Page 249 - 《振动工程学报》2026年第5期
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第 5 期                 麦耘翔,等:外流与段塞内流联合作用下弹性管流致振动特性研究                                        1453


                                                                             ∆f in (−0.008,0.042,−1.021)
                     1.0    ∆f in (−0.065,0.068,−0.024) =4.3%     1.0   l/L=0.96  ∆f ex (1.612,0.087,−0.316)  =62.1%
                        l/L=0.96  ∆f ex (2.251,0.151,−0.109)
                     0.9                                          0.9       l/L=0.86  ∆f in (−0.185,0.021,−0.532)  =38.1%
                                ∆f in (−0.237,0.060,−0.035)                       ∆f ex (1.448,0.077,0.285)
                                         =10.9%
                     0.8    l/L=0.86  ∆f ex (2.046,−0.079,0.969)  0.8                 ∆f in (0.308,0.044,1.180)  =40.8%
                                    ∆f in (0.017,0.073,−0.234)                   l/L=0.76  ∆f ex (0.522,0.008,2.942)
                     0.7      l/L=0.76  ∆f ex (2.142,0.098,0.286)  =11.4%  0.7  ∆f in (0.140,0.035,−0.184)
                                                                                     =12.9%  l/L=0.66
                                       ∆f in (0.143,0.069,−0.048)           ∆f ex (1.819,0.043,−0.006)
                     0.6           l/L=0.66     =12.3%            0.6
                                       ∆f ex (1.301,0.040,0.376)             ∆f in (−0.350,0.015,−0.676) =73.8%  l/L=0.56
                    l / L  0.5      l/L=0.56  ∆f in (−0.340,0.062,−0.215)  =18.7%  l / L  0.5  ∆f ex (1.029,0.002,0.089)
                                                                             ∆f in (0.181,−0.042,1.649)
                                         ∆f ex (2.010,0.019,−0.830)
                     0.4            l/L=0.46  ∆f in (0.295,0.068,0.101)  0.4  ∆f ex (2.580,−0.035,0.278) =64.0%  l/L=0.46
                                         ∆f ex (2.063,−0.018,−0.493)  =15.0%        l/L=0.36  ∆f in (0.022,0.057,−0.372)  =19.1%
                     0.3           l/L=0.36  ∆f in (0.106,0.064,−0.110)  =14.8%  0.3  l/L=0.26  ∆f ex (1.801,−0.077,0.804)
                                        ∆f ex (1.003,−0.029,−0.499)                  ∆f in (−0.076,0.021,−0.325)
                                l/L=0.26  ∆f in (−0.290,0.077,−0.098)                          =14.5%
                     0.2                      =13.9%              0.2        l/L=0.16  ∆f ex (2.239,−0.111,−0.567)
                            l/L=0.16  ∆f ex (2.227,−0.111,−0.402)                ∆f in (2.088,−0.113,0.193)
                                 ∆f in (−0.035,0.066,0.140)              l/L=0.06         =62.2%
                     0.1  l/L=0.06  ∆f ex (1.613,−0.098,−0.452)  =9.5%  0.1       ∆f ex (0.094,0.059,1.301)
                           ∆f in (0.333,0.050,0.060)                        ∆f in (0.103,−0.081,1.288)  =89.9%
                      0   ∆f ex (1.732,−0.087,−0.033)  =19.7% ∆f in _total  −2.0  0  ∆f ex (1.522,−0.045,0.253)  −0.5
                      0  2   4        ∆f ex _total  =12.9%  −1.0  −1.5  0  2       ∆f in _total  =46.5%  0
                                                                                   ∆f ex _total
                                 6
                                    8  10  0  −0.5                        4  6   8           d CF  / D
                             d IL  / D          d CF  / D                d IL  / D  10 0.5
                        (a) ε g=0.1时,内/外流体力瞬时力比与对应相云图                (b) εg=0.3时,内/外流体力瞬时力比与对应相云图
                     (a) ε g =0.1, the instantaneous forces ratio and contour of phases  (b) ε g=0.3, the instantaneous forces ratio and contour of phases
                       related to internal flow and external current  related to internal flow and external current
                         2                                            2
                                        方差     时均值                                  方差     时均值
                         1                                            1
                         0                                            0
                           0.06  0.26  0.46  0.66  0.86                 0.06  0.26  0.46  0.66  0.86
                                       l / L                                         l / L
                          (c) εg=0.1时,内/外流体力比值时均值与方差                   (d) ε g=0.3时,内/外流体力比值时均值与方差
                       (c) ε g=0.1, the time-average values and variances of the  (d) ε g =0.3, the time-average values and variances of the
                         hydrodynamic forces related to internal flow and  hydrodynamic forces related to internal flow and
                         external current                              external current

                                    图 7 沿管轴向内流与外流作用力瞬时比值、相云图、时均值及方差
              Fig. 7 Instantaneous ratio, contour of phases, time-average values and variances of the hydrodynamic forces related to internal flow
                    and external current along the pipe axis

