calculo de tuberías

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e 0.00016 D 0.0508 ⱴ(visc 1.14E-06 Ta 15 V supuesto F V (calculada) 3.31 147498.246 0.02738257 3.763589198 NO 3.764 167710.817 0.02718811 3.776247406 NO 3.776 168274.884 0.027063 3.784459246 NO 3.784 168640.816 0.02697763 3.790093868 NO 3.790 168891.902 0.02691541 3.794216268 NO 3.794 169075.602 0.02728279 3.770068659 NO 3.770 167999.551 6.02738257 0.26126485 NO Re=Dϒ/ⱴ

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Hoja1e0.00016D0.0508(viscocidad cinematica)0.00000114Ta15

V supuestoRe=D/FV (calculada)1/raiz(f)colebrooka-b3.31147498.2456140350.02738256833.7635891976NO6.04314354096.04291993840.00023.764167710.8168744140.02718811293.7762474056NO6.06471598666.05400632480.01073.776168274.8843885540.02706300483.7844592463NO6.07871794916.05409450730.02463.784168640.8155348010.02697763093.7900938675NO6.08832876596.05414414930.03423.790168891.9021673630.02691541043.7942162678NO6.09536191166.05417206260.04123.794169075.6021094890.02728278613.770068659NO6.05418434366.0548284375-0.00063.770167999.5507685346.02738256830.2612648504NO0.40731989316.1360311439-5.7287

METODO 1Ks/D0.001Re200000Fi0.001E0.00000001NFiXg(x)Fi+1prueba10.0010031.622786.351570.02479NO20.024796.351576.911910.02093NO30.020936.911916.894630.02104NO40.021046.894636.895160.02103NO50.021036.895166.895140.02103NO60.021036.895146.895140.02103OK70.021036.895146.895140.02103OK80.021036.895146.895140.02103OK90.021036.895146.895140.02103OK100.021036.895146.895140.02103OK110.021036.895146.895140.02103OK120.021036.895146.895140.02103OK130.021036.895146.895140.02103OK140.021036.895146.895140.02103OK150.021036.895146.895140.02103OK

METODO NEWTON RAPHSONA (m^2)0.0177Q(m^3/s)0.042V(m/s)2.3728813559L(m)970XiF(xi)F'(xi)Xi+1|xi+1-xi|QdHLVp|Vi