火灾引发超高层建筑非连续倒塌模拟研究

为了解超高层建筑发生火灾后变形特征及失稳后的非连续坍塌过程,掌握引起变形和坍塌的原因,将三维颗粒流软件(PFC3D)作为模拟平台,设置核心筒-框架结构的超高层建筑火灾区域,并模拟坍塌过程。在考虑钢筋和混凝土共同作用结果的基础上,提出火灾区域中构件属性设置方法及模拟步骤。分析得到造成建筑结构摆动的3种原因,一是火区位置不同导致上部结构对火区的压力不同,二是火区位置不同导致结构受到的约束不同,三是受热膨胀性使构件产生不同程度变形。结果表明:燃烧温度为500℃,3 h后建筑发生摆动,表现出对火区位置和燃烧时间敏感的特征。1 000℃下1 h内,建筑物首先发生破坏的是梁构件,然后是承重柱。即建筑一旦进入结构破坏阶段,坍塌将是迅速且不可逆的。     

Minimum ignition energy of mixtures of combustible dusts

Most industrial powder processes handle mixtures of various flammable powders. Consequently, hazard evaluation leads to a reduction of the disaster damage that arises from dust explosions. Determining the minimum ignition energy (MIE) of flammable mixtures is critical for identifying possibility of accidental hazard in industry. The aim of this work is to measure the critical ignition energy of different kinds of pure dusts with various particle sizes as well as mixtures thereof.The results show that even the addition of a modest amount of a highly flammable powder to a less combustible powder has a significant impact on the MIE. The MIE varies considerably when the fraction of the highly flammable powder exceeds 20%. For dust mixtures consisting of combustible dusts, the relationship between the ignition energy of the mixture and the minimum ignition energy of the components follows the so-called harmonic model based upon the volume fraction of the pure dusts in the mixture. This correlation provides results which show satisfactory agreement with the experimental values.     

Propagation of ethylene–air flames in closed cylindrical vessels with asymmetrical ignition

A study of explosions in several elongated cylindrical vessels with length to diameter L/D = 2.4–20.7 and ignition at vessel's bottom is reported. Ethylene–air mixtures with variable concentration between 3.0 and 10.0 vol% and pressures between 0.30 and 1.80 bara were experimentally investigated at ambient initial temperature. For the whole range of ethylene concentration, several characteristic stages of flame propagation were observed. The height and rate of pressure rise in these stages were found to depend on ethylene concentration, on volume and asymmetry ratio L/D of each vessel. High rates of pressure rise were found in the early stage; in later stages lower rates of pressure rise were observed due to the increase of heat losses. The peak explosion pressures and the maximum rates of pressure rise differ strongly from those measured in centrally ignited explosions, in all examined vessels. In elongated vessels, smooth p(t) records have been obtained for the explosions of lean C₂H₄–air mixtures. In stoichiometric and rich mixtures, pressure oscillations appear even at initial pressures below ambient, resulting in significant overpressures as compared to compact vessels. In the stoichiometric mixture, the frequency of the oscillations was close to the fundamental characteristic frequency of the tube.     

Thermal radiation from vapour cloud explosions

The current study estimates the radiation flux emitted from hot extended gas clouds characteristic of vapour cloud explosions along with the corresponding level of irradiance posed on particles suspended in the unburnt part of the cloud ahead of an advancing flame front. The data presented permits an assessment of the plausibility of combustion initiation by such particles due to forward thermal radiation. The thermal radiation will depend on the emissivity of the burned volume, which relates to the concentration of gaseous and particulate combustion products. A sensitivity analysis has been carried out to account for variations in the equivalence ratio, mixture pressure and radiative heat losses. The spatial distribution of irradiance ahead of the flame front has been computed by introducing appropriate geometrical factors to explore the impact of cloud size. Using fuel rich ethylene-air mixtures it has been shown that high flame emissivities can be achieved at path lengths of order 1 m even in the presence of very low soot volume fractions. The emissivity of gas-soot mixtures will hence be mainly determined by the soot concentration and to a lesser extent by the mixture temperature. Our analysis suggests that the role of forward thermal radiation as a contributing factor to flame propagation in large scale vapour cloud explosions can not currently be ruled out.     

