BBBB

Simulation Results

NETWORK SIMULATION SOLVED

Input File

Input Reprint

Solution History

Node Summary

Link Summary

Device Summary

Structure Summary

Velocity Summary

Results Summary

Flash Summary

Pump Summary

PhaseData

L000

$ SIMSCI PIPEPHASE Version 9.6.0 keyword file...

$

$General Data Section

$

TITLE PROJECT=KEROSENO, PROBLEM=BOMBEOLIQUI, *

USER=ALVAROQUINT, DATE=112714, SITE=COCHABAMBA

$

DESCRIPTION Simulacion de estacion de Bombeo Para Materia DE Transporte

DESCRIPTION de Hidrocarburos. Simulacion Con los datos del

DESCRIPTION Caso de Estudio Propuestos Por el Ingeniero

DESCRIPTION Marco Paniagua

$

CALCULATION NETWORK, Compositional, PRANDTL, *

TRUEMWD

$

DEFAULT IDPIPE=3.068, IDTUBING=4.026, IDANNULUS=6.065, *

TAMBIENT=60, HAUSEN

$

PRINT INPUT=FULL, DEVICE=FULL, PLOT=FULL, *

PROPERTY=FULL, FLASH=FULL, MAP=NONE, *

CONNECT=NONE, MERGESUB, ITER, *

SUMMARY=BOTH, DATABASE=FULL, SIMULATOR=PART

$

SEGMENT AUTO=OFF, DLHORIZ(FT)=2000, DLVERT(FT)=500

$

LIMITS PRES(MIN)=0, PRES(MAX)=50000

$

$Component Data Section

$

COMPONENT DATA

$

PETRO(API) 1, KEROSENE, 175.000, 49.910, 240.000

LIBID 2, H2O / *

3, N2 , BANK=SIMSCI , PROCESS

$

PHASE VL=1,3

$

ASSAY CHARACTERIZE=SIMSCI, MW=SIMSCI, CONVERSION=API94, *

CURVEFIT=IMPR, FIT=SPLINE

$

$Network Data Section

$

Index

Input File: C:\Users\VAIO\Desktop\Trabajo de Tranporte Ultimo\Trasiente\BBBB

NETWORK DATA

$

SOLUTION PBALANCE, FLOWAL=2, STEP=1

$

TOLERANCE PRESSURE=0.1

$

$Thermodynamic Data Section

$

THERMODYNAMIC DATA

$

METHOD SET=SET01, SYSTEM=SRK

$

WATER PROPERTY=Super

$

KVALUE BANK=SimSci

$

$PVT Data Section

$

PVT PROPERTY DATA

$

SET SETNO=1, SET=SET01

$

$Structure Data Section

$

STRUCTURE DATA

$

SOURCE NAME=S000, IDNAME=S000, PRIORITY=0, *

PRES=5000, TEMP=60, RATE(W)=1300, *

XCORD=-139, YCORD=369, *

COMP(M)=1, 99 / 2, 0.8 / 3, 0.2

$

SINK NAME=D000, IDNAME=D000, PRES(ESTI)=1, *

RATE(ESTI)=1, XCORD=1964, YCORD=477

$

$

$

LINK NAME=L000, FROM=S000, TO=D000, *

IDNAME=L000, IDFROM=S000, IDTO=D000

PIPE NAME=P000, LENGTH(MI)=50, ROUGH(IN)=7.341e-003

PUMP NAME=P002, PRES=30000

COOLER NAME=C000, TOUT=30

PIPE NAME=P001, LENGTH(MI)=1, ROUGH(IN)=7.341e-003

$

$ End of keyword file...

$

END

Input Data

PROBLEM DESCRIPTION

SIMULACION DE ESTACION DE BOMBEO PARA MATERIA DE TRANSPORTE

DE HIDROCARBUROS. SIMULACION CON LOS DATOS DEL

CASO DE ESTUDIO PROPUESTOS POR EL INGENIERO

MARCO PANIAGUA

CALCULATION OPTIONS

RUN TYPE........ NETWORK

FLUID TYPE...... COMPOSITIONAL

DIMENSIONAL UNITS - PETROLEUM

TEMPERATURE..... DEG F PRESSURE........ PSIG

MOLAR RATE...... MOLE/HR WEIGHT RATE..... LB/HR

LIQUID RATE..... BBL/DAY VAPOR RATE...... MM FT3/DAY

COARSE LENGTH... FT FINE LENGTH..... IN

DENSITY/GRAVITY. DEG API VISCOSITY....... CP

DUTY............ MM BTU/HR POWER........... HP

VELOCITY........ MPH

DEFAULTS

FLOW EFFICIENCY............ 100.00 PERCENT

HAZEN-WILLIAMS COEFF....... 150.00

ROUGHNESS.................. 0.00180 IN

AMBIENT TEMPERATURE........ 60.00 DEG F

TEMPERATURE GRADIENT....... 1.00 DEG F/100 FT

PIPE U-FACTOR.............. 1.000 BTU/HR-FT2-F

TUBING U-FACTOR............ 1.000 BTU/HR-FT2-F

ANNULUS U-FACTOR........... 1.000 BTU/HR-FT2-F

INSIDE DIAMETER - PIPE..... 3.068 IN

INSIDE DIAMETER - TUBING... 4.026 IN

INSIDE DIAMETER - ANNULUS.. 6.065 IN

LAMINAR INSIDE FILM COEFF.. HAUSEN

FLOW CODES

PIPE FLOW CODE IS BEGGS-BRILL (MOODY)

REYNOLDS NUMBER(LAMINAR)..... 3000.0000

TUBING FLOW CODE IS BEGGS-BRILL (MOODY)

ANNULUS FLOW CODE IS BEGGS-BRILL (MOODY)

