POLIDUCTO SANTA CRUZ - CHORETY.docx

UNIVERSIDAD PRIVADA DOMINGO SAVIO

DISEÑO DE POLIDUCTOS

DISEÑO DE OLEODUCTOS 1.- ELEGIR TRAMO refinería palmasola (santa cruz) – chorety (Camiri) rutas Ruta 1

longitud 242 km

Cruces especiales 31M+22P+2R+2A=57

2.-CAPACIDAD AÑO

DIESEL OIL (BPD)

2016 2017 2018 2019 2020 2021 2022 2023 2024 2025 2026 2027 2028 2029 2030 2031 2032 2033 2034 2035 2036

5369,93 5722,20 6097,57 6497,57 6923,82 7378,02 7862,02 8377,76 8927,35 9512,98 10137,03 10802,02 11510,63 12265,73 13070,36 13927,78 14841,44 15815,04 16852,50 17958,03 19136,07

GASOLINA ESPECIAL (BPD) 3760,88 4039,94 4339,70 4661,71 5007,61 5379,17 5778,30 6207,05 6667,62 7162,35 7693,80 8264,68 8877,92 9536,66 10244,28 11004,41 11820,94 12698,05 13640,24 14652,35 15739,55

CARBURANTE TASA DE CRECIMIENTO DIESEL GASOLINA GLP JET FUEL KEROSENE

1,0656 1,0742 1,0721 1,0749 1,0549

GLP (BPD)

1084,37 1162,55 1246,37 1336,24 1432,58 1535,87 1646,60 1765,32 1892,60 2029,06 2175,36 2332,20 2500,35 2680,63 2873,90 3081,11 3303,26 3541,42 3796,76 4070,50 4363,99

JET FUEL (BPD) 147,99 159,07 170,99 183,80 197,56 212,36 228,27 245,36 263,74 283,49 304,73 327,55 352,09 378,46 406,80 437,27 470,03 505,23 543,07 583,75 627,47

KEROSENE (BPD) 33,00 34,81 36,72 38,74 40,87 43,11 45,48 47,97 50,61 53,38 56,32 59,41 62,67 66,11 69,74 73,57 77,61 81,87 86,36 91,10 CAPACIDAD 96,10 39963,19

3.-PERFIL TOPOGRAFICO

N

Distancia (km)

1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20

elevación (msnm)

0 1.88 8.27 13.9 25.6 51.1 62.8 74.8 95.1 116 128 137 146 158 173 190 203 211 223 242

4.-PARAMETROS DE DIESEL ºAPI=29.29 Q = 39963,19 BPD =1665.13 BHP T= 60 ºC µ= 3.5 cp. L= 242 km = 150.28 MILLAS # cruces= 57 Pmin= 200 psi MOP= 1440 psi ρagua= 62.4lb/pie3 GE =

0.88

426 420 456 485 602 587 650 612 527 429 585 818 950 1078 1065 965 1008 1151 1422 794

5.- DISEÑO MECANICO

1. 2.

  =    ∗   erosion = √ . ∗. =13.49/ max=0.5∗13.49=6.74 /

 =  0.011915∗ ,. =8.405   =8.625  3.

4. Normalizar

con

(API 5L x52)

5. esfuerzo admisible E=1 F = 0.5 (ASME B 31.4) SMYS = 52000 psi δadm = EF* SMYS * E

δadm = 0.5 * 52000 * 1 = 26000psi

6.- espesor τ=

 ∗ δd ∗  ∗  ∗. =0.2389  τ.     20 ñ = ..pu 0.12  = 0.3915 pulg = τ=

τreal

τreal

7.- normalizar espesor con tabla API 5L x52 τ = 0.406 pulg

8.- ID = OD – (2 * Espesor) ID = 8.625 pulg – (2 * 0.406) = 7.813 pulg características del ducto: 8.625 pulg * 7.813 pulg * 0.406 pulg * 52000 psi

9.MAOP = 2 * δadm*



..  pu = 2447.77 psi

MAOP = 2 * 26000 psi *

6.- DISEÑO HIDRAULICO altura inicial= 1397.64 pies (H1) altura final= 2604.99 pies (H2) D int supuesto = 4 pulg E= 0.0007 NRe= 2214*1665.13 BHP/(4*3.5cp) =263328.42

F= -4log F= -4log

[.∗  .∗  ] .∗] [..∗  .

