210 04 p mc 001 estudio hidraulico

N: MEMORIA DE CALCULO 210-04-P-MC-001

Hoja: CLIENTE:

1 de 26 CHACO S.A.

PROYECTO: INGENIERIA DE DETALLE

READECUACION COMPRESOR # 9 A INTERMEDIA PLANTA CARRASCO TITULO:

MEMORIA DE CALCULO ESTUDIO HIDRAULICO

NDICE DE REVISIONES

Gonzalo Cabrera

DECS SRL Waldo Marze

COPETROL SRL Jerry Fletcher CHACO S.A.

ELABORADO POR REVISADO POR APROBADO POR

Fecha Revisin Observaciones

31-Ago-09 0 Emitido para Aprobacin.

N: MEMORIA DESCRIPTIVA 210-04-P-MC-001

Hoja: PROYECTO: 2 de 26

INGENIERIA DE DETALLE READECUACION COMPRESOR # 9 A INTERMEDIA

PLANTA CARRASCO

TITULO: MEMORIA DE CALCULO ESTUDIO HIDRAULICO

TABLA DE CONTENIDO

1. INTRODUCCION...................................................................................................................................... 3

2. OBJETIVO. .............................................................................................................................................. 3

3. PARAMETROS DE DISEO ...................................................................................................................... 3

3.1. CONDICIONES DEL FLUJO ........................................................................................................................... 3 3.2. CROMATOGRAFA DEL GAS ........................................................................................................................ 4

4. METODOLOGIA DE CALCULO. ................................................................................................................ 4

5. RESULTADOS OBTENIDOS ...................................................................................................................... 7

6. CONCLUSIONES Y RECOMENDACIONES. .............................................................................................. 10

7. ANEXO. ................................................................................................................................................ 11




PLANTA CARRASCO


1. INTRODUCCION.

Como parte de los trabajos de ingeniera de detalle del proyecto READECUACION COMPRESOR

# 9 A INTERMEDIA PLANTA CARRASCO, se requiere verificar los dimetros de las lneas de

succin y descarga para las nuevas condiciones de operacin mediante un estudio hidrulico.

2. OBJETIVO.

El objetivo del presente documento es detallar la metodologa y el estudio hidrulico realizado tanto

para la lnea de succin como para la lnea de descarga del Compresor # 9.

3. PARAMETROS DE DISEO

3.1. Condiciones del Flujo

Las condiciones de flujo en la succin del compresor son:

Presin (psig) : 467

Temperatura (F) : 72

Las condiciones de flujo en la descarga del compresor son:

Presin (psig) : 1200

Temperatura (F) : 120

El caudal de diseo es:

Caudal (MMSCFD) : 35 MMSCFD




PLANTA CARRASCO


3.2. Cromatografa del Gas

La cromatografa de gas adoptada es la proporcionada por el cliente, que corresponde al

separador V-400

COMPOSICION V - 400 (BBL 3, 8, 11LC) N2 0.2599

CO2 2.8716 C1 87.4763 C2 5.4572 C3 2.2282 iC4 0.3094 nC4 0.6489 iC5 0.2140 C5 0.2008 nC6 0.1639 C7+ 0.1698

TOTAL 100

Este gas tiene una gravedad especfica de 0.662.

4. METODOLOGIA DE CALCULO. El clculo se lo realizo mediante una simulacin hidrulica utilizando el programa Pispesim en el

modo composicional. Para poder considerar en el clculo las prdidas de carga en accesorios y

vlvulas, a las longitudes de tubera se le adiciono las longitudes equivalentes de los accesorios y

vlvulas en funcin a la Tabla 1. Las longitudes equivalentes calculadas para cada dimetro se

encuentran resumidas en la Tabla 2. EN lo que concierne a la lnea de succin, se simulo el tramo

de 6 a la salida del separador, luego el cabezal de 12 y la entrada al compresor de 10. La Figura

1 muestra el escenario utilizado en la simulacin.

La condicin de diseo para que los dimetros propuestos sean considerados aceptables, es que

la velocidad no exceda los 60 ft/seg. Los clculos se los realizo con una rugosidad de la tubera de




PLANTA CARRASCO


2000 micropulgadas lo cual representara la condicin operativa mas critica con una tubera de

acero al carbono con varios anos de uso. La tubera de succin fue considerada como espesor

estndar y la tubera de descarga SCH 80.

Tabla 1. Longitudes Equivalentes para Vlvulas y Accesorios en Pies

Fuente: Gas Processors & Suppliers Association GPSA, Engineering Data Book.