Index

BASE CONDITIONS

STANDARD TEMPERATURE..... 60.00 DEG F

STANDARD PRESSURE........ 0.00 PSIG

LIMITS

MINIMUM PRESSURE......... 0.00 PSIG

MAXIMUM PRESSURE......... 50000.00 PSIG

MINIMUM TEMPERATURE...... -60.00 DEG F

MAXIMUM TEMPERATURE...... 800.00 DEG F

PRINT OPTIONS

INPUT........... GENERAL ASSAY COMPONENT

PVT FLOW TABLE METHOD

SOURCE STRUCTURE W ANALYSIS

GAS LIFT CASE STUDY

CONNECT......... FULL

PVTGEN.......... NONE

SUMMARY......... BOTH

DEVICE.......... FULL

PROPERTY........ FULL

FLASH........... FULL

STREAM.......... SUMMARY

INTERMEDIATE ITERATION PRINTOUT REQUESTED

MERGED SUBNETWORKS REQUESTED

SEGMENTATION OPTIONS

LENGTH CHANGE - HORIZONTAL....... 2000.0 FT

VERTICAL......... 500.0 FT

MAXIMUM NUMBER OF SEGMENTS....... 20

SOLUTION METHODS/TOLERANCES

NETWORK SOLUTION METHOD IS PBAL

MAXIMUM ITERATIONS..................... 20

MAXIMUM NUMBER OF INTERVAL HALVINGS.... 3

ABSOLUTE PRESSURE TOLERANCE............ 0.100000 PSIG

RATE PERTURBATION...................... 0.010000

METHOD OF INITIAL SOLUTION ESTIMATION.. FLOW = 2

ZERO FLOW IN CHECK VALVES.............. OFF

CHOKE CRITICAL FLOW MODEL (FORTUNATI) . EXPONENTIAL

NEW ACCELERATION OPTION IS............. OFF

SOURCE S000

(S000)

PHASE IS MIXED

THIS SOURCE IS ON

RATE...................... 1300.0000 LB/HR

PRESSURE.................. 5000.0041 PSIG

TEMPERATURE............... 60.00 DEG F

LINK L000

LINK IS FROM "S000 " TO "D000 "

"L000" FROM "S000" TO "D000"

DEVICE SA001, P000, IS A PIPE

FLOW CODE IS BEGGS-BRILL (MOODY)

INSIDE DIAMETER.............. 3.0680 IN

LENGTH....................... 264000.0 FT

ELEVATION CHANGE............. 0.0 FT

FLOW EFFICIENCY.............. 100.00 PERCENT

HEAT LOSS COEFFICIENT........ 1.00000 BTU/HR-FT2-F

ROUGHNESS.................... 0.00734 IN

AMBIENT TEMPERATURE.......... 60.00 DEG F

DEVICE SA002, P002, IS A PUMP

THIS IS A SURFACE DEVICE

NUMBER OF STAGES............. 1

OUTLET PRESSURE.............. 30000.00 PSIG

ADIABATIC EFFICIENCY......... 100.00 PERCENT

DEVICE SA003, C000 IS A COOLER

OUTLET TEMPERATURE........... 30.00 DEG F

PRESSURE DROP................ 0.00 PSIG

OVERALL HEAT TRANS. COEFF.... 20.0000 BTU/HR-FT2-F

DEVICE SA004, P001, IS A PIPE

FLOW CODE IS BEGGS-BRILL (MOODY)

INSIDE DIAMETER.............. 3.0680 IN

LENGTH....................... 5280.0 FT

ELEVATION CHANGE............. 0.0 FT

FLOW EFFICIENCY.............. 100.00 PERCENT

HEAT LOSS COEFFICIENT........ 1.00000 BTU/HR-FT2-F

ROUGHNESS.................... 0.00734 IN

AMBIENT TEMPERATURE.......... 60.00 DEG F

JUNCTIONS AND SINKS

SINK D000

(D000)

ESTIMATED RATE............ 1.0000 LB/HR

ESTIMATED PRESSURE........ 1.0000 PSIG

END OF INPUT PROCESSING -- NO ERRORS

-- NO WARNINGS

==============================================================================

VLE K-VALUE DATA FOR SET 'SET01'

SRK PURE COMPONENT DATA

COMP CRITICAL CRITICAL ALPHA C1 C2 C3

TEMPERATURE PRESSURE TYPE

DEG F PSIG

---- ---------- ---------- ----- ---------- ---------- ----------

1 586.94 443.92 1 0.9182 N/A N/A

2 705.16 3184.11 2 1.0000 0.6620 0.8000

3 -232.51 478.43 1 0.5391 N/A N/A

SRK INTERACTION PARAMETERS

KIJ = A(I,J) + B(I,J)/T + C(I,J)/T**2

I J KA(I,J) KB(I,J) KC(I,J) UNITS FROM

--- --- ---------- ---------- ---------- ----- ----

1 2 0.3657 0.00 0.00 DEG K WATER CORRELATION

1 3 0.2000 0.00 0.00 DEG K MW CORRELATION

2 3 0.5300 0.00 0.00 DEG K SIMSCI BANK

==============================================================================

THERMODYNAMIC SETS USED FOR EACH UNIT OPERATION

DEFAULT METHOD IS SET01

THERMODYNAMIC SET UNIT OPERATIONS

----------------- ---------------

SET01

==============================================================================

THERMODYNAMIC METHODS USED FOR EACH SET

THERMODYNAMIC SET SET01 (DEFAULT)

PROPERTY METHOD

-------- ------

KVALUE(VLE) SOAVE-REDLICH-KWONG

KVALUE(LLE) UNSPECIFIED

KVALUE(SLE) UNSPECIFIED

LIQUID ENTHALPY SOAVE-REDLICH-KWONG

VAPOR ENTHALPY SOAVE-REDLICH-KWONG

LIQUID DENSITY API

VAPOR DENSITY SOAVE-REDLICH-KWONG

LIQUID ENTROPY SOAVE-REDLICH-KWONG

VAPOR ENTROPY SOAVE-REDLICH-KWONG

LIQUID VISCOSITY PETROLEUM

VAPOR VISCOSITY PETROLEUM

LIQUID CONDUCTIVITY PETROLEUM

VAPOR CONDUCTIVITY PETROLEUM

SURFACE TENSION PETROLEUM

LIQUID DIFFUSIVITY UNSPECIFIED

==============================================================================

COMPONENT COMP. TYPE PHASE MOL. WEIGHT API

--------------------- ----------- ----------- ----------- -----------

1 KEROSENE PETRO CUT VAP/LIQ 175.000 49.910

2 H2O LIBRARY VAP/LIQ 18.015 10.000

3 N2 LIBRARY VAP/LIQ 28.013 43.460

COMPONENT NBP CRIT. TEMP. CRIT. PRES. CRIT. VOLM.