=15.98

−−.∗ ∗(−)]  Dint= . ∗()`^. .∗.∗ .   Dint= . ` .  ∗.  (.  .  ) .∗.  ^. .∗. Q=0.084668*F*Dint2.5[

0.5

Dint= 12.5 pulg

error= (

−  )*100%

F (estimado) 10 15,98

d(estimado) 4 12.5

NRe 263328,42 84265.09

determinar el factor de faning f=

.   [( .ɛ+.. )]

f=

F 15.98 14.19

Dint 12.5 12.66

Error (%) 68 1.26

.   [( ..∗. +...)] = 0.02109

Caída de presión por fricción

 = 0.0605 * f * ∗   = 0.0605 * 0.02109 * 0.88 * 39963, 19 = 5.51 psi /milla .   < 1 psi/pie = 0.11326 psi/pie

norma:

perfil hidráulico

N

Distancia (millas)

elevación (msnm)

   (psi)

(psi)

(psi)

Presión (psi)

1

0

426

1440

2

1.17

420

6,44

-2,28

4,16

1435,84

3

5.14

456

21,87

13,71

35,58

1400,26

4

8.64

485

19,28

11,047

30,327

1369,933

5

15.91

602

40,057

44,57

84,627

1285,306

6

31.75

587

87,27

-5,71

81,56

1203,746

7

39.02

650

40,057

24

64,057

1139,689

8

46.48

612

41,1

-14,47

26,63

1113,059

9

59.09

527

69,48

-32,38

37,1

1075,959

10

72.08

429

71,57

-37,33

34,24

1041,719

11

79.54

585

41,1

59,42

100,52

941,199

12

85.13

818

30,8

88,76

119,56

821,639

13

90.72

950

30,8

50,28

81,08

740,559

14

98.18

1078

41,1

48,76

89,86

650,699

15

107.50

1065

51,35

-4,95

46,4

604,299

16

118.06

965

58,18

-38,095

20,085

584,214

17

126.14

1008

44,52

16,38

60,9

523,314

18

131.11

1151

27,38

54,47

81,85

441,464

19

138.57

1422

41,1

103,23

144,33

297,134

20

150.37

794

65,018

-239,24

-174,222

471,356

1600

1600

1400

1400

1200

1200

1000

1000

N O I C A V E L E

800

800

600

600

400

400

200

200

0

0

DISTANCIA

N O I S E R P

DISEÑO DE POLIDUCTO 1.- ELEGIR TRAMO refinería palmasola (santa cruz) – Planta chorety (Camiri) rutas Ruta 1

longitud 242 km


2.-CAPACIDAD AÑO

DIESEL OIL (BPD)

2016 2017 2018 2019 2020 2021 2022 2023 2024 2025 2026 2027 2028 2029 2030 2031 2032 2033 2034 2035 2036

5369,93 5722,20 6097,57 6497,57 6923,82 7378,02 7862,02 8377,76 8927,35 9512,98 10137,03 10802,02 11510,63 12265,73 13070,36 13927,78 14841,44 15815,04 16852,50 17958,03 19136,07



1,0656 1,0742 1,0721 1,0749 1,0549

GLP (BPD)

1084,37 1162,55 1246,37 1336,24 1432,58 1535,87 1646,60 1765,32 1892,60 2029,06 2175,36 2332,20 2500,35 2680,63 2873,90 3081,11 3303,26 3541,42 3796,76 4070,50 4363,99

JET FUEL (BPD) 147,99 159,07 170,99 183,80 197,56 212,36 228,27 245,36 263,74 283,49 304,73 327,55 352,09 378,46 406,80 437,27 470,03 505,23 543,07 583,75 627,47

KEROSENE (BPD) 33,00 34,81 36,72 38,74 40,87 43,11 45,48 47,97 50,61 53,38 56,32 59,41 62,67 66,11 69,74 73,57 77,61 81,87 86,36 91,10 96,10

