presentacion de datos pract .doc

PRESENTACION DE DATOS

Cuadro N 1: perdidas de cargas distribuidas experimentalmente; j experimental, Darcy, Blasius, Moody para las tuberas T1, T2, T3, T4.PERDIDAS DE CARGA DISTRIBUIDAS EXPERIMENTALMENTE

N de PruebaQ(M3/h)Q(M3/s)P (mmHg) T1P (mmHg) T2P (mmHg) T3P (mmHg) T4

10.200.000055564686

20.300.000083336481822

30.400.000111118682828

40.500.00013889121043838

50.600.00016667141325054

60.700.00019444181686066

70.800.00022222222147680

80.900.00025000262609298

91.000.0002777830330114118

101.250.0003472242462164170

111.500.0004166762666236240

121.750.0004861184768308314

132.000.00055556106-408368

Cuadro N 2: valores hallados ( j experimental, Darcy, Blasius, Moody) para el tubo T1*16mm y presentacin de datos.PERDIDAS DE CARGA DISTRIBUIDAS EN LA TUBERIA T1

CARACTERISTICAS DEL TUBO

TIPO DE TUBO T1RUGOSIDAD

DIAMETRO16mm0.016e/d1mmHg = 133.3 Pa

LONGITUD1.27K(mm)0.007133.3

COMPARACION DE LOS VALORES EXPERIMENTALES Y TEORICOS

N de PruebaQ(M3/h)Q(M3/s)RefP (mmHg) T1P (Pa) P /L (mmHg/m) J ExperimentalJ DarcyJ BlasiusJ Moody

10.200.0000564420.970.03984533.203.150.040.010.010.01

20.300.0000836631.460.03546799.804.720.060.030.020.02

30.400.0001118841.940.032881066.406.300.090.050.030.03

40.500.00013911052.430.0309121599.609.450.130.080.050.05

50.600.00016713262.910.0296141866.2011.020.150.110.060.06

60.700.00019415473.400.0285182399.4014.170.190.150.080.08

70.800.00022217683.880.0276222932.6017.320.240.200.110.11

80.900.00025019894.370.0269263465.8020.470.280.250.130.13

91.000.00027822104.850.0263303999.0023.620.320.310.160.16

101.250.00034727631.070.0251425598.6033.070.450.490.230.24

111.500.00041733157.280.0242628264.6048.820.660.710.320.33

121.750.00048638683.490.02358411197.2066.140.900.960.420.44

132.000.00055644209.710.022910614129.8083.461.131.260.530.56

Cuadro N 3: comparacin de resultados ( j experimental, Darcy, Blasius, Moody) para el tubo T1*16mm y presentacin de datos.Q(M3/s)J ExperimentalJ DarcyJ BlasiusJ Moody

0.0000560.040.010.010.01

0.0000830.060.030.020.02

0.0001110.090.050.030.03

0.0001390.130.080.050.05

0.0001670.150.110.060.06

0.0001940.190.150.080.08

0.0002220.240.200.110.11

0.0002500.280.250.130.13

0.0002780.320.310.160.16

0.0003470.450.490.230.24

0.0004170.660.710.320.33

0.0004860.900.960.420.44

0.0005561.131.260.530.56

Grfico N 1: comparacin de resultados ( j experimental, Darcy, Blasius, Moody) para el tubo T1*16mm y presentacin de datos.

Cuadro N 4: valores hallados ( j experimental, Darcy, Blasius, Moody) para el tubo T2*10mm y presentacin de datos.PERDIDAS DE CARGA DISTRIBUIDAS EN LA TUBERIA T2



DIAMETRO10mm0.01e/d1mmHg = 133.3 Pa



N de PruebaQ(M3/h)Q(M3/s)RefP (mmHg) T2P (Pa) P /L (mmHg/m) J ExperimentalJ DarcyJ BlasiusJ Moody

10.200.0000567073.550.03526799.804.720.060.180.090.09

20.300.00008310610.330.0317486398.4037.800.510.410.180.18

30.400.00011114147.110.0296689064.4053.540.730.720.300.30

40.500.00013917683.880.028210413863.2081.891.111.130.440.45

50.600.00016721220.660.027113217595.60103.941.411.620.600.62

60.700.00019424757.440.026316822394.40132.281.802.210.790.82

70.800.00022228294.210.025621428526.20168.502.292.880.991.05

80.900.00025031830.990.025126034658.00204.722.783.651.221.30

91.000.00027835367.770.024633043989.00259.843.534.511.471.57

101.250.00034744209.710.023746261584.60363.784.947.042.172.36

111.500.00041753051.650.023166688777.80524.417.1310.142.993.31

121.750.00048661893.590.0226768102374.40604.728.2213.803.914.40

132.000.00055670735.530.0222-0.0018.024.945.65

Cuadro N 5: comparacin de resultados (j experimental, Darcy, Blasius, Moody) para el tubo T2*10mm y presentacin de datos.Q(M3/s)J ExperimentalJ DarcyJ BlasiusJ Moody

