16
Constantes cd diametro densidade g dPo 0.61 0.042 996 9.8 12578 0.61 0.042 996 9.8 12664 0.61 0.042 996 9.8 12065 0.61 0.042 996 9.8 12527 0.61 0.042 996 9.8 11707 0.61 0.042 996 9.8 11040 Constantes cd diametro densidade g dPo 0.61 0.042 996 9.8 14509 0.61 0.042 996 9.8 14167 0.61 0.042 996 9.8 14253 0.61 0.042 996 9.8 14595 0.61 0.042 996 9.8 14458 0.61 0.042 996 9.8 13159

Graficos Relatorio de Dinamica de Fluidos

Embed Size (px)

DESCRIPTION

ghc

Citation preview

Page 1: Graficos Relatorio de Dinamica de Fluidos

Bomba simples

Caudal

Constantescd diametro densidade g dPo Pe1

0.61 0.042 996 9.8 12578 263.180.61 0.042 996 9.8 12664 262.940.61 0.042 996 9.8 12065 264.650.61 0.042 996 9.8 12527 262.70.61 0.042 996 9.8 11707 261.470.61 0.042 996 9.8 11040 257.81

Bombas em serie

Constantescd diametro densidade g dPo Pe1

0.61 0.042 996 9.8 14509 269.040.61 0.042 996 9.8 14167 267.090.61 0.042 996 9.8 14253 268.070.61 0.042 996 9.8 14595 268.310.61 0.042 996 9.8 14458 264.890.61 0.042 996 9.8 13159 264.65

Bombas em paralelo

Page 2: Graficos Relatorio de Dinamica de Fluidos

Constantescd diametro densidade g dPo dP1

0.61 0.042 996 9.8 32454.000 62842.0000.61 0.042 996 9.8 32095.000 65635.0000.61 0.042 996 9.8 31582.000 64238.0000.61 0.042 996 9.8 30659.000 62305.0000.61 0.042 996 9.8 27703.000 67676.0000.61 0.042 996 9.8 21225.000 72188.000

Page 3: Graficos Relatorio de Dinamica de Fluidos

Bomba simples

Rotacoes

Qv H dPo Pe1 Qv Pe10.00424511 6.35152881 12339 263.92 0.00420459 263.92

0.0042596 6.32415335 11194 232.18 0.00400476 232.180.00415764 6.52137869 8853 211.43 0.00356146 211.43

0.0042365 6.35283709 7144 183.84 0.00319929 183.840.00409549 6.54079055 5127 145.75 0.00271029 145.750.00397711 6.64119767 3657 106.93 0.002289 106.93

Bombas em serie

Caudal

Pe2 Qv H1 H2 HT dPo Qv274.41 0.00455934 6.04545926 6.16612576 12.211585 14.321 0.00014324268.31 0.00450529 6.07365146 6.10139437 12.1750458 12.578 0.00013424272.22 0.00451894 6.07751804 6.17160428 12.2491223 10.801 0.0001244270.75 0.00457283 6.01126667 6.06593288 12.0771995 8.357 0.00010942265.38 0.00455132 5.96269559 5.97372553 11.9364211 6.101 9.34946E-05268.07 0.00434205 6.24441329 6.32510815 12.5695214 4.238 7.79253E-05

Bombas em paralelo

Caudal

Page 4: Graficos Relatorio de Dinamica de Fluidos

dP2 Pe1 Pe2 H1 Qv1 H2 Qv262090.000 252.44 248.05 6.43820179 0.00401708 6.36115892 0.0039949660479.000 251.71 250.49 6.72434637 0.00383498 6.19611097 0.0041417462090.000 251.95 256.10 6.58122285 0.00392218 6.36115892 0.0041247162197.000 249.02 248.54 6.3831858 0.00399685 6.37212114 0.0039959365205.000 246.09 245.85 6.93344808 0.00363635 6.6802926 0.0037704171758.000 235.84 236.33 7.39570527 0.00326702 7.3516515 0.0032934

Qv1 H1 Qv2 H20.00401708 6.43820179 0.00399496 6.361158920.00383498 6.72434637 0.00414174 6.196110970.00392218 6.58122285 0.00412471 6.361158920.00399685 6.3831858 0.00399593 6.372121140.00363635 6.93344808 0.00377041 6.68029260.00326702 7.39570527 0.0032934 7.3516515

Page 5: Graficos Relatorio de Dinamica de Fluidos

Rotacoes

Pe1 Pe2 PT268.07 271.00 539.06238.04 247.56 485.60217.04 227.05 444.09185.79 201.42 387.21147.22 173.58 320.80105.96 140.38 246.34

Rotacoes

0.00395 0.004 0.00405 0.0041 0.00415 0.0042 0.00425 0.00436.1

6.2

6.3

6.4

6.5

6.6

6.7

Curvas caracteristicas de bomba simples (Altura Vs Caudal)

H

Q (m^3/s)

H(m

)

0.0043 0.00435 0.0044 0.00445 0.0045 0.00455 0.004602468

101214

Curva Caracteristica de Bombas em serie (Altura Vs Caudal)

H1H2HT

Q(m^3/s

H(m

)

Page 6: Graficos Relatorio de Dinamica de Fluidos

HT QvT dPo Pe1 Pe2 Pm6.51524465 0.00681895 32761 252.69 254.88 253.787.25258176 0.00678113 30061 220.70 229.74 225.226.80128678 0.00672672 25361 201.42 215.82 208.626.39425047 0.00662769 19858 178.71 200.44 189.587.18660356 0.00630009 13381 142.58 171.14 156.867.43975904 0.00551451 8938 107.67 139.16 123.41

