水头损失计算

局部水头损失hω（阀门）（m）阻力系数λ局部阻力系数ξ流速Vg0.3971840440.0239282120.4571.886280849.810.5510536890.0239282120.4172.263537019.810.2129503770.022517310.31.615564619.81D0.2141141790.021060392 0.31.753773519.81hω（弯头）阻力系数λ局部阻力系数ξ流速Vg0.3452022180.025360073 0.71.59.810.3069003820.023928212 0.71.59.810.2753175840.022517310.71.59.811.3481093360.023928212 0.73.144 9.81A0.5832257010.022517310.72.183 9.81B1.3481093360.023928212 0.73.144 9.81C0.5832257010.022517310.72.183 9.81D 1.9412774440.023928212 0.73.773 9.81E 1.9412774440.023928212 0.73.773 9.81F 0.8398450090.022517310.72.620 9.81沿程水头损失hf阻力系数λg谢才系数C糙率n 0.2362531080.0239282129.8157.26962890.0090.2499461450.0239282129.8157.26962890.0090.0998492740.02251731 9.8159.03658720.009总水头损失H管径起点值总水头损失H主管道水头63121.32384158813.3275121.41480059713.4190120.86343481912.86hω（三通1）阻力系数λ局部阻力系数ξ流速Vg1.2902910690.025360073 1.13.119 9.811.7511057580.023928212 1.13.144 9.81A0.1857904730.020181836 1.11.132 9.81B0.1857904730.020181836 1.11.132 9.81C0.1857904730.020181836 1.11.132 9.81D0.2675382810.020181836 1.11.358 9.81E 0.2675382810.020181836 1.11.358 9.81F 0.2675382810.020181836 1.11.358 9.81hω（变径）阻力系数λ局部阻力系数ξ流速Vg0.9451129150.023928212 0.33.144 9.81A10.3888794330.022517310.32.183 9.81A20.0972198580.022517310.31.092 9.81B2.2362400970.025360073 0.34.456 9.81C0.9451129150.023928212 0.33.144 9.81D0.2141141790.021060392 0.31.754 9.81D0.8050464350.025360073 0.32.673 9.81E 1.3609625980.023928212 0.33.773 9.81E 0.8050464350.025360073 0.32.673 9.81F 0.5599863830.022517310.32.620 9.81F 0.8050464350.025360073 0.32.673 9.81hω（三通2）阻力系数λ局部阻力系数ξ流速VgA0.7775719690.022517311.12.183 9.81B1.7511057580.023928212 1.13.144 9.81C0.7775719690.022517311.12.183 9.81D0.4649375450.021060392 1.11.754 9.81E 2.5215922910.023928212 1.13.773 9.81F 1.1197036350.022517311.12.620 9.81总损...