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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
L001
L002
L003
Case Study Summary
Input File: D:\Transporte y Almacenamiento de HC\INTEBTO TARDE
$ SIMSCI PIPEPHASE Version 9.6.0 keyword file...
$
$General Data Section
$
TITLE DATE=11/16/14
$
$
DIMENSION RATE(GV)=CFD
$
CALCULATION NETWORK, Gas, PRANDTL
$
DEFAULT IDPIPE=4.026, IDTUBING=4.026, IDANNULUS=6.065, *
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
$
$Network Data Section
$
NETWORK DATA
$
SOLUTION PBALANCE, FLOWAL=2, STEP=1
$
TOLERANCE PRESSURE=0.1
$
$PVT Data Section
$
PVT PROPERTY DATA
$
SET SETNO=1, GRAV(SPGR)=0.85, CPRATIO=1.3
$
$Structure Data Section
$
STRUCTURE DATA
$
SOURCE NAME=S001, IDNAME=S001, PRIORITY=0, *
SETNO=1, PRES(ESTI)=1, TEMP=60, *
RATE=200, XCORD=-189, YCORD=284
Index
$
SOURCE NAME=S002, IDNAME=S002, PRIORITY=0, *
SETNO=1, PRES(ESTI)=1, TEMP=60, *
RATE(ESTI)=50, XCORD=781, YCORD=946
$
SINK NAME=D001, IDNAME=D001, PRES=300, *
RATE=250, XCORD=1644, YCORD=348
$
JUNCTION NAME=J001, IDNAME=J001, PRES(ESTI)= 1, *
TROCK=60, XCORD=858, YCORD=306
$
$
LINK NAME=L001, FROM=S001, TO=J001, *
IDNAME=L001, IDFROM=S001, IDTO=J001
PIPE NAME=P001, LENGTH=5000, ID=19, *
AIR, TAMB=60
$
LINK NAME=L002, FROM=J001, TO=D001, *
IDNAME=L002, IDFROM=J001, IDTO=D001
PIPE NAME=P003, LENGTH=5000, ID=19, *
AIR, TAMB=60
$
LINK NAME=L003, FROM=S002, TO=J001, *
IDNAME=L003, IDFROM=S002, IDTO=J001
PIPE NAME=P002, LENGTH=1.000e-005, ID=19, *
AIR, TAMB=60
$
$Case Study Data Section
$
CASE STUDY DATA
DESCRIPTION Case Study 01
PARAMETER CCLASS=PIPE , CNAME=P002 , VARI=PIPE ID , *
Value=12
$ End of keyword file...
$
END
Input Data
*** WARNING *****
PRESS: ESTIMATE AND FLOW DIRECTION INCONSISTENT
FOR FOLLOWING LINKS
LINK FROM NODE PRESSURE TO NODE PRESSURE
L002 J001 15.7 D001 314.7
CALCULATION OPTIONS
RUN TYPE........ NETWORK
FLUID TYPE...... GAS
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........ 80.00 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..... 4.026 IN
INSIDE DIAMETER - TUBING... 4.026 IN
INSIDE DIAMETER - ANNULUS.. 6.065 IN
LAMINAR INSIDE FILM COEFF.. HAUSEN
FLOW CODES
PIPE FLOW CODE IS MOODY
REYNOLDS NUMBER(LAMINAR)..... 3000.0000
TUBING FLOW CODE IS MOODY
ANNULUS FLOW CODE IS MOODY
Index
BASE CONDITIONS
STANDARD TEMPERATURE..... 60.00 DEG F
STANDARD PRESSURE........ 0.00 PSIG
LIMITS
MINIMUM PRESSURE......... 0.00 PSIG
MAXIMUM PRESSURE......... 24985.30 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
INTERMEDIATE ITERATION PRINTOUT REQUESTED
MERGED SUBNETWORKS REQUESTED
SEGMENTATION OPTIONS
LENGTH CHANGE - HORIZONTAL....... 2000.0 FT
VERTICAL......... 500.0 FT
MAXIMUM NUMBER OF SEGMENTS....... 20
PVT DATA SUMMARY
1 CORRELATION DATA SETS 0 ERRORS 0 WARNINGS
DEFAULT PVT METHODS OPTIONS
Z FACTOR METHOD.......... STANDING
GAS VISCOSITY METHOD..... LEE
CORRELATION SET DATA
CORRELATION SET NUMBER 1
GRAVITY OF GAS............ 0.8500 SPGR
SPECIFIC HEAT RATIO OF GAS 1.3000 CP/CV
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 S001
(S001)
THIS SOURCE IS ON
RATE...................... 200.0000 MM FT3/DAY
ESTIMATED PRESSURE........ 1.0000 PSIG
TEMPERATURE............... 60.00 DEG F
SOURCE S002
(S002)
THIS SOURCE IS ON
ESTIMATED RATE............ 49.9999 MM FT3/DAY
ESTIMATED PRESSURE........ 1.0000 PSIG
TEMPERATURE............... 60.00 DEG F
LINK L001
LINK IS FROM "S001 " TO "J001 "
"L001" FROM "S001" TO "J001"
DEVICE SA001, P001, IS A PIPE
FLOW CODE IS MOODY
INSIDE DIAMETER.............. 19.0000 IN
LENGTH....................... 5000.0 FT
ELEVATION CHANGE............. 0.0 FT
FLOW EFFICIENCY.............. 100.00 PERCENT
ROUGHNESS.................... 0.00180 IN
AMBIENT TEMPERATURE.......... 60.00 DEG F
WALL THICKNESS............... 0.3125 IN
INSULATION THICKNESS......... 0.0000 IN
THERMAL COND. OF PIPE........ 29.000 BTU/HR-FT-F
THERMAL COND. OF INSULATION.. 0.0150 BTU/HR-FT-F
THERMAL COND. OF SOIL........ 0.800 BTU/HR-FT-F
VELOCITY OF AIR.............. 10.000 MPH
DENSITY OF AIR............... 1.0000 SPGR
VISCOSITY OF AIR............. 0.0200000 CP
THERMAL COND. OF AIR......... 0.0150 BTU/HR-FT-F
EFF. OUTSIDE HEAT TRANS COEFF 2.681 BTU/HR-FT2-F
(RELATIVE TO PIPE OUTSIDE DIAMETER)
LINK L002
LINK IS FROM "J001 " TO "D001 "
"L002" FROM "J001" TO "D001"
DEVICE SA002, P003, IS A PIPE
FLOW CODE IS MOODY
INSIDE DIAMETER.............. 19.0000 IN
LENGTH....................... 5000.0 FT
ELEVATION CHANGE............. 0.0 FT
FLOW EFFICIENCY.............. 100.00 PERCENT
ROUGHNESS.................... 0.00180 IN
AMBIENT TEMPERATURE.......... 60.00 DEG F