F F PSIG BBL/LB-MOL

--------------------- ----------- ----------- ----------- -----------

1 KEROSENE 240.000 586.936 443.920 1.1529

2 H2O 212.000 705.164 3184.110 0.1596

3 N2 -320.451 -232.510 478.432 0.2545

COMPONENT ACEN. FACT. HEAT FORM. G FORM.

BTU/LB-MOL BTU/LB-MOL

--------------------- ----------- ----------- -----------

1 KEROSENE 0.28762 -63479.04 MISSING

2 H2O 0.34486 -103961.31 -98276.01

3 N2 0.03772 0.00 0.00

COMPONENT DATABANK(S) USED

--------------------- ---------------------

2 H2O SIMSCI

3 N2 SIMSCI

==============================================================================

==============================================================================

==============================================================================

==============================================================================

Solution History

R

PIPEPHASE Version 9.6 - INPUT MODULE

==========================================

*** SCANNING

GENERAL DATA

COMPONENT DATA

METHODS DATA

THERMODYNAMIC DATA

PROPERTY DATA

STRUCTURE DATA

END OF PRE-PROCESSING -- NO ERRORS

R

PIPEPHASE Version 9.6 - CROSS CHECKING MODULE

===================================================

*** CHECKING

GENERAL DATA

STRUCTURE DATA

CASE STUDY DATA

PVTG DATA

METHODS DATA

*** INPUT REPRINT

GENERAL DATA

METHODS DATA

STRUCTURE DATA

NETWORK DATA

*** FORMATTING DATA

END OF INPUT PROCESSING -- NO ERRORS

-- NO WARNINGS

END OF INPUT CROSS-CHECKING -- NO ERRORS.

R

PIPEPHASE Version 9.6 - CALCULATION MODULE

================================================

ITERATION NUMBER 0. 0

Index

LINK FROM TO FLOW RATE PRESSURE IN PRESSURE OUT

NAME NODE NODE M LB/HR PSIA PSIA

---- ---- ---- --------------- ----------- ------------

L000 S000 D000 1.300 5014.70 30014.47

***** PROBLEM SOLUTION REACHED *****

END OF NETWORK PROCESSING -- NO ERRORS

-- 1 WARNING

*** BASE CASE SOLVED ***

*** NETWORK SIMULATION SOLVED

CALCULATION STARTED 14:35:06 11/30/14

CALCULATION FINISHED 14:35:07 11/30/14

CALCULATION RUN TIME 0 HR 0 MIN 1 SEC

NETWORK SIMULATION SOLVED

Node Summary - Base CaseSimulacion de estacion de Bombeo Para Materia DE Transporte

Node Pressure Temperature

PSIG DEG F LB/HR LB/HR LB/HR

5,000.00 60.00 .262 1,298.70 1.04

29,999.77 60.02 -.262 -1,298.70 -1.04

Rates reported at standard conditions. Specified values are underlined.

Index

Gas Weight Rate

Oil Weight Rate

Water Weight Rate

S000D000


Gas GV Rate Oil LV Rate Water LV Rate

LB/HR MM FT3/DAY BBL/DAY BBL/DAY

1,300.00 0.00 114.12 0.07 1.06 0.78 1.00

-1,300.00 0.00 -114.12 -0.07 1.06 0.78 1.00

Total Weight Rate

Gas Specific Gravity

Oil Specific Gravity

Water Specific Gravity


N2 C02 H2S Wobbe Index GHV Value

Vol Pct Vol Pct Vol Pct BTU/STD FT3 BTU/STD FT3

0.20 0.00 0.00 3,868.78 9,501.58

0.20 0.00 0.00 3,868.78 9,501.58

Link Summary - Base CaseSimulacion de estacion de Bombeo Para Materia DE Transporte

Link Name Node Name Gas GV Rate Oil LV Rate Water LV Rate Pressure

MM FT3/DAY BBL/DAY BBL/DAY PSIG

In S000 0.0000 110.82 0.07 5,000.00

Out D000 0.0000 68.03 0.07 29,999.77

Rates reported at actual conditions. Gas holdup reported at standard conditions. Specified pressures are underlined.

Index

Inlet / Outlet

L000

Link Summary - Base CaseSimulacion de estacion de Bombeo Para Materia DE Transporte

Temperature Gas Holdup Liquid Holdup

PSIG DEG F MM SCF ABBLS

60.00

24,999.77 60.02 0.0000 2,462.21

Rates reported at actual conditions. Gas holdup reported at standard conditions. Specified pressures are underlined.

Pressure Change

Device Summary - Base CaseSimulacion de estacion de Bombeo Para Materia DE Transporte

Link Name Device Name Device Type

IN FT FT

L000 P000 PIPE 3.07 264,000.00 0.00

L000 P002 PUMP 0.00 0.00 0.00

L000 C000 XCH1 0.00 0.00 0.00

L000 P001 PIPE 3.07 5,280.00 0.00

Index

Inside Diameter

Measured Length

Elevation Change

Device Summary - Base CaseSimulacion de estacion de Bombeo Para Materia DE Transporte

PSIG DEG F LB/HR

4,995.12 60.01 0.00 1.00 1,300

30,000.00 153.72 1,300

30,000.00 30.00

29,999.77 60.02 0.00 1.00 1,300

Outlet Pressure

Outlet Temperature

Outlet In-Situ Quality

Outlet Liquid Holdup

Total Mass Rate

Structure Summary - Base CaseSimulacion de estacion de Bombeo Para Materia DE Transporte


IN IN FT

L000 P000 PIPE 3.07 3.07 264000.0

L000 P002 PUMP 0.0

L000 C000 XCH1 0.0

L000 P001 PIPE 3.07 3.07 5280.0

Index

Inlet Inside Diameter

Outlet Inside Diameter

Measured Length

Structure Summary - Base CaseSimulacion de estacion de Bombeo Para Materia DE Transporte

FT

0.0

0.0

0.0

0.0

Elevation Change

Velocity Summary - Base CaseSimulacion de estacion de Bombeo Para Materia DE Transporte


FT/SEC FT/SEC

L000 P000 PIPE 0.14 0.14

L000 P002 PUMP

L000 C000 XCH1

L000 P001 PIPE 0.08 0.09

Index

Inlet Mixture Velocity

Outlet Mixture Velocity

Velocity Summary - Base CaseSimulacion de estacion de Bombeo Para Materia DE Transporte

