InformeFinal2 Tablas
13
III. RESULTADO DE LABORATORIO. Numero de Reynolds Tablas y Graficas. Nro. Prueba d u (m2/s) Q R'e A (m2) v (m/s) Re (mm) (m) (Lt/H) (m3/s) (4*Q)/(u*d*π) (v*d)/u 1 12 0.012 0.00000105 15 4.17E-06 421.04 0.0001131 0.04 457.14 2 12 0.012 0.00000105 25 6.94E-06 701.74 0.0001131 0.06 685.71 3 12 0.012 0.00000105 35 9.72E-06 982.44 0.0001131 0.09 1028.57 4 12 0.012 0.00000105 45 1.25E-05 1263.13 0.0001131 0.11 1257.14 5 12 0.012 0.00000105 55 1.53E-05 1543.83 0.0001131 0.14 1600.00 6 12 0.012 0.00000105 65 1.81E-05 1824.53 0.0001131 0.16 1828.57 7 12 0.012 0.00000105 75 2.08E-05 2105.22 0.0001131 0.18 2057.14 8 12 0.012 0.00000105 85 2.36E-05 2385.92 0.0001131 0.21 2400.00 9 12 0.012 0.00000105 95 2.64E-05 2666.62 0.0001131 0.23 2628.57 10 12 0.012 0.00000105 105 2.92E-05 2947.31 0.0001131 0.26 2971.43 400.00 800.00 1200.00 1600.00 2000.00 2400.00 2800.00 3200.00 NRO. DE REYNOLDS (RE) CAUDAL (Q EN M3/S) NÚMERO DE REYNOLDS VS CAUDAL R'e Re 400.00 800.00 1200.00 1600.00 2000.00 2400.00 2800.00 3200.00 0.04 0.06 0.09 0.11 0.14 0.16 0.18 0.21 0.23 0.26 NRO. DE REYNOLDS (RE) VELOCIDAD(V EN M/S) NÚMERO DE REYNOLDS VS VELOCIDAD R'e Re
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InformeFinal2 Tablas
Transcript of InformeFinal2 Tablas
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III. RESULTADO DE LABORATORIO.
Numero de Reynolds Tablas y Graficas.
Nro. Prueba d u (m2/s) Q R'e A (m2) v (m/s) Re
(mm) (m) (Lt/H) (m3/s) (4*Q)/(u*d*) (v*d)/u
1 12 0.012 0.00000105 15 4.17E-06 421.04 0.0001131 0.04 457.14
2 12 0.012 0.00000105 25 6.94E-06 701.74 0.0001131 0.06 685.71
3 12 0.012 0.00000105 35 9.72E-06 982.44 0.0001131 0.09 1028.57
4 12 0.012 0.00000105 45 1.25E-05 1263.13 0.0001131 0.11 1257.14
5 12 0.012 0.00000105 55 1.53E-05 1543.83 0.0001131 0.14 1600.00
6 12 0.012 0.00000105 65 1.81E-05 1824.53 0.0001131 0.16 1828.57
7 12 0.012 0.00000105 75 2.08E-05 2105.22 0.0001131 0.18 2057.14
8 12 0.012 0.00000105 85 2.36E-05 2385.92 0.0001131 0.21 2400.00
9 12 0.012 0.00000105 95 2.64E-05 2666.62 0.0001131 0.23 2628.57
10 12 0.012 0.00000105 105 2.92E-05 2947.31 0.0001131 0.26 2971.43
400.00800.00
1200.001600.002000.002400.002800.003200.00
NR
O. D
E R
EYN
OLD
S (R
E)
CAUDAL (Q EN M3/S)
NMERO DE REYNOLDS VS CAUDAL
R'e
Re
400.00
800.00
1200.00
1600.00
2000.00
2400.00
2800.00
3200.00
0 . 0 4 0 . 0 6 0 . 0 9 0 . 1 1 0 . 1 4 0 . 1 6 0 . 1 8 0 . 2 1 0 . 2 3 0 . 2 6
NR
O. D
E R
EYN
OLD
S (R
E)
VELOCIDAD(V EN M/S)
NMERO DE REYNOLDS VS VELOCIDAD
R'e
Re
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Cargas Distribuidas en Tuberas Tablas y Graficas.