WALL THICKNESS............... 0.3125 IN
INSULATION THICKNESS......... 0.0000 IN
THERMAL COND. OF PIPE........ 29.000 BTU/HR-FT-F
THERMAL COND. OF INSULATION.. 0.0150 BTU/HR-FT-F
THERMAL COND. OF SOIL........ 0.800 BTU/HR-FT-F
VELOCITY OF AIR.............. 10.000 MPH
DENSITY OF AIR............... 1.0000 SPGR
VISCOSITY OF AIR............. 0.0200000 CP
THERMAL COND. OF AIR......... 0.0150 BTU/HR-FT-F
EFF. OUTSIDE HEAT TRANS COEFF 2.681 BTU/HR-FT2-F
(RELATIVE TO PIPE OUTSIDE DIAMETER)
LINK L003
LINK IS FROM "S002 " TO "J001 "
"L003" FROM "S002" TO "J001"
DEVICE SA003, P002, IS A PIPE
FLOW CODE IS MOODY
INSIDE DIAMETER.............. 19.0000 IN
LENGTH....................... 0.0 FT
ELEVATION CHANGE............. 0.0 FT
FLOW EFFICIENCY.............. 100.00 PERCENT
ROUGHNESS.................... 0.00180 IN
AMBIENT TEMPERATURE.......... 60.00 DEG F
WALL THICKNESS............... 0.3125 IN
INSULATION THICKNESS......... 0.0000 IN
THERMAL COND. OF PIPE........ 29.000 BTU/HR-FT-F
THERMAL COND. OF INSULATION.. 0.0150 BTU/HR-FT-F
THERMAL COND. OF SOIL........ 0.800 BTU/HR-FT-F
VELOCITY OF AIR.............. 10.000 MPH
DENSITY OF AIR............... 1.0000 SPGR
VISCOSITY OF AIR............. 0.0200000 CP
THERMAL COND. OF AIR......... 0.0150 BTU/HR-FT-F
EFF. OUTSIDE HEAT TRANS COEFF 2.681 BTU/HR-FT2-F
(RELATIVE TO PIPE OUTSIDE DIAMETER)
JUNCTIONS AND SINKS
JUNCTION J001
(J001)
ESTIMATED PRESSURE........ 1.0000 PSIG
SINK D001
(D001)
RATE...................... 250.0006 MM FT3/DAY
PRESSURE.................. 300.0001 PSIG
CASE NUMBER 1
-----------------
NEW OLD
CLASS NAME VARIABLE UNITS VALUE VALUE
===========================================================================
PIPE P002 PIPE ID IN 12.0
END OF INPUT PROCESSING -- NO ERRORS
-- 1 WARNING
===========================================================================
Solution History
R
PIPEPHASE Version 9.6 - INPUT MODULE
==========================================
*** SCANNING
GENERAL DATA
METHODS DATA
PROPERTY DATA
STRUCTURE DATA
CASE STUDY DATA
END OF PRE-PROCESSING -- NO ERRORS
R
PIPEPHASE Version 9.6 - CROSS CHECKING MODULE
===================================================
*** CHECKING
GENERAL DATA
PROPERTY DATA
STRUCTURE DATA
CASE STUDY DATA
PVTG DATA
METHODS DATA
*** INPUT REPRINT
GENERAL DATA
GENERAL DATA
METHODS DATA
STRUCTURE DATA
NETWORK DATA
CASE STUDY DATA
*** FORMATTING DATA
END OF INPUT PROCESSING -- NO ERRORS
-- 1 WARNING
END OF INPUT CROSS-CHECKING -- NO ERRORS.
R
PIPEPHASE Version 9.6 - CALCULATION MODULE
================================================
Index
ITERATION NUMBER 0. 0
LINK FROM TO FLOW RATE PRESSURE IN PRESSURE OUT IMBALANCE
NAME NODE NODE MCFD PSIA PSIA PSIA
---- ---- ---- --------------- ----------- ------------ -------------
L001 S001 J001 200000.000 15.70 -346.75
L003 S002 J001 50001.000 15.70 15.70 362.447
L002 J001 D001 250001.000 -346.75 -910.14 -1224.837
MAX PRESSURE IMBALANCE = -1224.8372320 PSI AT NODE D001
RMS AVERAGE PRESSURE IMBALANCE = 903.2148049 PSI
ITERATION NUMBER 1. 0
LINK FROM TO FLOW RATE PRESSURE IN PRESSURE OUT IMBALANCE
NAME NODE NODE MCFD PSIA PSIA PSIA
---- ---- ---- --------------- ----------- ------------ -------------
L001 S001 J001 200000.000 17820.87 17820.15
L003 S002 J001 50001.000 910.17 910.17 -16909.986
L002 J001 D001 250001.000 17820.15 17819.05 17504.355
MAX PRESSURE IMBALANCE = 17504.3546602 PSI AT NODE D001
RMS AVERAGE PRESSURE IMBALANCE = 17209.7362419 PSI
ITERATION NUMBER 1. 1
LINK FROM TO FLOW RATE PRESSURE IN PRESSURE OUT IMBALANCE
NAME NODE NODE MCFD PSIA PSIA PSIA
---- ---- ---- --------------- ----------- ------------ -------------
L001 S001 J001 200000.000 8918.28 8917.34
L003 S002 J001 50001.000 462.93 462.93 -8454.403
L002 J001 D001 250001.000 8917.34 8915.87 8601.169
MAX PRESSURE IMBALANCE = 8601.1686102 PSI AT NODE D001
RMS AVERAGE PRESSURE IMBALANCE = 8528.1013955 PSI
ITERATION NUMBER 1. 2
LINK FROM TO FLOW RATE PRESSURE IN PRESSURE OUT IMBALANCE
NAME NODE NODE MCFD PSIA PSIA PSIA
---- ---- ---- --------------- ----------- ------------ -------------
L001 S001 J001 200000.000 4466.99 4465.92
L003 S002 J001 50001.000 239.32 239.32 -4226.601
L002 J001 D001 250001.000 4465.92 4464.25 4149.552
MAX PRESSURE IMBALANCE = -4226.6014678 PSI AT NODE J001
RMS AVERAGE PRESSURE IMBALANCE = 4188.2540852 PSI
ITERATION NUMBER 1. 3
LINK FROM TO FLOW RATE PRESSURE IN PRESSURE OUT IMBALANCE
NAME NODE NODE MCFD PSIA PSIA PSIA
---- ---- ---- --------------- ----------- ------------ -------------
L001 S001 J001 200000.000 2241.35 2239.99
