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101.
Low-concentration gas transported in pipelines may lead to explosion accidents because gas with a concentration of less than 30% is prone to explode. To reduce the incidence of gas explosions, water sealing of fire barriers is implemented, and explosion venting devices are installed along the pipeline. To investigate their suppression effect on low-concentration gas explosion, experiments using methane–air premixed gas under different conditions were implemented on a DN500 pipeline test system. The effects of three types of explosion venting forms (rupture disc, asbestos board, and plastic film) on explosion overpressure and flame were compared and analysed. Results show that the rupture disc, asbestos board, and plastic film can achieve adequate explosion venting, causing the peak decay rates of explosion overpressure to reach 82.37%, 81.72%, and 90.79%, respectively. The foregoing indicates that the greater the static activation pressure of the explosion venting form, the higher the peak explosion overpressure at each measurement point. Moreover, the shorter the explosion flame duration, the greater the flame propagation velocity. The research results provide an essential theoretical foundation for the effective suppression of gas explosion accidents in the process of low-concentration gas transportation. 相似文献
102.
Ou-Sup Han Masaaki Yashima Toei Matsuda Hidenori Matsui Atsumi Miyake Terushige Ogawa 《Journal of Loss Prevention in the Process Industries》2000,13(6):449-457
The structure of flame propagating through lycopodium dust clouds has been investigated experimentally. Upward propagating laminar flames in a vertical duct of 1800 mm height and 150×150 mm square cross-section are observed, and the leading flame front is also visualized using by a high-speed video camera. Although the dust concentration decreases slightly along the height of duct, the leading flame edge propagates upwards at a constant velocity. The maximum upward propagating velocity is 0.50 m/s at a dust concentration of 170 g/m3. Behind the upward propagating flame, some downward propagating flames are also observed. Despite the employment of nearly equal sized particles and its good dispersability and flowability, the reaction zone in lycopodium particles cloud shows the double flame structure in which isolated individual burning particles (0.5–1.0 mm in diameter) and the ball-shaped flames (2–4 mm in diameter; the combustion time of 4–6 ms) surrounding several particles are included. The ball-shaped flame appears as a faint flame in which several luminous spots are distributed, and then it turns into a luminous flame before disappearance. In order to distinguish these ball-shaped flames from others with some exceptions for merged flames, they are defined as independent flames in this study. The flame thickness in a lycopodium dust flame is observed to be 20 mm, about several orders of magnitude higher than that of a premixed gaseous flame. From the microscopic visualization, it was found that the flame front propagating through lycopodium particles is discontinuous and not smooth. 相似文献
103.
In this paper flame microstructures and propagation characteristic of methane explosion are studied by high speed schlieren photography technique. By experiment it shows that flame front surface and inner flow field of methane explosion has distinctly fractal characteristic, the effect of the wrinkle of flame front surface and inner reactants on flame propagation can be directly reflect by fractal dimensions. Fractal dimension has a direct relation to flame structure and flame propagation characteristics, and it is the important parameter to scale the flame propagation velocity and flame temperature. 相似文献
104.
服装热阻和湿阻的测量与计算 总被引:1,自引:0,他引:1
热阻和湿阻是影响服装热湿舒适性的两个重要参数,其测量方法对于研究和改善服装的热湿舒适性具有重要意义。本文介绍了面料和服装的热阻、湿阻的概念和测量方法,以一件连体型防静电无尘服为例,使用出汗暖体假人"Newton",对其热阻、湿阻进行测量,详细阐述了服装的局部到整体的热阻、湿阻的测量与计算,并分析了服装各个局部热阻、湿阻的特点。 相似文献
105.
随着环保意识的增强,开发高性能生物基环氧树脂以减少对石油基双酚A二缩水甘油醚(DGEBA)和4, 4’-二氨基二苯甲烷(DDM)的依赖越来越受到重视。基于腰果酚、苯酚、甲醛溶液和氯代磷酸二苯酯等原料合成了三种官能团数目可调控的腰果酚基羟基型固化剂(P1C1F-0.6DCP、P2C1F-0.6DCP和P3C1F-0.6DCP)并对其阻燃环氧树脂开展了相应的研究。垂直燃烧和极限氧指数(LOI)结果表明,DGEBA/P1C1F-0.6DCP、DGEBA/P2C1F-0.6DCP和DGEBA/P3C1F-0.6DCP均能通过V-0级别并且LOI值均在29%左右。锥形量热仪测试结果表明,DGEBA/P1C1F-0.6DCP、DGEBA/P2C1F-0.6DCP和DGEBA/P3C1F-0.6DCP的热释放速率峰值(pHRR)分别比DGEBA/DDM降低了68.4%、64.7%和70.7%。通过炭渣的形貌和结构分析,含磷腰果酚基羟基型固化剂的阻燃机理在于能够在燃烧过程中促进形成质量更高的炭渣,发挥更好的隔热、隔氧的效果。 相似文献
106.