Perdida de Carga Distribuidas en la Tuberia T1
Caracteristicas del Tubo
Tipo de Tubo "T1"
Rugosidad ( e )
0.007 Diametro (d) 16 mm = 0.016 m e/d
0.006
Longitud (l) 1270 mm = 1.270 m Viscosidad (m2/s)
0.00000105 Comparacion de los Valores Experimentales y Teoricos
Prueba Q Q Re f P P P/l J (Darcy) (Blasius) (Moody)
N (m3/h) (m3/s)
(mmHg) (Pa) (mmHg/m) (exper.) k J Re K J J
1 0.20 0.0001 4210.45 0.298 3 399.96 187.50 0.032 0.004 0.013 4420.97 0.003 0.009 0.072
2 0.30 0.0001 6315.67 0.296 5 666.60 312.50 0.054 0.004 0.028 6631.46 0.003 0.019 0.162
3 0.40 0.0001 8420.90 0.295 8 1066.56 500.00 0.086 0.004 0.050 8841.94 0.003 0.032 0.287
4 0.50 0.0001 10526.12 0.294 10 1333.20 625.00 0.107 0.004 0.078 11052.43 0.003 0.047 0.447
5 0.60 0.0002 12631.34 0.293 12 1599.84 750.00 0.128 0.004 0.113 13262.91 0.002 0.064 0.642
6 0.70 0.0002 14736.57 0.293 16 2133.12 1000.00 0.171 0.004 0.154 15473.40 0.002 0.084 0.873
7 0.80 0.0002 16841.79 0.293 20 2666.40 1250.00 0.214 0.004 0.201 17683.88 0.002 0.107 1.140
8 0.90 0.0003 18947.02 0.293 24 3199.68 1500.00 0.257 0.004 0.254 19894.37 0.002 0.131 1.441
9 1.00 0.0003 21052.24 0.292 30 3999.60 1875.00 0.321 0.004 0.314 22104.85 0.002 0.158 1.778
10 1.25 0.0003 26315.30 0.292 44 5866.08 2750.00 0.471 0.004 0.490 27631.07 0.002 0.233 2.776
11 1.50 0.0004 31578.36 0.292 58 7732.56 3625.00 0.621 0.004 0.706 33157.28 0.002 0.320 3.994
12 1.75 0.0005 36841.42 0.292 76 10132.32 4750.00 0.813 0.004 0.961 38683.49 0.002 0.420 5.434
13 2.00 0.0006 42104.48 0.292 96 12798.72 6000.00 1.027 0.004 1.255 44209.71 0.002 0.530 7.094
Perdida de Carga Distribuidas en la Tuberia T2
Caracteristicas del Tubo
Tipo de Tubo "T2"
Rugosidad ( e )
0.007 Diametro (d) 10 mm = 0.01 m e/d
0.006
-
Longitud (l) 1270 mm = 1.270 m Viscosidad (m2/s)
0.00000105 Comparacion de los Valores Experimentales y Teoricos
Prueba Q Q Re f P P P/l J (Darcy) (Blasius) (Moody)
N (m3/h) (m3/s)
(mmHg) (Pa) (mmHg/m) (exper.) k J Re K J J
1 0.20 0.0001 6736.72 0.484 2 266.64 200.00 0.02 0.006 0.180 7073.55 0.003 0.088 1.235
2 0.30 0.0001 10105.08 0.482 40 5332.80 4000.00 0.43 0.006 0.406 10610.33 0.003 0.179 2.768
3 0.40 0.0001 13473.43 0.481 62 8265.84 6200.00 0.66 0.006 0.721 14147.11 0.002 0.296 4.911
4 0.50 0.0001 16841.79 0.481 88 11732.16 8800.00 0.94 0.006 1.127 17683.88 0.002 0.437 7.664
5 0.60 0.0002 20210.15 0.480 118 15731.76 11800.00 1.26 0.006 1.622 21220.66 0.002 0.601 11.027
6 0.70 0.0002 23578.51 0.480 152 20264.64 15200.00 1.63 0.006 2.208 24757.44 0.002 0.787 15.000
