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NATURAL GAS LIQUEFACTION PROCESS FOR LNG

机译:液化天然气的天然气液化工艺

摘要

Embodiments of this invention relate to a process for liquefaction of natural gas and other methane-rich gas streams, and more particularly to a process for producing liquefied natural gas (LNG). In a first step of the process, a first fraction of the feed gas is withdrawn, compressed to a pressure greater than or equal to 1500 psia, cooled and expanded to a lower pressure to cool the withdrawn first fraction. The remaining fraction of the feed stream is cooled by indirect heat exchange with the expanded first fraction in a first heat exchange process. In a second step a separate stream comprising flash vapor is compressed, cooled and expanded to a lower pressure providing another cold stream. This cold stream is used to cool the remaining feed gas stream in a second indirect heat exchange process. The expanded stream exiting from the second heat exchange process is used for supplemental cooling in the first indirect heat exchange step. The remaining feed gas is subsequently expanded to a lower pressure, thereby partially liquefying this feed gas stream. The liquefied fraction of this stream is withdrawn from the process as LNG having a temperature corresponding to the bubble point pressure.
机译:本发明的实施方案涉及液化天然气和其他富含甲烷的气流的方法,更具体地涉及生产液化天然气(LNG)的方法。在该方法的第一步中,进料气体的第一馏分被抽出,压缩至大于或等于1500psia的压力,冷却并膨胀至较低压力以冷却抽出的第一馏分。进料流的剩余部分通过在第一热交换过程中与膨胀的第一部分间接热交换而冷却。在第二步骤中,将包含闪蒸气体的分离流压缩,冷却并膨胀至较低压力,从而提供另一冷流。该冷物流用于在第二间接热交换过程中冷却剩余的进料气流。从第二热交换过程中流出的膨胀流在第一间接热交换步骤中用于补充冷却。随后将剩余的原料气膨胀至较低的压力,从而部分液化该原料气流。该物流的液化馏分以具有对应于起泡点压力的温度的LNG形式从过程中排出。

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