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A novel anti‐freezing methane propellant subcooling approach and its performance analysis

机译:一种新型的抗冻甲烷推进剂过冷方法及其性能分析

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Abstract Using subcooled propellant could improve the overall performance of spacecraft. In cryogenic propellant subcooling process, liquid nitrogen is the most common cold source. For methane propellant, ice blockage may occur in the propellant subcooling operation since the saturation temperature of liquid nitrogen is lower than the freezing temperature of liquid methane. In this paper, a novel anti‐freezing subcooling approach for methane propellant is proposed. By mixing light alkane such as ethane or propane into methane, a methane mixture propellant with lower freezing temperature could be prepared. To guide the propellant preparation, the working principle of the subcooling scheme is introduced, and the thermodynamic performance of the mixed propellant is analyzed. The results show that for the methane–ethane system, the lowest freezing temperature is 72.9?K when the methane mole fraction is about 0.71. Icing‐free subcooling can be achieved in a liquid nitrogen heat exchanger subcooled approach when the methane fraction is controlled within 0.54 to 0.80. For the methane–propane system, the minimum freezing temperature of 72.0?K occurs at the methane fraction of 0.68, and the non‐icing range is about 0.42–0.79. For the methane–ethane–propane ternary system, the lowest solidification temperature even reaches 63.1?K. Moreover, apparent propellant densification could be yielded by the proposed subcooling scheme. In general, the present subcooling scheme can effectively avoid the freezing risk in the methane subcooling process and also prepare a densified methane propellant, and the new scheme is beneficial for fully exploiting the potential performance of the subcooled methane propellant.
机译:摘要 使用过冷推进剂可以提高航天器的整体性能。在低温推进剂过冷过程中,液氮是最常见的冷源。对于甲烷推进剂,由于液氮的饱和温度低于液态甲烷的冻结温度,因此推进剂过冷运行中可能会发生冰堵塞。本文提出了一种新的甲烷推进剂防冻过冷方法。通过将乙烷或丙烷等轻质烷烃混合到甲烷中,可以制备出具有较低冷冻温度的甲烷混合物推进剂。为指导推进剂制备,介绍了过冷方案的工作原理,分析了混合推进剂的热力学性能。结果表明:甲烷-乙烷体系的最低冻结温度为72.9?当甲烷摩尔分数约为0.71时,K.当甲烷分数控制在0.54至0.80之间时,液氮换热器过冷方法可以实现无结冰过冷。对于甲烷-丙烷体系,最低冻结温度为72.0?K出现在0.68的甲烷馏分处,非结冰范围约为0.42-0.79。对于甲烷-乙烷-丙烷三元体系,最低凝固温度甚至达到63.1?K。此外,拟议的过冷方案可以产生明显的推进剂致密化。总的来说,本过冷方案能够有效避免甲烷过冷过程中的冻结风险,同时制备致密甲烷推进剂,有利于充分挖掘过冷甲烷推进剂的潜在性能。

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