Comparative study of CO2-N2 and N2-N2 dual expansion in natural gas liquefaction process

None Elieze Jackson, None John Vitus Anele, None Peter Odiboroghene Muwarure
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Abstract

The processes were modelled using the Aspen Hysys version 11. The paper compared two refrigeration systems with different refrigerants, CO2-N2 and N2-N2, and their expenders. The parameters compared are the liquefaction power, specific power, production capacity, and heat duty of the expander cycle. The liquefaction power of CO2-N2 (547.669kW) is lower than that of N2-N2 (815.85kW). The specific power consumption for CO2-N2 was 0.44096kW/kg, and for N2-N2 was 0.6569kW/kg. The production capacity N2-N2 gave a higher value of 6945.6MTPA than CO2-N2 4904.38MTPA.
天然气液化过程中CO2-N2和N2-N2双重膨胀的比较研究
这些过程使用Aspen Hysys版本11进行建模。本文比较了CO2-N2和N2-N2两种不同制冷剂的制冷系统及其开销。比较了膨胀机循环的液化功率、比功率、生产能力和热负荷等参数。CO2-N2的液化功率(547.669kW)低于N2-N2的液化功率(815.85kW)。CO2-N2比电耗为0.44096kW/kg, N2-N2比电耗为0.6569kW/kg。N2-N2的生产能力为6945.6MTPA,高于CO2-N2的4904.38MTPA。
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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