7 0.80 0.0002 26946.87 0.480 193 25730.76 19300.00 2.07 0.006 2.884 28294.21 0.002 0.994 19.582
8 0.90 0.0003 30315.23 0.480 234 31196.88 23400.00 2.50 0.006 3.650 31830.99 0.002 1.222 24.774
9 1.00 0.0003 33683.59 0.480 283 37729.56 28300.00 3.03 0.006 4.506 35367.77 0.002 1.469 30.576
10 1.25 0.0003 42104.48 0.479 404 53861.28 40400.00 4.32 0.006 7.041 44209.71 0.002 2.171 47.749
11 1.50 0.0004 50525.38 0.479 592 78925.44 59200.00 6.33 0.006 10.139 53051.65 0.002 2.987 68.733
12 1.75 0.0005 58946.28 0.479 796 106122.72 79600.00 8.52 0.006 13.800 61893.59 0.002 3.912 93.527
13 2.00 0.0006 67367.17 0.479
Perdida de Carga Distribuidas en la Tuberia T3
Caracteristicas del Tubo
Tipo de Tubo "T3"
Rugosidad ( e )
0.007 Diametro (d) 15.5 mm = 0.0155 m e/d
0.006
Longitud (l) 1270 mm = 1.270 m Viscosidad (m2/s)
0.00000105 Comparacion de los Valores Experimentales y Teoricos
Prueba Q Q Re f P P P/l J (Darcy) (Blasius) (Moody)
N (m3/h) (m3/s)
(mmHg) (Pa) (mmHg/m) (exper.) k J Re K J J
1 0.20 0.0001 4346.27 0.307 2 266.64 129.03 0.02 0.004 0.015 4563.58 0.003 0.011 0.087
-
2 0.30 0.0001 6519.40 0.305 13 1733.16 838.71 0.14 0.004 0.034 6845.37 0.003 0.022 0.195
3 0.40 0.0001 8692.54 0.303 20 2666.40 1290.32 0.21 0.004 0.060 9127.17 0.003 0.037 0.346
4 0.50 0.0001 10865.67 0.303 32 4266.24 2064.52 0.34 0.004 0.094 11408.96 0.003 0.054 0.539
5 0.60 0.0002 13038.81 0.302 42 5599.44 2709.68 0.45 0.004 0.135 13690.75 0.002 0.075 0.775
6 0.70 0.0002 15211.94 0.302 52 6932.64 3354.84 0.56 0.004 0.184 15972.54 0.002 0.098 1.054
7 0.80 0.0002 17385.08 0.302 66 8799.12 4258.06 0.71 0.004 0.240 18254.33 0.002 0.124 1.376
8 0.90 0.0003 19558.21 0.301 81 10798.92 5225.81 0.87 0.004 0.304 20536.12 0.002 0.152 1.740
9 1.00 0.0003 21731.35 0.301 104 13865.28 6709.68 1.11 0.004 0.375 22817.91 0.002 0.183 2.147
10 1.25 0.0003 27164.18 0.301 141 18798.12 9096.77 1.51 0.004 0.586 28522.39 0.002 0.271 3.352
11 1.50 0.0004 32597.02 0.301 218 29063.76 14064.52 2.33 0.004 0.844 34226.87 0.002 0.373 4.823
12 1.75 0.0005 38029.85 0.301 304 40529.28 19612.90 3.25 0.004 1.149 39931.35 0.002 0.488 6.561
13 2.00 0.0006 43462.69 0.301 356 47461.92 22967.74 3.81 0.004 1.501 45635.83 0.002 0.616 8.566
Perdida de Carga Distribuidas en la Tuberia T4
Caracteristicas del Tubo
Tipo de Tubo "T4"
Rugosidad ( e )
0.007 Diametro (d) 15.5 mm = 0.0155 m e/d
0.006
Longitud (l) 1270 mm = 1.270 m Viscosidad (m2/s)
