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991.
避难硐室的构建研究对硐室安全避险功能的实现具有重要意义。根据旬东井下人员分布及巷道布置情况,确定利用4-2采煤区现有巷道构建100人规模永久避难硐室;根据巷道尺寸、人均面积及设备体积等,计算得硐室有效宽度为4.6m,高度为3.5m,总长度为63.4m,人均面积为1.2m2;通过气密试验,测定0.135MPa避险区内外压差可达1980Pa;通过分析人员避险需求,确定旬东永久避难硐室生命保障系统由防火防爆系统、密闭缓冲系统、气幕隔绝系统、供氧系统、制冷除湿系统及附属系统组成。 相似文献
992.
粉尘爆炸是工业爆炸灾害的重要形式。建立可燃颗粒非均相系统的燃烧爆轰模型,基于Eulerian-Eulerian数值描述方法,采取有限差分方法编制非均相系统燃烧和爆轰发展的数值模拟程序,对封闭空间内两相非定常爆轰过程进行研究。数值分析可燃颗粒尺度、颗粒浓度对非均相系统燃烧、爆轰特性的影响。结果表明:在一定的范围内,当可燃颗粒的体积分数为10%,粒径0.5mm时,流场的燃烧爆轰效应最强。即10.6ms时刻,流场压力值达到28MPa,温度高达2600K,颗粒燃烧效率最高。 相似文献
993.
The traditional defence against propagating coal dust explosions is the application of dry stone dust. This proven and effective safety measure is strictly regulated based on extensive international experience. While new products, such as foamed stone dust, offer significant practical benefits, no benchmark tests currently exist to certify their dust lifting performance in comparison to dry stone dust. This paper reviews the coal dust explosion mechanism, and argues that benchmark testing should focus on dust lifting during the initial development of the explosion, prior to arrival of the flame. In a practical context, this requires the generation of shock waves with Mach numbers ranging from 1.05 to 1.4, and test times of the order of 10's to 100's of milliseconds. These proposed test times are significantly longer than previous laboratory studies, however, for certification purposes, it is argued that the dust lifting behaviour should be examined over the full timescales of an actual explosion scenario. These conditions can be accurately targeted using a shock tube at length scales of approximately 50 m. It is further proposed that useful test time can be maximised if an appropriately sized orifice plate is fitted to the tube exit, an arrangement which also offers practical advantages for testing. The paper demonstrates this operating capability with proof-of-concept experiments using The University of Queensland's X3 impulse facility. 相似文献
994.
Gas explosion is the leading accident in underground coal mining in China. Using the self-improved 20 L spherical experimental system, the impacts of 8% CO2, ABC powder at various concentrations and mixture of them on the suppression of mine gas explosion were investigated. The results indicate that cooperative synergism exists between ABC powder and CO2. Their combination has a better effect than each of the two components acting alone, especially for the gas of larger concentration. When 0.25 g/L ABC powder was mixed with 8% CO2, the explosion limits were reduced by about 55%, the time to reach the peak explosion pressure was prolonged 3.56 times on average. Meanwhile, the maximum explosion pressure declined on an average of 59.4% and the maximum explosion overpressure rising rate decreased on an average of 91.1%. A combination of 0.20 g/L ABC powder and 8% CO2 completely suppressed 11% gas explosion. The explosion suppression mechanism of CO2 and ABC powder were probed theoretically. CO2 plays a key part in the whole explosion processes, and it can effectively suppress the forward reaction between gas and oxygen. While it is during the middle-later period of explosion processes that ABC powder plays a critical role. The particles decomposed from heated ABC powder such as nitrogen and phosphor will react with free radicals rapidly. Besides, atoms as N, P are capable of participating in chain reaction and reacting with active groups, significantly suppressing the gas explosion. 相似文献
995.
《Process Safety and Environmental Protection》2014,92(5):430-441
Since the massive use and production of fuel oil and natural gas, the excavating locations of buried energy-carrying material are moving further away from onshore, eventually requiring floating production systems like floating production, storage and offloading (FPSO). Among those platforms, LNG-FPSO will play a leading role to satisfy the global demands for the natural gas in near future; the LNG-FPSO system is designed to deal with all the LNG processing activities, near the gas field. However, even a single disaster on an offshore plant would put the whole business into danger. In this research, the risk of fire and explosion in the LNG-FPSO is assessed by quantitative risk analysis, including frequency and consequence analyses, focusing on the LNG liquefaction process (DMR cycle). The consequence analysis is modeled by using a popular analysis tool PHAST. To assess the risk of this system, 5 release model scenarios are set for the LNG and refrigerant leakages from valves, selected as the most probable scenarios causing fire and explosion. From the results, it is found that the introduction of additional protection methods to reduce the effect of fire and explosion under ALARP criteria is not required, and two cases of the selection of independent protection layers are recommended to meet the SIL level of failure rate for safer design and operation in the offshore environment. 相似文献
996.
《Process Safety and Environmental Protection》2014,92(6):669-679
Several major accidents caused by metal dusts were recorded in the past few years. For instance, in 2011, three accidents caused by iron dust killed five workers at the Hoeganaes Corp. facility in Gallatin, Tennessee (USA). In order to prevent such accidents, a dynamic approach to risk management was defined in this study. The method is able to take into account new risk notions and early warnings and to systematically update the related risk. It may be applied not only in the design phase of a system, but also throughout the system lifetime as a support to a more precise and robust decision making process. The synergy of two specific techniques for hazard identification and risk assessment was obtained: the Dynamic Procedure for Atypical Scenarios Identification (DyPASI) and the Dynamic Risk Assessment (DRA) methods. To demonstrate its effectiveness, this approach was applied to the analysis of Gallatin metal dust accidents. The application allowed collecting a number of risk notions related to the plant, equipment and materials used. The analysis of risk notions by means of this dynamic approach could have led to enhanced hazard identification and dynamic real-time risk assessment. However, the approach described is effective only if associated to a proper safety culture, in order to produce an appropriate and robust decision making response to emerging risk issues. 相似文献
997.
998.
为了研究水平管道内障碍物数量对瓦斯爆炸的影响,利用自制的水平管道式气体爆炸试验装置,选用阻塞率为60%的圆环型障碍物,在常温常压下对管道内障碍物数量分别为1片、3片、5片和7片时瓦斯(试验气体为甲烷与空气的混合物,下同)爆炸过程进行试验研究。结果表明:瓦斯的爆炸压力及其上升速率均随障碍物数量的增加呈先增后减的变化规律,而火焰传播速度则随着障碍物数量的增加单调递增,但递增幅度逐渐减小。在密闭置障管道内瓦斯的爆炸压力及其上升速率随测试位置长径比的增大先减小后增大,而火焰传播速度则随测试位置长径比的增大单调递减。 相似文献
999.
1000.
瓦斯爆炸事故是煤矿的主要灾害之一,为了预防和控制煤矿井下瓦斯爆炸事故的发生,国内外研究者采用理论、实验室实验和数值模拟实验等手段对瓦斯爆炸机理、瓦斯爆炸传播规律等进行了深入研究,本文从瓦斯爆炸实验室实验和瓦斯爆炸数值模拟实验两方面入手,对瓦斯爆炸的研究进展情况进行了分析总结.对于瓦斯爆炸实验室研究,分析总结了现有瓦斯爆炸实验手段以及瓦斯爆炸传播特性研究情况;对于数值实验研究,分析总结了瓦斯爆炸数值模拟模型、现有瓦斯爆炸数值模拟商业软件以及软件应用情况.最后对瓦斯爆炸未来需要深入研究的问题提出了展望. 相似文献