CAPACIDAD 39963,19


N

Distancia (km)

1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20

elevación (msnm)

0 1.88 8.27 13.9 25.6 51.1 62.8 74.8 95.1 116 128 137 146 158 173 190 203 211 223 242

4.-PARAMETROS DE LA GASOLINA ºAPI= 60 Q = 39963,19 BPD =1665.13 BHP T= 60 ºC µ= 3.5 cp. L= 242 km = 150.28 MILLAS # cruces= 57 Pmin= 200 psi MOP= 1440 psi ρagua= 62.4lb/pie3 GE =

0.739

426 420 456 485 602 587 650 612 527 429 585 818 950 1078 1065 965 1008 1151 1422 794


1. 2.

  =    ∗   erosion = √ .∗. =14.726 / max=0.5 ∗14.726=7.363 /

 =  0.011915∗ ,. =8.04173   =8.625  3.

4. Normalizar

con

(API 5L x52)


δadm = 0.5 * 52000 * 1 = 26000psi

6.- espesor τ=

 ∗ δd ∗  ∗  ∗. =0.2389  τ.     20 ñ = ..pu 0.12  = 0.3915 pulg = τ=

τreal

τreal



9.MAOP = 2 * δadm*



..  pu = 2447.77 psi

MAOP = 2 * 26000 psi *


F= -4log F= -4log

[.∗  .∗  ] .∗] [..∗  .

=15.98

−−.∗ ∗(−)]  Dint= . ∗()`^. .∗.∗ .   Dint= . ` .  ∗.  (.  .  ) .∗.  ^. .∗. Q=0.084668*F*Dint2.5[

0.5

Dint= 11.45 pulg

error= (

−  )*100%


d(estimado) 4 11,45

NRe 263328,42 91992,46


.   [( .ɛ+.. )]

f=

F 15.98 15.07

Dint 11.45 11.72

Error (%) 65,06 2,30

.   [( ..∗. +...)] = 0.01852

caída de presión por fricción

 = 0.0605 * f * ∗   = 0.0605 * 0.01852 * 0.739 * 39963, 19 = 5.98 psi /milla .   < 1 psi/pie = 0.11326 psi/pie

norma:

perfil hidráulico N

Distancia (millas)

elevación (msnm)

   (psi)

1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20

0 1.17 5.14 8.64 15.91 31.75 39.02 46.48 59.09 72.08 79.54 85.13 90.72 98.18 107.50 118.06 126.14 131.11 138.57 150.37

426 420 456 485 602 587 650 612 527 429 585 818 950 1078 1065 965 1008 1151 1422 794

6.99 23.74 20.93 43.47 94.72 43.47 44.61 75.41 77.68 44.61 33.43 33.43 44.61 55.73 63.15 48.32 29.72 44.61 70.56

(psi)

-1.91 11.52 9.27 37.43 -4.80 20.15 -12.16 -27.19 -31.35 49.91 74.54 42.23 40.95 -4.16 -31.99 13.76 45.75 86.70 -200.91

(psi) 5.08 35.26 30.20 80.90 89.92 63.62 32.45 48.22 46.33 94.52 107.97 75.66 85.56 51.57 31.76 62.08 75.47 131.31 -129.44

Presión (psi) 1440 1434.92 1399.66 1369.46 1288.56 1198.64 1135.02 1102.57 1054.35 1008.02 913.5 805.53 729.87 644.31 592.74 560.98 498.90 423.43 292.12 421.56

1600

1600

1400

1400

1200

1200

1000

1000

N O I C A V E L E

800

800

600

600

400

400

200

200

0

0

DISTANCIA

N O I S E R P


longitud 242 km


2.-CAPACIDAD AÑO

DIESEL OIL (BPD)

2016 2017 2018 2019 2020 2021 2022 2023 2024 2025 2026 2027 2028 2029 2030 2031 2032 2033 2034 2035 2036

5369,93 5722,20 6097,57 6497,57 6923,82 7378,02 7862,02 8377,76 8927,35 9512,98 10137,03 10802,02 11510,63 12265,73 13070,36 13927,78 14841,44 15815,04 16852,50 17958,03 19136,07