PLANTA CARRASCO


DESCRIPCION DIAMETRO CANTIDAD UNIDAD LONG. EQUIVALENTE

TUBERIA 12" 8.583 m 8.58 mTE REDUCTORA 12"x10" 1 pza 16.76 mTE REDUCTORA 12"x6" 1 pza 16.76 m

42.11 m

TUBERIA 10" 9.242 m 9.24 mCODO 10" 1 pza 3.66 mVALVULA BOLA 10" 1 pza 2.13 mVALVULA SDV 10" 1 pza 2.13 mTE REDUCTORA 10"x6" 1 pza 14.32 m

31.49 m

TUBERIA 6" 136.648 m 136.65 mCODO 6" 15 pza 36.57 mTE 6" 5 pza 42.67 mREDUCTOR 6"x4" 2 pza 2.44 mVALVULA BOLA 6" 5 pza 6.10 mVALVULA DE CONTROL 4" 1 pza 39.62 mVALVULA DE RETENCION 6" 1 pza 14.63 m

278.68 m

DESCRIPCION DIAMETRO CANTIDAD UNIDAD LONG. EQUIVALENTETUBERIA 6" 65.575 m 65.58 mCODO 6" 8 pza 19.51 mTE 6" 2 pza 17.07 mVALVULA BOLA 6" 1 pza 1.22 mVALVULA SDV 6" 1 pza 1.22 mVALVULA DE RETENCION 6" 1 pza 14.63 m

119.22 mSub-total

LINEA DE DESCARGA 6"

Sub-total

Sub-total

Sub-total

6"

12"

10"

LINEA DE SUCCION




PLANTA CARRASCO


Figura 1. Escenario Simulado.

5. RESULTADOS OBTENIDOS

La Figura 2 muestra el perfil de presiones obtenido y la Figura 3 muestra el perfil de velocidades.

La Tabla 3 resume los resultados principales de cada una de las simulaciones. El Anexo contiene

los resultados de la simulacin para la lnea de succin y descarga.

Tabla 3. Resultados Lnea de Succin y Descarga

Linea Dimetros pulgadas

Presin Cabecera

psig

Presin Final Lnea

psig

P psi

Velocidad Mxima ft/s

Succin 12, 10 y 6 467 427.8 39.2 62.9

Descarga 6 1200 1195.1 4.9 31.2




PLANTA CARRASCO


Figura 2. Perfil de Presiones.




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Figura 3. Perfil de Velocidades.




PLANTA CARRASCO


6. CONCLUSIONES Y RECOMENDACIONES. 1) La mxima velocidad se obtuvo en el tramo de 6 de la lnea de succin y fue de 62.9

ft/seg. Se pone a consideracin de Chaco el reemplazar esta lnea por una de dimetro

de 8 para tener un comportamiento hidrulico ptimo.

2) La presin de succin en el compresor seria de 427.9 psig. Se deber verificar la mnima

presin de succin del compresor en base a este parmetro.

3) La mxima velocidad registrada en la lnea de descarga fue de 31.2 ft/seg.

4) La presin de llegada en el punto de entrega a proceso (final de la lnea de descarga)

sera de 1195 psig.




PLANTA CARRASCO


7. ANEXO.

************ PIPESIM ************ Date : 31/08/09 * (Release 3.70 13/11/03) * Time : 17:00:44 * MULTIPHASE FLOW SIMULATOR * INPUT DATA ECHO * * INPUT DATA ECHO PC/DIGITAL * Schlumberger * INPUT DATA ECHO * London * Site : Licensed *********************************** Code : BJA

Data File : \\Serverdecs\PROYECTOS\Proyectos 2009\COPETROL\COMPRESOR # 9 CARRASCO\Proyecto\SIMULACION HIDRAULICA SUCCION Y DESCARGA\Compresor 9 Carrasco.pst

"C:\Archivos de programa\Schlumberger\PIPESIM\programs\psengine.exe" "\\Serverdecs\PROYECTOS\Proyectos 2009\COPETROL\COMPRESOR # 9 CARRASCO\Proyecto\SIMULACION HIDRAULICA SUCCION Y DESCARGA\Compresor 9 Carrasco.pst" -h C_19881 -v1