0.0000560.060.180.090.09

0.0000830.510.410.180.18

0.0001110.730.720.300.30

0.0001391.111.130.440.45

0.0001671.411.620.600.62

0.0001941.802.210.790.82

0.0002222.292.880.991.05

0.0002502.783.651.221.30

0.0002783.534.511.471.57

0.0003474.947.042.172.36

0.0004177.1310.142.993.31

0.0004868.2213.803.914.40

0.0005560.0018.024.945.65

Grfico N 2: comparacin de resultados ( j experimental, Darcy, Blasius, Moody) para el tubo T2*10mm y presentacin de datos.

Cuadro N 6: comparacin de resultados (j experimental, Darcy, Blasius, Moody) para el tubo T1*16mm y T2*10mm y presentacin de datos.PERDIDAS DE CARGA DISTRIBUIDAS EN LAS TUBERIAS T1, T2

COMPARACION DE LAS PERDIDAS DE CARGA

Nro de PruebaQ(M3/h)Q(M3/s)J Experimental T1 (16mm)J Experimental T2 (10mm)

10.200.0000560.040.06

20.300.0000830.060.51

30.400.0001110.090.73

40.500.0001390.131.11

50.600.0001670.151.41

60.700.0001940.191.80

70.800.0002220.242.29

80.900.0002500.282.78

91.000.0002780.323.53

101.250.0003470.454.94

111.500.0004170.667.13

121.750.0004860.908.22

132.000.0005561.13

Grfico N 3: comparacin de resultados (j experimental, Darcy, Blasius, Moody) para el tubo T1*16mm y T2*10mm y presentacin de datos.

Cuadro N 7: valores hallados (j experimental, Darcy, Blasius, Moody) para el tubo con codos T3*15.5mm y presentacin de datos.

PERDIDAS DE CARGA DISTRIBUIDAS EN LA TUBERIA T3



DIAMETRO15.5mm0.0155e/d1mmHg = 133.3 Pa



Nro de PruebaQ(M3/h)Q(M3/s)RefP (mmHg) T3P (Pa) P /L (mmHg/m) J ExperimentalJ DarcyJ BlasiusJ Moody

10.200.0000564563.580.039581066.406.300.090.020.010.01

20.300.0000836845.370.0351182399.4014.170.190.030.020.02

30.400.0001119127.170.0325283732.4022.050.300.060.040.04

40.500.00013911408.960.0307385065.4029.920.410.090.050.05

50.600.00016713690.750.0294506665.0039.370.530.140.070.08

60.700.00019415972.540.0283607998.0047.240.640.180.100.10

70.800.00022218254.330.02757610130.8059.840.810.240.120.13

80.900.00025020536.120.02679212263.6072.440.980.300.150.15

91.000.00027822817.910.026111415196.2089.761.220.380.180.19

101.250.00034728522.390.025016421861.20129.131.750.590.270.28

111.500.00041734226.870.024123631458.80185.832.530.840.370.39

121.750.00048639931.350.023430841056.40242.523.301.150.490.51

132.000.00055645635.830.022840854386.40321.264.371.500.620.65

Cuadro N 8: comparacin de resultados (j experimental, Darcy, Blasius, Moody) para el tubo con curvas T3*15.5mm y presentacin de datos.Q(M3/s)J ExperimentalJ DarcyJ BlasiusJ Moody

0.0000560.090.020.010.01

0.0000830.190.030.020.02

0.0001110.300.060.040.04

0.0001390.410.090.050.05

0.0001670.530.140.070.08

0.0001940.640.180.100.10

0.0002220.810.240.120.13

0.0002500.980.300.150.15

0.0002781.220.380.180.19

0.0003471.750.590.270.28

0.0004172.530.840.370.39

0.0004863.301.150.490.51

0.0005564.371.500.620.65

Grfico N 4: comparacin de resultados (j experimental, Darcy, Blasius, Moody) para el tubo con codos T3*15.5mm y presentacin de datos.