0.00000105 Comparacion de los Valores Experimentales y Teoricos
Prueba Q Q Re f P P P/l J (Darcy) (Blasius) (Moody)
N (m3/h) (m3/s)
(mmHg) (Pa) (mmHg/m) (exper.) k J Re K J J
1 0.20 0.0001 4346.27 0.307 2 266.64 129.03 0.02 0.004 0.015 4563.58 0.003 0.011 0.087
2 0.30 0.0001 6519.40 0.305 11 1466.52 709.68 0.12 0.004 0.034 6845.37 0.003 0.022 0.195
3 0.40 0.0001 8692.54 0.303 18 2399.76 1161.29 0.19 0.004 0.060 9127.17 0.003 0.037 0.346
4 0.50 0.0001 10865.67 0.303 30 3999.60 1935.48 0.32 0.004 0.094 11408.96 0.003 0.054 0.539
5 0.60 0.0002 13038.81 0.302 41 5466.12 2645.16 0.44 0.004 0.135 13690.75 0.002 0.075 0.775
6 0.70 0.0002 15211.94 0.302 54 7199.28 3483.87 0.58 0.004 0.184 15972.54 0.002 0.098 1.054
-
7 0.80 0.0002 17385.08 0.302 68 9065.76 4387.10 0.73 0.004 0.240 18254.33 0.002 0.124 1.376
8 0.90 0.0003 19558.21 0.301 87 11598.84 5612.90 0.93 0.004 0.304 20536.12 0.002 0.152 1.740
9 1.00 0.0003 21731.35 0.301 108 14398.56 6967.74 1.16 0.004 0.375 22817.91 0.002 0.183 2.147
10 1.25 0.0003 27164.18 0.301 146 19464.72 9419.35 1.56 0.004 0.586 28522.39 0.002 0.271 3.352
11 1.50 0.0004 32597.02 0.301 231 30796.92 14903.23 2.47 0.004 0.844 34226.87 0.002 0.373 4.823
12 1.75 0.0005 38029.85 0.301 337 44928.84 21741.94 3.61 0.004 1.149 39931.35 0.002 0.488 6.561
13 2.00 0.0006 43462.69 0.301 374 49861.68 24129.03 4.00 0.004 1.501 45635.83 0.002 0.616 8.566
0.000
1.000
2.000
3.000
4.000
5.000
6.000
0.0001 0.0001 0.0001 0.0001 0.0002 0.0002 0.0002 0.0003 0.0003 0.0003 0.0004 0.0005 0.0006
J (A
dim
enci
on
al)
Caudal (m3/s)
Comparacin de Prdidas de Carga de Diferentes Tuberias
T1
T2
T3
T4
-
0.0000.2000.4000.6000.8001.0001.2001.4001.600
J (A
dim
enci
on
al)
Caudal (m3/s)
Comparacin de Valores Eperimentales y Tericos T1
J (exper.)
(Darcy)
(Blasius)
(Moody)0.002.004.006.008.00
10.0012.0014.0016.00
J (A
dim
enci
on
al)
Caudal (m3/s)
Comparacin de Valores Eperimentales y Tericos T2
J (exper.)
(Darcy)
(Blasius)
(Moody)
0.00
1.00
2.00
3.00
4.00
5.00
6.00
J (A
dim
enci
on
al)
Caudal (m3/s)
Comparacin de Valores Eperimentales y Tericos T3
J (exper.)
(Darcy)
(Blasius)
(Moody)
0.00
1.00
2.00
3.00
4.00
5.00
6.00
0.0
00
1
0.0
00
1
0.0
00
1
0.0
00
1
0.0
00
2
0.0
00
2
0.0
00
2
0.0
00
3
0.0
00
3
0.0
00
3
0.0
00
4
0.0
00
5
0.0
00
6
J (A
dim
enci
on
al)
Caudal (m3/s)
Comparacin de Valores Eperimentales y Tericos T4
J (exper.)
(Darcy)
(Blasius)
(Moody)
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Perdidas de Carga Concentrada en Codos Tuberas Tablas y Graficas.
