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R
PIPEPHASE Version 9.1 MACHINE IBMPC INPUT LISTING - PAGE 1
==============================================================================
$ SIMSCI PIPEPHASE Version 9.1 keyword file...
$
$ General Data Section
$
TITLE DATE=05/16/12
$
$
DIMENSION RATE(LV)=BPD
$
CALCULATION NETWORK, LIQUID, PRANDTL
$
DEFAULT IDPIPE=4.026, IDTUBING=4.026, IDRISER=4.026, *
IDANNULUS=6.065, HAUSEN
$
PRINT INPUT=FULL, DEVICE=FULL, PLOT=FULL, *
PROPERTY=FULL, MAP=TAITEL, MERGESUB, *
DATABASE=FULL, SIMULATOR=PART
$
SEGMENT AUTO=OFF, DLHORIZ(FT)=2000, DLVERT(FT)=500
$
$ 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(WATER, SPGR)=1.01567, VISC=100, 2.32/ 140, 2.18
CORRELATION VISC(LIQ)=ASME
$
$ Structure Data Section
$
STRUCTURE DATA
$
SOURCE NAME=P250, IDNAME=P250, PRIORITY=0, *
SETNO=1, PRES(ESTI)=116, TEMP=100, *
RATE=2.0000e+005, XCORD=-504, YCORD=130
$
$~SINK NAME=D001, IDNAME=D001, PRES=1200, *
$~ RATE(ESTI)=8000, XCORD=2562, YCORD=1932
SINK NAME=D002, IDNAME=D002, PRES(ESTI)=1200, *
RATE=56000, XCORD=979, YCORD=1085
SINK NAME=MPG1154, IDNAME=MPG1, PRES=1200, *
RATE(ESTI)=16000, XCORD=1668, YCORD=-372
SINK NAME=MPG10218, IDNAME=MPG2, PRES=1200, *
RATE(ESTI)=16000, XCORD=1245, YCORD=-347
SINK NAME=MPG1035, IDNAME=MPG3, PRES=1200, *
RATE(ESTI)=16000, XCORD=2142, YCORD=-360
SINK NAME=MPG716, IDNAME=MPG7, PRES=1200, *
RATE(ESTI)=16000, XCORD=2558, YCORD=-64
SINK NAME=MPGBE, IDNAME=MPGB, PRES=1200, *
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PIPEPHASE Version 9.1 MACHINE IBMPC INPUT LISTING - PAGE 2
==============================================================================
RATE(ESTI)=16000, XCORD=2667, YCORD=416
SINK NAME=POZO2, IDNAME=POZ1, PRES=1200, *
RATE(ESTI)=16000, XCORD=2281, YCORD=1201
SINK NAME=POZO3, IDNAME=POZ2, PRES=1200, *
RATE(ESTI)=16000, XCORD=1808, YCORD=1228
SINK NAME=POZO4, IDNAME=POZ3, PRES=1200, *
RATE(ESTI)=16000, XCORD=1412, YCORD=1186
SINK NAME=POZO1, IDNAME=POZO, PRES=1200, *
RATE(ESTI)=16000, XCORD=2579, YCORD=871
$
JUNCTION NAME=J000, IDNAME=J000, XCORD=95, *
YCORD=-203
JUNCTION NAME=J001, IDNAME=J001, XCORD=76, *
YCORD=142
JUNCTION NAME=J002, IDNAME=J002, XCORD=68, *
YCORD=663
JUNCTION NAME=J004, IDNAME=J004, XCORD=615, *
YCORD=-409
JUNCTION NAME=J005, IDNAME=J005, XCORD=612, *
YCORD=-33
JUNCTION NAME=J006, IDNAME=J006, XCORD=614, *
