Ductos de gas
Páginas: 78 (19310 palabras)
Publicado: 21 de noviembre de 2009
ANEXO 1 SIMULACIÓN
1.1 Reporte de Cálculo Hidráulico en Pals 2000 R5. Presión de operación a la llegada de C.P.G. Poza Rica de 25 kg/cm2 man (150 MMPCSD).
DISEÑO, SUMINISTRO Y CONSTRUCCIÓN DE GASODUCTOS
MC-A-77-104
ELABORÓ: JJG
REV. No. 0
FECHA: 12/01/2009 119408MCA77104_0
(Name)
BATERÍA DE SEPARACIÓN FOBOS I
37.5 MMPCSD
39.93 kg/cm2
0+857.34 0+900.00 1+006.361+057.27 1+202.65 1+380.00 1+420.59 1+600.00 1+720.00 1+992.45 2+082.39 2+254.77 2+337.87 2+536.43 2+717.68 2+780.00
0+000.00
0+128.23
0+621.41
0+746.49
P
P
P
P
P
P
P
P
P
P
P
P
P
P
P
P
P
P
P
P
Line 0
P
5+707.60 5+626.12 5+496.83 5+096.99 4+911.48 4+574.37 4+401.66 4+257.44 3+900.00 Mixer 0 3+632.70 3+398.15 3+232.66ALIMENTACIÓN 37.5 MMPCSD
6+117.43
6+105.13
6+000.00
5+801.53
3+179.12
3+029.60
3+000.00
P
P
P
P
P
P
P
P
P
P
P
P
P
M
P
P
P
P
P
P
6+365.70 Line 1
P P
7+273.74 7+452.84 7+495.24 7+709.24 7+789.53 Mixer 1 8+105.58 8+385.74 8+549.41 9+000.00 9+094.49
BS FURBEROS I 37.5 MMPCSD
6+539.93
6+839.89
7+140.067+257.20
9+681.00
10+018.92
10+046.19
10+231.27
10+278.27
P
P
P
P
P
P
P
P
P
M
P
P
P
P
P
P
P
P
P
P
10+449.58 Line 2
P
13+185.63 12+891.55 12+808.20 12+703.31 12+635.54 12+351.36 12+188.27 12+000.00 11+906.34 11+862.76 11+611.25 Mixer 2
ALIMENTACIÓN 37.5 MMPCSD
11+154.94 10+985.15 10+911.08
P
13+711.55
13+628.6913+423.21
13+383.47
10+797.78
P
P
P
P
P
P
P
P
P
P
P
P
P
P
P
M
P
P
P
P
13+791.38
P
13+852.57
13+909.68
14+209.14
14+393.74
14+605.87
14+825.16
15+000.00
15+030.50
15+653.16
15+700.30
16+412.41
16+540.81
16+792.96
16+926.67
16+977.06
17+176.49
17+300.74
17+654.7517+716.56
17+803.93
P
P
P
P
P
P
P
P
P
P
P
P
P
P
P
P
18+719.29
P
18+696.49
P
18+338.51
P
18+319.79
P
18+189.21
30.30 kg/cm2
P
P
BATERÍA DE SEPARACIÓN TAJÍN V
P
P
P
PALS2000 R5 (Build 5.0.4)
G:\proc\work\LIBROS DUCTOS\Libros Gasoductos\1194 Gasoducto Pozos Fobos - BS Tajín V\REV 0(12-01-2009)\119408MCA77104_0.pa5
Fluor
Client: Plant: Site: Revision: PEMEX EXPLORACIÓN Y PRODUCCIÓN PALEOCANAL CHICONTEPEC II GASODUCTO FOBOS I - BS TAJÍN V 0
Contract: Date:
7325 12/01/2009 By: Chk'd: FGH 1 of 22 App'd: MGP JJG
SUMMARY
(150 MMPCSD, 25.00 kg/cm2) Engineer: Page
