q(L/s)h(m)sq^12650300591.839081.17 3.89937248.0395763502002769.829020 1.10793255.39658-8590300537.20770-67.33-2.4353436.17019-5
330
300
300.47210-102.36-3.1482230.75632
-0.57625170.3627
△q 1.69125435502004352.588
0100.43525943.5258873602002848.967022.65
1.46158464.5291-9490100156305.40-5-3.90763781.5269-6350200
2769.829
0-20
-1.1079355.39658-3.11872944.9785
△q
1.650156-100-12-198.08120110
48.533.42-48.50
4270259538.2871033.420.60121117.98956-35502004352.5880-10-0.4352643.52588-2650300591.8390-81.17-3.8993748.03957-1
320389
211.3998-48.96-198.0840.6655841.874080.432162151.4291
△q
-1.42695
流量初分配注:曼宁公式Nm=0.012 m=5.333 k =10.29N^23
1
2
注:管段【1】和【4】为两条平行管道的等效管段。
环号管段编号
s=k*l/D^
m he (m)
L (m)
D (mm)
q(L/s)h(m)sq^1q(L/s)h(m)sq^1
管内流速节点水头地面标高84.2882 4.2047249.88504 1.19243420.0411 1.1124955.510410.637928-65.6387-2.3145335.26164-0.9286-100.669-3.0450430.24815
-1.42417
-0.04236170.9052
△q -0.1239413.07710.74433956.919240.41625724.30016 1.68230869.230340.773498-3.34984-1.75397523.5987-0.42652-20.0411-1.1124955.51041-0.63793
-0.43982705.2587
△q -0.31181-199.50712031.99305-48.50
31.993050.55096717.221450.607248-13.0771-0.7443456.91924-0.41626-84.2882-4.2047249.88504-1.19243-199.50740.5456542.17574-1.67868
-0.35244166.2015
△q
-1.06029
第二次平差
水力分析结果
见第二页
第一次平差
自由水压二页