1,0656 1,0742 1,0721 1,0749 1,0549

GLP (BPD)

1084,37 1162,55 1246,37 1336,24 1432,58 1535,87 1646,60 1765,32 1892,60 2029,06 2175,36 2332,20 2500,35 2680,63 2873,90 3081,11 3303,26 3541,42 3796,76 4070,50 4363,99

JET FUEL (BPD) 147,99 159,07 170,99 183,80 197,56 212,36 228,27 245,36 263,74 283,49 304,73 327,55 352,09 378,46 406,80 437,27 470,03 505,23 543,07 583,75 627,47

KEROSENE (BPD) 33,00 34,81 36,72 38,74 40,87 43,11 45,48 47,97 50,61 53,38 56,32 59,41 62,67 66,11 69,74 73,57 77,61 81,87 86,36 91,10 96,10

CAPACIDAD 39963,19


N

Distancia (km)

1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20

elevación (msnm)

0 1.88 8.27 13.9 25.6 51.1 62.8 74.8 95.1 116 128 137 146 158 173 190 203 211 223 242

4.-PARAMETROS DE GLP ºAPI= 116.75 Q = 39963,19 BPD =1665.13 BHP T= 60 ºC µ= 3.5 cp. L= 242 km = 150.28 MILLAS # cruces= 57 Pmin= 200 psi MOP= 1440 psi ρagua= 62.4lb/pie3 GE =

0.57

426 420 456 485 602 587 650 612 527 429 585 818 950 1078 1065 965 1008 1151 1422 794


1. 2.

  =    ∗   erosion = √ . ∗. =16.76 / max=0.5∗16.76=8.38 /

 =  0.011915∗ ,. =7.5379   =8.625  3.

4. Normalizar

con

(API 5L x52)


δadm = 0.5 * 52000 * 1 = 26000psi

6.- espesor τ=

 ∗ δd ∗  ∗  ∗. =0.2389  τ.     20 ñ = ..pu 0.12  = 0.3915 pulg = τ=

τreal

τreal



9.MAOP = 2 * δadm*



..  pu = 2447.77 psi

MAOP = 2 * 26000 psi *


F= -4log F= -4log

[.∗  .∗  ] .∗] [..∗  .

=15.98

−−.∗ ∗(−)]  Dint= . ∗()`^. .∗.∗ .   Dint= . ` .  ∗.  (.  .  ) .∗.  ^. .∗. Q=0.084668*F*Dint2.5[

0.5

Dint= 10.66 pulg

error= (

−  )*100%


d(estimado) 4 10.66

NRe 263328,42 98809.91


.   [( .ɛ+.. )]

f=

F 15.98 14.43

Dint 10.66 11.10

.   [( ..∗. +...)] = 0.0209

Error (%) 62.47 3.96


 = 0.0605 * f * ∗   = 0.0605 * 0.0209 * 0.57* 39963, 19 = 6.83 psi /milla .   < 1 psi/pie = 0.1293 psi/pie

norma:

perfil hidráulico

N

Distancia (millas)

elevación (msnm)

   (psi)

(psi)

(psi)

Presión (psi)

1

0

426

1440

2

1.17

420

7,99

-1,48

6,51

1433,49

3

5.14

456

27,11

8,88

35,99

1397,5

4

8.64

485

23,9

7,15

31,05

1366,45

5

15.91

602

49,65

28,87

78,52

1287,93

6

31.75

587

108,18

-3,7

104,48

1183,45

7

39.02

650

49,65

15,54

65,19

1118,26

8

46.48

612

50,95

-9,37

41,58

1076,68

9

59.09

527

86,12

-20,97

65,15

1011,53

10

72.08

429

88,72

-24,18

64,54

946,99

11

79.54

585

50,95

38,49

89,44

857,55

12

85.13

818

38,17

57,49

95,66

761,89

13

90.72

950

38,17

32,57

70,74

691,15

14

98.18

1078

50,95

31,58

82,53

608,62

15

107.50

1065

63,65

-3,2

60,45

548,17

16

118.06

965

72,12

-24,67

47,45

500,72

17

126.14

1008

55,18

10,61

65,79

434,93

18

131.11

1151

33,94

35,28

69,22

365,71

19

138.57

1422

50,95

66,87

117,82

247,89

20

150.37

794

80,59

-154,96

-74,37

322,26

1600

1600

1400

1400

1200

1200

1000

1000

N O I C A V E L E

800

800

600

600

400

400

200

200

0

0

DISTANCIA

N O I S E R P


longitud 242 km


2.-CAPACIDAD AÑO

DIESEL OIL (BPD)

