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真实气体效应对SCO2离心压气机气动性能的影响

许鹏程 邹正平 付超 王一帆

许鹏程, 邹正平, 付超, 等. 真实气体效应对SCO2离心压气机气动性能的影响[J]. 航空动力学报, 2025, 40(5):20230498 doi: 10.13224/j.cnki.jasp.20230498
引用本文: 许鹏程, 邹正平, 付超, 等. 真实气体效应对SCO2离心压气机气动性能的影响[J]. 航空动力学报, 2025, 40(5):20230498 doi: 10.13224/j.cnki.jasp.20230498
XU Pengcheng, ZOU Zhengping, FU Chao, et al. Study of real-gas effects on aerodynamic performance of SCO2 centrifugal compressors[J]. Journal of Aerospace Power, 2025, 40(5):20230498 doi: 10.13224/j.cnki.jasp.20230498
Citation: XU Pengcheng, ZOU Zhengping, FU Chao, et al. Study of real-gas effects on aerodynamic performance of SCO2 centrifugal compressors[J]. Journal of Aerospace Power, 2025, 40(5):20230498 doi: 10.13224/j.cnki.jasp.20230498

真实气体效应对SCO2离心压气机气动性能的影响

doi: 10.13224/j.cnki.jasp.20230498
基金项目: 安徽合肥通用机械研究院压缩机技术国家重点实验室开放基金(SKL-YSJ201803)
详细信息
    作者简介:

    许鹏程(1995-),男,博士生,主要从事叶轮机气体动力学研究

    通讯作者:

    邹正平(1970-),男,教授,博士,主要从事高超声速航空发动机、叶轮机气体动力学研究。E-mail:zouzhengping@buaa.edu.cn

  • 中图分类号: V231.3;TH452

Study of real-gas effects on aerodynamic performance of SCO2 centrifugal compressors

  • 摘要:

    利用相似理论和数值模拟对压气机中真实气体气动与工质热物性耦合影响性能的问题进行解耦,对比研究了不同进口工况下超临界二氧化碳离心压气机特性和内部流场,探讨了近临界点真实气体物性变化和冷凝对压气机焓增、效率、堵塞边界的影响。结果表明:真实气体效应的影响可分为蕴含于气动性能参数热力学定义中的热力学影响和蕴含于压气机内部流场中的气动影响,其中气动影响占主导;研究气动影响时可借助相似性能参数排除热力学层面的干扰,当真实气体效应增强时,工质压缩性的减弱将导致叶轮扭速降低从而使相似焓增减小,叶轮负荷的减轻会减小负荷相关气动损失从而使相似效率提升,两相流的存在以及喉道冷凝诱发的提前堵塞会导致堵塞边界的前移。

     

  • 图 1  SCO2压气机几何模型

    Figure 1.  Geometric model of SCO2 compressor

    图 2  MIT CO2喷管试验件及二维计算网格[24]

    Figure 2.  CO2 Laval nozzle from MIT and its 2D mesh[24]

    图 3  Sandia压气机试验件及计算网格[25]

    Figure 3.  Sandia compressor and its computational mesh[25]

    图 4  不同温度分辨率下的比定压热容曲线

    Figure 4.  Curves for constant-pressure specific heat at different temperature resolutions

    图 5  剪切干涉仪拍摄的喷管内部冷凝液滴分布[24]

    Figure 5.  Condensation fog in the nozzle test section photographed by a shear interferometer[24]

    图 6  均相平衡态相变数值模拟得到的喷管内部湿度分布

    Figure 6.  Wetness distribution inside the nozzle obtained by numerical simulation with homogeneous equilibrium model

    图 7  Sandia压气机数值与试验特性曲线对比

    Figure 7.  Comparison of numerical and experimental characteristic curves for the Sandia compressor

    图 8  一维扩张通道的流动参数分布

    Figure 8.  Flow parameter distributions in a 1D diffuser

    图 9  一维收缩通道的流动参数分布

    Figure 9.  Flow parameter distributions in a 1D nozzle

    图 10  沿近临界点等熵线膨胀过程的密流变化

    Figure 10.  Mass flux density distribution in an expansion process along an isentrope

    图 11  沿等熵线的声速变化与喷管马赫数分布

    Figure 11.  Variation of sonic speed along an isentrope and the Ma distribution in the nozzle

    图 12  不同工况的堵塞状态下喉道、相变位置、Ma=1位置的空间分布

    Figure 12.  Spatial distribution of throat, phase-transition position and Ma=1 position under different inlet conditions

    图 13  真实气体效应影响压气机气动性能的分析思路

    Figure 13.  Analytical strategies for real-gas effects on the aerodynamic performance of compressors

    图 14  进口工况对CO2压气机气动性能的热力学影响

    Figure 14.  Thermodynamic effects of inlet conditions on aerodynamic performance of CO2 compressors

    图 15  近临界点与远临界点压缩过程的等熵压缩功对比

    Figure 15.  Comparison of isentropic compression work for compression processes beginning from near and far critical points