L003 S002 J001 50001.000 127.51 127.51 -2112.483
L002 J001 D001 250001.000 2239.99 2237.89 1923.186
MAX PRESSURE IMBALANCE = -2112.4834327 PSI AT NODE J001
RMS AVERAGE PRESSURE IMBALANCE = 2020.0531606 PSI
ITERATION NUMBER 2. 0
LINK FROM TO FLOW RATE PRESSURE IN PRESSURE OUT IMBALANCE
NAME NODE NODE MCFD PSIA PSIA PSIA
---- ---- ---- --------------- ----------- ------------ -------------
L001 S001 J001 200000.000 319.67 304.24
L003 S002 J001 50001.000 317.73 317.73 13.488
L002 J001 D001 250001.000 304.24 278.19 -36.511
MAX PRESSURE IMBALANCE = -36.5107539 PSI AT NODE D001
RMS AVERAGE PRESSURE IMBALANCE = 27.5224121 PSI
ITERATION NUMBER 3. 0
LINK FROM TO FLOW RATE PRESSURE IN PRESSURE OUT IMBALANCE
NAME NODE NODE MCFD PSIA PSIA PSIA
---- ---- ---- --------------- ----------- ------------ -------------
L001 S001 J001 200000.000 350.91 337.10
L003 S002 J001 50001.000 337.27 337.27 0.171
L002 J001 D001 250001.000 337.10 314.12 -0.575
MAX PRESSURE IMBALANCE = -0.5753054 PSI AT NODE D001
RMS AVERAGE PRESSURE IMBALANCE = 0.4244156 PSI
ITERATION NUMBER 4. 0
LINK FROM TO FLOW RATE PRESSURE IN PRESSURE OUT IMBALANCE
NAME NODE NODE MCFD PSIA PSIA PSIA
---- ---- ---- --------------- ----------- ------------ -------------
L001 S001 J001 200000.000 351.42 337.63
L003 S002 J001 50001.000 337.63 337.63 0.000
L002 J001 D001 250001.000 337.63 314.70 0.000
MAX PRESSURE IMBALANCE = -0.0000747 PSI AT NODE D001
RMS AVERAGE PRESSURE IMBALANCE = 0.0000561 PSI
***** PROBLEM SOLUTION REACHED *****
END OF NETWORK PROCESSING -- NO ERRORS
-- NO WARNINGS
*** BASE CASE SOLVED ***
ITERATION NUMBER 0. 0
LINK FROM TO FLOW RATE PRESSURE IN PRESSURE OUT IMBALANCE
NAME NODE NODE MCFD PSIA PSIA PSIA
---- ---- ---- --------------- ----------- ------------ -------------
L001 S001 J001 200000.000 351.42 337.63
L003 S002 J001 50001.000 337.63 337.63 0.000
L002 J001 D001 250001.000 337.63 314.70 0.000
***** PROBLEM SOLUTION REACHED *****
END OF NETWORK PROCESSING -- NO ERRORS
-- NO WARNINGS
*** CASE 1 SOLVED ***
END OF CASE STUDY PROCESSING -- NO ERRORS
-- NO WARNINGS
*** NETWORK SIMULATION SOLVED
CALCULATION STARTED 19:17:53 11/16/14
CALCULATION FINISHED 19:17:54 11/16/14
CALCULATION RUN TIME 0 HR 0 MIN 0 SEC
NETWORK SIMULATION SOLVED
Node Summary - Base Case
Node Pressure Temperature Gas GV Rate N2 C02
PSIG DEG F MM FT3/DAY Vol Pct Vol Pct
S001 336.73 60.00 200.000 0.00 0.00
J001 322.93 60.00 .000 0.00 0.00
S002 322.93 60.00 50.001 0.00 0.00
D001 300.00 60.00 -250.001 0.00 0.00
Rates reported at standard conditions. Specified values are underlined.
Node Summary - Case 1Case Study 01
Node Pressure Temperature Gas GV Rate N2 C02
PSIG DEG F MM FT3/DAY Vol Pct Vol Pct
S001 336.73 60.00 200.000 0.00 0.00
J001 322.93 60.00 .000 0.00 0.00
S002 322.93 60.00 50.001 0.00 0.00
D001 300.00 60.00 -250.001 0.00 0.00
Rates reported at standard conditions. Specified values are underlined.
Index
Node Summary - Base Case
H2S
Vol Pct
.000
.000
.000
.000
Node Summary - Case 1Case Study 01
H2S
Vol Pct
.000
.000
.000
.000
Link Summary - Base Case
Link Name Node Name Gas GV Rate Oil LV Rate Water LV Rate Pressure
MM FT3/DAY BBL/DAY BBL/DAY PSIG
In S001 7.3622 0.00 0.00 336.73
Out J001 7.7043 0.00 0.00 322.93
In J001 9.6304 0.00 0.00 322.93
Out D001 10.4241 0.00 0.00 300.00
In S002 1.9261 0.00 0.00 322.93
Out J001 1.9261 0.00 0.00 322.93
Rates reported at actual conditions. Gas holdup reported at standard conditions. Specified pressures are underlined.
Link Summary - Case 1Case Study 01
Link Name Node Name Gas GV Rate Oil LV Rate Water LV Rate Pressure
MM FT3/DAY BBL/DAY BBL/DAY PSIG
In S001 7.3622 0.00 0.00 336.73
Out J001 7.7043 0.00 0.00 322.93
In J001 9.6304 0.00 0.00 322.93
Out D001 10.4241 0.00 0.00 300.00
In S002 1.9261 0.00 0.00 322.93
Out J001 1.9261 0.00 0.00 322.93
Rates reported at actual conditions. Gas holdup reported at standard conditions. Specified pressures are underlined.
Index
Inlet / Outlet
L001
L002
L003
Inlet / Outlet
L001
L002
L003
Link Summary - Base Case
Temperature Gas Holdup Liquid Holdup
PSIG DEG F MM SCF STB
60.00
-13.80 60.00 0.2614 0.00
60.00
-22.93 60.00 0.2458 0.00
60.00
0.00 60.00 0.0000 0.00
Rates reported at actual conditions. Gas holdup reported at standard conditions. Specified pressures are underlined.
Link Summary - Case 1Case Study 01
Temperature Gas Holdup Liquid Holdup
PSIG DEG F MM SCF STB
60.00
-13.80 60.00 0.2614 0.00
60.00
-22.93 60.00 0.2458 0.00
60.00
0.00 60.00 0.0000 0.00
Rates reported at actual conditions. Gas holdup reported at standard conditions. Specified pressures are underlined.