YCORD=421
JUNCTION NAME=J007, IDNAME=J007, XCORD=598, *
YCORD=940
$~JUNCTION NAME=J008, IDNAME=J008, XCORD=1538, *
$~ YCORD=1971
JUNCTION NAME=J021, IDNAME=J021, XCORD=1518, *
YCORD=430
$
$
LINK NAME=L001, FROM=P250, TO=J001, *
IDNAME=L001, IDFROM=P250, IDTO=J001
PIPE NAME=P000, LENGTH(M)=1, NOMD=20, *
SCHED= 40, U=1
$
LINK NAME=L003, FROM=J001, TO=J000, *
IDNAME=L003, IDFROM=J001, IDTO=J000
PIPE NAME=P001, LENGTH(M)=10, NOMD=20, *
SCHED= 40, U=1
$
LINK NAME=L004, FROM=J001, TO=J002, *
IDNAME=L004, IDFROM=J001, IDTO=J002
PIPE NAME=P002, LENGTH(M)=10, NOMD=20, *
SCHED= 40, U=1
$
LINK NAME=L006, FROM=J021, TO=D002, *
IDNAME=L006, IDFROM=J021, IDTO=D002
PIPE NAME=P016, LENGTH(M)=30, NOMD=20, *
SCHED= 80, U=1
$
$~LINK NAME=L007, FROM=J008, TO=D001, *
$~ IDNAME=L007, IDFROM=J008, IDTO=D001
$~PIPE NAME=P039, LENGTH(M)=500, NOMD=6, *
$~ SCHED= 80, U=1
$
LINK NAME=L010, FROM=J000, TO=J004, *
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PIPEPHASE Version 9.1 MACHINE IBMPC INPUT LISTING - PAGE 3
==============================================================================
IDNAME=L010, IDFROM=J000, IDTO=J004
PIPE NAME=P004, LENGTH(M)=6, NOMD=10, *
SCHED= 40, U=1
PIPE NAME=P005, LENGTH(M)=6, NOMD=10, *
SCHED= 80, U=1
$
LINK NAME=L018, FROM=J004, TO=J005, *
IDNAME=L018, IDFROM=J004, IDTO=J005
PIPE NAME=P012, LENGTH(M)=7, NOMD=20, *
SCHED= 80, U=1
$
LINK NAME=L024, FROM=J006, TO=J021, *
IDNAME=L024, IDFROM=J006, IDTO=J021
PIPE NAME=P015, LENGTH(M)=60, NOMD=20, *
SCHED= 80, U=1
$
LINK NAME=L030, FROM=J005, TO=J006, *
IDNAME=L030, IDFROM=J005, IDTO=J006
PIPE NAME=P013, LENGTH(M)=7, NOMD=20, *
SCHED= 80, U=1
$
LINK NAME=L032, FROM=J007, TO=J006, *
IDNAME=L032, IDFROM=J007, IDTO=J006
PIPE NAME=P014, LENGTH(M)=6, NOMD=20, *
SCHED= 80, U=1
$
LINK NAME=L075, FROM=J021, TO=MPG1154, *
IDNAME=L075, IDFROM=J021, IDTO=MPG1
PIPE NAME=P027, LENGTH(M)=450, NOMD=6, *
SCHED= 80, U=1
MREGULATOR NAME=R001, QRATE=16000
PIPE NAME=P044, LENGTH(M)=2, NOMD=6, *
SCHED= 80, U=1
$
LINK NAME=L077, FROM=J021, TO=MPG10218, *
IDNAME=L077, IDFROM=J021, IDTO=MPG2
PIPE NAME=P028, LENGTH(M)=1550, NOMD=6, *
SCHED= 80, U=1
MREGULATOR NAME=R002, QRATE=16000
PIPE NAME=P043, LENGTH(M)=2, NOMD=6, *
SCHED= 80, U=1
$
LINK NAME=L079, FROM=J021, TO=MPG1035, *
IDNAME=L079, IDFROM=J021, IDTO=MPG3
PIPE NAME=P029, LENGTH(M)=1380, NOMD=6, *
SCHED= 80, U=1
MREGULATOR NAME=R003, QRATE=16000