    图 16  ΠU =1.33时压气机的特性曲线对比

    Figure 16.  Comparison of the characteristic curves at the speed line ΠU =1.33

    图 17  ΠU=1.33时压气机的相似性能曲线对比

    Figure 17.  Comparison of the similitude performance at the speed line ΠU=1.33

    图 18  设计点进口速度三角形形状对比

    Figure 18.  Comparison of the inlet velocity triangles at design point

    图 19  设计点进口相对欧拉数的展向分布对比

    Figure 19.  Comparison of the inlet spanwise distribution of the relative Eu at design point

    图 20  径向速度增大导致扭速减小

    Figure 20.  Decrease of twisted velocity due to increase in radial velocity

    图 21  设计点不同损失成分的熵产对比

    Figure 21.  Comparison of entropy generation for different losses

    图 22  3个算例中湍流耗散熵产对比

    Figure 22.  Comparison of turbulent dissipative entropy production in three cases

    图 23  3个算例中湍流耗散熵产的各项分量对比

    Figure 23.  Comparison of turbulent dissipative entropy production components in three cases

    图 24  离心叶轮内叶根、叶中、叶尖负荷分布对比

    Figure 24.  Comparison of blade loading at root, mid and tip in impeller

    图 25  离心叶轮内不同流向位置的二次流强度对比

    Figure 25.  Comparison of the secondary flow intensity at different streamwise locations in impeller

    图 26  无叶扩压器内不同流向位置的流动不均匀度对比

    Figure 26.  Comparison of flow non-uniformity at different streamwise locations in vaneless diffuser

    图 27  堵塞工况下进口速度三角形对比

    Figure 27.  Comparison of inlet velocity triangles at choking condition

    图 28  堵塞工况下90%叶高截面的湿度分布对比

    Figure 28.  Comparison of wetness contour on 90% span at choking condition

    图 29  堵塞工况下90%叶高截面的相对马赫数分布对比

    Figure 29.  Comparison of the relative Mach number contour on 90% span at choking condition

    图 30  3个算例中压气机流量增大时进口速度三角形的变化

    Figure 30.  Changes in inlet velocity triangles with increasing mass flow in three cases

    表  1  SCO2压气机设计工况与几何尺寸

    Table  1.   Operation conditions and dimensions of the studied SCO2 compressor

    类型 参数 数值
    设计工况 进口总温T01/K 305
    进口总压p01/kPa 7000
    转速N/(r/min) 50000
    流量$ \dot m $/(kg/s) 20.5
    总压比πtt 3.25
    几何尺寸 进口轮毂半径/mm 10
    进口轮缘半径/mm 25.87
    进口轮缘叶片角/(°) −65
    出口半径/mm 50.57
    出口叶高/mm 4
    出口后弯角/(°) −50
    叶顶间隙/mm 0.2
    主叶片数 9
    分流叶片数 9
    下载: 导出CSV

    表  2  叶轮机通用相似参数

    Table  2.   Similitude parameters for gas turbomachinery

    相似参数 表达式
    流量相似参数$ {\varPi _{\dot m}} $ $ \dfrac{{\dot m\sqrt {{R_{\text{g}}}{T_{01}}} }}{{{p_{01}}}}\sqrt {\dfrac{{{Z_{01}}}}{{{n_{\text{s}}}}}{{\left( {\dfrac{{{n_{\text{s}}} + 1}}{2}} \right)}^{\tfrac{{{n_{\text{s}}} + 1}}{{{n_{\text{s}}} - 1}}}}} $
    转速相似参数$ {\varPi _U} $ $ \dfrac{{{u_2}}}{{\sqrt {{n_{\text{s}}}{Z_{01}}{R_{\text{g}}}{T_{01}}} }} $
    黏性相似参数$ {\varPi _\nu } $ $ \dfrac{{\rho {u_2}{r_2}}}{\mu } $
    焓增相似参数$ {\varPi _{\Delta H}} $ $ \dfrac{{\Delta H}}{{{n_{\text{s}}}{Z_{01}}{R_{\text{g}}}{T_{01}}}} $
    效率相似参数$ {\varPi _\eta } $ $ {\eta _{\text{p}}} $
    下载: 导出CSV

    表  3  3种工质的相似运行工况

    Table  3.   Similar operating conditions for the three fluids

    算例工质T01/Kp01/kPaZ01nsN/(r/min)Re/108
    理想气体理想气体CO2305700011.28568 3002.98
    真实气体真实气体CO230570000.51.38450 0003.24
    近临界点真实气体真实气体CO2 (近临界)30575000.331.47742 2223.25
    下载: 导出CSV

    表  4  真实气体效应在热力学层面和气动层面对等熵效率影响的对比

    Table  4.   Comparison of real-gas effects on isentropic efficiency at thermodynamic and aerodynamic levels %

    算例 效率 效率提升 (相对于理想气体)
    理论ηis(相似转换) 实际ηis(CFD) 热力学层面 气动层面 合计
    理想气体 89.5 89.5
    真实气体 89.8 90.5 +0.3 +0.7 +1.0
    近临界点真实气体 90.1 91.4 +0.6 +1.3 +1.9
    下载: 导出CSV
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  • 收稿日期:  2023-07-31
  • 网络出版日期:  2024-12-22

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