Pressure Change
Pressure Change
Device Summary - Base Case
Link Name Device Name Device Type
IN FT FT
L001 P001 PIPE 19.00 5,000.00 0.00
L002 P003 PIPE 19.00 5,000.00 0.00
L003 P002 PIPE 19.00 0.00 0.00
Device Summary - Case 1Case Study 01
Link Name Device Name Device Type
IN FT FT
L001 P001 PIPE 19.00 5,000.00 0.00
L002 P003 PIPE 19.00 5,000.00 0.00
L003 P002 PIPE 12.00 0.00 0.00
Index
Inside Diameter
Measured Length
Elevation Change
Inside Diameter
Measured Length
Elevation Change
Device Summary - Base Case
Std Gas Rate
PSIG DEG F MM FT3/DAY
322.93 60.00 200.00
300.00 60.00 250.00
322.93 60.00 50.00
Device Summary - Case 1Case Study 01
Std Gas Rate
PSIG DEG F MM FT3/DAY
322.93 60.00 200.00
300.00 60.00 250.00
322.93 60.00 50.00
Outlet Pressure
Outlet Temperature
Outlet Pressure
Outlet Temperature
Structure Summary - Base Case
Link Name Device Name Device Type
IN IN FT
L001 P001 PIPE 19.00 19.00 5000.0
L002 P003 PIPE 19.00 19.00 5000.0
L003 P002 PIPE 19.00 19.00 0.0
Structure Summary - Case 1Case Study 01
Link Name Device Name Device Type
IN IN FT
L001 P001 PIPE 19.00 19.00 5000.0
L002 P003 PIPE 19.00 19.00 5000.0
L003 P002 PIPE 12.00 12.00 0.0
Index
Inlet Inside Diameter
Outlet Inside Diameter
Measured Length
Inlet Inside Diameter
Outlet Inside Diameter
Measured Length
Structure Summary - Base Case
FT
0.0
0.0
0.0
Structure Summary - Case 1Case Study 01
FT
0.0
0.0
0.0
Elevation Change
Elevation Change
Velocity Summary - Base Case
Link Name Device Name Device Type
FT/SEC FT/SEC
L001 P001 PIPE 43.52 45.02
L002 P003 PIPE 57.15 60.64
L003 P002 PIPE 11.32 11.32
Velocity Summary - Case 1Case Study 01
Link Name Device Name Device Type
FT/SEC FT/SEC
L001 P001 PIPE 43.52 45.02
L002 P003 PIPE 57.15 60.64
L003 P002 PIPE 28.38 28.38
Index
Inlet Mixture Velocity
Outlet Mixture Velocity
Inlet Mixture Velocity
Outlet Mixture Velocity
Velocity Summary - Base Case
Critical Velocity Erosional Velocity Pressure Change
FT/SEC FT/SEC PSI/FT PSI/FT PSIG
1,134.86 76.79 -0.0027 -0.0028 -13.80
1,136.19 79.71 -0.0045 -0.0047 -22.93
1,140.26 77.02 -0.0002 -0.0002 0.00
Velocity Summary - Case 1Case Study 01
Critical Velocity Erosional Velocity Pressure Change
FT/SEC FT/SEC PSI/FT PSI/FT PSIG
1,134.86 76.79 -0.0027 -0.0028 -13.80
1,136.19 79.71 -0.0045 -0.0047 -22.93
1,140.26 77.02 -0.0019 -0.0019 0.00
Inlet Pressure Gradient
Outlet Pressure Gradient
Inlet Pressure Gradient
Outlet Pressure Gradient
Results Summary - Base Case
Link Name Device Name Device Type Inlet Pressure
MM FT3/DAY PSIG PSIG
L001 P001 PIPE 7.40 336.73 322.93
L002 P003 PIPE 9.72 322.93 300.00
L003 P002 PIPE 1.93 322.93 322.93
Results Summary - Case 1Case Study 01
Link Name Device Name Device Type Inlet Pressure
MM FT3/DAY PSIG PSIG
L001 P001 PIPE 7.40 336.73 322.93
L002 P003 PIPE 9.72 322.93 300.00
L003 P002 PIPE 1.93 322.93 322.93
Index
Seg 1 Gas Flow Rate
Outlet Pressure
Seg 1 Gas Flow Rate
Outlet Pressure
Results Summary - Base Case
DEG F DEG F
60.00 60.00
60.00 60.00
60.00 60.00
Results Summary - Case 1Case Study 01
DEG F DEG F
60.00 60.00
60.00 60.00
60.00 60.00
Inlet Temperature
Outlet Temperature
Inlet Temperature
Outlet Temperature
Temperature Pressure Report - Base Case
Name Pressure Temperature
FT FT IN PSIG DEG F
P001 PIPE Inlet 0.00 0.00 19.00 336.73 60.00
P001 PIPE Seg 1 1,250.00 0.00 19.00 333.34 60.00
P001 PIPE Seg 2 2,500.00 0.00 19.00 329.91 60.00
P001 PIPE Seg 3 3,750.00 0.00 19.00 326.44 60.00
P001 PIPE Outlet 5,000.00 0.00 19.00 322.93 60.00
Index
L001 - Base Case
Device Type
Device Seg
MWD Or Total Length
TVD Or Total Elevation
Inside Diameter
0.00 1,000.00 2,000.00 3,000.00 4,000.00 5,000.00 6,000.00315.00
320.00
325.00
330.00
335.00
340.00
Surface Pressure Plot for Link L001 - Base Case
Fluid
Distance from Inlet, FT
Pres
sure
, PSI
G
0.00 1,000.00 2,000.00 3,000.00 4,000.00 5,000.00 6,000.000.00
10.00
20.00
30.00
40.00
50.00
60.00
70.00
Surface Temperature Plot for Link L001 - Base Case
Fluid Ambient
Distance from Inlet, FT
Tem
pera
ture
, DEG
F
Holdup and Velocity Report - Base Case
Name
ABBLS FT/SEC FT/SEC
P001 PIPE Inlet
P001 PIPE Seg 1 0.000 0.000 0.000 0.000 43.519
P001 PIPE Seg 2 0.000 0.000 0.000 0.000 44.004
P001 PIPE Seg 3 0.000 0.000 0.000 0.000 44.503
P001 PIPE Outlet 0.000 0.000 0.000 0.000 45.018
Pressure Gradient Report - L001 Base Case
Name
PSI/FT PSI/FT PSI/FT PSIG PSIG
P001 PIPE Inlet
P001 PIPE Seg 1 -0.00271 0.00000 -0.00271 -3.38 0.00
P001 PIPE Seg 2 -0.00274 0.00000 -0.00274 -3.42 0.00
P001 PIPE Seg 3 -0.00277 0.00000 -0.00277 -3.46 0.00
P001 PIPE Outlet -0.00280 0.00000 -0.00281 -3.50 0.00
Viscosity Density Report - Base Case
Name Oil Viscosity Liquid Density Vapor Density
CP CP CP LB/FT3 LB/FT3
P001 PIPE Inlet
P001 PIPE Seg 1 0.00000 0.00000 0.01041 0.00000 1.754
P001 PIPE Seg 2 0.00000 0.00000 0.01040 0.00000 1.735
P001 PIPE Seg 3 0.00000 0.00000 0.01039 0.00000 1.715
P001 PIPE Outlet 0.00000 0.00000 0.01038 0.00000 1.696
Friction Report - Base Case
Device Type
Device Seg
No Slip Liquid Holdup
Slip Liquid Holdup
Total Liquid Holdup
Liquid Superficial
Velocity
Gas Superficial
Velocity
Device Type
Device Seg
Friction Pressure Gradient
Elevation Pressure Gradient
Total Pressure Gradient
