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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
Node Summary - Base CaseSimulacion de estacion de Bombeo Para Materia DE Transporte
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
Node Summary - Base CaseSimulacion de estacion de Bombeo Para Materia DE Transporte
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
Link Name Device Name Device Type
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
Link Name Device Name Device Type
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
Distance from Inlet, FT
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
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
Distance from Inlet, FT
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
Surface Temperature Plot for Link L000 - Base Case
Fluid Ambient
Distance from Inlet, FT
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
Surface Temperature Plot for Link L000 - Base Case
Fluid Ambient
Distance from Inlet, FT
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