Perdidas de Carga Distribuidas en las Tuberas T1, T2, T3, T4
COMPARACION DE LAS PERDIDAS DE CARGA
Prueba N Elemento Diametro (mmm) ngulo () Q (m3/h) Q (m3/s) P (mmHg) J Exper. (Pa)
01 G1 14.5 90 0.25 6.94E-05 266.64 86.66
02 G1 14.5 90 0.50 1.39E-04 399.96 346.64
03 G1 14.5 90 0.75 2.08E-04 1066.56 779.94
04 G1 14.5 90 1.00 2.78E-04 1999.8 1386.56
05 G1 14.5 90 1.25 3.47E-04 2933.04 2166.50
06 G1 14.5 90 1.50 4.17E-04 4266.24 3119.76
07 G1 14.5 90 1.75 4.86E-04 5599.44 4246.35
01 G2 27 45 0.25 6.94E-05 266.64 1.47
02 G2 27 45 0.50 1.39E-04 399.96 5.88
03 G2 27 45 0.75 2.08E-04 1066.56 13.24
04 G2 27 45 1.00 2.78E-04 1999.8 23.54
05 G2 27 45 1.25 3.47E-04 2933.04 36.78
06 G2 27 45 1.50 4.17E-04 4266.24 52.96
07 G2 27 45 1.75 4.86E-04 5599.44 72.08
01 C1 27 90 0.25 6.94E-05 266.64 7.21
02 C1 27 90 0.50 1.39E-04 399.96 28.83
03 C1 27 90 0.75 2.08E-04 1066.56 64.88
04 C1 27 90 1.00 2.78E-04 1999.8 115.33
05 C1 27 90 1.25 3.47E-04 2933.04 180.21
06 C1 27 90 1.50 4.17E-04 4266.24 259.50
07 C1 27 90 1.75 4.86E-04 5599.44 353.21
-
Perdidas de Carga Distribuidas en las Valvulas Tablas y Graficas.
Perdidas de Carga Distribuidas en las Valvulas de Interceptacion V1, V2, V3, V4, V5, V6
Comparacion de Perdidas Experimentalmente.
Prueba N Valvula Q (m3/H) Q (m3/s) Q (m6/s2) P Exp. (mmHg) P Exp. (Pa)
01
V1
0.25 6.94E-05 4.82E-09 1 133.32
02 0.50 1.39E-04 1.93E-08 2 266.64
03 0.75 2.08E-04 4.34E-08 3.1 413.30
04 1.00 2.78E-04 7.72E-08 10 1333.22
05 1.25 3.47E-04 1.21E-07 13 1733.19
06 1.50 4.17E-04 1.74E-07 21 2799.77
0.00
500.00
1000.00
1500.00
2000.00
2500.00
3000.00
3500.00
4000.00
4500.00
6.94E-05 1.39E-04 2.08E-04 2.78E-04 3.47E-04 4.17E-04 4.86E-04
P
(P
a)
Caudal (m3/s)
Comparacin del Valor Experimental y Terico C1
G1
G2
C1
-
07 1.75 4.86E-04 2.36E-07 29 3866.35
08 2.00 5.56E-04 3.09E-07 38 5066.25
01
V2
0.25 6.94E-05 4.82E-09 12 1599.87
02 0.50 1.39E-04 1.93E-08 36 4799.61
03 0.75 2.08E-04 4.34E-08 56 7466.05
04 1.00 2.78E-04 7.72E-08 93 12398.98
05 1.25 3.47E-04 1.21E-07 130 17331.91
06 1.50 4.17E-04 1.74E-07 185 24664.64
07 1.75 4.86E-04 2.36E-07 250 33330.59
08 2.00 5.56E-04 3.09E-07 310 41329.93
01
V3
0.25 6.94E-05 4.82E-09 9 1199.90
02 0.50 1.39E-04 1.93E-08 17 2266.48
03 0.75 2.08E-04 4.34E-08 30 3999.67
04 1.00 2.78E-04 7.72E-08 50 6666.12
05 1.25 3.47E-04 1.21E-07 79 10532.47
06 1.50 4.17E-04 1.74E-07 110 14665.46
07 1.75 4.86E-04 2.36E-07 145 19331.74
08 2.00 5.56E-04 3.09E-07 190 25331.25
01
V4
