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A realistic vapour phase heat transfer model for the weathering of LNG stored in large tanks

机译:用于储存大型坦克的LNG风化的现实气相传热模型

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A new non-equilibrium model relevant to LNG weathering in large storage tanks under constant pressure has been developed. It treats the heat influx from the surroundings into the vapour and liquid phases separately and allows for heat transfer between the two phases. The main heat transfer mechanisms in the vapour phase are assumed to be advection, due to upward flow of evaporated LNG, and conduction.It has been observed that the vapour temperature increases monotonically as a function of the height, in agreement with recent experimental results. In all the simulations performed the vapour to liquid heat transfer was small, also in line with recent experimental findings, and is estimated to contribute less than 0.3% to boil-off gas rates. The results of this work indicate that the heat transfer by the advective upward flow dominates the energy transfer within the vapour, while the natural convection, in the body of the vapour, can be neglected. The initial liquid filling has a pronounced effect on all the relevant variables, leading to a decrease in vapour temperature and boil-off gas temperature and an increase in boil-off rates. A rule of thumb for estimating the boil-off gas temperature in industrial storage tanks is provided. (C) 2019 Elsevier Ltd. All rights reserved.
机译:开发了一种新的非平衡模型,其在恒定压力下的大型储罐中的LNG风化。它分别将来自周围的热量与蒸汽和液相视为蒸汽和液相,并且允许两相之间的热传递。由于蒸发的LNG的向上流动,假设蒸汽相中的主传热机制是平整的,并且已经观察到蒸汽温度随着高度的函数单调而增加,同时与最近的实验结果单调。在所有模拟中,蒸汽到液体传热小,也符合最近的实验结果,估计促使蒸发汽油速率小于0.3%。这项工作的结果表明,通过方向向上流动的传热主导蒸汽内的能量转移,而在蒸汽体中的自然对流,可以忽略。初始液体填充物对所有相关变量具有明显的影响,导致蒸汽温度和蒸发气体温度降低,蒸发速率增加。提供了一种用于估算工业储罐中蒸汽气体温度的拇指。 (c)2019 Elsevier Ltd.保留所有权利。

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