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The Application of Numerical Simulation to Liquid Pipeline Leakage at LNG Terminal in China

机译:数值模拟在中国LNG终端液体管道泄漏的应用

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In 2018, China's natural gas import reached 90.39 million tons, and the liquefied natural gas (LNG) import was 53.78 million tons, accounting for 59.5% of total natural gas imports. With the construction of LNG terminals, more studies on the leakage of LNG storage and transportation facilities have emerged to prevent catastrophic consequences such as explosions and frostbite. However, most of previous researches focused on gas pipeline leakage after LNG gasification, and few of those have been done on LNG liquid pipeline leakage. In this paper, Fluent software is used to numerically simulate the process of LNG liquid pipeline leakage. After the occurrence of LNG leakage, it will suffer the process of endothermic, evaporation, and diffusion, which is considered as a two-phase diffusion process. The Euler-Lagrangian method is introduced to simulate the diffusion process of gas phase and liquid phase separately. In the simulation, the liquid phase is regarded as discrete droplets for discrete processing. The movement trajectory, heat transfer process and evaporation process of each droplet are tracked respectively. Different from the liquid phase, the gas phase is regarded as a continuous phase and the Navier-Stokes equations are adopted for calculation. Thereafter, coupling calculations of two phase are performed to determine the concentration field and temperature field of the LNG liquid pipeline leakage. As a supplement to this research, the influence of wind speed on LNG leakage and diffusion process is analysed in detail. Finally, the numerical simulation method is applied to a coastal LNG terminal in northern China to determine the distribution of natural gas concentration and temperature, as well as delimit the combustion range. The results can provide scientific reference for the delimitation of risky zones and the formulation of emergency response strategy.
机译:2018年,中国的天然气进口达到9039万吨,液化天然气(LNG)进口5378万吨,占天然气总进口的59.5%。随着LNG终端的构建,已经出现了更多关于液化天然气储存和运输设施泄漏的研究,以防止灾难性后果如爆炸和冻伤。然而,以前的大多数研究专注于LNG气化后的气体管道泄漏,并且已经在LNG液体管道泄漏上进行了很少的方法。在本文中,流利的软件用于数字地模拟LNG液体管道泄漏的过程。在液化液晶泄漏后,它将遭受吸热,蒸发和扩散的过程,其被认为是两相扩散过程。引入欧拉拉格朗江法分别模拟气相和液相的扩散过程。在模拟中,液相被视为离散处理的离散液滴。分别跟踪每个液滴的运动轨迹,传热过程和蒸发过程。与液相不同,气相被认为是连续相位,采用Navier-Stokes方程进行计算。此后,进行两相的耦合计算以确定LNG液体管道泄漏的浓度场和温度场。作为本研究的补充,详细分析了风速对LNG泄漏和扩散过程的影响。最后,数值模拟方法应用于北方北部的沿海LNG终端,以确定天然气浓度和温度的分布,以及界定燃烧范围。结果可以为风险区域的划界和应急响应策略的制定提供科学参考。

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