Friction Pressure Change
Elevation Pressure Change
Device Type
Device Seg
Liquid Viscosity
Vapor Viscosity
Name
LB/FT3 FT/SEC IN CP
P001 PIPE Inlet
P001 PIPE Seg 1 1.754 43.519 19.000 0.010 0.012
P001 PIPE Seg 2 1.735 44.004 19.000 0.010 0.012
P001 PIPE Seg 3 1.715 44.503 19.000 0.010 0.012
P001 PIPE Outlet 1.696 45.018 19.000 0.010 0.012
Heat Transfer Report - Base Case
Name
BTU/HR-FT-F
P001 PIPE Inlet
P001 PIPE Seg 1 0.015 0.0064 0.0009 0.0000 0.3611
P001 PIPE Seg 2 0.015 0.0064 0.0009 0.0000 0.3611
P001 PIPE Seg 3 0.015 0.0064 0.0009 0.0000 0.3611
P001 PIPE Outlet 0.015 0.0064 0.0009 0.0000 0.3611
Case Study 01
Temperature Pressure Report - Case 1Case Study 01
Name Pressure Temperature
FT FT IN PSIG DEG F
P001 PIPE Inlet 0.00 0.00 19.00 336.73 60.00
P001 PIPE Seg 1 1,250.00 0.00 19.00 333.34 60.00
P001 PIPE Seg 2 2,500.00 0.00 19.00 329.91 60.00
P001 PIPE Seg 3 3,750.00 0.00 19.00 326.44 60.00
P001 PIPE Outlet 5,000.00 0.00 19.00 322.93 60.00
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
L001 - Case 1
Device Type
Device Seg
MWD Or Total Length
TVD Or Total Elevation
Inside Diameter
0.00 1,000.00 2,000.00 3,000.00 4,000.00 5,000.00 6,000.00315.00
320.00
325.00
330.00
335.00
340.00
Surface Pressure Plot for Link L001 - Case 1
Fluid
Distance from Inlet, FT
Pres
sure
, PSI
G
0.00 1,000.00 2,000.00 3,000.00 4,000.00 5,000.00 6,000.000.00
10.00
20.00
30.00
40.00
50.00
60.00
70.00
Surface Temperature Plot for Link L001 - Case 1
Fluid Ambient
Distance from Inlet, FT
Tem
pera
ture
, DEG
F
Holdup and Velocity Report - Case 1Case Study 01
Name
ABBLS FT/SEC FT/SEC
P001 PIPE Inlet
P001 PIPE Seg 1 0.000 0.000 0.000 0.000 43.519
P001 PIPE Seg 2 0.000 0.000 0.000 0.000 44.004
P001 PIPE Seg 3 0.000 0.000 0.000 0.000 44.503
P001 PIPE Outlet 0.000 0.000 0.000 0.000 45.018
Pressure Gradient Report - L001 Case 1Case Study 01
Name
PSI/FT PSI/FT PSI/FT PSIG PSIG
Device Type
Device Seg
No Slip Liquid Holdup
Slip Liquid Holdup
Total Liquid Holdup
Liquid Superficial
Velocity
Gas Superficial
Velocity
Device Type
Device Seg
Friction Pressure Gradient
Elevation Pressure Gradient
Total Pressure Gradient
Friction Pressure Change
Elevation Pressure Change
0.00 1,000.00 2,000.00 3,000.00 4,000.00 5,000.00 6,000.00315.00
320.00
325.00
330.00
335.00
340.00
Surface Pressure Plot for Link L001 - Case 1
Fluid
Distance from Inlet, FT
Pres
sure
, PSI
G
0.00 1,000.00 2,000.00 3,000.00 4,000.00 5,000.00 6,000.000.00
10.00
20.00
30.00
40.00
50.00
60.00
70.00
Surface Temperature Plot for Link L001 - Case 1
Fluid Ambient
Distance from Inlet, FT
Tem
pera
ture
, DEG
F
P001 PIPE Inlet
P001 PIPE Seg 1 -0.00271 0.00000 -0.00271 -3.38 0.00
P001 PIPE Seg 2 -0.00274 0.00000 -0.00274 -3.42 0.00
P001 PIPE Seg 3 -0.00277 0.00000 -0.00277 -3.46 0.00
P001 PIPE Outlet -0.00280 0.00000 -0.00281 -3.50 0.00
Viscosity Density Report - Case 1Case Study 01
Name Oil Viscosity Liquid Density Vapor Density
CP CP CP LB/FT3 LB/FT3
P001 PIPE Inlet
P001 PIPE Seg 1 0.00000 0.00000 0.01041 0.00000 1.754
P001 PIPE Seg 2 0.00000 0.00000 0.01040 0.00000 1.735
P001 PIPE Seg 3 0.00000 0.00000 0.01039 0.00000 1.715
P001 PIPE Outlet 0.00000 0.00000 0.01038 0.00000 1.696
Friction Report - Case 1Case Study 01
Name
LB/FT3 FT/SEC IN CP
P001 PIPE Inlet
P001 PIPE Seg 1 1.754 43.519 19.000 0.010 0.012
P001 PIPE Seg 2 1.735 44.004 19.000 0.010 0.012
P001 PIPE Seg 3 1.715 44.503 19.000 0.010 0.012
P001 PIPE Outlet 1.696 45.018 19.000 0.010 0.012
Heat Transfer Report - Case 1Case Study 01
Name
BTU/HR-FT-F
P001 PIPE Inlet
P001 PIPE Seg 1 0.015 0.0064 0.0009 0.0000 0.3611
P001 PIPE Seg 2 0.015 0.0064 0.0009 0.0000 0.3611
P001 PIPE Seg 3 0.015 0.0064 0.0009 0.0000 0.3611
P001 PIPE Outlet 0.015 0.0064 0.0009 0.0000 0.3611
Device Type
Device Seg
Liquid Viscosity
Vapor Viscosity
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
Temperature Pressure Report - Base Case
U Factor
DEG F
60.00 0.00 X
60.00 2.71 X
60.00 2.71 X
60.00 2.71 X
60.00 2.71 X
Ambient Temperature
Device Domain
BTU/HR-FT2-F
0.00 1,000.00 2,000.00 3,000.00 4,000.00 5,000.00 6,000.000.00
10.00
20.00
30.00
40.00
50.00
60.00
70.00
Surface Temperature Plot for Link L001 - Base Case
Fluid Ambient
Distance from Inlet, FT
Tem
pera
ture
, DEG
F
Holdup and Velocity Report - Base Case
Sonic Velocity
FT/SEC FT/SEC
43.519 1,134.863 ---- 1-PH
44.004 1,135.525 ---- 1-PH
44.503 1,136.191 ---- 1-PH
45.018 1,136.860 ---- 1-PH
Pressure Gradient Report - L001 Base Case
PSIG
-3.39
-3.43
-3.47
-3.51
Viscosity Density Report - Base Case
Slip Density
LB/FT3 LB/FT3
1.754 1.754
1.735 1.735
1.715 1.715
1.696 1.696
Friction Report - Base Case
Mixture Velocity
Flow Regime Corr / T-D
Total Pressure Change
No Slip Density
DYNES/CM
1.728E+07 0.000
1.729E+07 0.000
1.731E+07 0.000
1.732E+07 0.000
Heat Transfer Report - Base Case
BTU/LB BTU/LB
Case Study 01
Temperature Pressure Report - Case 1Case Study 01
U Factor
DEG F
60.00 0.00 X
60.00 2.71 X
60.00 2.71 X
60.00 2.71 X
60.00 2.71 X
Reynolds Number
Liquid Surface Tension
Liquid Enthalpy
Vapor Enthalpy
Hydrate Formation
Ambient Temperature
Device Domain
BTU/HR-FT2-F
0.00 1,000.00 2,000.00 3,000.00 4,000.00 5,000.00 6,000.000.00
10.00
20.00
30.00
40.00
50.00
60.00
70.00