Critical Velocity Erosional Velocity Pressure Change

FT/SEC FT/SEC PSI/FT PSI/FT PSIG

0.00 14.13 0.0000 0.0000 -4.89

25,004.88

0.00

0.00 11.05 0.0000 0.0000 -0.23

Inlet Pressure Gradient

Outlet Pressure Gradient

Results Summary - Base CaseSimulacion de estacion de Bombeo Para Materia DE Transporte

Link Name Device Name Device Type Inlet Pressure

LB/HR PSIG PSIG

L000 P000 PIPE 1,300.00 5,000.00 4,995.12

L000 P002 PUMP 1,300.00 4,995.12 30,000.00

L000 C000 XCH1 30,000.00 30,000.00

L000 P001 PIPE 1,300.00 30,000.00 29,999.77

Index

Seg 1 Mixture Flow Rate

Outlet Pressure

Results Summary - Base CaseSimulacion de estacion de Bombeo Para Materia DE Transporte

Inlet Quality Outlet Quality

DEG F DEG F Fraction Fraction

60.00 60.01 0.0000 0.0000

60.01 153.72

153.72 30.00

30.00 60.02 0.0000 0.0000

Inlet Temperature

Outlet Temperature

Simulacion de estacion de Bombeo Para Materia DE Transporte Vapor Liquid1 Vap+Liq1 Liquid2

Temp DEG F 60.00

Pressure PSIG 5000.00

COMPONENT Mole Fraction

KEROSENE 0.000000 0.997680 0.997680 0.000000

H2O 0.000000 0.000305 0.000305 1.000000

N2 0.000000 0.002016 0.002016 0.000000

TOTAL RATES

Weight Rate LB/HR 0.00 1,298.96 1,298.96 1.04

Molar Rate MOLE/HR 0.00 7.44 7.44 0.06

PHASE PROPERTIES

Mass Fraction 0.000000 0.999200 0.999200 0.000800

Volume Fraction 0.000000 0.999357 0.999357 0.000643

Density LB/FT3 0.00 50.10 62.35

Actual SPGR 0.0000 0.8034 0.9997

Viscosity CP 0.0000 0.8094 1.1192

Enthalpy BTU/LB 0.000 20.414 42.068

Surface Tension DYNES/CM 25.815 72.910

Molecular Wt 0.000 174.656 174.656 18.015

Simulacion de estacion de Bombeo Para Materia DE Transporte Vapor Liquid1 Vap+Liq1 Liquid2

Temp DEG F 60.02

Pressure PSIG 29999.77

COMPONENT Mole Fraction

KEROSENE 0.000000 0.997680 0.997680 0.000000

H2O 0.000000 0.000305 0.000305 1.000000

N2 0.000000 0.002016 0.002016 0.000000

TOTAL RATES

Weight Rate LB/HR 0.00 1,298.96 1,298.96 1.04

Molar Rate MOLE/HR 0.00 7.44 7.44 0.06

PHASE PROPERTIES

Index

Flash Report for Node S000 - Base Case

Flash Report for Node D000 - Base Case

Mass Fraction 0.000000 0.999200 0.999200 0.000800

Volume Fraction 0.000000 0.998954 0.998954 0.001046

Density LB/FT3 0.00 81.62 62.35

Actual SPGR 0.0000 1.3088 0.9997

Viscosity CP 0.0000 7.0402 1.1189

Enthalpy BTU/LB 0.000 74.897 107.282

Surface Tension DYNES/CM 25.814 72.909

Molecular Wt 0.000 174.656 174.656 18.015

Simulacion de estacion de Bombeo Para Materia DE TransporteTotal

0.990000

0.008000

0.002000

1,300.00

7.49

1.000000

1.000000

20.431

173.450

Simulacion de estacion de Bombeo Para Materia DE TransporteTotal

0.990000

0.008000

0.002000

1,300.00

7.49

1.000000

1.000000

74.923

173.450

Pump Summary - Base CaseSimulacion de estacion de Bombeo Para Materia DE Transporte

Name Head

BBL/DAY PSIG PSIG DEG F FT HEAD

P002 110.892 4995.116 29999.999 153.724 71854.188

Index

Actual Inlet Rate

Suction Pressure

Outlet Pressure

Outlet Temperature

Pump Summary - Base CaseSimulacion de estacion de Bombeo Para Materia DE Transporte

Efficiency Power Stage

HP

1.000 49.157 1.000

Phase Envelope for - L000 Base CaseSimulacion de estacion de Bombeo Para Materia DE Transporte

Link Name Pressure Temperature

PSIG DEG F

L000 0 240.342219580058 2

L000 25.2516979228513 312.832024542749 2

L000 44.8989131927527 346.865487516806 2

L000 74.2091141722662 384.389536607311 2

L000 117.934795886334 425.893555665923 2

L000 183.165847788581 471.929288186654 2

L000 280.479142069474 523.098966621975 2

L000 345.831710523699 550.790775763052 2

L000 421.926364686998 578.624123166006 2

L000 435.740695550686 583.22967198946 2

L000 -14.442906517067 59.99 9

L000 -13.7524835878543 99.99 9

L000 -11.8232080718467 139.99 9

L000 -7.23589200923005 179.99 9

L000 2.36063788020953 219.99 9

L000 20.4697876587438 259.99 9

L000 51.8860523962168 299.99 9

L000 102.732148656834 339.99 9

L000 180.393826467882 379.99 9

L000 293.366821189668 419.99 9

L000 5000.0041 59.9999999999999 8

L000 4999.7596710117 59.9906679256201 8

L000 4999.51524443984 60.0078340674148 8

L000 4999.27081903993 59.9906678857715 8

L000 4999.02639481193 60.007834094966 8

L000 4998.7819717558 59.9906678489147 8

L000 4998.53754987149 60.007834122412 8

L000 4998.29312915897 59.9906678114947 8

L000 4998.04870961819 60.0078341503894 8

L000 4997.8042912491 59.9906677744781 8

L000 4997.55987405167 60.0078341778973 8

L000 4997.31545802585 59.9906677374957 8

L000 4997.07104317161 60.0078342055475 8

L000 4996.82662948889 59.9906677005779 8

L000 4996.58221697766 60.0078342329081 8

L000 4996.33780563786 59.9906676639046 8

L000 4996.09339546948 60.0078342603561 8

L000 4995.84898647245 59.9906676272585 8

L000 4995.60457864673 60.0078342878657 8

L000 4995.36017199229 59.9906675903068 8

L000 4995.11576650908 60.0078343152647 8

Index

L000 30000 153.724179423226 8

L000 30000 30 8

L000 29999.9099332618 67.3410894250076 8

L000 29999.8247687882 58.2441831736026 8

L000 29999.7695606498 60.019522800575 8

Phase Envelope for - L000 Base CaseSimulacion de estacion de Bombeo Para Materia DE Transporte

