秦海玲,李静,周刚,等. 5 t/d氢液化器流程设计及分析[J]. 真空与低温,2024,30(4):355−360. DOI: 10.12446/j.issn.1006-7086.2024.04.002
引用本文: 秦海玲,李静,周刚,等. 5 t/d氢液化器流程设计及分析[J]. 真空与低温,2024,30(4):355−360. DOI: 10.12446/j.issn.1006-7086.2024.04.002
QIN H L,LI J,ZHOU G,et al. Process design and analysis of 5 t/d hydrogen liquefier[J]. Vacuum and Cryogenics,2024,30(4):355−360. DOI: 10.12446/j.issn.1006-7086.2024.04.002
Citation: QIN H L,LI J,ZHOU G,et al. Process design and analysis of 5 t/d hydrogen liquefier[J]. Vacuum and Cryogenics,2024,30(4):355−360. DOI: 10.12446/j.issn.1006-7086.2024.04.002

5 t/d氢液化器流程设计及分析

Process Design and Analysis of 5 t/d Hydrogen Liquefier

  • 摘要: 超大型低温制冷系统是前沿科学装置和高新技术应用等领域的重大支撑装备。在国家重点研发计划课题的支持下,中国科学院理化技术研究所开展了5 t/d大型氢液化装置工艺流程设计工作,以制冷效率、各子系统的相互协调性为目标,通过分析,成功确定 5 t/d液氢制取装备大型低温制冷系统各关键部件的基本规格以及进出口压力、温度、流量等参数,满足了设计需求。为未来大型氢液化器的落地实施和流程的进一步优化提供了指导。

     

    Abstract: The ultra large cryogenic system is a major supporting equipment in cutting-edge scientific devices and high-tech applications. With the support of key deployment projects of the Chinese Academy of Sciences, the Technical Institute of Physics and Chemistry CAS has carried out process design work for a 5 ton per day large-scale hydrogen liquefaction device. Through data exchange technology, the connection between low-temperature physical properties databases of ortho-hydrogen, para-hydrogen, and equilibrium hydrogen and commercial process simulation software has been solved, and a process design and simulation platform for large-scale hydrogen cryogenic machines has been established. On this basis, with the goal of refrigeration efficiency and the coordination of various subsystems, the basic specifications of key components of the large-scale cryogenic system for 5 ton per day liquid hydrogen production equipment, as well as parameters such as inlet and outlet pressure, temperature, and flow rate, were successfully determined through optimization analysis. This has laid the foundation for further design and optimization of the future hydrogen liquefaction process.

     

/

返回文章
返回