0.25 6.94E-05 4.82E-09 28 3733.03
02 0.50 1.39E-04 1.93E-08 80 10665.79
03 0.75 2.08E-04 4.34E-08 158 21064.93
04 1.00 2.78E-04 7.72E-08 290 38663.49
05 1.25 3.47E-04 1.21E-07 441 58795.16
06 1.50 4.17E-04 1.74E-07 650 86659.54
07 1.75 4.86E-04 2.36E-07
0.00
08 2.00 5.56E-04 3.09E-07
0.00
01 V5
0.25 6.94E-05 4.82E-09 3 399.97
02 0.50 1.39E-04 1.93E-08 3 399.97
-
03 0.75 2.08E-04 4.34E-08 3 399.97
04 1.00 2.78E-04 7.72E-08 3 399.97
05 1.25 3.47E-04 1.21E-07 3 399.97
06 1.50 4.17E-04 1.74E-07 3 399.97
07 1.75 4.86E-04 2.36E-07 3 399.97
08 2.00 5.56E-04 3.09E-07 3 399.97
01
V6
0.25 6.94E-05 4.82E-09 16 2133.16
02 0.50 1.39E-04 1.93E-08 50 6666.12
03 0.75 2.08E-04 4.34E-08 98 13065.59
04 1.00 2.78E-04 7.72E-08 160 21331.58
05 1.25 3.47E-04 1.21E-07 258 34397.17
06 1.50 4.17E-04 1.74E-07 370 49329.28
07 1.75 4.86E-04 2.36E-07 480 63994.74
08 2.00 5.56E-04 3.09E-07 625 83326.48
-
Perdidas de Carga Tubo Venturi, Diafragma y Pitot Tablas y Graficas.
Perdidas en el Tubo Venturi, Diafragma y Pitot
Comparacin de las Prdidas
Prueba N Instrumento Q (m3/H) Q (m3/s) P Exp. (mmHg) P Exp. (Pa)
01 Venturi 0.25 6.94E-05 4 533.29
02 Venturi 0.50 1.39E-04 8 1066.58
03 Venturi 0.75 2.08E-04 16 2133.16
04 Venturi 1.00 2.78E-04 28 3733.03
05 Venturi 1.25 3.47E-04 41 5466.22
06 Venturi 1.50 4.17E-04 58 7732.70
200.00
10200.00
20200.00
30200.00
40200.00
50200.00
60200.00
70200.00
80200.00
90200.00
4.82E-09 1.93E-08 4.34E-08 7.72E-08 1.21E-07 1.74E-07 2.36E-07 3.09E-07
P
(Pa)
Caudal^2 (m6/s2)
Comparacin de Prdidas de Vlvulas - Q^2
V1
V2
V3
V4
V5
V6
-
07 Venturi 1.75 4.86E-04 74 9865.86
08 Venturi 2.00 5.56E-04 0 0.00
01 Diafragma 0.25 6.94E-05 3 399.97
02 Diafragma 0.50 1.39E-04 16 2133.16
03 Diafragma 0.75 2.08E-04 12 1599.87
04 Diafragma 1.00 2.78E-04 22 2933.09
05 Diafragma 1.25 3.47E-04 30 3999.67
06 Diafragma 1.50 4.17E-04 45 5999.51
07 Diafragma 1.75 4.86E-04 74 9865.86
08 Diafragma 2.00 5.56E-04 96 12798.95
01 Pitot 0.25 6.94E-05 6 799.934211
02 Pitot 0.50 1.39E-04 12 1599.86842
03 Pitot 0.75 2.08E-04 20 2666.44737
04 Pitot 1.00 2.78E-04 32 4266.31579
05 Pitot 1.25 3.47E-04 44 5866.18421
06 Pitot 1.50 4.17E-04 62 8265.98684
07 Pitot 1.75 4.86E-04 81 10799.1118
08 Pitot 2.00 5.56E-04 106 14132.1711
-
200.00
2200.00
4200.00
6200.00
8200.00
10200.00
12200.00
14200.00
6.94E-05 1.39E-04 2.08E-04 2.78E-04 3.47E-04 4.17E-04 4.86E-04 5.56E-04
P
(Pa)
Caudal (m3/s)
Comparacin de Prdidas de Carga en los Tubos Venturi, Diafragma y Pitot
Venturi
Diafragma
Pitot