Data Description

Dew Point

Dew Point

Dew Point

Dew Point

Dew Point

Dew Point

Dew Point

Dew Point

Dew Point

Dew Point

Water Saturation

Water Saturation

Water Saturation

Water Saturation

Water Saturation

Water Saturation

Water Saturation

Water Saturation

Water Saturation

Water Saturation

Link Traverse

Link Traverse

Link Traverse

Link Traverse

Link Traverse

Link Traverse

Link Traverse

Link Traverse

Link Traverse

Link Traverse

Link Traverse

Link Traverse

Link Traverse

Link Traverse

Link Traverse

Link Traverse

Link Traverse

Link Traverse

Link Traverse

Link Traverse

Link Traverse

Link Traverse

Link Traverse

Link Traverse

Link Traverse

Link Traverse

Simulacion de estacion de Bombeo Para Materia DE Transporte

Temperature Pressure Report - Base CaseSimulacion de estacion de Bombeo Para Materia DE Transporte

Name Pressure Temperature

FT FT IN PSIG DEG F

P000 PIPE Inlet 0.000 0.000 3.068 5000.004 60.000

P000 PIPE Seg 1 13200.000 0.000 3.068 4999.760 59.991

P000 PIPE Seg 2 26400.000 0.000 3.068 4999.515 60.008

P000 PIPE Seg 3 39600.000 0.000 3.068 4999.271 59.991

P000 PIPE Seg 4 52800.000 0.000 3.068 4999.026 60.008

P000 PIPE Seg 5 66000.000 0.000 3.068 4998.782 59.991

P000 PIPE Seg 6 79200.000 0.000 3.068 4998.537 60.008

P000 PIPE Seg 7 92400.000 0.000 3.068 4998.293 59.991

P000 PIPE Seg 8 105600.000 0.000 3.068 4998.049 60.008

P000 PIPE Seg 9 118800.000 0.000 3.068 4997.804 59.991

P000 PIPE Seg 10 132000.000 0.000 3.068 4997.560 60.008

P000 PIPE Seg 11 145200.000 0.000 3.068 4997.315 59.991

P000 PIPE Seg 12 158400.000 0.000 3.068 4997.071 60.008

P000 PIPE Seg 13 171600.000 0.000 3.068 4996.827 59.991

P000 PIPE Seg 14 184800.000 0.000 3.068 4996.582 60.008

P000 PIPE Seg 15 198000.000 0.000 3.068 4996.338 59.991

P000 PIPE Seg 16 211200.000 0.000 3.068 4996.093 60.008

P000 PIPE Seg 17 224400.000 0.000 3.068 4995.849 59.991

P000 PIPE Seg 18 237600.000 0.000 3.068 4995.604 60.008

P000 PIPE Seg 19 250800.000 0.000 3.068 4995.360 59.991

P000 PIPE Outlet 264000.000 0.000 3.068 4995.116 60.008

P002 PUMP Inlet 264000.000 0.000 0.000 4995.116 60.008

P002 PUMP Outlet 264000.000 0.000 0.000 29999.999 153.724

C000 XCH1 Inlet 264000.000 0.000 0.000 29999.999 153.724

C000 XCH1 Outlet 264000.000 0.000 0.000 29999.999 30.000

P001 PIPE Inlet 264000.000 0.000 3.068 29999.999 30.000

P001 PIPE Seg 1 266000.000 0.000 3.068 29999.910 67.341

P001 PIPE Seg 2 268000.000 0.000 3.068 29999.826 58.244

P001 PIPE Outlet 269280.000 0.000 3.068 29999.769 60.020

Index

L000 - Base Case

Device Type

Device Seg

MWD Or Total Length

TVD Or Total Elevation

Inside Diameter

0.000 100000.000 200000.000 300000.0000.000

5000.000

10000.000

15000.000

20000.000

25000.000

30000.000

35000.000

Surface Pressure Plot for Link L000 - Base Case

Fluid

Distance from Inlet, FT

Pres

sure

, PSI

G

0.000 100000.000 200000.000 300000.0000.000

20.000

40.000

60.000

80.000

100.000

120.000

140.000

160.000

180.000

Surface Temperature Plot for Link L000 - Base Case

Fluid Ambient


Tem

pera

ture

, DEG

F

0.000 100000.000 200000.000 300000.0000.000

5000.000

10000.000

15000.000

20000.000

25000.000

30000.000

35000.000

Surface Pressure Plot for Link L000 - Base Case

Fluid


Pres

sure

, PSI

G

0.000 100000.000 200000.000 300000.0000.000

20.000

40.000

60.000

80.000

100.000

120.000

140.000

160.000

180.000


Fluid Ambient


Tem

pera

ture

, DEG

F

0 100 200 300 400 500 600 700-5000

0

5000

10000

15000

20000

25000

30000

35000

Phase Envelope for L000 - Base Case

Fluid Water Saturation Fluid Traverse

Temperature, DEG F

Pres

sure

, PSI

G

Equipment Report - Base CaseSimulacion de estacion de Bombeo Para Materia DE Transporte

Name Pressure Temperature Property

FT FT PSIG DEG F

P000 PIPE Inlet 0.000 0.000 5000.004 60.000

P000 PIPE Outlet 264000.000 0.000 4995.116 60.008

P002 PUMP Inlet 264000.000 0.000 4995.116 60.008

Avail. Power

Req. Power

Speed

Efficiency

P002 PUMP Outlet 264000.000 0.000 29999.999 153.724

C000 XCH1 Inlet 264000.000 0.000 29999.999 153.724

Avail. Duty.

Req. Duty.

