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Optimisation of expansion liquefaction processes using mixed refrigerant N-2-CH4

机译:使用N-2-CH4混合制冷剂优化膨胀液化工艺

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摘要

An expansion process with a pre-cooling system is simulated and optimised by Aspen HYSYS and MATLAB (TM). Taking advantage of higher specific refrigeration effect of methane and easily reduced refrigeration temperature of nitrogen, the designed process adopts N-2-CH4 as a mixed refrigerant. Based on the different thermodynamic properties and sensitivity difference of N-2 and CH4 over the same heat transfer temperature range, this work proposes a novel method of matching refrigerant composition which aims at single-stage or multi-stage series expansion liquefaction processes with pre-cooling systems. This novel method is applied successfully in propane pre-cooled N-2-CH4 expansion process, and the unit power consumption is reduced to 7.09 kWh/kmol, which is only 535% higher than the global optimised solutions obtained by genetic algorithm. This novel method can fulfil the accomplishments of low energy consumption and high liquefaction rate, and thus decreases the gap between the mixed refrigerant and expansion processes in energy consumption. Furthermore, the high exergy efficiency of the process indicates good adaptability to varying natural gas compositions. (C) 2015 Elsevier Ltd. All rights reserved.
机译:通过Aspen HYSYS和MATLAB(TM)对预冷系统的膨胀过程进行了仿真和优化。利用甲烷更高的比制冷效果和容易降低氮的制冷温度的优势,设计工艺采用了N-2-CH4作为混合制冷剂。基于相同传热温度范围内N-2和CH4的不同热力学性质和灵敏度差异,这项工作提出了一种新颖的制冷剂成分匹配方法,该方法旨在将单级或多级串联膨胀液化工艺与预冷却系统。该新方法成功地应用于丙烷预冷的N-2-CH4膨胀过程,单位能耗降低到7.09 kWh / kmol,仅比遗传算法获得的全局最优解高535%。该新方法可以实现低能耗,高液化率的目的,从而减小了混合制冷剂与膨胀过程之间的能耗差距。此外,该方法的高火用效率表明其对变化的天然气成分具有良好的适应性。 (C)2015 Elsevier Ltd.保留所有权利。

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