Experiments using an open space dust explosion apparatus and a standard 20 L explosion apparatus on nano and micron polymethyl methacrylate dust explosions were conducted to reveal the differences in flame and pressure evolutions. Then the effect of combustion and flame propagation regimes on the explosion overpressure characteristics was discussed. The results showed that the flame propagation behavior, flame temperature distribution and ion current distribution all demonstrated the different flame structures for nano and micron dust explosions. The combustion and flame propagation of 100 nm and 30 μm PMMA dust clouds were mainly controlled by the heat transfer efficiency between the particles and external heat sources. Compared with the cluster diffusion dominant combustion of 30 μm dust flame, the premixed-gas dominant combustion of 100 nm dust flame determined a quicker pyrolysis and combustion reaction rate, a faster flame propagation velocity, a stronger combustion reaction intensity, a quicker heat release rate and a higher amount of released reaction heat, which resulted in an earlier pressure rise, a larger maximum overpressure and a higher explosion hazard class. The complex combustion and propagation regime of agglomerated particles strongly influenced the nano flame propagation and explosion pressure evolution characteristics, and limited the maximum overpressure. 相似文献
107.
Combustible dust explosions continue to present a significant threat toward operating personnel and pneumatic conveyance equipment in a wide variety of processing industries. Following ignition of suspended fuel within a primary enclosure volume, propagation of flame and pressure fronts toward upstream or downstream interconnected enclosures can result in devastating secondary explosions if not impeded through an appropriate isolation mechanism. In such occurrences, an accelerated flame front may result in flame jet ignition within the secondary vessel, greatly increasing the overall explosion severity. Unlike an isolated deflagration event with quantifiable reduced pressures (vent sizing according to NFPA 68 guidance), oscillation of pressure between primary and secondary process vessels leads to uncertain overpressure effects. Dependent on details of the application such as relative enclosure volumes, relief area, fuel type, suspended concentration, duct size, and duct length, the maximum system pressure in both interconnected vessels can be unpredictable. This study proposes the use of FLame ACceleration Simulator (FLACS) computational fluid dynamics (CFD) modeling to provide reliable consequence predictions for specific case scenarios of dust deflagrations involving interconnected equipment. Required minimum supplement to the originally calculated relief area (Av) was determined through iterative simulation, allowing for reduced explosion pressures (Pred) to be maintained below theoretical enclosure design strengths (Pes). 相似文献
108.
109.
The oil industry operates installations and processes with important quantities of flammable substances within a wide range of pressures and temperatures. A particular hazard for this type of installations is an accidental release of a large quantity of flammable material resulting in a devastating vapor cloud explosion.Extensive research was conducted to assess the efficiency of chemicals for inhibition of flames. Especially alkali metal compounds (especially carbonates and bicarbonates of sodium and potassium) have shown to be one of the more efficient flame inhibitor species.In this paper, the principles of flame inhibition by alkali metal compounds are briefly explained. Based on these principles, a practical implementation of an industrial system for chemical inhibition of vapor cloud explosions is discussed. This implementation is based on the use of dry powders of carbonates and bicarbonates of sodium and potassium as flame inhibitor species.The efficiency of the final design of the inhibition system was tested and confirmed on a very large scale in Vapor Cloud Explosion tests in California (US) in September 2016. Several projects in TOTAL were identified in which the VCE inhibition technology is implemented (new cracker units in Daesan (South-Korea) and in Port Arthur (United States)). 相似文献
110.
为探究不同尺寸方形油盘对双馈异步风力发电机组机舱中典型混合油品燃烧特性的影响,自主设计和搭建了热平板诱导油品加热燃烧测定实验系统。将液压油(CALTEXRANDO HDZ32)和齿轮箱油(CALTEXMEROPA320)按1∶1质量(各40.0g)比例均匀混合后,盛装于横截面尺寸分别为6.5cm×6.5cm、10.0cm×10.0cm、13.5cm×13.5cm 的钢制油盘中,利用热平板加热和诱导盘内同样质量混合油品燃烧,利用摄像机记录其燃烧行为和阶段节点时间,利用热电偶树、温度采集模块对油品燃烧对应阶段节点液内和上方火焰中心轴温度分布进行测定。观察发现,液/齿混合油品在加热后出现液内流动、蒸发、冒泡、气化、燃烧、发烟、火焰蹿高等典型传热传质和液相燃烧现象。实验结果表明,随油盘横截面尺寸递增,混合油品着火时间依次缩短(最高1048.0s),燃烧持续时间依次递减(最高1980.0s),燃烧液内最高温度依次升高(最高564.3 ℃),中心轴第一层火焰熄灭温度依次升高(最高489.2 ℃)。小尺寸油盘内油品交流换热过程缓慢,质量损失速率较低,着火前阶段出现最大质量损失速率(0.041g/s);中大尺寸油盘内对流、传质和传热过程明显增强,质量损失速率较高,火焰蹿高节点时出现最大质量损失速率(0.25g/s和0.29g/s) 相似文献