采用泄爆管的粉尘爆炸在泄放过程中的压力特性

以2μm铝粉为介质,在内径68mm、高305mm的钢制圆柱容器顶端连接内径25mm、不同长度的钢制泄爆管,开展了粉尘爆炸泄放实验。通过分别改变泄爆管长度及粉尘的质量浓度,研究粉尘爆炸泄放过程中容器及泄爆管内的压力特性,重点在探索泄放过程中二次爆炸发生的条件。结果表明,在本实验条件下,当泄爆管长度LT≥1 500mm,粉尘质量浓度ρ≥500g/m3时,泄爆管内发生二次爆炸的几率很高。二次爆炸产生的压力波分别向爆炸容器及泄爆管末端2个方向传播。向爆炸容器传播的压力波阻碍并扰乱泄放过程,导致容器内残余未燃粉尘反应,使容器内压力出现二次峰值。

泄压与隔爆联用的粉尘爆炸压力特性

作为目前市场上运用最广泛的隔爆产品,隔爆翻板阀一般与泄压板联用,以防止粉尘爆炸传播。为了探究粉尘爆炸时泄压与隔爆联用对容器内压力及隔爆效果的影响,进行了工业规模的粉尘爆炸实验。实验结果表明:由于隔爆翻板阀的影响,容器内部出现了二次峰值压力;随着隔爆翻板阀安装距离的增加,容器内两个峰值压力的时间间隔从28.2 ms增加到62.3 ms,且到达隔爆翻板阀前的峰值压力从0.067 MPa上升至0.101 MPa;泄压面积的增大会导致容器内部和隔爆翻板阀前端峰值压力降低,并可能导致隔爆失败。

瓦斯与煤尘混合物爆炸特性数值模拟仿真

运用Fluent对瓦斯煤尘混合物爆炸过程进行了数值模拟,并对爆炸过程中爆炸超压和火焰温度,进行了分析.结果表明:在爆炸初始3ms内的火焰温度上升速率达到了3 000K/ms,火焰最高温度达到了3 400K.瓦斯煤尘混合物爆炸的最大爆炸超压随着煤尘粒径的增大而减小;当瓦斯浓度为5%,煤尘浓度为390g/m3时,瓦斯煤尘混合物爆炸的最大爆炸超压值最高.该模拟仿真系统的仿真结果为预防煤矿瓦斯、瓦斯煤尘爆炸提供数据基础和参考.

Study on explosion process of methane-coal dust mixture

The experimental system of 10 m3 large-scale multiphase combustion explosion tank was used for research into the explosion development process under the ignition conditions of methane-coal dust-air mixture, and the overpressure development processes of the mixture at different distances were obtained. For the methane-coal dust-air mixture with an equivalence ratio of 1, the explosion pressure and pressure rise rate reached their maximum under a methane concentration of 8% and a coal dust concentration of 25 g/m3, while the maximum explosion pressure and pressure rise rate both occurred 0.5 m away from the ignition point under a methane concentration of between 4.5% and 8%, and a coal dust concentration of between 25 g/m3 and 1 O0 g/m3. Moreover, the greater the explosion intensity of mixture, the closer the occurrence location of maximum overpres- sure was to the ignition source.