General Name Line No. Process Conditions Mass Flow Std. Volume Flow Viscosity Temperature Molecular Weight CompressibilityInlet-Outlet Conditions Density (In | Out) Velocity (In | Out) % Critical Flow - (In | Out) Velocity Head (In | Out) Dynamic Pressure (In | Out) Static Pressure (In | Out) Details Design Factor - Frictional Only Connect Effect Pipe Data Size (Nominal | Schedule) Inside Diameter
0+000.00 0 kg/hr MMSCFD cP °C 37,921.41 37.500 0.011 30.0 20.3 0.997 kg/m³ m/s % kg/cm² kg/cm²g kg/cm²g % kg/cm² in in 32.462.75 0.78 0.00 39.93 39.93 32.46 2.75 0.78 0.00 39.93 39.93 120.00 0.00 User 15.250 0.00 0.00005 0.012 32.46 2.75 0.00 246.19 3,037,346 0.78 0.000 0.00 89.42
0+128.23 1 37,921.41 37.500 0.011 30.0 20.3 0.997 32.46 2.75 0.78 0.00 39.93 39.93 32.50 2.75 0.78 0.00 39.99 39.99 120.00 0.00 User 15.250 128.23 0.00005 0.012 32.50 2.75 0.00 245.83 3,037,346 0.78 0.022 -8.98 69.41
0+621.41 2 37,921.4137.500 0.011 30.0 20.3 0.997 32.50 2.75 0.78 0.00 39.99 39.99 32.43 2.76 0.78 0.00 39.90 39.90 120.00 0.00 User 15.250 493.18 0.00005 0.012 32.43 2.76 0.00 246.38 3,037,346 0.78 0.022 2.39 89.94
0+746.49 3 37,921.41 37.500 0.011 30.0 20.3 0.997 32.43 2.76 0.78 0.00 39.90 39.90 32.42 2.76 0.78 0.00 39.89 39.89 120.00 0.00 User 15.250 125.08 0.00005 0.012 32.42 2.76 0.00 246.46 3,037,346 0.78...
1.1 Reporte de Cálculo Hidráulico en Pals 2000 R5. Presión de operación a la llegada de C.P.G. Poza Rica de 25 kg/cm2 man (150 MMPCSD).
DISEÑO, SUMINISTRO Y CONSTRUCCIÓN DE GASODUCTOS
MC-A-77-104
ELABORÓ: JJG
REV. No. 0
FECHA: 12/01/2009 119408MCA77104_0
(Name)
BATERÍA DE SEPARACIÓN FOBOS I
37.5 MMPCSD
39.93 kg/cm2
0+857.34 0+900.00 1+006.361+057.27 1+202.65 1+380.00 1+420.59 1+600.00 1+720.00 1+992.45 2+082.39 2+254.77 2+337.87 2+536.43 2+717.68 2+780.00
0+000.00
0+128.23
0+621.41
0+746.49
P
P
P
P
P
P
P
P
P
P
P
P
P
P
P
P
P
P
P
P
Line 0
P
5+707.60 5+626.12 5+496.83 5+096.99 4+911.48 4+574.37 4+401.66 4+257.44 3+900.00 Mixer 0 3+632.70 3+398.15 3+232.66ALIMENTACIÓN 37.5 MMPCSD
6+117.43
6+105.13
6+000.00
5+801.53
3+179.12
3+029.60
3+000.00
P
P
P
P
P
P
P
P
P
P
P
P
P
M
P
P
P
P
P
P
6+365.70 Line 1
P P
7+273.74 7+452.84 7+495.24 7+709.24 7+789.53 Mixer 1 8+105.58 8+385.74 8+549.41 9+000.00 9+094.49
BS FURBEROS I 37.5 MMPCSD
6+539.93
6+839.89
7+140.067+257.20
9+681.00
10+018.92
10+046.19
10+231.27
10+278.27
P
P
P
P
P
P
P
P
P
M
P
P
P
P
P
P
P
P
P
P
10+449.58 Line 2
P
13+185.63 12+891.55 12+808.20 12+703.31 12+635.54 12+351.36 12+188.27 12+000.00 11+906.34 11+862.76 11+611.25 Mixer 2