Device DP

C000 XCH1 Outlet 264000.000 0.000 29999.999 30.000

P001 PIPE Inlet 264000.000 0.000 29999.999 30.000

P001 PIPE Outlet 269280.000 0.000 29999.769 60.020

Holdup and Velocity Report - Base CaseSimulacion de estacion de Bombeo Para Materia DE Transporte

Name

ABBLS FT/SEC FT/SEC

P000 PIPE Inlet

P000 PIPE Seg 1 1.000 1.000 120.697 0.140 0.000

P000 PIPE Seg 2 1.000 1.000 241.394 0.140 0.000

P000 PIPE Seg 3 1.000 1.000 362.090 0.140 0.000

P000 PIPE Seg 4 1.000 1.000 482.787 0.140 0.000

P000 PIPE Seg 5 1.000 1.000 603.484 0.140 0.000

Device Type

Device Seg

MWD Or Total Length

TVD Or Total Elevation

Device Type

Device Seg

No Slip Liquid Holdup

Slip Liquid Holdup

Total Liquid Holdup

Liquid Superficial

Velocity

Gas Superficial

Velocity

0 100 200 300 400 500 600 700-5000

0

5000

10000

15000

20000

25000

30000

35000

Phase Envelope for L000 - Base Case

Fluid Water Saturation Fluid Traverse

Temperature, DEG FPr

essu

re, P

SIG

P000 PIPE Seg 6 1.000 1.000 724.181 0.140 0.000

P000 PIPE Seg 7 1.000 1.000 844.878 0.140 0.000

P000 PIPE Seg 8 1.000 1.000 965.574 0.140 0.000

P000 PIPE Seg 9 1.000 1.000 1,086.271 0.140 0.000

P000 PIPE Seg 10 1.000 1.000 1,206.968 0.140 0.000

P000 PIPE Seg 11 1.000 1.000 1,327.665 0.140 0.000

P000 PIPE Seg 12 1.000 1.000 1,448.362 0.140 0.000

P000 PIPE Seg 13 1.000 1.000 1,569.058 0.140 0.000

P000 PIPE Seg 14 1.000 1.000 1,689.755 0.140 0.000

P000 PIPE Seg 15 1.000 1.000 1,810.452 0.140 0.000

P000 PIPE Seg 16 1.000 1.000 1,931.149 0.140 0.000

P000 PIPE Seg 17 1.000 1.000 2,051.846 0.140 0.000

P000 PIPE Seg 18 1.000 1.000 2,172.543 0.140 0.000

P000 PIPE Seg 19 1.000 1.000 2,293.239 0.140 0.000

P000 PIPE Outlet 1.000 1.000 2,413.936 0.140 0.000

P002 PUMP Inlet

P002 PUMP Outlet

C000 XCH1 Inlet

C000 XCH1 Outlet

P001 PIPE Inlet

P001 PIPE Seg 1 1.000 1.000 2,432.223 0.082 0.000

P001 PIPE Seg 2 1.000 1.000 2,450.511 0.087 0.000

P001 PIPE Outlet 1.000 1.000 2,462.215 0.086 0.000

Pressure Gradient Report - L000 Base CaseSimulacion de estacion de Bombeo Para Materia DE Transporte

Name

PSI/FT PSI/FT PSI/FT PSIG PSIG

P000 PIPE Inlet

P000 PIPE Seg 1 -0.00002 0.00000 -0.00002 -0.24 0.00

P000 PIPE Seg 2 -0.00002 0.00000 -0.00002 -0.24 0.00

P000 PIPE Seg 3 -0.00002 0.00000 -0.00002 -0.24 0.00

P000 PIPE Seg 4 -0.00002 0.00000 -0.00002 -0.24 0.00

P000 PIPE Seg 5 -0.00002 0.00000 -0.00002 -0.24 0.00

P000 PIPE Seg 6 -0.00002 0.00000 -0.00002 -0.24 0.00

P000 PIPE Seg 7 -0.00002 0.00000 -0.00002 -0.24 0.00

P000 PIPE Seg 8 -0.00002 0.00000 -0.00002 -0.24 0.00

P000 PIPE Seg 9 -0.00002 0.00000 -0.00002 -0.24 0.00

P000 PIPE Seg 10 -0.00002 0.00000 -0.00002 -0.24 0.00

P000 PIPE Seg 11 -0.00002 0.00000 -0.00002 -0.24 0.00

P000 PIPE Seg 12 -0.00002 0.00000 -0.00002 -0.24 0.00

P000 PIPE Seg 13 -0.00002 0.00000 -0.00002 -0.24 0.00

P000 PIPE Seg 14 -0.00002 0.00000 -0.00002 -0.24 0.00

P000 PIPE Seg 15 -0.00002 0.00000 -0.00002 -0.24 0.00

P000 PIPE Seg 16 -0.00002 0.00000 -0.00002 -0.24 0.00

Device Type

Device Seg

Friction Pressure Gradient

Elevation Pressure Gradient

Total Pressure Gradient

Friction Pressure Change

Elevation Pressure Change

P000 PIPE Seg 17 -0.00002 0.00000 -0.00002 -0.24 0.00

P000 PIPE Seg 18 -0.00002 0.00000 -0.00002 -0.24 0.00

P000 PIPE Seg 19 -0.00002 0.00000 -0.00002 -0.24 0.00

P000 PIPE Outlet -0.00002 0.00000 -0.00002 -0.24 0.00

P002 PUMP Inlet

P002 PUMP Outlet

C000 XCH1 Inlet

C000 XCH1 Outlet

P001 PIPE Inlet

P001 PIPE Seg 1 -0.00005 0.00000 -0.00005 -0.09 0.00

P001 PIPE Seg 2 -0.00004 0.00000 -0.00004 -0.09 0.00

P001 PIPE Outlet -0.00004 0.00000 -0.00004 -0.06 0.00

Viscosity Density Report - Base CaseSimulacion de estacion de Bombeo Para Materia DE Transporte

