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面向高马赫数固体超燃的液氨冷却特性

段艳娟 王乐清 姜俞光 刘国柱 杨玉新 范玮

段艳娟, 王乐清, 姜俞光, 等. 面向高马赫数固体超燃的液氨冷却特性[J]. 航空动力学报, 2025, 40(6):20220920 doi: 10.13224/j.cnki.jasp.20220920
引用本文: 段艳娟, 王乐清, 姜俞光, 等. 面向高马赫数固体超燃的液氨冷却特性[J]. 航空动力学报, 2025, 40(6):20220920 doi: 10.13224/j.cnki.jasp.20220920
DUAN Yanjuan, WANG Leqing, JIANG Yuguang, et al. Cooling characteristics of liquid ammonia for hypersonic solid-fueled scramjet[J]. Journal of Aerospace Power, 2025, 40(6):20220920 doi: 10.13224/j.cnki.jasp.20220920
Citation: DUAN Yanjuan, WANG Leqing, JIANG Yuguang, et al. Cooling characteristics of liquid ammonia for hypersonic solid-fueled scramjet[J]. Journal of Aerospace Power, 2025, 40(6):20220920 doi: 10.13224/j.cnki.jasp.20220920

面向高马赫数固体超燃的液氨冷却特性

doi: 10.13224/j.cnki.jasp.20220920
基金项目: 国家自然科学基金(U22B2091,51906207); 航空飞行器热管理与能量利用工业和信息化部重点实验室基金(CEPE2022019)
详细信息
    作者简介:

    段艳娟(1984-),女,高级工程师,博士,主要从事高马赫数固体超燃冲压发动机燃烧及冷却技术等方面的研究工作

    通讯作者:

    姜俞光(1990-),男,副教授,博士,主要从事超燃冲压发动机/爆震发动机先进冷却技术等方面的研究工作。E-mail:jiangyuguang@nwpu.edu.cn

  • 中图分类号: V233.5

Cooling characteristics of liquid ammonia for hypersonic solid-fueled scramjet

  • 摘要:

    拟使用液氨作为新型氮基燃料再生冷却剂,考虑超燃冲压发动机真实工作温度和压力参数,建立三维流动传热裂解模型,分析液氨流动传热特性,并与传统碳氢燃料进行对比。利用PR状态方程和Chung方法,描述液氨和正癸烷的物性参数;基于Lee蒸发模型,计算冷却剂的相变;基于液氨与正癸烷的简化裂解机理,建立再生冷却通道中流体的流动传热裂解模型。数值研究了不同温度、压力下液氨的流动传热特性;对比分析相同条件下,液氨与碳氢燃料的热沉规律。结果表明液氨传热能力随压力上升而提升,压力由3 MPa提升至17 MPa时,平均表面传热系数增幅8.02%;相同质量流量下,以液氨作为冷却剂将大幅提升冷却能力,非裂解区最高壁温降幅度36.3%,裂解区为9.1%。

     

  • 图 1  单通道流动传热模型

    Figure 1.  Flow and heat transfer model in single channel

    图 2  矩形通道计算网格

    Figure 2.  Mesh of rectangular channel

    图 3  不同压力下氨物性参数

    Figure 3.  Physical parameters of ammonia under different pressures

    图 4  外壁面温度数值模拟和实验结果比较

    Figure 4.  Comparison of wall temperature numerical simulation and experimental results

    图 5  非裂解条件不同压力下冷却通道受热壁温分布

    Figure 5.  Temperature contours of the heated wall in the non-cracking zone under different pressures

    图 6  不同亚临界压力下通道平均沿程参数

    Figure 6.  Average thermal parameters under different subcritical pressures

    图 7  不同亚临界压力下通道沿程平均参数

    Figure 7.  Average parameters along the channel under different sub-critical pressures

    图 8  沿程流体平均温度

    Figure 8.  Average fluid temperature along the flow direction

    图 9  不同亚临界压力对应位置截面液氨体积分数

    Figure 9.  Volume fraction of liquid ammonia in the cross section corresponding to different sub-critical pressures

    图 10  不同超临界压力下受热面平均表面传热系数

    Figure 10.  Average surface heat transfer coefficient of heating surface under different supercritical pressures

    图 11  不同超临界压力下通道受热壁面沿程平均温度

    Figure 11.  Average temperature along the channel heating wall under different supercritical pressures