                                                                               ∆f in (−0.152,0.016,−0.097)
                               ∆f in (0.281,0.043,0.331)                   l/L=0.96      =7.6%
                                        =35.5%                    1.0          ∆f ex (1.956,0.117,−1.319)  l/L=0.86
                   1.0     l/L=0.96  ∆f ex (0.668,0.054,1.030)                      ∆f in (−0.189,0.033,−0.005)
                        ∆f in (0.367,0.068,0.267)                               l/L=0.86      =8.7%
                   0.9  ∆f ex (1.239,0.063,0.401) =35.2%  l/L=0.86  0.9              ∆f ex (2.045,0.117,−0.836)
                                                                            ∆f in (−0.009,0.015,−0.004)
                            ∆f in (−0.304,0.027,−0.466)           0.8                =0.8%  l/L=0.76  l/L=0.66
                   0.8      ∆f ex (1.907,0.066,0.552)  =28.0%  l/L=0.76     ∆f ex (2.246,0.099,−0.707)
                                                                               ∆f in (0.022,0.011,0.024)
                   0.7        ∆f in (−0.046,0.018,−0.032)  =3.3%  l/L=0.66  0.7  ∆f ex (1.779,0.051,−0.006) =1.9%  l/L=0.66
                              ∆f ex (1.494,0.048,0.955)
                   0.6          ∆f in (0.306,0.029,0.743)  =33.3%  l/L=0.56  0.6  ∆f in (−0.056,0.034,−0.148)  =8.3%  l/L=0.56  l/L=0.46
                                ∆f ex (0.827,−0.020,2.273)                      ∆f ex (1.604,−0.004,−1.111)
                   l / L  0.5  ∆f ex (−0.314,0.023,−2.678)  =34.9%  l/L=0.46  l / L  0.5  ∆f ex (1.714,−0.027,−0.946)  =6.2%  l/L=0.46
                                                                                 ∆f in (−0.054,0.044,0.100)
                                ∆f in (0.238,0.051,−0.909)
                   0.4        ∆f in (−0.163,0.037,0.034)  =15.4%  l/L=0.36  0.4  ∆f in (−0.017,0.008,0.026)  =1.8%  l/L=0.36  l/L=0.26
                             ∆f ex (1.070,−0.031,−0.285)                       ∆f ex (1.678,−0.051,0.598)
                            ∆f in (0.016,0.002,0.170)                       ∆f in (0.011,0.004,−0.108)
                   0.3      ∆f ex (2.259,−0.108,0.877)  =7.0%  l/L=0.26  0.3  ∆f ex (1.421,−0.082,0.924) =6.4%  l/L=0.26
                                                                                 l/L=0.16  ∆f in (−0.006,0.009,0.211)
                   0.2          l/L=0.16 ∆f in (0.256,0.038,−0.449)  =40.4%  0.2              =8.9%  l/L=0.06
                                                                                     ∆f ex (1.981,−0.106,1.289)
                           l/L=0.06  ∆f ex (0.209,−0.004,−1.266)            l/L=0.06 ∆f in (0.061,0.052,−0.121)
                   0.1         ∆f in (0.431,0.038,−1.024)  =56.9%  0.1         ∆f ex (1.507,−0.068,1.072)  =7.9%
                               ∆f ex (0.639,−0.042,−1.846)
                     0              ∆f in _total   −0.5             0              ∆f in _total  =5.9%  −0.2
                     0  2  4       ∆f ex _total  =28.8%  0          0  2  4        ∆f ex _total  0.2  0
                              6
                                  8  10 1.0  0.5                             6   8  10 1.0  0.4
                            d IL  / D        d CF  / D                     d IL  / D        d CF  / D
                       (a) ε g=0.5时,内/外流体力瞬时力比与对应相云图                 (b) εg=0.7时,内/外流体力瞬时力比与对应相云图
                    (a) ε g =0.5, the instantaneous forces ratio and contour of phases  (b) ε g=0.7, the instantaneous forces ratio and contour of phases
                      related to internal flow and external current  related to internal flow and external current
                      0.4             方差     时均值                     0.4            方差     时均值
                      0.2                                            0.2
                       0                                              0
                         0.06  0.26  0.46  0.66  0.86                   0.06  0.26  0.46  0.66  0.86
                                     l / L                                          l / L
                        (c) εg=0.5时,内/外流体力比值时均值与方差                     (d) ε g=0.7时,内/外流体力比值时均值与方差
                     (c) ε g=0.5, the time-average values and variances of the  (d) ε g =0.7, the time-average values and variances of the
                       hydrodynamic forces related to internal flow and  hydrodynamic forces related to internal flow and
                       external current                               external current

                             图 8 沿管轴向内流与外流作用力瞬时比值、相云图、时均值、方差及选定截面涡量图
              Fig. 8 Instantaneous ratio, contour of phases, time-average values and variances of the hydrodynamic forces related to internal flow
                    and external current along the pipe axis and vorticity magnitude contours of the selected section
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