PIPE NAME=P042, LENGTH(M)=2, NOMD=6, *
SCHED= 80, U=1
$
LINK NAME=L080, FROM=J021, TO=MPG716, *
IDNAME=L080, IDFROM=J021, IDTO=MPG7
PIPE NAME=P030, LENGTH(M)=1600, NOMD=6, *
SCHED= 80, U=1
MREGULATOR NAME=R004, QRATE=16000
PIPE NAME=P041, LENGTH(M)=2, NOMD=6, *
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PIPEPHASE Version 9.1 MACHINE IBMPC INPUT LISTING - PAGE 4
==============================================================================
SCHED= 80, U=1
$
LINK NAME=L081, FROM=J021, TO=MPGBE, *
IDNAME=L081, IDFROM=J021, IDTO=MPGB
PIPE NAME=P031, LENGTH(M)=4280, NOMD=6, *
SCHED= 80, U=1
MREGULATOR NAME=R005, QRATE=16000
PIPE NAME=P045, LENGTH(M)=2, NOMD=6, *
SCHED= 80, U=1
$
LINK NAME=L083, FROM=J021, TO=POZO1, *
IDNAME=L083, IDFROM=J021, IDTO=POZO
PIPE NAME=P032, LENGTH(M)=3000, NOMD=6, *
SCHED= 80, U=1
$D~MREGULATOR NAME=R006, QRATE=16000
$D~PIPE NAME=P046, LENGTH(M)=2, NOMD=6, *
$D~ SCHED= 80, U=1
$
LINK NAME=L084, FROM=J021, TO=POZO2, *
IDNAME=L084, IDFROM=J021, IDTO=POZ1
PIPE NAME=P033, LENGTH(M)=3000, NOMD=6, *
SCHED= 80, U=1
$D~MREGULATOR NAME=R007, QRATE=16000
$D~PIPE NAME=P047, LENGTH(M)=2, NOMD=6, *
$D~ SCHED= 80, U=1
$
LINK NAME=L086, FROM=J021, TO=POZO3, *
IDNAME=L086, IDFROM=J021, IDTO=POZ2
PIPE NAME=P034, LENGTH(M)=3000, NOMD=6, *
SCHED= 80, U=1
$D~MREGULATOR NAME=R008, QRATE=16000
$D~PIPE NAME=P048, LENGTH(M)=2, NOMD=6, *
$D~ SCHED= 80, U=1
$
LINK NAME=L088, FROM=J021, TO=POZO4, *
IDNAME=L088, IDFROM=J021, IDTO=POZ3
PIPE NAME=P035, LENGTH(M)=3000, NOMD=6, *
SCHED= 80, U=1
$D~MREGULATOR NAME=R009, QRATE=16000
$D~PIPE NAME=P049, LENGTH(M)=2, NOMD=6, *
$D~ SCHED= 80, U=1
$
LINK NAME=L099, FROM=J000, TO=J005, *
IDNAME=L099, IDFROM=J000, IDTO=J005
PIPE NAME=P006, LENGTH(M)=6, NOMD=10, *
SCHED= 40, U=1
PIPE NAME=P007, LENGTH(M)=6, NOMD=10, *
SCHED= 120, U=1
$
LINK NAME=L100, FROM=J002, TO=J006, *
IDNAME=L100, IDFROM=J002, IDTO=J006
PIPE NAME=P008, LENGTH(M)=6, NOMD=10, *
SCHED= 40, U=1
PIPE NAME=P009, LENGTH(M)=6, NOMD=10, *
SCHED= 80, U=1
$
R
PIPEPHASE Version 9.1 MACHINE IBMPC INPUT LISTING - PAGE 5
==============================================================================
LINK NAME=L101, FROM=J002, TO=J007, *
IDNAME=L101, IDFROM=J002, IDTO=J007
PIPE NAME=P010, LENGTH(M)=6, NOMD=10, *
SCHED= 40, U=1
PIPE NAME=P011, LENGTH(M)=6, NOMD=10, *
SCHED= 80, U=1
$
$ End of keyword file...