Surface Temperature Plot for Link L001 - Case 1
Fluid Ambient
Distance from Inlet, FT
Tem
pera
ture
, DEG
F
Holdup and Velocity Report - Case 1Case Study 01
Sonic Velocity
FT/SEC FT/SEC
43.519 1,134.863 ---- 1-PH
44.004 1,135.525 ---- 1-PH
44.503 1,136.191 ---- 1-PH
45.018 1,136.860 ---- 1-PH
Pressure Gradient Report - L001 Case 1Case Study 01
PSIG
Mixture Velocity
Flow Regime Corr / T-D
Total Pressure Change
0.00 1,000.00 2,000.00 3,000.00 4,000.00 5,000.00 6,000.000.00
10.00
20.00
30.00
40.00
50.00
60.00
70.00
Surface Temperature Plot for Link L001 - Case 1
Fluid Ambient
Distance from Inlet, FT
Tem
pera
ture
, DEG
F
-3.39
-3.43
-3.47
-3.51
Viscosity Density Report - Case 1Case Study 01
Slip Density
LB/FT3 LB/FT3
1.754 1.754
1.735 1.735
1.715 1.715
1.696 1.696
Friction Report - Case 1Case Study 01
DYNES/CM
1.728E+07 0.000
1.729E+07 0.000
1.731E+07 0.000
1.732E+07 0.000
Heat Transfer Report - Case 1Case Study 01
BTU/LB BTU/LB
No Slip Density
Reynolds Number
Liquid Surface Tension
Liquid Enthalpy
Vapor Enthalpy
Hydrate Formation
Temperature Pressure Report - Base Case
Name Pressure Temperature
FT FT IN PSIG DEG F
P003 PIPE Inlet 0.00 0.00 19.00 322.93 60.00
P003 PIPE Seg 1 1,250.00 0.00 19.00 317.37 60.00
P003 PIPE Seg 2 2,500.00 0.00 19.00 311.69 60.00
P003 PIPE Seg 3 3,750.00 0.00 19.00 305.91 60.00
P003 PIPE Outlet 5,000.00 0.00 19.00 300.00 60.00
Index
L002 - Base Case
Device Type
Device Seg
MWD Or Total Length
TVD Or Total Elevation
Inside Diameter
0.00 1,000.00 2,000.00 3,000.00 4,000.00 5,000.00 6,000.00285.00
290.00
295.00
300.00
305.00
310.00
315.00
320.00
325.00
Surface Pressure Plot for Link L002 - Base Case
Fluid
Distance from Inlet, FT
Pres
sure
, PSI
G
0.00 1,000.00 2,000.00 3,000.00 4,000.00 5,000.00 6,000.000.00
10.00
20.00
30.00
40.00
50.00
60.00
70.00
Surface Temperature Plot for Link L002 - Base Case
Fluid Ambient
Distance from Inlet, FT
Tem
pera
ture
, DEG
F
Holdup and Velocity Report - Base Case
Name
ABBLS FT/SEC FT/SEC
P003 PIPE Inlet
P003 PIPE Seg 1 0.000 0.000 0.000 0.000 57.149
P003 PIPE Seg 2 0.000 0.000 0.000 0.000 58.240
P003 PIPE Seg 3 0.000 0.000 0.000 0.000 59.391
P003 PIPE Outlet 0.000 0.000 0.000 0.000 60.637
Pressure Gradient Report - L002 Base Case
Name
PSI/FT PSI/FT PSI/FT PSIG PSIG
P003 PIPE Inlet
P003 PIPE Seg 1 -0.00443 0.00000 -0.00445 -5.54 0.00
P003 PIPE Seg 2 -0.00452 0.00000 -0.00454 -5.65 0.00
P003 PIPE Seg 3 -0.00461 0.00000 -0.00463 -5.76 0.00
P003 PIPE Outlet -0.00470 0.00000 -0.00473 -5.88 0.00
Viscosity Density Report - Base Case
Name Oil Viscosity Liquid Density Vapor Density
CP CP CP LB/FT3 LB/FT3
P003 PIPE Inlet
P003 PIPE Seg 1 0.00000 0.00000 0.01037 0.00000 1.670
P003 PIPE Seg 2 0.00000 0.00000 0.01036 0.00000 1.639
P003 PIPE Seg 3 0.00000 0.00000 0.01034 0.00000 1.607
P003 PIPE Outlet 0.00000 0.00000 0.01033 0.00000 1.574
Friction Report - Base Case
Device Type
Device Seg
No Slip Liquid Holdup
Slip Liquid Holdup
Total Liquid Holdup
Liquid Superficial
Velocity
Gas Superficial
Velocity
Device Type
Device Seg
Friction Pressure Gradient
Elevation Pressure Gradient
Total Pressure Gradient
Friction Pressure Change
Elevation Pressure Change
Device Type
Device Seg
Liquid Viscosity
Vapor Viscosity
Name
LB/FT3 FT/SEC IN CP
P003 PIPE Inlet
P003 PIPE Seg 1 1.670 57.149 19.000 0.010 0.012
P003 PIPE Seg 2 1.639 58.240 19.000 0.010 0.012
P003 PIPE Seg 3 1.607 59.391 19.000 0.010 0.012
P003 PIPE Outlet 1.574 60.637 19.000 0.010 0.012
Heat Transfer Report - Base Case
Name
BTU/HR-FT-F
P003 PIPE Inlet
P003 PIPE Seg 1 0.015 0.0052 0.0009 0.0000 0.3611
P003 PIPE Seg 2 0.015 0.0052 0.0009 0.0000 0.3611
P003 PIPE Seg 3 0.015 0.0052 0.0009 0.0000 0.3611
P003 PIPE Outlet 0.015 0.0052 0.0009 0.0000 0.3611
Case Study 01
Temperature Pressure Report - Case 1Case Study 01
Name Pressure Temperature
FT FT IN PSIG DEG F
P003 PIPE Inlet 0.00 0.00 19.00 322.93 60.00
P003 PIPE Seg 1 1,250.00 0.00 19.00 317.37 60.00
P003 PIPE Seg 2 2,500.00 0.00 19.00 311.69 60.00
P003 PIPE Seg 3 3,750.00 0.00 19.00 305.91 60.00
P003 PIPE Outlet 5,000.00 0.00 19.00 300.00 60.00
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
L002 - Case 1
Device Type
Device Seg
MWD Or Total Length
TVD Or Total Elevation
Inside Diameter
0.00 1,000.00 2,000.00 3,000.00 4,000.00 5,000.00 6,000.00285.00
290.00
295.00
300.00
305.00
310.00
315.00
320.00
325.00
Surface Pressure Plot for Link L002 - Case 1
Fluid
Distance from Inlet, FT
Pres
sure
, PSI
G
0.00 1,000.00 2,000.00 3,000.00 4,000.00 5,000.00 6,000.000.00
10.00
20.00
30.00
40.00
50.00
60.00
70.00
Surface Temperature Plot for Link L002 - Case 1
Fluid Ambient
Distance from Inlet, FT
Tem
pera
ture
, DEG
F
Holdup and Velocity Report - Case 1Case Study 01
Name
ABBLS FT/SEC FT/SEC
P003 PIPE Inlet
P003 PIPE Seg 1 0.000 0.000 0.000 0.000 57.149
P003 PIPE Seg 2 0.000 0.000 0.000 0.000 58.240
P003 PIPE Seg 3 0.000 0.000 0.000 0.000 59.391
P003 PIPE Outlet 0.000 0.000 0.000 0.000 60.637
Pressure Gradient Report - L002 Case 1Case Study 01
Name
PSI/FT PSI/FT PSI/FT PSIG PSIG
Device Type
Device Seg
No Slip Liquid Holdup
Slip Liquid Holdup
Total Liquid Holdup
Liquid Superficial
Velocity
Gas Superficial
Velocity
Device Type
Device Seg
Friction Pressure Gradient
