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Exergy and Energy Analysis of Propane Precooled Mixed Refrigerant Process for Liquefaction of Natural Gas

机译:丙烷液化丙烷预冷混合制冷工艺的火用和能量分析。

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In this work, liquefied natural gas (LNG) production cycle by means of Propane Precooled Mixed Refrigerant (PPMR) Process has been studied. Energy and exergy steady equations of equipments in the PPMR cycle have been established. The equipments are described using rigorous thermodynamics and no significant simplification is assumed. Taken some operating parameters as key parameters, influences of these parameters on coefficient of performance (COP) and exergy efficiency of the cascading cycle are analyzed. The results indicate that the PPMR cycle has good performance, with COP and exergy efficiency of 1.725 and 37.78%, respectively, for a typical operating condition. The power consumed for liquefaction of natural gas (NG) is equal to 42.2 MW. Parametric analyses are performed for the PPMR cycle to evaluate the effects of key factors on the performance of this process through simulation calculations. Results show that the COP and exergy efficiency will be improved with increasing of the inlet pressure of mixed refrigerant (MR) compressors, decreasing of the NG and MR temperature after precooling process, outlet pressure of turbine, inlet temperature of MR compressor and NG temperature after cooling in Mean Cryogenic Heat Exchanger (MCHE).
机译:在这项工作中,已经研究了通过丙烷预冷混合制冷剂(PPMR)工艺生产液化天然气(LNG)的过程。建立了PPMR循环中设备的能量和火用稳态方程。使用严格的热力学对设备进行了描述,并且没有任何明显的简化。以一些运行参数为关键参数,分析了这些参数对级联循环的性能系数(COP)和火用效率的影响。结果表明,PPMR循环具有良好的性能,在典型的工作条件下,COP和火用效率分别为1.725和37.78%。液化天然气(NG)所消耗的功率等于42.2兆瓦。对PPMR周期执行参数分析,以通过模拟计算评估关键因素对该过程性能的影响。结果表明,随着混合制冷剂压缩机进口压力的增加,预冷过程中NG和MR温度的降低,涡轮出口压力,MR压缩机进口温度和NG温度的提高,COP和火用效率将得到提高。在平均低温热交换器(MCHE)中冷却。

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