程度和不同结构(平面、立体)的障碍物爆炸模型,模拟分析不同布置情况对气体爆炸压力场的影响程度和规律。研究表明:改变障碍物的阻塞程度和结构(平面、立体)都会影响可燃气体的爆炸超压峰值。同种障碍物结构下,随着阻塞率的增加,气体爆炸压力的增加程度在一定范围内呈现出先增大后减小的变化情况;相同阻塞率下,立体障碍物对爆炸压力场产生的影响明显大于平面障碍物。研究立体障碍物与平面障碍物对加速燃烧的影响情况旨在为工业生产过程中的实际应用提供理论依据和基础,为防控气体爆炸灾害提供一定参考借鉴作用。  相似文献   
45.
为了研究油气浓度对半开口管道爆炸超压特性与火焰行为的影响,建立半开口透明管道实验台架,采用5种不同初始油气浓度,进行了一系列油气爆炸对比实验。研究结果表明:油气浓度对油气爆炸超压峰值以及升压速率有显著影响,二者都呈现随浓度的增加先增大后减小的变化规律;油气浓度对火焰锋面传播速度有着显著影响,在当量浓度比下,火焰锋面的传播速度最大,并且火焰锋面的传播距离也最远;管道内的火焰行为可以分为4个阶段;油气浓度对火焰传播形态以及传播速度有明显的影响,对火焰传播形态的影响主要体现在破坏变形以及管道外爆炸阶段,随着浓度增加,爆炸半径先增大后减小,火焰传播速度呈现相同的变化规律。  相似文献   
46.
To further elucidate the influence mechanism of side vents on the dynamic characteristics of gas explosions in tubes is helpful to design more reasonable vent layouts. In this paper, 9.5% methane-air explosion experiments were conducted in a tube with two side-vented ducts, and the effects of vent layouts and vent areas on the dynamic characteristics of explosion overpressure and flame propagation speed were investigated. The results demonstrate that under the same condition with a single vent area of 100 mm × 100 mm, when only the end vent is open, the maximum explosion overpressure and the maximum flame propagation speed are the highest among the five vent layouts. When the side vents 1 and 2 and the end vent are open, the maximum explosion overpressure is the lowest, and an unusual discovery is that the flame front changes into a hemispherical shape, finger shape, quasi-plane shape, tulip shape and wrinkled structure. When only side vent 1 is open, a unique Helmholtz oscillation occurs, and a new discovery is that there is a consistent oscillation relationship among the overpressure, flame propagation speed and flame structure. Helmholtz oscillation occurs only when a single vent area is 100 mm × 100 mm–60 mm × 60 mm, and the oscillation degree decreases with decreasing vent area. During the vent failure stage, the maximum explosion overpressure is generated, the flame front begins to appear irregular shape, and the flame propagation speed shows a prominent characteristic peak. After the vent failure stage, the driving effect of the end vent on the flame is higher than that of the side vent on the flame. Furthermore, the correlation equations of the mathematical relationships among the maximum explosion overpressure Pred, the static activation pressure Pstat and the vent coefficient Kv under four vent layouts are established, respectively.  相似文献   
47.
The production and storage of liquefied petroleum gas (LPG) is gradually becoming larger and more intensive, which greatly increases the risk of the domino effect of an explosion accident in a storage tank area while improving production and management efficiency. This paper describes the construction of the domino effect scene of an explosion accident in an LPG storage tank area, the analysis of the characteristics of the LPG tank explosion shock wave and the target storage tank failure, and the creation of an ANSYS numerical model to derive the development trend and expansion law of the domino accident in the LPG storage tank area. The research showed that: 400 m3 tank T1 explosion shock waves spread to T2, T4, T5, T3, and T6, and the tank overpressures of 303 kPa, 303 kPa, 172 kPa, 81 kPa, and 61 kPa respectively. The critical values of the target storage tank failure overpressure-range threshold were 70 kPa and 60 m. After the explosion of the initial unit T1 tank, at 38 ms, the T2 and T4 storage tanks failed and exploded; at 56 ms, the T5 storage tank exploded for the third time; at 82 ms, the T3 storage tank exploded for the fourth time; and at 102 ms, the T6 storage tank exploded for the fifth time. With the increase of explosion sources, the failure overpressure of the target storage tank increased, and the interval between explosions continuously shortened, which reflected the expansion effect of the domino accident. The domino accident situation deduction in the LPG storage tank area provided a scientific basis for the safety layout, accident prevention and control, emergency rescue, and management of a chemical industry park.  相似文献   
48.
The obstacle structure in the vapor cloud has a significant influence on the gas explosion. Obstacles could not only lead to the acceleration of flame, but also they may occupy some space, thus affecting the amount of combustible gas. In this paper, a new two-step method was proposed to respectively study the effects of the obstacles amount and volume blockage ratio (VBR) on the gas explosion by using Computation Fluid Dynamic software AutoReaGas, and the obstacles in the vapor cloud were set to “Solid” instead of “Subgrid”. Based on the results and analysis, it is found that the peak overpressure and the maximum combustion rate rise with the increase of the number of obstacles for a single VBR, which indicated that the vapor cloud explosion of more obstacles was more dangerous for a single VBR. However, under a single number of obstacles, the peak overpressure and the maximum combustion rate increase firstly and then decrease as VBR increases and reach the highest at the VBR of 0.74, which indicated that the intensity of vapor cloud explosion reach a peak at a certain VBR in the middle instead of the largest. In addition, the existence and structure of obstacles have little effect on the size of explosion fireball when the size and concentration of combustible gas cloud are the same.  相似文献   
49.
沸腾液体扩展蒸气爆炸机理及相关计算理论模型研究   总被引:16,自引:1,他引:15  
剖析了沸腾液体扩展蒸气爆炸 (BLEVE)的发生、发展过程 ,阐述了其机理及相关条件 ,研究并提出了两种BLEVE火球热辐射模拟计算理论模型 ,即近地面和抬升火球模型 ,以及爆炸超压模型。与有关实验结果比较和与已有模型的对比计算表明了所建模型的有效性  相似文献   
50.
对油气在封闭管道内的爆炸特性进行研究,发现爆炸超压发展过程可以分为3个阶段:第1次超压上升阶段、第2次超压上升阶段和超压下降阶段。初始油气浓度对爆炸初始阶段的发展有很大影响,油气浓度为1.73%时发展最激烈;当初始油气浓度较高时,在最大超压峰值附近,会产生压力振荡现象;初始油气浓度对Tulip火焰的形成及发展有较大影响,各种浓度油气的爆炸,都有形成Tulip火焰的趋势;当油气浓度适中时,Tulip火焰会一直传播到管道末端,当油气浓度较高或较低时,火焰锋面会经由鲨鱼嘴形状火焰转变为刀尖形火焰,当初始油气浓度为1.73%时,最容易发展形成Tuilp火焰。  相似文献   
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