2016 2017 2018 2019 2020 2021 2022 2023 2024 2025 2026 2027 2028 2029 2030 2031 2032 2033 2034 2035 2036

5369,93 5722,20 6097,57 6497,57 6923,82 7378,02 7862,02 8377,76 8927,35 9512,98 10137,03 10802,02 11510,63 12265,73 13070,36 13927,78 14841,44 15815,04 16852,50 17958,03 19136,07



1,0656 1,0742 1,0721 1,0749 1,0549

GLP (BPD)

1084,37 1162,55 1246,37 1336,24 1432,58 1535,87 1646,60 1765,32 1892,60 2029,06 2175,36 2332,20 2500,35 2680,63 2873,90 3081,11 3303,26 3541,42 3796,76 4070,50 4363,99

JET FUEL (BPD) 147,99 159,07 170,99 183,80 197,56 212,36 228,27 245,36 263,74 283,49 304,73 327,55 352,09 378,46 406,80 437,27 470,03 505,23 543,07 583,75 627,47

KEROSENE (BPD) 33,00 34,81 36,72 38,74 40,87 43,11 45,48 47,97 50,61 53,38 56,32 59,41 62,67 66,11 69,74 73,57 77,61 81,87 86,36 91,10 96,10

CAPACIDAD 39963,19


N

Distancia (km)

1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20

elevación (msnm)

0 1.88 8.27 13.9 25.6 51.1 62.8 74.8 95.1 116 128 137 146 158 173 190 203 211 223 242

4.PARAMETROS DEL JET FUEL ºAPI= 36.95 Q = 39963,19 BPD =1665.13 BHP T= 60 ºC µ= 3.5 cp. L= 242 km = 150.28 MILLAS # cruces= 57 Pmin= 200 psi MOP= 1440 psi ρagua= 62.4lb/pie3 GE =

0.84

426 420 456 485 602 587 650 612 527 429 585 818 950 1078 1065 965 1008 1151 1422 794


1. 2.

  =    ∗   erosion = √ . ∗. =13.81/ max=0.5 ∗13.81=6.905 /

 =  0.011915∗ ,. =8.30   =8.625  3.

4. Normalizar

con

(API 5L x52)

5. esfuerzo admisible E=1 F = 0.5 (ASME B 31.4) SMYS = 52000 psi

δadm = 0.5 * 52000 * 1 = 26000psi

δadm = EF* SMYS * E

6.- espesor τ=

 ∗ δd ∗  ∗  ∗. =0.2389  τ.     20 ñ = ..pu 0.12  = 0.3915 pulg = τ=

τreal

τreal



9.MAOP = 2 * δ adm*



6.- DISEÑO HIDRAULICO

..  pu = 2447.77 psi

MAOP = 2 * 26000 psi *

altura inicial= 1397.64 pies (H1) altura final= 2604.99 pies (H2) D int supuesto = 4 pulg E= 0.0007 NRe= 2214*1665.13 BHP/(4*3.5cp) =263328.42

F= -4log F= -4log

[.∗  .∗  ] .∗] [..∗  .