1 $# PIPESIM build: 031103-1.45.00 SP2 on Mon Aug 31 17:00:43 2009 2 $ \\Serverdecs\PROYECTOS\Proyectos 2009\COPETROL\COMPRESOR # 9 CARRASCO\Proyecto\SIMULACION HIDRAULICA SUCCION Y DESCARG ... A\Compresor 9 Carrasco.pst 3 4 header proj = 'READECUACION COMPRESOR # 9 CARRASCO' user = 'Gonzalo Cabrera' 5 job 'PIPESIM Job' 6 7 units input=eng output=eng 8 options eofs = 1 9 HEAT PARTBURYMETHOD = 2 10 11 options thmethod = 1 ppmethod = 1 12 print primary auxiliary profile fluid echo 13 noprint summary 14 print cases = 1 15 plot FORMAT = BJA 16 print REPORTS = ON 17 18 $********************************************* 19 $ User Units 20 $********************************************* 21 22 plotfiledata "*modelunit ENERGY PER MASS (HEAD) , ft-lbf/lbm" 23 plotfiledata "*modelunit HEAT TRANSFER COEFFICIENT , Btu/hr/ft2/F" 24 plotfiledata "*modelunit SPECIFIC VOLUME MOLE , ft3/mol" 25 plotfiledata "*modelunit ENERGY PER MASS (ENTHALPY) , Btu/lb" 26 plotfiledata "*modelunit (JONES A GAS) , (psi/mmscf/d)^2" 27 plotfiledata "*modelunit FREQUENCY , hz" 28 plotfiledata "*modelunit PER LENGTH , shots/ft"Page: 1

29 plotfiledata "*modelunit (JONES B GAS) , psi2/mmscf/d" 30 plotfiledata "*modelunit VELOCITY , ft/s" 31 plotfiledata "*modelunit FLOW RATE VOLUME BASIS (LIQ) , bbl/d" 32 plotfiledata "*modelunit FLOW RATE VOLUME BASIS (GAS) , mmcf/d" 33 plotfiledata "*modelunit VOLUME (GAS) , ft3" 34 plotfiledata "*modelunit VOLUME PER VOLUME (LGR) , STB/mmscf" 35 plotfiledata "*modelunit STD VOLUME PER VOLUME (GLR) , scf/bbl" 36 plotfiledata "*modelunit VOLUME PER VOLUME (GLR) , scf/STB" 37 plotfiledata "*modelunit TEMPERATURE , F" 38 plotfiledata "*modelunit MASS , lb" 39 plotfiledata "*modelunit STD VOLUME GAS RATE (RECIPROCAL) , 1/mmscfd" 40 plotfiledata "*modelunit STD VOLUME GAS RATE , mmscf/d" 41 plotfiledata "*modelunit DENSITY LIQUID , lb/ft3" 42 plotfiledata "*modelunit VOLUME PER STD VOLUME , bbl/mmscf" 43 plotfiledata "*modelunit (JONES A LIQ) , psi/(STB/d)^2" 44 plotfiledata "*modelunit COMPRESSIBILITY , 1/psi" 45 plotfiledata "*modelunit UNITLESS , " 46 plotfiledata "*modelunit (JONES B LIQ) , psi/STB/d" 47 plotfiledata "*modelunit SPECIFIC PRODUCTIVITY INDEX (LIQ) , STB/d/psi" 48 plotfiledata "*modelunit LENGTH SHORTRANGE , inches" 49 plotfiledata "*modelunit RATIO (%) , %" 50 plotfiledata "*modelunit STD VOLUME LIQUID RATE (RECIPROCAL) , 1/stbd" 51 plotfiledata "*modelunit PRESSURE (DELTA) , psi" 52 plotfiledata "*modelunit (TEMPERATURE PER PRESSURE) , F/psi" 53 plotfiledata "*modelunit VOLUME (LIQUID) , ft3" 54 plotfiledata "*modelunit AREA EARTH SURFACE , ft2" 55 plotfiledata "*modelunit SPECIFIC PRODUCTIVITY INDEX (LIQ PER LENGTH) , STB/d/psi/ft" 56 plotfiledata "*modelunit VISCOSITY DYNAMIC , cP" 57 plotfiledata "*modelunit FLOW RATE VOLUME BASIS (GAS) , ACFM" 58 plotfiledata "*modelunit THERMAL CONDUCTIVITY , Btu/hr/ft/F" 59 plotfiledata "*modelunit SPECIFIC PRODUCTIVITY INDEX (GAS) , mmscf/d/psi2" 60 plotfiledata "*modelunit AREA , in2" 61 plotfiledata "*modelunit PERMEABILITY , md" 62 plotfiledata "*modelunit SPECIFIC ENTROPY , Btu/lb/F" 63 plotfiledata "*modelunit POWER , hp" 64 plotfiledata "*modelunit PRESSURE GRADIENT , psi/ft" 65 plotfiledata "*modelunit SURFACE TENSION , dyne/cm" 66 plotfiledata "*modelunit TIME , hr" 67 plotfiledata "*modelunit SPECIFIC PRODUCTIVITY INDEX (GAS PER LENGTH) , mmscf/d/psi2/ft" 68 plotfiledata "*modelunit STD VOLUME LIQUID RATE , STB/d" 69 plotfiledata "*modelunit PRESSURE , psia" 70 plotfiledata "*modelunit FLOW RATE MASS BASIS , lb/s" 71 plotfiledata "*modelunit LENGTH MIDRANGE , ft" 72 $********************************************* 73 74 $*********************************************Page: 2

