manning en tuberias
DESCRIPTION
Cálculo del flujo por tuberías por gravedad.TRANSCRIPT
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18.00 0.50 0.13 0.79 0.2724.00 0.50 0.28 0.96 0.4630.00 0.50 0.51 1.11 0.60
DIMETRO NOMINAL
(PULG)PENDIENTE
(%)
CAUDAL A TUBO LLENO(M3/S)
VELOCIDADA TUBO LLENO
(M/S)
TIRANTE DE TRABAJO DE TUB.
(M)
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0.09 0.850.26 1.090.98 1.27
CAUDAL A TUBO PARCIALMENTE
LLENO(M3/S)
VELOCIDAD(M/S)
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DETERMINACIN DE TUBERIATUBERIA PEAD CORRUGADA - PLUVIAL
Dia. Nominal : 18 plg0.450 mDia. Interior : 0.457 m
A : 0.16400.0050 m/m0.021 Manning 0.011-0.021 MANUAL TUBERIA CORRUGADA
CAUDAL - TUBO LLENO
1.4357 m0.1143 m
Q = 0.1300130.045 lps
V = 0.7928 m/s
m2
Pendiente S :Coeficiente de friccin n :
Pm =Rh =
m3/s
R_h=A/PmP_m=D Q= A/n Rh^(2/3) S^(1/2)
V=1/n R_h^(2/3)S^(1/2)
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DIMENSIONES TUBO PEAD CORRUGADO PLUVIAL
Diametro Nominal Diametro Interior
Dn Di
4 0.100 0.1020 4.026 0.150 0.1520 5.988 0.200 0.2030 7.99
10 0.250 0.2540 10.0012 0.300 0.3050 12.0115 0.375 0.3810 15.0018 0.450 0.4570 17.9924 0.600 0.6100 24.0230 0.750 0.7620 30.0036 0.900 0.9150 36.0242 1.050 1.0670 42.0148 1.200 1.2190 47.9960 1.500 1.5240 60.00
N-CMT-3-06-10
MANUAL TUBERIA CORRUGADA
-
DETERMINACIN DE TUBERIATUBERIA PEAD CORRUGADA - PLUVIAL
Dia. Nominal : 18 plg0.450 mDia. Interior : 0.457 m
A : 0.10090.0050 m/m0.021 Manning 0.011-0.021 MANUAL TUBERIA CORRUGADA
CAUDAL - TUBO LLENO
0.8013 m0.1259 m
Q = 0.085385.318 lps
V = 0.8458 m/s
m2
Pendiente S :Coeficiente de friccin n :
Pm =Rh =
m3/s
R_h=A/PmP_m=D Q= A/n Rh^(2/3) S^(1/2)
V=1/n R_h^(2/3)S^(1/2)
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MANUAL TUBERIA CORRUGADA
Usar = Ecuacion B
Ecuacion A 0.457
0.27Ecuacion B
=-2arcsen[1-(2y/D)]
=-2arcsen[(2y/D)-1]
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= 3.5068583398
= 3.5068583398
-
DETERMINACIN DE TUBERIATUBERIA PEAD CORRUGADA - PLUVIAL
Dia. Nominal : 24 plg0.600 mDia. Interior : 0.610 m
A : 0.29220.0050 m/m0.021 Manning 0.011-0.021 MANUAL TUBERIA CORRUGADA
CAUDAL - TUBO LLENO
1.9164 m0.1525 m
Q = 0.2809280.886 lps
V = 0.9611 m/s
m2
Pendiente S :Coeficiente de friccin n :
Pm =Rh =
m3/s
R_h=A/PmP_m=D Q= A/n Rh^(2/3) S^(1/2)
