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Performance improvement of nitrogen expansion liquefaction process for small-scale LNG plant

机译:小型液化天然气厂氮膨胀液化工艺的性能改进

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摘要

Liquefaction of natural gas is usually a kind of high energy consumption process. Therefore, any performance improvement of the liquefaction process will definitely reduce the energy consumption. Nitrogen expansion liquefaction process is regarded as a suitable process for small-scale LNG plant due to its simplicity, quick startup and convenient maintenance. However, the disadvantage of the process is high-energy consumption. An efficient way to lower its energy consumption is to add a precooling cycle. In this paper, two different precooling cycles including propane precooling cycle and R410a precooling cycle are proposed to the nitrogen expansion liquefaction process to improve the liquefaction process performance. Unit energy consumption as an objective function is optimized in terms of several key operating parameters. Based on the optimization results, the effects of the liquefaction rate and methane recovery rate on the process performance are investigated. The thermodynamic analyses are adopted to the processes as well as the two precooling cycles. Furthermore, the exergy analyses of the main equipment are also presented and discussed. The results show that the unit energy consumption for the nitrogen expansion process with R410a precooling and with propane precooling reduce by 22.74% and 20.02% respectively, compared with nitrogen expansion process without precooling.
机译:天然气的液化通常是一种高能耗的过程。因此,液化过程中任何性能的改善都必将减少能耗。氮膨胀液化工艺因其简单,快速启动和维护方便而被认为是小型液化天然气工厂的合适工艺。但是,该方法的缺点是高能耗。降低能耗的有效方法是增加预冷周期。本文针对氮气膨胀液化过程提出了丙烷预冷循环和R410a预冷循环两种不同的预冷循环,以提高液化过程的性能。根据几个关键操作参数优化了单位能耗作为目标函数。根据优化结果,研究了液化率和甲烷回收率对工艺性能的影响。对过程以及两个预冷循环均采用热力学分析。此外,还介绍和讨论了主要设备的火用分析。结果表明,与不进行预冷的氮气膨胀工艺相比,R410a预冷和丙烷预冷氮气膨胀工艺的单位能耗分别降低了22.74%和20.02%。

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