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The effect of the vent burst pressure on explosion venting of a rich methane-air mixture was experimentally investigated in a small cylindrical vessel. The experimental results show that Helmholtz oscillation of the internal flame bubble of the methane-air mixture can occur in a vessel with a vent area much smaller than that reported by previous researchers, and the period of Helmholtz oscillation decreases slightly when the vent burst pressure increases. The maximum overpressure in the vessel increases approximately linearly with the increase in the vent burst pressure; however, the pressure peaks induced by Helmholtz oscillation always remain approximately several kilopascals. The external flame reaches its maximum length in a few milliseconds after vent failure and then oscillates in accordance with the pressure oscillation in the vessel. The maximum length of the external flame increases, but its duration time decreases with the increase in the vent burst pressure. 相似文献
53.
The possibility of ignition and flame propagation in accumulated difluoromethane (CH2F2, R32) was examined experimentally, simulating a situation in which a service operative uses a kerosene lighter for smoking. To simulate the situation where a kerosene cigarette lighter is used in accumulated R32, electrodes fixed in the windbreak of the lighter were remotely supplied with electricity to generate sparks of various durations but of similar energies to those of actual sparks generated by rubbing a flint to ignite the fuel in the lighter. We identified several cases of ignition and formation of an open flame in the windbreak of the lighter, and the flame propagated to the accumulated R32 when it was supplied with sufficient energy from the spark. Gas chromatographic analyses confirmed that the mixture in the windbreak of the kerosene lighter consisted mainly of vaporized fuel and air, with no R32. Therefore, even if the lighter is located in accumulated R32, an open flame can be generated in the windbreak of the kerosene cigarette lighter through ignition by the spark energy generated by friction between the flint and the flint wheel. Our results confirmed that there is a real possibility of ignition and flame propagation when a kerosene cigarette lighter is used in accumulated R32 under the leak rate conditions of the present experiment. 相似文献
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用萃取火焰AAS法测定汽车道旁树叶中的铅含量 总被引:4,自引:0,他引:4
主要介绍了用碘化钾-甲基异丁基甲酮(KI-MIBK)萃取汽车道旁植物叶片中的微量铅,然后用原子吸收分光光度法(AAS)测定,该方法的精密度和准确度均有较满意的结果 相似文献
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火焰振荡频率是火灾科学研究领域的一个重要基本参数,对横向风下火焰振荡频率的研究可以为火灾图像探测的参数设置提供理论依据。针对浮力扩散火焰(0.6×10~(-5)弗洛德数Fr2×10~(-2),10~2理查德森数Ri10~5),本研究将横向风条件下火焰结构假设为倾斜的柱状,通过对燃烧产生的浮力和横向风产生的拖曳力进行动力学分析,得出横向风条件下火焰振荡频率表达公式。结合实验结果得出,火焰振荡频率的理论值和实验值均随拖曳系数的增大(即外界风速的增加)而增大,但实验值的上升趋势较理论值平缓.这是因为公式忽略了风速对火焰温度和系数K的影响。 相似文献
58.
In the research field of chemical safety, the computer-aided simulation for occurrence and process of disasters has become a major trend in current research, in which the establishment of evolution system for chemical multi disasters is the key point. In the paper, the study lays emphasis on the simulation and application of a spread model for chemical multi disasters. After establishing a disaster network, we defined microcosmic elements of spread model specifically. Combined with guideline of chemical disaster (e.g. guideline of heat flux for damages or injure, guideline of evaluation for buildings based explosion and overpressure, and guideline of evaluation for human exposure to toxic gases), the weight of impact can be computed using new comprehensive algorithms. Simultaneously, the paper also uses an approach on simulating multiple failure events to describe random factors of triggering disasters. At last, the experimental case of alkyl aluminum leakage in a polypropylene plant shows the result of simulation with table of 5 major series of disasters and distribution diagram of nodes (disasters) in disaster network. This proves the validity and practicability of the simulation system in the establishment and feedback of contingency plan of large-scale petrochemical enterprises. 相似文献
59.
A. Grov H.E.Z. OpsvikR.K. Eckhoff 《Journal of Loss Prevention in the Process Industries》2011,24(5):552-557
Electrical apparatus for use in the presence of explosive gas atmospheres has to be specially designed to prevent the apparatus from igniting the gas. Flameproof design is one of several options, and one requirement is then that any holes and slits in the enclosure wall be designed to prevent a possible gas explosion inside the enclosure from being transmitted to an explosive gas cloud outside it. Current standards (IEC) require that joint surfaces have a surface roughness of <6.3 μm. Any damaged joint surface has be restored to this quality. The present investigation has demonstrated that flame gap surfaces in flameproof electrical apparatuses can suffer considerable mechanical and corrosive damage before the flame gaps no longer function satisfactorily. In some cases very significant mechanical surface damage in fact improves the gap performance. This indicates that current high costs of repairing and replacing flameproof electrical apparatus in process plants offshore and onshore can be reduced considerably without any increase of the explosion risk. 相似文献
60.
Evaporating liquid flow in a channel (An integral model based on shallow water flow approximation) 总被引:1,自引:0,他引:1
Phani K. Raj 《Journal of Loss Prevention in the Process Industries》2011,24(6):886-899
Liquefied Natural Gas (LNG) storage facilities generally include channels to convey potential spills of the liquid to an impoundment. There is increasing concern that dispersion of vapors generated by flow of LNG in a channel may lead to higher than limit vapor concentrations for safety at site boundary from channels that may be close to the dike walls. This issue is of recent concern to regulatory agencies, because the calculation of vapor hazard distance(s) from LNG flow in a channel is not required under existing LNG facility siting standards or regulations.An important parameter that directly affects the calculated LNG vapor dispersion distance is the source strength (i.e., the rate of vaporization of LNG flow from the wetted channel surfaces, as a function of spatial position and time). In this paper a model is presented which considers the variation of the depth of the flowing LNG with spatial location and time, and calculates the spatial and temporal dependence of the mass rate of vapor generation. Self similar profiles for the spatial variation of the thermal boundary layer in the liquid wetted wall and liquid depth variation are assumed. The variation with time of the location of the liquid spread front and the evaporation rate are calculated for the case of a constant LNG spill rate into a rectangular channel. The effects of two different channel slopes are evaluated. Details of the results and their impact on dispersion distances are discussed. 相似文献