75 $ CORRELATIONS 76 $********************************************* 77 78 vcorr type = HBR angle = 45 ffactor = 1 hfactor = 1 79 hcorr type = BBR ffactor = 1 hfactor = 1 80 sphase corr = Moody 81 82 $********************************************* 83 $ FLUID DATA - _default 84 $ Description : 85 $********************************************* 86 87 comp file = '\\Serverdecs\PROYECTOS\Proyectos 2009\COPETROL\COMPRESOR # 9 CARRASCO\Proyecto\SIMULACION HIDRAULICASUCCIO ... N Y DESCARGA\Compresor 9 Carrasco.ptt' 88 89 90 $********************************************* 91 $ Inlet 92 $********************************************* 93 94 inlet temp = 72 pres = 481.696 95 96 97 $********************************************* 98 $ OPERATION 99 $********************************************* 100 include 'Compresor 9 Carrasco_PTProf.inc' o_PTProf.inc 1 $# on Mon Aug 31 17:00:43 2009 o_PTProf.inc 2 o_PTProf.inc 3 $************************************************************** o_PTProf.inc 4 $ Pressure/Temperature Profiles o_PTProf.inc 5 $************************************************************** o_PTProf.inc 6 plot casedata jobdata xycase = bd o_PTProf.inc 7 rate gas = 35 MMSCFD o_PTProf.inc 8 inlet pres = 481.696 psia 101 102 $********************************************* 103 PROFILE 104 $********************************************* 105 $ *** Profile Description from node : V-400 106 107 FLOWLINE label = 'Tramo de 6' 108 slug piss = on size = ssb 109 pipe id = 6.065 wt = 0.28 flowtype = tubing roughness = 0.002 110 heat ifc = input u = inputPage: 3

111 node dist = 0 elev = 0 temp = 72 u = 0.2 112 node dist = 457.152 elev = 0 113 node dist = 914.304 elev = 0 temp = 72 u = 0.2 114 115 FLOWLINE label = 'Tramo de 12' 116 slug piss = on size = ssb 117 pipe id = 12 wt = 0.375 flowtype = tubing roughness = 0.002 118 heat ifc = input u = input 119 node dist = 0 elev = 0 temp = 72 u = 0.2 120 node dist = 14.0797 elev = 0 121 node dist = 28.1594 elev = 0 temp = 72 u = 0.2 122 123 FLOWLINE label = 'Tramo de 10' 124 slug piss = on size = ssb 125 pipe id = 10.02 wt = 0.365 flowtype = tubing roughness = 0.002 126 heat ifc = input u = input 127 node dist = 0 elev = 0 temp = 72 u = 0.2 128 node dist = 51.6568 elev = 0 129 node dist = 103.314 elev = 0 temp = 72 u = 0.2 130 131 COMPRESSOR label = 'Compresor # 9' route = Adiabatic pout = 1214.7 eff = 90 stonewall = on 132 FLOWLINE label = 'LINEA DE 6' 133 slug piss = on size = ssb 134 pipe id = 5.761 wt = 0.432 flowtype = tubing roughness = 0.002 135 heat ifc = input u = input 136 node dist = 0 elev = 0 temp = 120 u = 0.2 137 node dist = 195.571 elev = 0 138 node dist = 391.142 elev = 0 temp = 120 u = 0.2 139

NO SYNTAX ERRORS DETECTED.