ALIMENTACIÓN 37.5 MMPCSD
11+154.94 10+985.15 10+911.08
P
13+711.55
13+628.6913+423.21
13+383.47
10+797.78
P
P
P
P
P
P
P
P
P
P
P
P
P
P
P
M
P
P
P
P
13+791.38
P
13+852.57
13+909.68
14+209.14
14+393.74
14+605.87
14+825.16
15+000.00
15+030.50
15+653.16
15+700.30
16+412.41
16+540.81
16+792.96
16+926.67
16+977.06
17+176.49
17+300.74
17+654.7517+716.56
17+803.93
P
P
P
P
P
P
P
P
P
P
P
P
P
P
P
P
18+719.29
P
18+696.49
P
18+338.51
P
18+319.79
P
18+189.21
30.30 kg/cm2
P
P
BATERÍA DE SEPARACIÓN TAJÍN V
P
P
P
PALS2000 R5 (Build 5.0.4)
G:\proc\work\LIBROS DUCTOS\Libros Gasoductos\1194 Gasoducto Pozos Fobos - BS Tajín V\REV 0(12-01-2009)\119408MCA77104_0.pa5
Fluor
Client: Plant: Site: Revision: PEMEX EXPLORACIÓN Y PRODUCCIÓN PALEOCANAL CHICONTEPEC II GASODUCTO FOBOS I - BS TAJÍN V 0
Contract: Date:
7325 12/01/2009 By: Chk'd: FGH 1 of 22 App'd: MGP JJG
SUMMARY
(150 MMPCSD, 25.00 kg/cm2) Engineer: Page
General Name Line No. Process Conditions Mass Flow Std. Volume Flow Viscosity Temperature Molecular Weight CompressibilityInlet-Outlet Conditions Density (In | Out) Velocity (In | Out) % Critical Flow - (In | Out) Velocity Head (In | Out) Dynamic Pressure (In | Out) Static Pressure (In | Out) Details Design Factor - Frictional Only Connect Effect Pipe Data Size (Nominal | Schedule) Inside Diameter
0+000.00 0 kg/hr MMSCFD cP °C 37,921.41 37.500 0.011 30.0 20.3 0.997 kg/m³ m/s % kg/cm² kg/cm²g kg/cm²g % kg/cm² in in 32.462.75 0.78 0.00 39.93 39.93 32.46 2.75 0.78 0.00 39.93 39.93 120.00 0.00 User 15.250 0.00 0.00005 0.012 32.46 2.75 0.00 246.19 3,037,346 0.78 0.000 0.00 89.42
0+128.23 1 37,921.41 37.500 0.011 30.0 20.3 0.997 32.46 2.75 0.78 0.00 39.93 39.93 32.50 2.75 0.78 0.00 39.99 39.99 120.00 0.00 User 15.250 128.23 0.00005 0.012 32.50 2.75 0.00 245.83 3,037,346 0.78 0.022 -8.98 69.41
0+621.41 2 37,921.4137.500 0.011 30.0 20.3 0.997 32.50 2.75 0.78 0.00 39.99 39.99 32.43 2.76 0.78 0.00 39.90 39.90 120.00 0.00 User 15.250 493.18 0.00005 0.012 32.43 2.76 0.00 246.38 3,037,346 0.78 0.022 2.39 89.94
0+746.49 3 37,921.41 37.500 0.011 30.0 20.3 0.997 32.43 2.76 0.78 0.00 39.90 39.90 32.42 2.76 0.78 0.00 39.89 39.89 120.00 0.00 User 15.250 125.08 0.00005 0.012 32.42 2.76 0.00 246.46 3,037,346 0.78...
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