Elevation Pressure Gradient
Total Pressure Gradient
Friction Pressure Change
Elevation Pressure Change
0.00 1,000.00 2,000.00 3,000.00 4,000.00 5,000.00 6,000.00285.00
290.00
295.00
300.00
305.00
310.00
315.00
320.00
325.00
Surface Pressure Plot for Link L002 - Case 1
Fluid
Distance from Inlet, FT
Pres
sure
, PSI
G
0.00 1,000.00 2,000.00 3,000.00 4,000.00 5,000.00 6,000.000.00
10.00
20.00
30.00
40.00
50.00
60.00
70.00
Surface Temperature Plot for Link L002 - Case 1
Fluid Ambient
Distance from Inlet, FT
Tem
pera
ture
, DEG
F
P003 PIPE Inlet
P003 PIPE Seg 1 -0.00443 0.00000 -0.00445 -5.54 0.00
P003 PIPE Seg 2 -0.00452 0.00000 -0.00454 -5.65 0.00
P003 PIPE Seg 3 -0.00461 0.00000 -0.00463 -5.76 0.00
P003 PIPE Outlet -0.00470 0.00000 -0.00473 -5.88 0.00
Viscosity Density Report - Case 1Case Study 01
Name Oil Viscosity Liquid Density Vapor Density
CP CP CP LB/FT3 LB/FT3
P003 PIPE Inlet
P003 PIPE Seg 1 0.00000 0.00000 0.01037 0.00000 1.670
P003 PIPE Seg 2 0.00000 0.00000 0.01036 0.00000 1.639
P003 PIPE Seg 3 0.00000 0.00000 0.01034 0.00000 1.607
P003 PIPE Outlet 0.00000 0.00000 0.01033 0.00000 1.574
Friction Report - Case 1Case Study 01
Name
LB/FT3 FT/SEC IN CP
P003 PIPE Inlet
P003 PIPE Seg 1 1.670 57.149 19.000 0.010 0.012
P003 PIPE Seg 2 1.639 58.240 19.000 0.010 0.012
P003 PIPE Seg 3 1.607 59.391 19.000 0.010 0.012
P003 PIPE Outlet 1.574 60.637 19.000 0.010 0.012
Heat Transfer Report - Case 1Case Study 01
Name
BTU/HR-FT-F
P003 PIPE Inlet
P003 PIPE Seg 1 0.015 0.0052 0.0009 0.0000 0.3611
P003 PIPE Seg 2 0.015 0.0052 0.0009 0.0000 0.3611
P003 PIPE Seg 3 0.015 0.0052 0.0009 0.0000 0.3611
P003 PIPE Outlet 0.015 0.0052 0.0009 0.0000 0.3611
Device Type
Device Seg
Liquid Viscosity
Vapor Viscosity
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
Temperature Pressure Report - Base Case
U Factor
DEG F
60.00 0.00 X
60.00 2.72 X
60.00 2.72 X
60.00 2.72 X
60.00 2.72 X
Ambient Temperature
Device Domain
BTU/HR-FT2-F
0.00 1,000.00 2,000.00 3,000.00 4,000.00 5,000.00 6,000.000.00
10.00
20.00
30.00
40.00
50.00
60.00
70.00
Surface Temperature Plot for Link L002 - Base Case
Fluid Ambient
Distance from Inlet, FT
Tem
pera
ture
, DEG
F
Holdup and Velocity Report - Base Case
Sonic Velocity
FT/SEC FT/SEC
57.149 1,136.191 ---- 1-PH
58.240 1,137.152 ---- 1-PH
59.391 1,138.113 ---- 1-PH
60.637 1,139.343 ---- 1-PH
Pressure Gradient Report - L002 Base Case
PSIG
-5.56
-5.67
-5.78
-5.91
Viscosity Density Report - Base Case
Slip Density
LB/FT3 LB/FT3
1.670 1.670
1.639 1.639
1.607 1.607
1.574 1.574
Friction Report - Base Case
Mixture Velocity
Flow Regime Corr / T-D
Total Pressure Change
No Slip Density
DYNES/CM
2.168E+07 0.000
2.171E+07 0.000
2.174E+07 0.000
2.177E+07 0.000
Heat Transfer Report - Base Case
BTU/LB BTU/LB
Case Study 01
Temperature Pressure Report - Case 1Case Study 01
U Factor
DEG F
60.00 0.00 X
60.00 2.72 X
60.00 2.72 X
60.00 2.72 X
60.00 2.72 X
Reynolds Number
Liquid Surface Tension
Liquid Enthalpy
Vapor Enthalpy
Hydrate Formation
Ambient Temperature
Device Domain
BTU/HR-FT2-F
0.00 1,000.00 2,000.00 3,000.00 4,000.00 5,000.00 6,000.000.00
10.00
20.00
30.00
40.00
50.00
60.00
70.00
Surface Temperature Plot for Link L002 - Case 1
Fluid Ambient
Distance from Inlet, FT
Tem
pera
ture
, DEG
F
Holdup and Velocity Report - Case 1Case Study 01
Sonic Velocity
FT/SEC FT/SEC
57.149 1,136.191 ---- 1-PH
58.240 1,137.152 ---- 1-PH
59.391 1,138.113 ---- 1-PH
60.637 1,139.343 ---- 1-PH
Pressure Gradient Report - L002 Case 1Case Study 01
PSIG
Mixture Velocity
Flow Regime Corr / T-D
Total Pressure Change
0.00 1,000.00 2,000.00 3,000.00 4,000.00 5,000.00 6,000.000.00
10.00
20.00
30.00
40.00
50.00
60.00
70.00
Surface Temperature Plot for Link L002 - Case 1
Fluid Ambient
Distance from Inlet, FT
Tem
pera
ture
, DEG
F
-5.56
-5.67
-5.78
-5.91
Viscosity Density Report - Case 1Case Study 01
Slip Density
LB/FT3 LB/FT3
1.670 1.670
1.639 1.639
1.607 1.607
1.574 1.574
Friction Report - Case 1Case Study 01
DYNES/CM
2.168E+07 0.000
2.171E+07 0.000
2.174E+07 0.000
2.177E+07 0.000
Heat Transfer Report - Case 1Case Study 01
BTU/LB BTU/LB
No Slip Density
Reynolds Number
Liquid Surface Tension
Liquid Enthalpy
Vapor Enthalpy
Hydrate Formation
Temperature Pressure Report - Base Case
Name Pressure Temperature
FT FT IN PSIG DEG F
P002 PIPE Inlet 0.00 0.00 19.00 322.93 60.00
P002 PIPE Outlet 0.00 0.00 19.00 322.93 60.00
Index
L003 - Base Case
Device Type
Device Seg
MWD Or Total Length
TVD Or Total Elevation
Inside Diameter
0.00 0.00 0.000.00
50.00
100.00
150.00
200.00
250.00
300.00
350.00
Surface Pressure Plot for Link L003 - Base Case
Fluid
Distance from Inlet, FT
Pres
sure
, PSI
G
0.00 0.00 0.000.00
10.00
20.00
30.00
40.00
50.00
60.00
70.00
Surface Temperature Plot for Link L003 - Base Case
Fluid Ambient
Distance from Inlet, FT
Tem
pera
ture
, DEG
F
Holdup and Velocity Report - Base Case
Name
ABBLS FT/SEC FT/SEC
P002 PIPE Inlet
P002 PIPE Outlet 0.000 0.000 0.000 0.000 11.322
Pressure Gradient Report - L003 Base Case
Name
PSI/FT PSI/FT PSI/FT PSIG PSIG
P002 PIPE Inlet
P002 PIPE Outlet -0.00018 0.00000 -0.00018 0.00 0.00
Viscosity Density Report - Base Case
Name Oil Viscosity Liquid Density Vapor Density
CP CP CP LB/FT3 LB/FT3
P002 PIPE Inlet