Page: 4

************ PIPESIM ************ Date : 31/08/09 * (Release 3.70 13/11/03) * Time : 17:00:44 * MULTIPHASE FLOW SIMULATOR * Case no. 1 Fluid Property Data * * Case no. 1 Fluid Property Data PC/DIGITAL * Schlumberger * Case no. 1 Fluid Property Data * London * Site : Licensed *********************************** Code : BJA

Project : READECUACION COMPRESOR # 9 CARRASCO User : Gonzalo Cabrera Data File : \\Serverdecs\PROYECTOS\Proyectos 2009\COPETROL\COMPRESOR # 9 CARRASCO\Proyecto\SIMULACION HIDRAULICA SUCCION Y DESCARGA\Compresor 9 Carrasco.pst

Job : 'PIPESIM Job' Case 1 :

*********************************************************** * Compositional Case * * Properties and Flow Rates at the System Inlet * ***********************************************************

Composition data: ----------------

Composition obtained from ......... supplied .pvt file "\\Serverdecs\PROYECTOS\Proyectos 2009\COPETROL\COMPRESOR# 9 CARRASCO\Proyecto\SIMULACION HIDRAULICA SUCCION Y DESCARGA\Compresor 9 Carrasco.ptt" Composition Mangler handle ........ E4554F9F Fluid title ....................... ...untitled. Molecular Weight .................. 19.161 Fluid physical property tables .... will be created on-the-fly by "inline flashing"

Table Pressure and Temperature grid points : ------------------------------------------

Pressures (psia) 14.5 21.7 32.4 48.4 72.4 108.2 161.8 241.9 361.6 540.5 807.9 1207.6 1805.2 2698.4 4033.6 6029.5 9012.9 13472.6 20139.1 30104.1 Temperatures (F) -60.0 -30.0 0.0 30.0 60.0 90.0 120.0 150.0 180.0 210.0 240.0 270.0 300.0 330.0 360.0 390.0 420.0 450.0 480.0 510.0Page: 5

Component molar flowrates and characterization values : -----------------------------------------------------

Component Mole % Molecular Boiling Specific Critical Critical Acentric Weight Point Gravity Temperature Pressure Factor (F) (F) (psia)

Nitrogen .2599000 28.01348 -320.4436 .2813015 -232.5244 492.5191 .03720000 Carbon Dioxide 2.8715999 44.00980 -63.66999 .8394406 87.76078 1069.987 .2230000 Methane 87.4763031 16.04280 -258.7360 .1460437 -116.6548 667.0576 .01040000 Ethane 5.4572001 30.07000 -127.4800 .3664479 89.92399 706.5948 .09910000 Propane 2.2282000 44.09560 -43.77998 .5159282 206.0600 616.0710 .1520000 Isobutane .3094000 58.12220 10.88604 .5621799 274.4600 527.9374 .1844000 Butane .6489000 58.12220 31.10000 .5837152 305.6180 550.5632 .1985000 Isopentane .2140000 72.15030 82.18401 .6242590 369.1400 489.7924 .2270000 Pentane .2008000 72.14878 96.90800 .6300491 385.7900 488.2695 .2513000 Hexane .1639000 86.17536 155.7140 .6627554 454.4060 437.7384 .2979000 Heptane .1698000 100.2020 209.1740 .6875612 512.5640 395.5179 .3498000

Stock-tank properties & Composition Manager attributes: -------------------------------------------------------

Origin of composition : file "\\Serverdecs\PROYECTOS\Proyectos 2009\COPETROL\COMPRESOR # 9 CARRASCO\Proyecto\SIMULACION HIDRAULICA SUCCION Y DESCARGA\Compresor"

Composition Manager Handle : E4554F9F Equation of state : RKS Viscosity model : PEDERSEN Fraction Liquid by Volume : 0.000000 BIP set : OIL4 Watercut in Liquid : 0.0000 % Cricondenbar : 0.0000 PSIA Water Specific Gravity : 1.020000 "One component" behaviour : NO Oil Specific Gravity : 0.850000 Table fill type : 1 Gas Specific Gravity : 0.661651 Physical Properties Package : Multiflash Gas Molar Volume : 2642.51 lb.mol/mmscf Inline flashing : YES

Page: 6

Stock-tank Component Phase Split : --------------------------------

Mole % Molar Flow Rate (lb.mol/s)

Feed Vapour Feed Vapour ------------------------------------------------------------ Nitrogen 0.260 0.260 .002782129 .002782129 Carbon Dioxide 2.872 2.872 .03073937 .03073937 Methane 87.476 87.476 .9364000 .9364000 Ethane 5.457 5.457 .05841722 .05841722 Propane 2.228 2.228 .02385202 .02385202 Isobutane 0.309 0.309 .003312007 .003312007 Butane 0.649 0.649 .006946223 .006946224 Isopentane 0.214 0.214 .002290787 .002290787 Pentane 0.201 0.201 .002149486 .002149486 Hexane 0.164 0.164 .001754486 .001754486 Heptane 0.170 0.170 .001817643 .001817643 ------------------------------------------------------------ Total 100.000 100.000 1.070461 1.070461

Mole split 100.000 100.000 % Mass split 100.000 100.000 % Volume split 100.000 99.999 %