V=1/n R_h^(2/3)S^(1/2)
-
DIMENSIONES TUBO PEAD CORRUGADO PLUVIAL
Diametro Nominal Diametro Interior
Dn Di
4 0.100 0.1020 4.026 0.150 0.1520 5.988 0.200 0.2030 7.99
10 0.250 0.2540 10.0012 0.300 0.3050 12.0115 0.375 0.3810 15.0018 0.450 0.4570 17.9924 0.600 0.6100 24.0230 0.750 0.7620 30.0036 0.900 0.9150 36.0242 1.050 1.0670 42.0148 1.200 1.2190 47.9960 1.500 1.5240 60.00
N-CMT-3-06-10
MANUAL TUBERIA CORRUGADA
-
DETERMINACIN DE TUBERIATUBERIA PEAD CORRUGADA - PLUVIAL
Dia. Nominal : 24 plg0.600 mDia. Interior : 0.610 m
A : 0.23640.0050 m/m0.021 Manning 0.011-0.021 MANUAL TUBERIA CORRUGADA
CAUDAL - TUBO LLENO
1.2834 m0.1842 m
Q = 0.2578257.750 lps
V = 1.0902 m/s
m2
Pendiente S :Coeficiente de friccin n :
Pm =Rh =
m3/s
R_h=A/PmP_m=D Q= A/n Rh^(2/3) S^(1/2)
V=1/n R_h^(2/3)S^(1/2)
-
MANUAL TUBERIA CORRUGADA
Usar = Ecuacion B
Ecuacion A 0.610
0.46Ecuacion B
=-2arcsen[1-(2y/D)]
=-2arcsen[(2y/D)-1]
-
= 4.2077720125
= 4.2077720125
-
DETERMINACIN DE TUBERIATUBERIA PEAD CORRUGADA - PLUVIAL
Dia. Nominal : 30 plg0.750 mDia. Interior : 0.762 m
A : 0.45600.0050 m/m0.021 Manning 0.011-0.021 MANUAL TUBERIA CORRUGADA
CAUDAL - TUBO LLENO
2.3939 m0.1905 m
Q = 0.5084508.390 lps
V = 1.1148 m/s
m2
Pendiente S :Coeficiente de friccin n :
Pm =Rh =
m3/s
R_h=A/PmP_m=D Q= A/n Rh^(2/3) S^(1/2)
V=1/n R_h^(2/3)S^(1/2)
-
DIMENSIONES TUBO PEAD CORRUGADO PLUVIAL
Diametro Nominal Diametro Interior
Dn Di
4 0.100 0.1020 4.026 0.150 0.1520 5.988 0.200 0.2030 7.99
10 0.250 0.2540 10.0012 0.300 0.3050 12.0115 0.375 0.3810 15.0018 0.450 0.4570 17.9924 0.600 0.6100 24.0230 0.750 0.7620 30.0036 0.900 0.9150 36.0242 1.050 1.0670 42.0148 1.200 1.2190 47.9960 1.500 1.5240 60.00
N-CMT-3-06-10
MANUAL TUBERIA CORRUGADA
-
DETERMINACIN DE TUBERIATUBERIA PEAD CORRUGADA - PLUVIAL
Dia. Nominal : 30 plg0.750 mDia. Interior : 0.762 m
A : 0.38520.0050 m/m0.021 Manning 0.011-0.021 MANUAL TUBERIA CORRUGADA
CAUDAL - TUBO LLENO
1.6636 m0.2315 m
Q = 0.4891489.056 lps
V = 1.2697 m/s
m2
Pendiente S :Coeficiente de friccin n :
Pm =Rh =
m3/s
R_h=A/PmP_m=D Q= A/n Rh^(2/3) S^(1/2)
V=1/n R_h^(2/3)S^(1/2)
-
MANUAL TUBERIA CORRUGADA
Usar = Ecuacion B
Ecuacion A 0.762
0.6Ecuacion B
=-2arcsen[1-(2y/D)]
=-2arcsen[(2y/D)-1]
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= 4.3663197838
= 4.3663197838
RESUMENCULVERT 18"CULVERT 24"CULVERT 30"