=15.98

−−.∗ ∗(−)]  Dint= . ` .  ∗() .∗ ∗  ^. .   Dint= . `^.  .  ) .∗...∗.∗.(.   Q=0.084668*F*Dint2.5[

0.5

Dint= 11.45 pulg

error= (

−  )*100%

F (estimado) 10 15.98

d(estimado) 4 11.91

NRe 263328.42 88439.43


.   [( .ɛ+.. )]

f=

F 15.98 15.02

Dint 11.91 12.22

Error (%) 66.41 2.54

.   [( ..∗. +...)] = 0.01865


 = 0.0605 * f * ∗  19 = 5.55 psi /milla  = 0.0605 * 0.01865 * 0.84 * 39963, .   < 1 psi/pie = 0.1051 psi/pie

norma:


Distancia (millas)

elevación (msnm)

   (psi)

1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20

0 1.17 5.14 8.64 15.91 31.75 39.02 46.48 59.09 72.08 79.54 85.13 90.72 98.18 107.50 118.06 126.14 131.11 138.57 150.37

426 420 456 485 602 587 650 612 527 429 585 818 950 1078 1065 965 1008 1151 1422 794

6.49 22.03 19.43 40.35 87.91 40.35 41.40 69.99 72.09 41.40 31.02 31.02 41.40 51.73 58.61 44.84 27.58 41.40 65.49

(psi)

-2.18 13.09 10.55 42.55 -5.45 22.91 -13.82 -30.91 -35.64 56.73 84.73 48 46.55 -4.73 -36.36 15.64 52 98.55 -228.36

(psi) 4.31 35.12 29.98 82.9 82.46 63.26 27.58 39.08 36.45 98.13 115.75 79.02 87.95 47 21.95 60.48 79.58 139.95 -162.87

Presión (psi) 1440 1435.69 1400.57 1370.59 1287.69 1205.23 1141.97 1114.39 1075.31 1038.86 940.73 824.98 745.96 658.01 611.01 589.06 528.58 449 309.05 471.92

1600

1600

1400

1400

1200

1200

1000

1000

N O I C A V E L E

800

800

600

600

400

400

200

200

0

0

DISTANCIA

N O I S E R P


longitud 242 km


2.-CAPACIDAD AÑO

DIESEL OIL (BPD)

2016 2017 2018 2019 2020 2021 2022 2023 2024 2025 2026 2027 2028 2029 2030 2031 2032 2033 2034 2035 2036

5369,93 5722,20 6097,57 6497,57 6923,82 7378,02 7862,02 8377,76 8927,35 9512,98 10137,03 10802,02 11510,63 12265,73 13070,36 13927,78 14841,44 15815,04 16852,50 17958,03 19136,07



1,0656 1,0742 1,0721 1,0749 1,0549

GLP (BPD)

1084,37 1162,55 1246,37 1336,24 1432,58 1535,87 1646,60 1765,32 1892,60 2029,06 2175,36 2332,20 2500,35 2680,63 2873,90 3081,11 3303,26 3541,42 3796,76 4070,50 4363,99

JET FUEL (BPD) 147,99 159,07 170,99 183,80 197,56 212,36 228,27 245,36 263,74 283,49 304,73 327,55 352,09 378,46 406,80 437,27 470,03 505,23 543,07 583,75 627,47

KEROSENE (BPD) 33,00 34,81 36,72 38,74 40,87 43,11 45,48 47,97 50,61 53,38 56,32 59,41 62,67 66,11 69,74 73,57 77,61 81,87 86,36 91,10 96,10

CAPACIDAD 39963,19


N

Distancia (km)

1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20

elevación (msnm)

0 1.88 8.27 13.9 25.6 51.1 62.8 74.8 95.1 116 128 137 146 158 173 190 203 211 223 242

4.-PARAMETROS DEL KEROSENE ºAPI= 45.38 Q = 39963,19 BPD =1665.13 BHP T= 60 ºC µ= 3.5 cp. L= 242 km = 150.28 MILLAS # cruces= 57 Pmin= 200 psi MOP= 1440 psi ρagua= 62.4lb/pie3 GE =

0.80

426 420 456 485 602 587 650 612 527 429 585 818 950 1078 1065 965 1008 1151 1422 794


1. 2.

  =    ∗   erosion = √ . ∗. =14.15 / max=0.5 ∗14.15=7.075 /

 =  0.011915∗ ,. =8.20   =8.625  3.