Mass rate 20.51154 20.51154 lb/s Volume rate 3.49904E07 3.49900E07 ft3/day Volume rate 6232058. 6231995. bbl/day

Molecular Weight 19.16141 19.16141 g/mol Enthalpy -166.7660 -166.7660 BTU/mol Entropy .8055700 .8055700 BTU/mol.F Gibbs Energy -585.3965 BTU/mol Isobaric Heat Cap. 9.201900 BTU/mol.F Isochoric Heat Cap. 7.188726 BTU/mol.F Joule Thompson Coef. .07333708 BTU/mol.F Molar Volume .3783203 ft3/mol Compressibility (Z) .9972228 Density .05064811 .05064863 lb/ft3 Speed of Sound 1310.146 ft/s Viscosity .01090681 cP Thermal Conductivity .01727274 BTU/Hr.ft. Gross Heating Value 1101.125 1101.125 btu/scf Gross Heating Value 21785.86 21785.86 btu/lb Page: 7

WOBE index 1353.793 1353.793

Methods Data : ------------

Fluid properties obtained by ...... method 1: interpolation from tables throughout Temperature-Energy balance by ..... method 1: interpolation from tables throughout Physical Properties Package ....... Multiflash

Fluid Thermal Conductivity Data : ------------------------------- Oil Conductivity .................. .80000E-01 (btu/hr/ft/F) Gas Conductivity .................. .20000E-01 (btu/hr/ft/F) Water Conductivity ................ .35000 (btu/hr/ft/F) Run Data : -------- Inlet Temperature ................. 72.000 (F) Inlet Pressure .................... 481.70 (psia) Stock-tank Flow Rate Data : ------------------------- Gross liquid flow rate ............ .00000 (stb/d) Gross oil flow rate ............... .00000 (stb/d) Gas flow rate ..................... 35.000 (mmft3d) Mass flow rate .................... 20.512 (lb/s) Water cut ......................... .00000 (%) Gas Liquid ratio .................. infinite (scf/stb) Gas Oil ratio ..................... infinite (scf/stb) Oil Gas ratio ..................... .00000 (bbl/mmscf) Liquid Gas ratio .................. .00000 (bbl/mmscf) Water Gas ratio ................... .00000 (bbl/mmscf) Gas Water ratio ................... infinite (scf/stb)Page: 8

Inlet Enthalpy .................... -19.522 (Btu/lb)

Page: 9

************ PIPESIM ************ Date : 31/08/09 * (Release 3.70 13/11/03) * Time : 17:00:44 * MULTIPHASE FLOW SIMULATOR * Case no. 1 Profile & Flow Correlations * * Case no. 1 Profile & Flow Correlations PC/DIGITAL * Schlumberger * Case no. 1 Profile & Flow Correlations * London * Site : Licensed *********************************** Code : BJA

Project : READECUACION COMPRESOR # 9 CARRASCO User : Gonzalo Cabrera Data File : \\Serverdecs\PROYECTOS\Proyectos 2009\COPETROL\COMPRESOR # 9 CARRASCO\Proyecto\SIMULACION HIDRAULICA SUCCION Y DESCARGA\Compresor 9 Carrasco.pst

Job : 'PIPESIM Job' Case 1 :

Profile Data ------------ Node Node Node Section Total Ambient Input no. distance elevation length length temp. U (feet) (feet) (feet) (feet) (F) (Btu/hr/ft2/F) Fluid

FLOWLINE Tramo de 6 1 0.0 0.0 0.0 0.0 72.0 0.200 DRAULICA SUCCION Y DESCARGA\Compresor 9 2 457.2 0.0 457.2 457.2 72.0 0.200 DRAULICA SUCCION Y DESCARGA\Compresor 9 3 914.3 0.0 457.2 914.3 72.0 0.200 DRAULICA SUCCION Y DESCARGA\Compresor 9 FLOWLINE Tramo de 12 4 0.0 0.0* 0.0 914.3 72.0 0.200 DRAULICA SUCCION Y DESCARGA\Compresor 9 5 14.1 0.0 14.1 928.4 72.0 0.200 DRAULICA SUCCION Y DESCARGA\Compresor 9 6 28.2 0.0 14.1 942.5 72.0 0.200 DRAULICA SUCCION Y DESCARGA\Compresor 9 FLOWLINE Tramo de 10 7 0.0 0.0* 0.0 942.5 72.0 0.200 DRAULICA SUCCION Y DESCARGA\Compresor 9