Name Oil Viscosity Liquid Density Vapor Density

CP CP CP LB/FT3 LB/FT3

P000 PIPE Inlet

P000 PIPE Seg 1 0.80942 0.80962 0.00000 50.11241 0.000

P000 PIPE Seg 2 0.80938 0.80958 0.00000 50.11227 0.000

P000 PIPE Seg 3 0.80936 0.80956 0.00000 50.11223 0.000

P000 PIPE Seg 4 0.80935 0.80955 0.00000 50.11219 0.000

P000 PIPE Seg 5 0.80933 0.80953 0.00000 50.11214 0.000

P000 PIPE Seg 6 0.80931 0.80951 0.00000 50.11209 0.000

P000 PIPE Seg 7 0.80930 0.80950 0.00000 50.11205 0.000

P000 PIPE Seg 8 0.80928 0.80948 0.00000 50.11201 0.000

P000 PIPE Seg 9 0.80926 0.80946 0.00000 50.11196 0.000

P000 PIPE Seg 10 0.80924 0.80944 0.00000 50.11192 0.000

P000 PIPE Seg 11 0.80923 0.80943 0.00000 50.11188 0.000

P000 PIPE Seg 12 0.80921 0.80941 0.00000 50.11183 0.000

P000 PIPE Seg 13 0.80919 0.80939 0.00000 50.11179 0.000

P000 PIPE Seg 14 0.80918 0.80938 0.00000 50.11174 0.000

P000 PIPE Seg 15 0.80916 0.80936 0.00000 50.11169 0.000

P000 PIPE Seg 16 0.80914 0.80934 0.00000 50.11165 0.000

P000 PIPE Seg 17 0.80912 0.80932 0.00000 50.11161 0.000

P000 PIPE Seg 18 0.80911 0.80931 0.00000 50.11156 0.000

P000 PIPE Seg 19 0.80909 0.80929 0.00000 50.11151 0.000

P000 PIPE Outlet 0.80907 0.80927 0.00000 50.11147 0.000

P002 PUMP Inlet

P002 PUMP Outlet

C000 XCH1 Inlet

C000 XCH1 Outlet

P001 PIPE Inlet

P001 PIPE Seg 1 7.71674 7.70968 0.00000 85.38980 0.000

P001 PIPE Seg 2 6.88867 6.88267 0.00000 80.61817 0.000

Device Type

Device Seg

Liquid Viscosity

Vapor Viscosity

P001 PIPE Outlet 7.08977 7.08350 0.00000 81.91420 0.000

Friction Report - Base CaseSimulacion de estacion de Bombeo Para Materia DE Transporte

Name

LB/FT3 FT/SEC IN CP

P000 PIPE Inlet

P000 PIPE Seg 1 50.112 0.140 3.068 0.810 0.044

P000 PIPE Seg 2 50.112 0.140 3.068 0.810 0.044

P000 PIPE Seg 3 50.112 0.140 3.068 0.810 0.044

P000 PIPE Seg 4 50.112 0.140 3.068 0.810 0.044

P000 PIPE Seg 5 50.112 0.140 3.068 0.810 0.044

P000 PIPE Seg 6 50.112 0.140 3.068 0.810 0.044

P000 PIPE Seg 7 50.112 0.140 3.068 0.809 0.044

P000 PIPE Seg 8 50.112 0.140 3.068 0.809 0.044

P000 PIPE Seg 9 50.112 0.140 3.068 0.809 0.044

P000 PIPE Seg 10 50.112 0.140 3.068 0.809 0.044

P000 PIPE Seg 11 50.112 0.140 3.068 0.809 0.044

P000 PIPE Seg 12 50.112 0.140 3.068 0.809 0.044

P000 PIPE Seg 13 50.112 0.140 3.068 0.809 0.044

P000 PIPE Seg 14 50.112 0.140 3.068 0.809 0.044

P000 PIPE Seg 15 50.112 0.140 3.068 0.809 0.044

P000 PIPE Seg 16 50.112 0.140 3.068 0.809 0.044

P000 PIPE Seg 17 50.112 0.140 3.068 0.809 0.044

P000 PIPE Seg 18 50.112 0.140 3.068 0.809 0.044

P000 PIPE Seg 19 50.112 0.140 3.068 0.809 0.044

P000 PIPE Outlet 50.111 0.140 3.068 0.809 0.044

P002 PUMP Inlet

P002 PUMP Outlet

C000 XCH1 Inlet

C000 XCH1 Outlet

P001 PIPE Inlet

P001 PIPE Seg 1 85.390 0.082 3.068 7.710 0.184

P001 PIPE Seg 2 80.618 0.087 3.068 6.883 0.165

P001 PIPE Outlet 81.914 0.086 3.068 7.084 0.169

Heat Transfer Report - Base CaseSimulacion de estacion de Bombeo Para Materia DE Transporte

Name

BTU/HR-FT-F

P000 PIPE Inlet

Device Type

Device Seg

Friction Density

Friction Velocity

Friction Diameter

Friction Viscosity

Friction Factor

Device Type

Device Seg

Fluid Thermal Conduct.

Inside Film Thermal

ResistancePipe Thermal

ResistanceInsulation Thermal

Resistance

Surrounding Thermal

Resistance

HR-FT2-F/BTU

HR-FT2-F/BTU

HR-FT2-F/BTU

HR-FT2-F/BTU

P000 PIPE Seg 1 0.0000 0.0000 0.0000 0.0000

P000 PIPE Seg 2 0.0000 0.0000 0.0000 0.0000

P000 PIPE Seg 3 0.0000 0.0000 0.0000 0.0000

P000 PIPE Seg 4 0.0000 0.0000 0.0000 0.0000

P000 PIPE Seg 5 0.0000 0.0000 0.0000 0.0000

P000 PIPE Seg 6 0.0000 0.0000 0.0000 0.0000

P000 PIPE Seg 7 0.0000 0.0000 0.0000 0.0000

P000 PIPE Seg 8 0.0000 0.0000 0.0000 0.0000

P000 PIPE Seg 9 0.0000 0.0000 0.0000 0.0000

P000 PIPE Seg 10 0.0000 0.0000 0.0000 0.0000

P000 PIPE Seg 11 0.0000 0.0000 0.0000 0.0000

P000 PIPE Seg 12 0.0000 0.0000 0.0000 0.0000

P000 PIPE Seg 13 0.0000 0.0000 0.0000 0.0000

P000 PIPE Seg 14 0.0000 0.0000 0.0000 0.0000

P000 PIPE Seg 15 0.0000 0.0000 0.0000 0.0000

P000 PIPE Seg 16 0.0000 0.0000 0.0000 0.0000

P000 PIPE Seg 17 0.0000 0.0000 0.0000 0.0000

P000 PIPE Seg 18 0.0000 0.0000 0.0000 0.0000

P000 PIPE Seg 19 0.0000 0.0000 0.0000 0.0000

P000 PIPE Outlet 0.0000 0.0000 0.0000 0.0000

P002 PUMP Inlet

P002 PUMP Outlet

C000 XCH1 Inlet

C000 XCH1 Outlet

P001 PIPE Inlet

P001 PIPE Seg 1 0.0000 0.0000 0.0000 0.0000

P001 PIPE Seg 2 0.0000 0.0000 0.0000 0.0000

P001 PIPE Outlet 0.0000 0.0000 0.0000 0.0000

Simulacion de estacion de Bombeo Para Materia DE Transporte

Temperature Pressure Report - Base CaseSimulacion de estacion de Bombeo Para Materia DE Transporte

