DETERMINATION OF OPERATING PARAMETERS OF A CRYOGENIC TANK FOR LOW-TONNAGE STORAGE OF LNG

N.K. Protozanov, R.A. Shestakov
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Abstract

In the modern world, the gas industry plays a key role in the fuel and energy complex of any country, ensuring energy security and economic development. With the constant consumption of natural gas, there is a need for efficient methods of its transportation and storage. One of the ways of transportation and storage of natural gas is its liquefaction.In the case of low-tonnage liquefied natural gas (LNG) production complexes, where we are talking about small volumes of production of the order of several thousand tons of LNG per year, in comparison with large-tonnage production, where productivity amounts to millions of tons of LNG per year, the efficiency of storage processes comes to the fore, as this allows for reliable and economically feasible operation of small-scale LNG complexes.In this context, determining the operating parameters of cryogenic tanks for low-tonnage storage of liquefied natural gas is becoming an urgent research topic. The method of storing cryogenic products in semi-insulated tanks has a number of advantages, such as low energy consumption, high efficiency, and long storage time.This article is devoted to determining the parameters of the cryogenic tank operation during low-tonnage storage of liquefied natural gas. The study is aimed at determining the parameters of the cryogenic tank operation based on the calculated heat flow to the stored LNG. In this paper, the authors developed and compared various calculation schemes of heat inflow, which considered such factors as heat transfer by radiation, convection and conduction, including heat inflows to LNG through thermal bridges and from the combined-cycle phase of stored liquefied gas.The result of the study is the revealed method for determining the heat flow to LNG stored in a cryogenic tank, which is optimal in terms of the accuracy of the results obtained and the simplicity of calculations. The results of this study can be used in the further development of storage technologies for both liquefied natural gas and other industrial gases.
确定低吨位液化气低温储罐的运行参数
在当今世界,天然气工业在任何国家的燃料和能源综合体中都发挥着关键作用,确保能源安全和经济发展。随着天然气的不断消耗,需要有高效的天然气运输和储存方法。在低吨位液化天然气(LNG)生产联合企业中,我们谈论的是每年生产几千吨液化天然气的小批量生产,而在大吨位生产中,每年的生产量达到数百万吨液化天然气,因此储存过程的效率就显得尤为重要,因为这可以使小规模液化天然气联合企业的运行可靠且经济可行。在这种情况下,确定用于低吨位液化天然气储存的低温储罐的运行参数正成为一个紧迫的研究课题。在半绝热罐中储存低温产品的方法具有能耗低、效率高、储存时间长等诸多优点。该研究旨在根据计算得出的储存液化天然气的热流量确定低温储罐的运行参数。在本文中,作者开发并比较了各种热流计算方案,这些方案考虑了辐射、对流和传导传热等因素,包括通过热桥流入液化天然气的热量和来自存储液化天然气联合循环阶段的热量。研究结果是所揭示的确定存储在低温罐中的液化天然气热流的方法,该方法在所获结果的准确性和计算的简便性方面都是最佳的。这项研究的结果可用于进一步开发液化天然气和其他工业气体的储存技术。
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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