The effect of favorable conditions within chemical process units on vapour cloud explosion overpressures

IF 4.2 3区 工程技术 Q2 ENGINEERING, CHEMICAL Journal of Loss Prevention in The Process Industries Pub Date : 2025-08-01 Epub Date: 2025-03-06 DOI:10.1016/j.jlp.2025.105617
Zhenmin Luo , Gang Wu , Fangming Cheng , Tao Wang
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Abstract

Accidents of flammable gas leaks and explosions are very likely to occur in process units of chemical plants due to various devices. Moreover, these facilities cause serious turbulence in the flow field, which may result in an explosion intensity that is difficult to be observed in previous conventional experiments. In this paper, we used the professional industrial disaster assessment software FLACS to reconstruct a real-size production unit, and obtained explosion overpressures under several cases by changing the size, concentration, location and ignition point of gas clouds. The experimental results demonstrate that the congestion of objects in an open environment can cause the explosion overpressure of cube-shaped gas clouds to reach a threshold sufficient to cause death or serious damage to facilities. However, this is not the case for pancake-shaped clouds. Furthermore, the explosion of confined spaces with large L/D ratios, as well as gas clouds covering multiple confined spaces, produce significantly greater blast overpressures than a single confined space, particularly if the ignition occurs in any one of these confined spaces. For a particular type of confined space, a reasonable method of characterizing the peak overpressure in terms of a degree of confinement parameter is proposed, and the two have a good linear correlation. There exist significant variations in the most sensitive concentrations during the overpressure rise phase corresponding to different operating conditions, whereas the range of most sensitive concentrations during the overpressure decline phase is concentrated within Φ = 1.3–1.4. Finally, the overpressure distribution patterns in the circumferential and elevational directions under a variety of cases are obtained for the most common cylindrical devices, and the determining factors affecting the results are discussed.
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化学过程单元内有利条件对蒸汽云爆炸超压的影响
化工厂工艺单元由于各种装置的存在,极易发生可燃气体泄漏和爆炸事故。此外,这些设施在流场中造成严重的湍流,可能导致以往常规实验难以观察到的爆炸强度。本文利用专业的工业灾害评估软件FLACS对一个实际规模的生产装置进行了重建,通过改变气体云的大小、浓度、位置和着火点,得到了几种情况下的爆炸超压。实验结果表明,开放环境中物体的拥挤会导致立方体气体云的爆炸超压达到足以造成死亡或对设施造成严重破坏的阈值。然而,对于煎饼状的云,情况并非如此。此外,具有大升深比的密闭空间的爆炸,以及覆盖多个密闭空间的气云,会产生比单个密闭空间更大的爆炸超压,特别是当点火发生在这些密闭空间中的任何一个时。对于特定类型的密闭空间,提出了一种用约束度参数来表征峰值超压的合理方法,两者具有良好的线性相关性。不同工况下超压上升阶段最敏感浓度存在显著差异,超压下降阶段最敏感浓度集中在Φ = 1.3 ~ 1.4范围内。最后,对最常见的圆柱形装置在不同工况下的周向和高向超压分布规律进行了分析,并对影响结果的决定因素进行了讨论。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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来源期刊
CiteScore
7.20
自引率
14.30%
发文量
226
审稿时长
52 days
期刊介绍: The broad scope of the journal is process safety. Process safety is defined as the prevention and mitigation of process-related injuries and damage arising from process incidents involving fire, explosion and toxic release. Such undesired events occur in the process industries during the use, storage, manufacture, handling, and transportation of highly hazardous chemicals.
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