4.7 Article

Rethinking ?BLEVE explosion? after liquid hydrogen storage tank rupture in a fire

期刊

INTERNATIONAL JOURNAL OF HYDROGEN ENERGY
卷 48, 期 23, 页码 8716-8730

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PERGAMON-ELSEVIER SCIENCE LTD
DOI: 10.1016/j.ijhydene.2022.09.114

关键词

Liquid hydrogen storage; Tank rupture in fire; Blast wave; CFD model; Validation; BLEVE

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This study aims to develop a CFD model capable of predicting the maximum pressure in the blast wave after the rupture of a liquid hydrogen storage tank in a fire. The research concludes that the maximum pressure is generated by a gaseous phase starting shock enhanced by the combustion reaction of hydrogen. The CFD model is updated to account for the cryogenic conditions of LH2 storage.
The underlying physical mechanisms leading to the generation of blast waves after liquid hydrogen (LH2) storage tank rupture in a fire are not yet fully understood. This makes it difficult to develop predictive models and validate them against a very limited number of experiments. This study aims at the development of a CFD model able to predict maximum pressure in the blast wave after the LH2 storage tank rupture in a fire. The performed critical review of previous works and the thorough numerical analysis of BMW experi-ments (LH2 storage pressure in the range 2.0-11.3 bar abs) allowed us to conclude that the maximum pressure in the blast wave is generated by gaseous phase starting shock enhanced by combustion reaction of hydrogen at the contact surface with heated by the shock air. The boiling liquid expanding vapour explosion (BLEVE) pressure peak follows the gaseous phase blast and is smaller in amplitude. The CFD model validated recently against high-pressure hydrogen storage tank rupture in fire experiments is essentially updated in this study to account for cryogenic conditions of LH2 storage. The simulation results provided insight into the blast wave and combustion dynamics, demonstrating that combustion at the contact surface contributes significantly to the generated blast wave, increasing the overpressure at 3 m from the tank up to 5 times. The developed CFD model can be used as a contemporary tool for hydrogen safety engineering, e.g. for assessment of hazard distances from LH2 storage.(c) 2022 The Author(s). Published by Elsevier Ltd on behalf of Hydrogen Energy Publications LLC. This is an open access article under the CC BY license (http://creativecommons.org/ licenses/by/4.0/).

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