Cuadro N 9: valores hallados ( j experimental, Darcy, Blasius, Moody) para l tuvo con curvas T4*15.5mm y presentacin de datos.PERDIDAS DE CARGA DISTRIBUIDAS EN LA TUBERIA T4



DIAMETRO15.5mm0.0155e/d1mmHg = 133.3 Pa



Nro de PruebaQ(M3/h)Q(M3/s)RefP (mmHg) T4P (Pa) P /L (mmHg/m) J ExperimentalJ DarcyJ BlasiusJ Moody

10.200.0000564563.580.03956799.804.720.060.020.010.01

20.300.0000836845.370.0351222932.6017.320.240.030.020.02

30.400.0001119127.170.0325283732.4022.050.300.060.040.04

40.500.00013911408.960.0307385065.4029.920.410.090.050.05

50.600.00016713690.750.0294547198.2042.520.580.140.070.08

60.700.00019415972.540.0283668797.8051.970.710.180.100.10

70.800.00022218254.330.02758010664.0062.990.860.240.120.13

80.900.00025020536.120.02679813063.4077.171.050.300.150.15

91.000.00027822817.910.026111815729.4092.911.260.380.180.19

101.250.00034728522.390.025017022661.00133.861.820.590.270.28

111.500.00041734226.870.024124031992.00188.982.570.840.370.39

121.750.00048639931.350.023431441856.20247.243.361.150.490.51

132.000.00055645635.830.022836849054.40289.763.941.500.620.65

Cuadro N 10: comparacin de resultados ( j experimental, Darcy, Blasius, Moody) para el tubo con curvas T4*15.5mm y presentacin de datos.Q(M3/s)J ExperimentalJ DarcyJ BlasiusJ Moody

0.0000560.060.020.010.01

0.0000830.240.030.020.02

0.0001110.300.060.040.04

0.0001390.410.090.050.05

0.0001670.580.140.070.08

0.0001940.710.180.100.10

0.0002220.860.240.120.13

0.0002501.050.300.150.15

0.0002781.260.380.180.19

0.0003471.820.590.270.28

0.0004172.570.840.370.39

0.0004863.361.150.490.51

0.0005563.941.500.620.65

Grfico N 5: comparacin de resultados ( j experimental, Darcy, Blasius, Moody) para el tubo con curvas T4*15.5mm y presentacin de datos.

Cuadro N 11: comparacin de resultados (j experimental, Darcy, Blasius, Moody) para el tubo T3*15.5mm codos y T4*15.5mm curvas y presentacin de datos.PERDIDAS DE CARGA DISTRIBUIDAS EN LAS TUBERIAS T3, T4


Nro de PruebaQ(M3/h)Q(M3/s)J Experimental T3 (15.5mm)J Experimental T4 (15.5mm)

10.200.0000560.090.06

20.300.0000830.190.24

30.400.0001110.300.30

40.500.0001390.410.41

50.600.0001670.530.58

60.700.0001940.640.71

70.800.0002220.810.86

80.900.0002500.981.05

91.000.0002781.221.26

101.250.0003471.751.82

111.500.0004172.532.57

121.750.0004863.303.36

132.000.0005564.373.94

Grfico N 6: comparacin de resultados (j experimental, Darcy, Blasius, Moody) para el tubo T3*15.5mm codos y T4*15.5mm curvas y presentacin de datos.

Cuadro N 12: comparacin de resultados J experimental las tuberas T1, T2, T3, T4.PERDIDAS DE CARGA DISTRIBUIDAS EN LAS TUBERIAS T1,T2,T3, T4


Nro de PruebaQ(M3/h)Q(M3/s)J Experimental T1 (16mm)J Experimental T2 (10mm)J Experimental T3 (15.5mm)J Experimental T4 (15.5mm)

10.200.0000560.040.060.090.06

20.300.0000830.060.510.190.24

30.400.0001110.090.730.300.30

40.500.0001390.131.110.410.41

50.600.0001670.151.410.530.58

60.700.0001940.191.800.640.71

70.800.0002220.242.290.810.86

80.900.0002500.282.780.981.05

91.000.0002780.323.531.221.26

101.250.0003470.454.941.751.82

111.500.0004170.667.132.532.57

121.750.0004860.908.223.303.36

132.000.0005561.134.373.94

Grfico N 7: comparacin de resultados J experimental para las tuberas T1, T2, T3, T4.

presentacion de datos pract .doc

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