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Duct-venting of dust explosions in a 20 L sphere at elevated static activation overpressures

机译:在静态激活超压升高的情况下,在20 L球体中进行粉尘爆炸的管道通风

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Ducts are often recommended in the design of dust explosion venting in order to discharge materials to safe locations. However, the maximum reduced overpressure increases in a duct-vented vessel rather than in a simply vented vessel. This needs to be studied further for understanding the duct-venting mechanism. Numerous duct-vented dust explosion experiments were conducted, using a 20 L spherical chamber at elevated static activation overpressures, ranging from 1.8 bar to 6 bar. Duct diameters of 15 mm and 28 mm, and duct lengths of 0 m (simply venting), I m and 2 m, were selected. Explosion pressures both in the vessel and in the duct were recorded by pressure sensors, with a frequency of 5 kHz. Flame signals in the duct were also obtained by phototransistors. Results indicate that the secondary explosion occurring in the duct increases the maximum reduced overpressure in the vessel. The secondary explosion is greatly affected by the duct diameter and static activation overpressure, and hence influences the amplification of the maximum reduced overpressure. Larger static activation overpressure decreases the severity of the secondary explosion, and hence decreases the increment in the maximum reduced overpressure. The secondary pressure peak is more obvious as the pressure accumulation is easier in a duct with a smaller diameter. However, the increment of the maximum reduced overpressure is smaller because blockage effect, flame front distortion, and turbulent mixing due to secondary explosion are weaker in a narrow duct. The influence of duct length on the maximum reduced overpressure is small at elevated static activation overpressures, ranging from 1.8 bar to 6 bar at 15 mm and 28 mm duct diameters. (C) 2014 Elsevier Ltd. All rights reserved.
机译:在粉尘爆炸通风的设计中通常建议使用风管,以将物料排放到安全的位置。但是,最大的减小的过压在通气管的容器中而不是在简单排气的容器中增加。这需要进一步研究,以了解管道通风机制。使用20 L球形腔室在升高的静态激活超压(范围为1.8 bar至6 bar)下进行了许多管道通风的粉尘爆炸实验。选择的风管直径为15 mm和28 mm,风管长度为0 m(简单通风),即I m和2 m。容器和管道中的爆炸压力均由压力传感器记录,频率为5 kHz。管道中的火焰信号也通过光电晶体管获得。结果表明,发生在导管中的二次爆炸增加了容器中最大的降低的过压。二次爆炸受到管道直径和静态激活超压的极大影响,因此会影响最大降低超压的放大。较大的静态激活超压降低了二次爆炸的严重性,因此降低了最大降低的超压的增量。由于在直径较小的管道中压力积累更容易,因此次级压力峰值更为明显。但是,最大减小的超压的增量较小,这是因为在狭窄的管道中,由于二次爆炸引起的阻塞效应,火焰前沿变形和湍流混合较弱。在升高的静态激活超压下,风管长度对最大降低的超压的影响很小,风管直径在15 mm和28 mm时范围从1.8 bar到6 bar。 (C)2014 Elsevier Ltd.保留所有权利。

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