    图 12  超临界压力下z=240 mm处流体导热系数

    Figure 12.  Thermal conductivity of fluid at z=240 mm under supercritical pressure

    图 13  不同超临界压力下通道中心面各参数分布

    Figure 13.  Thermal parameters on channel center surface under different supercritical pressures

    图 14  不同超临界压力下流体沿程平均温度

    Figure 14.  Average fluid temperature along the flow direction under different supercritical pressures

    图 15  不同压力下受热壁面温度分布

    Figure 15.  Temperature contours of the heated wall under different pressures

    图 16  不同压力下通道平均参数分布

    Figure 16.  Average thermal parameters under different pressures

    图 17  不同压力下通道中心面参数分布

    Figure 17.  Thermal parameters of channel center surface under different pressures

    图 18  非裂解区不同qf/mf下受热壁面温度分布

    Figure 18.  Temperature contours of the heated wall under different qf/mf in the non-cracking zone

    图 19  非裂解区不同qf/mf通道内部平均参数分布(Tin=300 K)

    Figure 19.  Average parameter distribution of different qf/mf channels in the non-cracking zone (Tin=300 K)

    图 20  非裂解区不同qf/mf下通道中心面液氨体积分数

    Figure 20.  Volume fraction of liquid ammonia of channel center surface under different qf/mf values in non-cracking zone

    图 21  裂解区不同qf/mf下受热壁面温度分布

    Figure 21.  Temperature contours of the heated wall under different qf/mf values in the cracking zone

    图 22  裂解区不同qf/mf下通道中心面氨质量分数

    Figure 22.  Mass fraction of ammonia of the channel center surface under different qf/mf values in the cracking zone

    图 23  裂解条件下不同qf/mf通道平均参数分布(Tin=680 K)

    Figure 23.  Average thermal parameters of different qf/mf values in the cracking zone (Tin=680 K)

    图 24  同质量流量条件下通道流体域下壁面沿程平均表面传热系数

    Figure 24.  Average heat transfer coefficient along the lower wall of the fluid domain with the same fluid mass flow rate

    图 25  同质量流量条件下受热壁面温度分布

    Figure 25.  Temperature contours of the heated wall with the same fluid mass flow rate

    图 26  3 MPa压力下氨与正癸烷的物理热沉

    Figure 26.  Physical heat sink of ammonia and n-Decane at 3 MPa

    图 27  通道中沿程流体物性

    Figure 27.  Fluid physical properties along the channel

    图 28  同质量流量条件下通道中心面温度分布

    Figure 28.  Temperature contours of the channel center surface with the same fluid mass flow rate

    表  1  单矩形通道网格无关性验证相关信息

    Table  1.   Single rectangular channel mesh independence verification related information

    网格
    编号
    首层网格
    厚度/m
    比例
    因子
    y+ 网格数/106 Tout,av/K
    Mesh A 10−5 1.15 < 1 1.994 480.2
    Mesh B 2.961 475.8
    Mesh C 4.516 473.4
    Mesh D 6.715 473.2
    下载: 导出CSV

    表  2  不同压力下的边界条件参数

    Table  2.   Boundary conditions under different pressures

    qf/(MW/m2 mf/(g/s) pout/MPa
    2 2.75 3
    2 2.75 6
    2 2.75 9
    2 2.75 13
    2 2.75 15
    2 2.75 17
    下载: 导出CSV

    表  3  不同工况下的边界条件参数

    Table  3.   Boundary condition parameters under different working conditions

    工况 qf/
    (MW/m2
    mf/
    (g/s)
    qf/mf)/
    (W·s/(kg·m2))
    pout/
    MPa
    Case a 2.0 3.00 0.667 3
    Case b 2.0 2.75 0.727 3
    Case c 2.5 2.75 0.909 3
    Case d 3.0 2.75 1.091 3
    下载: 导出CSV

    表  4  氨和碳氢燃料冷却能力对比分析计算工况

    Table  4.   Calculation conditions in the comparison of cooling capacities between ammonia and hydrocarbon fuel

    Case 流体种类 Tin/
    K
    mf/
    (g/s)
    pout/
    MPa
    qf/
    (MW/m2
    1 NH3 300 2.75 3 2
    2 C10H22 300 2.75 3 2
    3 NH3 680 2.75 3 2
    4 C10H22 680 2.75 3 2
    下载: 导出CSV
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  • 收稿日期:  2022-11-30
  • 网络出版日期:  2025-03-02

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