Page: 10

8 51.7 0.0 51.7 994.1 72.0 0.200 DRAULICA SUCCION Y DESCARGA\Compresor 9 9 103.3 0.0 51.7 1045.8 72.0 0.200 DRAULICA SUCCION Y DESCARGA\Compresor 9 FLOWLINE LINEA DE 6 10 0.0 0.0* 0.0 1045.8 120.0 0.200 DRAULICA SUCCION Y DESCARGA\Compresor 9 11 195.6 0.0 195.6 1241.4 120.0 0.200 DRAULICA SUCCION Y DESCARGA\Compresor 9 12 391.1 0.0 195.6 1436.9 120.0 0.200 DRAULICA SUCCION Y DESCARGA\Compresor 9

* - indicates a change of datum

Flow Correlations and options -----------------------------

Vertical Flow pattern ................................ Not used. Vertical Flow holdup ................................. Not used. Vertical Flow pressure loss .......................... Not used. Vertical Friction multiplier ......................... 1.0000 Vertical Holdup multiplier ........................... 1.0000 Horizontal Flow pattern .............................. BEGGS & BRILL Horizontal Flow holdup ............................... BEGGS & BRILL (REVISED) Horizontal Flow pressure loss ........................ BEGGS & BRILL (REVISED) Horizontal Friction multiplier ....................... 1.0000 Horizontal Holdup multiplier ......................... 1.0000 Horizontal / vertical swap angle .................... 45.00000 degrees from horizontal Single Phase Correlation ............................. Moody Diagram (Colebrook-White Eqn.) Liquid volume fraction lower limit ................... 1.000e-5 (Single-phase correlation will be used outside the limits, Liquid volume fraction upper limit ................... 0.990000 multi-phase correlations will be used inside the limits) Pipe Wall Roughness .................................. .0020000 (ins.) Erosion Velocity 'K' value ........................... 100.00

Page: 11

************ PIPESIM ************ Date : 31/08/09 * (Release 3.70 13/11/03) * Time : 17:00:44 * MULTIPHASE FLOW SIMULATOR * Case no. 1 Primary Output * * Case no. 1 Primary Output PC/DIGITAL * Schlumberger * Case no. 1 Primary Output * London * Site : Licensed *********************************** Code : BJA Project : READECUACION COMPRESOR # 9 CARRASCO User : Gonzalo Cabrera Data File : \\Serverdecs\PROYECTOS\Proyectos 2009\COPETROL\COMPRESOR # 9 CARRASCO\Proyecto\SIMULACION HIDRAULICA SUCCION Y DESCARGA\Compresor 9 Carrasco.pst Job : 'PIPESIM Job' Case 1 : Dist. Elev. Horiz. Vert. Pres. Temp. Mean Pressure Drop Liquid Free Densities Slug Flow Angle Devn. Vel. (psi) Flow Gas (lb/ft3) Number Pattern (feet) (feet) (deg) (deg) (psia) (F) (ft/s) Elev. Frictn. (bbl/d) (mmscfd) Liquid Gas (PI-SS) FLOWLINE Tramo de 6 1 0.0000 0.0000 0.000 90.00 481.70 72.000 57.729 0.0000 0.0000 9.5681 35.0476 38.672 1.7690 B/B DISTRIBUTED 2 457.15 0.0000 0.000 90.00 462.94 70.721 60.052 0.0000 18.712 8.9973 35.0476 38.672 1.7007 77873. B/B DISTRIBUTED 3 914.30 0.0000 0.000 90.00 443.19 69.360 62.735 0.0000 19.686 8.1037 35.0482 38.672 1.6281 43232. B/B DISTRIBUTED FLOWLINE Tramo de 12 (new datum) 4 0.0000 0.0000 0.000 90.00 442.81 69.360 16.041 0.0000 0.0000 8.0726 35.0483 38.672 1.6265 B/B SEGREGATED 5 14.080 0.0000 0.000 90.00 442.80 69.360 16.042 0.0000 .01245 8.0718 35.0482 38.672 1.6265 42752. B/B SEGREGATED 6 28.159 0.0000 0.000 90.00 442.79 69.359 16.042 0.0000 .01245 8.0709 35.0483 38.672 1.6264 42121. B/B SEGREGATED FLOWLINE Tramo de 10 (new datum) 7 0.0000 0.0000 0.000 90.00 442.77 69.359 23.009 0.0000 0.0000 8.0696 35.0483 38.672 1.6264 B/B DISTRIBUTED 8 51.657 0.0000 0.000 90.00 442.62 69.351 23.018 0.0000 .15531 8.0607 35.0483 38.672 1.6258 39983. B/B DISTRIBUTED 9 103.31 0.0000 0.000 90.00 442.46 69.342 23.026 0.0000 .15538 8.0516 35.0483 38.672 1.6252 38051. B/B DISTRIBUTED ** COMPRESSOR : POUT = 1214.7 psia Power = 1806.2 hp DP = 772.24 psi DT = 116.64 F Eff = 90% Route ADIABATICPage: 12

