M. Henriksen , H.E. Fossum , E. Åkervik , D. Bjerketvedt
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引用次数: 0
Abstract
Hydrogen’s low density and wide flammability range pose significant risks in the event of accidental releases, making understanding its dispersion characteristics crucial for adequate safety measures. The present work investigates the experimental hydrogen dispersion characteristics in a 5.8 m x 0.9 m x 0.8 m open-ended channel with mass flow rates ranging from 0.04 to 1.27 g/s with and without the presence of an obstacle. Twenty-nine hydrogen sensors were used to measure the hydrogen concentration in the air. The experiments are complemented by numerical results using the OpenFOAM® CFD framework, which was published previously. Two distinct dispersion models were identified, dependent on the mass flow rate. For low mass flow rate (low momentum) releases, the dispersion is related to the “filling box” model, resulting in a thin hydrogen cloud, and for high momentum releases, the dispersion is related to the “fading up box” model, characterized by light-fluid intrusion flow. A Froude concentration model that predicts the mean hydrogen concentration in the light-fluid gravity current is presented, which is in good agreement with the experimental results. The results contribute valuable data for validating numerical models.
氢的低密度和广泛的可燃性在意外释放事件中构成重大风险,因此了解其分散特性对于采取适当的安全措施至关重要。本文研究了一个5.8 m x 0.9 m x 0.8 m的开放式通道中氢气的实验分散特性,其质量流率范围为0.04至1.27 g/s,有无障碍物存在。29个氢气传感器被用来测量空气中的氢气浓度。实验与先前发表的OpenFOAM®CFD框架的数值结果相辅相成。确定了两种不同的分散模型,依赖于质量流量。对于低质量流率(低动量)释放,色散与“填充盒”模型有关,导致氢云稀薄;对于高动量释放,色散与“衰落盒”模型有关,特征为轻流体侵入流。提出了一个预测光流体重力流中平均氢浓度的弗劳德浓度模型,该模型与实验结果吻合较好。结果为验证数值模型提供了有价值的数据。
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.