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Cold exergy recovery during LNG regasification through a closed Brayton cycle

机译:通过封闭的布雷顿循环在液化天然气再气化过程中的冷能回收

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The liquified natural gas (LNG) regasification process is a source of cold exergy capable of being recovered for the exploitation of energy conversion. This paper presents a novel power plant structure that makes use of the LNG regasification process to increase the energy and exergy efficiency. The power plant consists of a closed Brayton cycle (CBC) fuelled by the flue gas released by the natural gas, where the cold exergy of the LNG is used to cool the compressor intake to reduce the compression work. As alternatives, helium and nitrogen are proposed as working fluids for the Brayton cycle. The research study is centred upon energy and exergy analyses, focused on establishing the operating conditions of maximum efficiency and selecting the working fluid, which is best suited for the regasification process. The results show a relevant increase in the overall efficiency approaching 60.82, an exergy efficiency of 59.08% and a specific power of 1.746 MW/(kg/s LNG).
机译:液化天然气(LNG)的再气化过程是一种冷的火用能源,能够将其回收用于能源转化。本文介绍了一种新颖的发电厂结构,该结构利用液化天然气的再气化过程来提高能源和火用效率。该发电厂由以天然气释放的烟气为燃料的密闭布雷顿循环(CBC)组成,在这里,液化天然气的冷能被用来冷却压缩机进气口,以减少压缩功。作为替代方案,提出了氦气和氮气作为布雷顿循环的工作流体。该研究集中在能量和火用分析上,重点是建立最大效率的运行条件并选择最适合再气化过程的工作流体。结果表明,总体效率显着提高,达到60.82,火用效率为59.08%,比功率为1.746 MW /(kg / s LNG)。

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