QvT HT QvT0.00681895 6.51524465 0.006851130.00678113 7.25258176 0.006562740.00672672 6.80128678 0.006027910.00662769 6.39425047 0.005333980.00630009 7.18660356 0.004378520.00551451 7.43975904 0.00357852

Page 7: Graficos Relatorio de Dinamica de Fluidos

0.002 0.0025 0.003 0.0035 0.004 0.00450

50

100

150

200

250

300

Curva caracteristica de bomba simples (Potencia Vs Caudal)

Pe1

Q(m^3/s)

Pe(W

)

0.0043 0.00435 0.0044 0.00445 0.0045 0.00455 0.004602468

101214

Curva Caracteristica de Bombas em serie (Altura Vs Caudal)

H1H2HT

Q(m^3/s

H(m

)

0.00007 0.00008 0.00009 0.0001 0.00011 0.00012 0.00013 0.00014 0.000150.00

100.00

200.00

300.00

400.00

500.00

600.00

Curva Caravteristicas de Bombas em serie (Potencia Vs Caudal)

Pe1Pe2PT

Q(m^3/s)

Pe(W

)

0.0032 0.0034 0.0036 0.0038 0.004 0.00425.8

66.26.46.66.8

77.27.47.6

Curva Caracteristica de Bombas em paralelo (Altura Vs Caudal)

H1

Q(m^3/s)

H(m

)

0.0032 0.0034 0.0036 0.0038 0.004 0.00425.5

6

6.5

7

7.5

Curva Caracteristica de Bombas em paralelo (Altura Vs Caudal)

H2

Q(m^3/s)

H(m

)

Page 8: Graficos Relatorio de Dinamica de Fluidos

QvT0.006851130.006562740.006027910.005333980.004378520.00357852

Pm253.78418

225.219727208.618164189.575195156.860352123.413086

0.0032 0.0034 0.0036 0.0038 0.004 0.00425.8

66.26.46.66.8

77.27.47.6

Curva Caracteristica de Bombas em paralelo (Altura Vs Caudal)

H1

Q(m^3/s)

H(m

)

0.0032 0.0034 0.0036 0.0038 0.004 0.00425.5

6

6.5

7

7.5

Curva Caracteristica de Bombas em paralelo (Altura Vs Caudal)

H2

Q(m^3/s)

H(m

)

Page 9: Graficos Relatorio de Dinamica de Fluidos

0.00007 0.00008 0.00009 0.0001 0.00011 0.00012 0.00013 0.00014 0.000150.00

100.00

200.00

300.00

400.00

500.00

600.00

Curva Caravteristicas de Bombas em serie (Potencia Vs Caudal)

Pe1Pe2PT

Q(m^3/s)

Pe(W

)

0.0032 0.0034 0.0036 0.0038 0.004 0.00425.5

6

6.5

7

7.5

Curva Caracteristica de Bombas em paralelo (Altura Vs Caudal)

H2

Q(m^3/s)

H(m

)

0.00540.0056 0.0058 0.006 0.0062 0.00640.0066 0.0068 0.0075.5

6

6.5

7

7.5

8

Curva Caracteristica de Bombas em paralelo (Altura Vs Caudal)

HT

Q(m^3/s)

H(m

)

Page 10: Graficos Relatorio de Dinamica de Fluidos

0.0032 0.0034 0.0036 0.0038 0.004 0.00425.5

6

6.5

7

7.5

Curva Caracteristica de Bombas em paralelo (Altura Vs Caudal)

H2

Q(m^3/s)

H(m

)

0.00540.0056 0.0058 0.006 0.0062 0.00640.0066 0.0068 0.0075.5

6

6.5

7

7.5

8

Curva Caracteristica de Bombas em paralelo (Altura Vs Caudal)

HT

Q(m^3/s)

H(m

)

Page 11: Graficos Relatorio de Dinamica de Fluidos

0.00540.0056 0.0058 0.006 0.0062 0.00640.0066 0.0068 0.0075.5

6

6.5

7

7.5

8

Curva Caracteristica de Bombas em paralelo (Altura Vs Caudal)

HT

Q(m^3/s)

H(m

)

0.003 0.004 0.005 0.006 0.007 0.0080

50100150200250300

Curva Caravteristicas de Bombas em paralelo (Potencia Vs Caudal)

Pm

Q(m^3/s)

Pe(W

)

Page 12: Graficos Relatorio de Dinamica de Fluidos

0.00540.0056 0.0058 0.006 0.0062 0.00640.0066 0.0068 0.0075.5

6

6.5

7

7.5

8

Curva Caracteristica de Bombas em paralelo (Altura Vs Caudal)

HT

Q(m^3/s)

H(m

)

0.003 0.004 0.005 0.006 0.007 0.0080

50100150200250300

Curva Caravteristicas de Bombas em paralelo (Potencia Vs Caudal)

Pm

Q(m^3/s)

Pe(W

)

Page 13: Graficos Relatorio de Dinamica de Fluidos

0.003 0.004 0.005 0.006 0.007 0.0080

50100150200250300

Curva Caravteristicas de Bombas em paralelo (Potencia Vs Caudal)

Pm

Q(m^3/s)

Pe(W

)

Page 14: Graficos Relatorio de Dinamica de Fluidos

0.003 0.004 0.005 0.006 0.007 0.0080

50100150200250300

Curva Caravteristicas de Bombas em paralelo (Potencia Vs Caudal)

Pm

Q(m^3/s)

Pe(W

)