DME简化反应模型及其在HCCI燃烧分析中的应用研究

提出了一个可应用于HCCI发动机工作过程研究的DME化学反应动力学简化模型,该模型由28种组分、38个基元反应组成,包括3个子模型,即低温反应和负温度系数区子模型、高温裂解和高温氧化子模型以及甲酸生成过程子模型.通过算例对比分析,该DME简化模型能正确揭示DME燃烧过程主要生成物组分的变化规律,能准确计算DME燃烧过程低温和高温阶段的放热特征时刻,其计算结果与详细机理计算结果吻合.相对于详细机理,简化模型节省了计算时间,为实现化学反应动力学与CFD多维模型耦合的燃烧计算提供了一个可行而有效的途径.     

DDS系列煤炭自燃阻化剂实验研究

为寻找高效阻化剂以防止煤炭自热引燃，在控温炉中对ＤＤＳ系列煤自燃阻化剂的阻化效果进行了实验研究，并与经前的阻化剂做了比较。实验采用烟煤作为试样，借助于著名的Ｆｒａｎｋ－Ｋａｍｅｎｅｔｓｋｉｉ模型，利用４，６，８和１０厘米立方体阻化煤磁地６０－２２０℃温度范围估测其氧化反应的活化能。     

基于活化能指标的煤自燃倾向性及发火期研究

在煤的自燃及热分析动力学的基础上,结合对神东矿区3种煤样进行了热重实验,运用热重分析手段对煤从常温到燃点之间的氧化热解过程进行了研究。运用不同动力学机制模型函数分别对热重分析数据进行了处理和相关性分析,结果表明煤炭氧化热解过程符合一级化学反应动力学机制,据此求出活化能等动力学参数。对基于活化能指标的煤的自燃倾向性及自然发火期进行了初步研究。经过研究发现,该方法是科学的、客观的。     

装药尺寸对传爆药传爆可靠性的影响

采用锰铜测压实验测定了强约束及弱约束条件下 ,不同装药直径的传爆药HMX/F2 64 1的爆压 ,实验混合炸药密度为 90 %的理论密度 ,研究的装药直径范围为 1.5～ 5 .0mm ,初步揭示出传爆序列小型化装药尺寸对传爆药传爆可靠性的影响。研究结果对传爆序列小型化装药尺寸的确定及其传爆可靠性的评价 ,具有重要的参考价值     

全煤开拓复杂构造易燃煤层自然发火防治

介绍了全煤开拓复杂构造易燃煤层自燃影响因素，分析了无煤柱开采综放工作面防灭火难点和自然发火原因，提出了防治技术对策。     

速生杨木粉尘最小点火能的实验研究

为防止木材加工中木质粉尘燃爆事故的发生,以纤维板生产中常见的原材料速生杨木粉尘作为研究对象,在分析粉尘粒径分布、元素分析、工业分析及形貌特征的基础上,采用1.2 L哈特曼管对3种不同粒径（0~50,＞50~96,＞96~180 μm）速生杨木粉尘进行最小点火能实验,探究点火延迟时间、喷粉压力、质量浓度和粒径分布对速生杨木粉尘最小点火能的影响及变化规律。研究结果表明:在质量浓度为500 g/m3时,分别增加点火延迟时间和喷粉压力,最小点火能都先减小后增大;最佳点火延迟时间和最佳喷粉压力分别为120 ms和120 kPa;粒径对最佳点火延迟时间和最佳喷粉压力无显著影响。在点火延迟和喷粉压力分别为120 ms和120 kPa条件下,最小点火能随质量浓度的增加先减小后增大。粉尘粒径与最小点火能呈正相关性,3种样品的最小点火能分别为1~3,1~3和7~13 mJ,对应的敏感质量浓度分别为500 ,750和1 250 g/m3,属于特别着火敏感性粉尘。