P002 PIPE Outlet 0.00000 0.00000 0.01038 0.00000 1.686
Friction Report - Base Case
Name
LB/FT3 FT/SEC IN CP
P002 PIPE Inlet
P002 PIPE Outlet 1.686 11.322 19.000 0.010 0.012
Heat Transfer Report - Base Case
Device Type
Device Seg
No Slip Liquid Holdup
Slip Liquid Holdup
Total Liquid Holdup
Liquid Superficial
Velocity
Gas Superficial
Velocity
Device Type
Device Seg
Friction Pressure Gradient
Elevation Pressure Gradient
Total Pressure Gradient
Friction Pressure Change
Elevation Pressure Change
Device Type
Device Seg
Liquid Viscosity
Vapor Viscosity
Device Type
Device Seg
Friction Density
Friction Velocity
Friction Diameter
Friction Viscosity
Friction Factor
Name
BTU/HR-FT-F
P002 PIPE Inlet
P002 PIPE Outlet 0.015 0.0232 0.0009 0.0000 0.3611
Case Study 01
Temperature Pressure Report - Case 1Case Study 01
Name Pressure Temperature
FT FT IN PSIG DEG F
P002 PIPE Inlet 0.00 0.00 12.00 322.93 60.00
P002 PIPE Outlet 0.00 0.00 12.00 322.93 60.00
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
L003 - Case 1
Device Type
Device Seg
MWD Or Total Length
TVD Or Total Elevation
Inside Diameter
0.00 0.00 0.000.00
50.00
100.00
150.00
200.00
250.00
300.00
350.00
Surface Pressure Plot for Link L003 - Case 1
Fluid
Distance from Inlet, FT
Pres
sure
, PSI
G
0.00 0.00 0.000.00
10.00
20.00
30.00
40.00
50.00
60.00
70.00
Surface Temperature Plot for Link L003 - Case 1
Fluid Ambient
Distance from Inlet, FT
Tem
pera
ture
, DEG
F
Holdup and Velocity Report - Case 1Case Study 01
Name
ABBLS FT/SEC FT/SEC
P002 PIPE Inlet
P002 PIPE Outlet 0.000 0.000 0.000 0.000 28.384
Pressure Gradient Report - L003 Case 1Case Study 01
Name
PSI/FT PSI/FT PSI/FT PSIG PSIG
P002 PIPE Inlet
P002 PIPE Outlet -0.00192 0.00000 -0.00193 0.00 0.00
Viscosity Density Report - Case 1Case Study 01
Name Oil Viscosity Liquid Density Vapor Density
CP CP CP LB/FT3 LB/FT3
P002 PIPE Inlet
P002 PIPE Outlet 0.00000 0.00000 0.01038 0.00000 1.686
Friction Report - Case 1Case Study 01
Name
LB/FT3 FT/SEC IN CP
P002 PIPE Inlet
P002 PIPE Outlet 1.686 28.384 12.000 0.010 0.013
Device Type
Device Seg
No Slip Liquid Holdup
Slip Liquid Holdup
Total Liquid Holdup
Liquid Superficial
Velocity
Gas Superficial
Velocity
Device Type
Device Seg
Friction Pressure Gradient
Elevation Pressure Gradient
Total Pressure Gradient
Friction Pressure Change
Elevation Pressure Change
Device Type
Device Seg
Liquid Viscosity
Vapor Viscosity
Device Type
Device Seg
Friction Density
Friction Velocity
Friction Diameter
Friction Viscosity
Friction Factor
0.00 0.00 0.000.00
50.00
100.00
150.00
200.00
250.00
300.00
350.00
Surface Pressure Plot for Link L003 - Case 1
Fluid
Distance from Inlet, FT
Pres
sure
, PSI
G
0.00 0.00 0.000.00
10.00
20.00
30.00
40.00
50.00
60.00
70.00
Surface Temperature Plot for Link L003 - Case 1
Fluid Ambient
Distance from Inlet, FT
Tem
pera
ture
, DEG
F
Heat Transfer Report - Case 1Case Study 01
Name
BTU/HR-FT-F
P002 PIPE Inlet
P002 PIPE Outlet 0.015 0.0096 0.0009 0.0000 0.3054
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
Temperature Pressure Report - Base Case
U Factor
DEG F
60.00 0.00 X
60.00 2.60 X
Ambient Temperature
Device Domain
BTU/HR-FT2-F
0.00 0.00 0.000.00
10.00
20.00
30.00
40.00
50.00
60.00
70.00
Surface Temperature Plot for Link L003 - Base Case
Fluid Ambient
Distance from Inlet, FT
Tem
pera
ture
, DEG
F
Holdup and Velocity Report - Base Case
Sonic Velocity
FT/SEC FT/SEC
11.322 1,140.262 ---- 1-PH
Pressure Gradient Report - L003 Base Case
PSIG
0.00
Viscosity Density Report - Base Case
Slip Density
LB/FT3 LB/FT3
1.686 1.686
Friction Report - Base Case
DYNES/CM
4.333E+06 0.000
Heat Transfer Report - Base Case
Mixture Velocity
Flow Regime Corr / T-D
Total Pressure Change
No Slip Density
Reynolds Number
Liquid Surface Tension
BTU/LB BTU/LB
Case Study 01
Temperature Pressure Report - Case 1Case Study 01
U Factor
DEG F
60.00 0.00 X
60.00 3.17 X
Liquid Enthalpy
Vapor Enthalpy
Hydrate Formation
Ambient Temperature
Device Domain
BTU/HR-FT2-F
0.00 0.00 0.000.00
10.00
20.00
30.00
40.00
50.00
60.00
70.00
Surface Temperature Plot for Link L003 - Case 1
Fluid Ambient
Distance from Inlet, FT
Tem
pera
ture
, DEG
F
Holdup and Velocity Report - Case 1Case Study 01
Sonic Velocity
FT/SEC FT/SEC
28.384 1,140.262 ---- 1-PH
Pressure Gradient Report - L003 Case 1Case Study 01
PSIG
0.00
Viscosity Density Report - Case 1Case Study 01
Slip Density
LB/FT3 LB/FT3
1.686 1.686
Friction Report - Case 1Case Study 01
DYNES/CM
6.860E+06 0.000
Mixture Velocity
Flow Regime Corr / T-D
Total Pressure Change
No Slip Density
Reynolds Number
Liquid Surface Tension
0.00 0.00 0.000.00
10.00
20.00
30.00
40.00
50.00
60.00
70.00
Surface Temperature Plot for Link L003 - Case 1
Fluid Ambient
Distance from Inlet, FT
Tem
pera
ture
, DEG
F
Heat Transfer Report - Case 1Case Study 01
BTU/LB BTU/LB
Liquid Enthalpy
Vapor Enthalpy
Hydrate Formation
Case Study SummaryCase Number Node Pressure Temperature
PSIG DEG F
BASE CASE S001 336.73 60.00
J001 322.93 60.00
S002 322.93 60.00
D001 300.00 60.00
CASE 1 S001 336.73 60.00
Case Study 01 J001 322.93 60.00
S002 322.93 60.00
D001 300.00 60.00
Index
Case Study SummaryGas Rate
MM FT3/DAY
200.000
0.000
50.001
-250.001
200.000
0.000
50.001
-250.001