U Factor Quality

DEG F

60.000 0.000 0.000 X

60.000 1.000 0.000 X

60.000 1.000 0.000 X

60.000 1.000 0.000 X

60.000 1.000 0.000 X

60.000 1.000 0.000 X

60.000 1.000 0.000 X

60.000 1.000 0.000 X

60.000 1.000 0.000 X

60.000 1.000 0.000 X

60.000 1.000 0.000 X

60.000 1.000 0.000 X

60.000 1.000 0.000 X

60.000 1.000 0.000 X

60.000 1.000 0.000 X

60.000 1.000 0.000 X

60.000 1.000 0.000 X

60.000 1.000 0.000 X

60.000 1.000 0.000 X

60.000 1.000 0.000 X

60.000 1.000 0.000 X

60.000 X

60.000 X

60.000 X

60.000 X

60.000 0.000 0.000 X

60.000 1.000 0.000 X

60.000 1.000 0.000 X

60.000 1.000 0.000 X

Ambient Temperature

Device Domain

BTU/HR-FT2-F

0.000 100000.000 200000.000 300000.0000.000

20.000

40.000

60.000

80.000

100.000

120.000

140.000

160.000

180.000


Fluid Ambient


Tem

pera

ture

, DEG

F

0.000 100000.000 200000.000 300000.0000.000

20.000

40.000

60.000

80.000

100.000

120.000

140.000

160.000

180.000


Fluid Ambient


Tem

pera

ture

, DEG

F

Equipment Report - Base CaseSimulacion de estacion de Bombeo Para Materia DE Transporte

Units Value

HP 0.000

HP 47.157

RPM

1.000

MM BTU/HR 0.000

MM BTU/HR -0.064

PSIG 0.000

Holdup and Velocity Report - Base CaseSimulacion de estacion de Bombeo Para Materia DE Transporte

Sonic Velocity

FT/SEC FT/SEC

0.140 0.000 1-PH 1-PH

0.140 0.000 1-PH 1-PH

0.140 0.000 1-PH 1-PH

0.140 0.000 1-PH 1-PH

0.140 0.000 1-PH 1-PH

Mixture Velocity

Flow Regime Corr / T-D

0.140 0.000 1-PH 1-PH

0.140 0.000 1-PH 1-PH

0.140 0.000 1-PH 1-PH

0.140 0.000 1-PH 1-PH

0.140 0.000 1-PH 1-PH

0.140 0.000 1-PH 1-PH

0.140 0.000 1-PH 1-PH

0.140 0.000 1-PH 1-PH

0.140 0.000 1-PH 1-PH

0.140 0.000 1-PH 1-PH

0.140 0.000 1-PH 1-PH

0.140 0.000 1-PH 1-PH

0.140 0.000 1-PH 1-PH

0.140 0.000 1-PH 1-PH

0.140 0.000 1-PH 1-PH

0.082 0.000 1-PH 1-PH

0.087 0.000 1-PH 1-PH

0.086 0.000 1-PH 1-PH

Pressure Gradient Report - L000 Base CaseSimulacion de estacion de Bombeo Para Materia DE Transporte

PSIG

-0.24

-0.24

-0.24

-0.24

-0.24

-0.24

-0.24

-0.24

-0.24

-0.24

-0.24

-0.24

-0.24

-0.24

-0.24

-0.24

Total Pressure Change

-0.24

-0.24

-0.24

-0.24

-0.09

-0.09

-0.06

Viscosity Density Report - Base CaseSimulacion de estacion de Bombeo Para Materia DE Transporte

Slip Density

LB/FT3 LB/FT3

50.112 50.112

50.112 50.112

50.112 50.112

50.112 50.112

50.112 50.112

50.112 50.112

50.112 50.112

50.112 50.112

50.112 50.112

50.112 50.112

50.112 50.112

50.112 50.112

50.112 50.112

50.112 50.112

50.112 50.112

50.112 50.112

50.112 50.112

50.112 50.112

50.112 50.112

50.111 50.111

85.390 85.390

80.618 80.618

No Slip Density

81.914 81.914

Friction Report - Base CaseSimulacion de estacion de Bombeo Para Materia DE Transporte

DYNES/CM

3.305E+03 25.845

3.305E+03 25.845

3.305E+03 25.845

3.305E+03 25.845

3.306E+03 25.845

3.306E+03 25.845

3.306E+03 25.845

3.306E+03 25.845

3.306E+03 25.845

3.306E+03 25.845

3.306E+03 25.845

3.306E+03 25.845

3.306E+03 25.845

3.306E+03 25.845

3.306E+03 25.845

3.306E+03 25.845

3.306E+03 25.845

3.306E+03 25.845

3.307E+03 25.845

3.307E+03 25.845

3.471E+02 26.534

3.888E+02 25.699

3.778E+02 25.915

Heat Transfer Report - Base CaseSimulacion de estacion de Bombeo Para Materia DE Transporte

BTU/LB BTU/LB

Reynolds Number

Liquid Surface Tension

Liquid Enthalpy

Vapor Enthalpy

Hydrate Formation

20.429 0.000 N

20.430 0.000 N

20.429 0.000 N

20.429 0.000 N

20.428 0.000 N

20.428 0.000 N

20.427 0.000 N

20.427 0.000 N

20.426 0.000 N

20.426 0.000 N

20.425 0.000 N

20.425 0.000 N

20.424 0.000 N

20.424 0.000 N

20.423 0.000 N

20.423 0.000 N

20.422 0.000 N

20.422 0.000 N

20.421 0.000 N

20.421 0.000 N

70.655 0.000 N

75.976 0.000 N

74.587 0.000 N

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