管线压力线计算.xls
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管线压力线计算.xls

管线压力线计算.xls

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输入计算参数面积A2.010619264流量Q2.8水力半径R0.4糙率n0.012→谢才系数C71.53118491圆管直径D1.6流量模数K90.96100584末端测压水位26.2流速V1.392605776序号桩号间距序号间距L沿程水头损失局部水头损失水头损失和各点测压水位hj=(Q*Q/K*K)*Lθζ局部水损1379.26734.225731942518.9171-2139.650.132326399300.0725689420.0071804410.1395068434.08622513533.6672-314.750.013976473300.0725689420.0071804410.02115691334.065068194542.1673-48.50.008054238300.0725689420.0071804410.01523467934.049833515562.0844-519.9170.018872502300.0725689420.0071804410.02605294334.023780566574.1395-612.0550.011422805300.0725689420.0071804410.01860324634.005177327631.5026-757.3630.054354738300.0725689420.0071804410.06153517933.943642148670.7077-839.2050.03714899100.007304220.0007227270.03787171733.905770429682.6618-911.9540.011327102600.3646249850.0360783560.04740545833.8583649610735.6559-1052.9940.05021486600.3646249850.0360783560.08629321633.7720717511743.15810-117.5030.007109524300.0725689420.0071804410.01428996433.7577817812788.39711-1245.2390.042866552300.0725689420.0071804410.05004699333.7077347913846.28212-1357.8850.054849363600.3646249850.0360783560.09092771933.6168070714994.713-14148.4180.140634583100.007304220.0007227270.1413573133.47544976151076.32214-1581.6220.077341535100.007304220.0007227270.07806426233.3973855161424.32215-163480.329749996300.0725689420.0071804410.33693043633.06045506171448.23516-1723.9130.022658942300.0725689420.0071804410.02983938233.03061568181527.38417-1879.1490.074998225300.0725689420.0071804410.08217866632.94843702191624.38418-19970.091913073300.0725689420.0071804410.09909351432.8493435201968.72719-20344.3430.326284778100.007304220.0007227270.32700750532.522336212715.66220-21746.9350.70776383100.007304220.0007227270.70848655731.81384944222798.93521-2283.2730.078905952300.0725689420.0071804410.08608639331.72776305232970.22722-23171.2920.162309012300.0725689420.0071804410.16948945331.55827359243050.69323-2480.4660.076246158300.0725689420.0071804410.08342659931.47484699253076.08724-2525.3940.024062274100.007304220.0007227270.02478500131.45006199263130.4225-