4. Normalizar

con

(API 5L x52)


δadm = 0.5 * 52000 * 1 = 26000psi

6.- espesor τ=

 ∗ δd ∗  ∗  ∗. =0.2389  τ ..pu 0.12  = 0.3915 pulg = .     20 ñ = τ=

τreal

τreal



9.MAOP = 2 * δadm*



..  pu = 2447.77 psi

MAOP = 2 * 26000 psi *


F= -4log F= -4log

[.∗  .∗  ] .∗] [..∗  .

=15.98

−−.∗ ∗(−)]  Dint= . ∗()`^. .∗.∗ .   Dint= . ` .  ∗.  (.  .  ) .∗.  ^. .∗. Q=0.084668*F*Dint2.5[

0.5

Dint= 11.73 pulg

error= (

−  )*100%


d(estimado) 4 11,73

NRe 263328,42 94637.35


.   [( .ɛ+.. )]

f=

F 15.98 15.12

Dint 11.73 12

.   [( ..∗ +...)] = 0.0209

Error (%) 65,89 2.25


 = 0.0605 * f * ∗   = 0.0605 * 0.0209 * 0.80* 39963,19 = 6.49 psi /milla   < 1 psi/pie = 0.1229 psi/pie

norma:


Distancia (millas)

elevación (msnm)

   (psi)

1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20

0 1.17 5.14 8.64 15.91 31.75 39.02 46.48 59.09 72.08 79.54 85.13 90.72 98.18 107.50 118.06 126.14 131.11 138.57 150.37

426 420 456 485 602 587 650 612 527 429 585 818 950 1078 1065 965 1008 1151 1422 794

7.53 25.77 22.72 47.18 102.80 47.18 48.42 81.84 84.31 48.42 36.28 37.12 47.57 60.49 68.53 52.44 32.26 48.42 76.58

(psi)

-2.07 12.47 10.04 40.52 -5.19 21.82 -13.16 -29.44 -33.94 54.03 80.69 45.71 44.33 -4.50 -34.63 14.89 49.52 93.85 -217.49

(psi) 5.46 38.24 32.76 87.7 97.61 69 35.26 52.4 50.37 102.45 116.97 82.83 91.9 55.99 33.9 67.33 81.78 142.27 -140.91

Presión (psi) 1440 1434.54 1396.3 1363.54 1275.84 1178.23 1109.23 1073.99 1021.59 971.22 868.77 751.8 668.97 577.07 521.08 487.18 419.85 338.07 195.8 1440 (EDB)

1600

1600

1400

1400

1200

1200

1000

1000

N O I C A V E L E

800

800

600

600

400

400

200

200

0

0

DISTANCIA

N O I S E R P

análisis económico: PRODUCTO GASOLINA KEROSENE JET FUEL DIESEL GLP

OD (pulg) 8.625 8.625 8.625 8.625 8.625

ID (pulg)

Τ (pulg) 0.406 0.406 0.406 0.406 0.406

7.813 7.813 7.813 7.813 7.813



(psi) 131.31 142.27 139.95 144.33 117.82

CRUCES

EST. DE BOMBEO

57 57 57 57 57

1 -

BHP (HP) 843.11 843.11 843.11 843.11 843.11

Se optó por análisis económico del Diesel debido a que este presenta una variación de presión más alta en relación a los demás productos. 843.11 HP * 15200 $us/HP = 12815272 $us

Vacero= − . ∗∗1.5 Vacero= ..−. ∗793963 ∗1.5 =∗ρ =3235079.50 ∗62.5 lb/gal

= 77025.7 BBL = 3235079.50 gal.

ρ acero = 62.5 lb/gal

= 202192468.8 lb. = 91712.96 Ton.

91712.96 Ton * 937 $us/Ton = 85935043.52 $us

31 montañas

= 1240000 $us

22 Pradera

= 440000 $us

2 Ríos

= 180000 $us

2 avenidas

= 160000 $us

0 localidades

= 0 $us

TOTAL

= 2020000 $us

CAPACIDAD

39963.19 BPD

LONGITUD

242 km

85935043.52 $us

CRUCES

57

2020000 $us

BHP

843.11 HP

12815272 $us

TOTAL

100770315.5 $us

POLIDUCTO SANTA CRUZ - CHORETY.docx

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