FLOWLINE LINEA DE 6 (new datum) 10 0.0000 0.0000 0.000 90.00 1214.6 185.98 31.071 0.0000 0.0000 0.0000 35.0000 .00010 3.6469 GAS 11 195.57 0.0000 0.000 90.00 1212.2 185.81 31.125 0.0000 2.4077 0.0000 35.0000 .00010 3.6406 Huge GAS 12 391.14 0.0000 0.000 90.00 1209.7 185.63 31.179 0.0000 2.4119 0.0000 35.0000 .00010 3.6342 Huge GAS

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************ PIPESIM ************ Date : 31/08/09 * (Release 3.70 13/11/03) * Time : 17:00:44 * MULTIPHASE FLOW SIMULATOR * Case no. 1 Auxiliary Output * * Case no. 1 Auxiliary Output PC/DIGITAL * Schlumberger * Case no. 1 Auxiliary Output * London * Site : Licensed *********************************** Code : BJA Project : READECUACION COMPRESOR # 9 CARRASCO User : Gonzalo Cabrera Data File : \\Serverdecs\PROYECTOS\Proyectos 2009\COPETROL\COMPRESOR # 9 CARRASCO\Proyecto\SIMULACION HIDRAULICA SUCCION Y DESCARGA\Compresor 9 Carrasco.pst Job : 'PIPESIM Job' Case 1 : Dist. Elev. Pipe Superficial Mass Flow Rates Viscosities Reynolds Liquid Liquid Enth. Itrn. Flash / Table I.D. Vel. (ft/s) (lb/s) (Centipoise) Number Volume Holdup NO. Interpolation (feet) (feet) (ins.) Liq. Gas Liq. Gas Liq. Gas /E6 Frn. Frn. (Btu/lb) T P Diagnostics FLOWLINE Tramo de 6 1 0. 0.0 6.065 0.003 57.73 0.02 20.49 0.260 0.0119 6.4558 0.00005 0.00232 -19.5 2 2 8388II 2 457. 0.0 6.065 0.003 60.05 0.02 20.49 0.260 0.0118 6.4882 0.00005 0.00218 -19.5 2 2 8388II 3 914. 0.0 6.065 0.003 62.73 0.02 20.49 0.260 0.0118 6.5232 0.00004 0.00199 -19.5 2 2 8388II FLOWLINE Tramo de 12 (new datum) 4 0. 0.0 12.000 0.001 16.04 0.02 20.49 0.260 0.0118 3.2972 0.00004 0.00570 -19.5 2 2 8388II 5 14. 0.0 12.000 0.001 16.04 0.02 20.49 0.260 0.0118 3.2972 0.00004 0.00570 -19.5 2 2 8388II 6 28. 0.0 12.000 0.001 16.04 0.02 20.49 0.260 0.0118 3.2972 0.00004 0.00570 -19.5 2 2 8388II FLOWLINE Tramo de 10 (new datum) 7 0. 0.0 10.020 0.001 23.01 0.02 20.49 0.260 0.0118 3.9488 0.00004 0.00231 -19.5 2 2 8388II 8 52. 0.0 10.020 0.001 23.02 0.02 20.49 0.260 0.0118 3.9489 0.00004 0.00230 -19.5 2 2 8388IIPage: 14

9 103. 0.0 10.020 0.001 23.02 0.02 20.49 0.260 0.0118 3.9491 0.00004 0.00230 -19.5 2 2 8388II FLOWLINE LINEA DE 6 (new datum) 10 0. 0.0 5.761 0.000 31.07 0.00 20.51 0.000 0.0151 5.3643 0.00000 0.00000 26.7 2 2 8II 11 196. 0.0 5.761 0.000 31.12 0.00 20.51 0.000 0.0151 5.3672 0.00000 0.00000 26.6 2 2 8II 12 391. 0.0 5.761 0.000 31.18 0.00 20.51 0.000 0.0151 5.3701 0.00000 0.00000 26.6 2 2 8II

Case 1 complete. Sections = 11 total segments = 48 run units = 544

System Plot file for this job is : Compresor 9 Carrasco.plt

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210-04-P-MC-001 Estudio Hidraulico_1.pdfANEXO A SIMULACION HIDRAULICA.pdf

210 04 p mc 001 estudio hidraulico

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