$
END
END OF PRE-PROCESSING -- NO ERRORS
-- NO WARNINGS
R
PIPEPHASE Version 9.1 INPUT PROCESSOR DIRECTORY
==============================================================================
PROJECT USER
PROBLEM DATE 05/16/12
PAGE CONTENTS
---- --------------------------------------------
1 GENERAL DATA
3 PVT DATA
3 CORRELATION SET DATA
METHODS DATA
4 SOLUTION METHODS/TOLERANCES
SOURCE DATA
5 SOURCE P250
STRUCTURE DATA
6 LINK L001
6 LINK L003
6 LINK L004
7 LINK L006
7 LINK L010
8 LINK L018
8 LINK L024
8 LINK L030
9 LINK L032
9 LINK L075
10 LINK L077
10 LINK L079
11 LINK L080
11 LINK L081
12 LINK L083
12 LINK L084
12 LINK L086
13 LINK L088
13 LINK L099
14 LINK L100
14 LINK L101
15 JUNCTIONS AND SINKS
17 NETWORK CONNECTIVITY
23 ERROR SUMMARY
UNABLE TO GET REQUIRED ORDERING
*** WARNING *****
PRESS: ESTIMATE AND FLOW DIRECTION INCONSISTENT
FOR FOLLOWING LINKS
LINK FROM NODE PRESSURE TO NODE PRESSURE
1 P250 130.7 J001 1214.7
7 J006 130.7 J021 1214.7
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 1
PROJECT INPUT
PROBLEM GENERAL DATA 05/16/12
==============================================================================
CALCULATION OPTIONS
RUN TYPE........ NETWORK
FLUID TYPE...... LIQUID
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
RISER 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 - RISER.... 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
RISER FLOW CODE IS MOODY
TUBING FLOW CODE IS MOODY
ANNULUS FLOW CODE IS MOODY
BASE CONDITIONS
STANDARD TEMPERATURE....... 60.00 DEG F
STANDARD PRESSURE.......... 0.000 PSIG
PRINT OPTIONS
INPUT........... GENERAL ASSAY COMPONENT
PVT FLOW TABLE METHOD
SOURCE STRUCTURE W ANALYSIS
GAS LIFT CASE STUDY
CONNECT......... PLOT
PVTGEN.......... NONE
SUMMARY......... BOTH
DEVICE.......... FULL
MAP............. TAITEL-DUKLER-BARNEA
PROPERTY........ FULL
MERGED SUBNETWORKS REQUESTED
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 2
PROJECT INPUT
PROBLEM GENERAL DATA 05/16/12
==============================================================================
SEGMENTATION OPTIONS
LENGTH CHANGE - HORIZONTAL....... 2000.0 FT
VERTICAL......... 500.0 FT
MAXIMUM NUMBER OF SEGMENTS....... 20
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 3
PROJECT INPUT
PROBLEM PVT DATA 05/16/12
==============================================================================
PVT DATA SUMMARY
1 CORRELATION DATA SETS 0 ERRORS 0 WARNINGS
DEFAULT PVT METHODS OPTIONS
Z FACTOR METHOD.......... STANDING
LIQUID VISCOSITY METHOD.. FOR OIL STANDING
FOR WATER ASME STEAM TABLE
CORRELATION SET DATA
CORRELATION SET NUMBER 1
GRAVITY OF WATER.......... 1.0157
VISCOSITY OF LIQUID
100.00 DEG F ........ 2.3200 CP
140.00 DEG F ........ 2.1800 CP
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 4
PROJECT INPUT
PROBLEM METHODS DATA 05/16/12
==============================================================================
SOLUTION METHODS/TOLERANCES
NETWORK SOLUTION METHOD IS PBAL
MAXIMUM ITERATIONS..................... 20
MAXIMUM NUMBER OF INTERVAL HALVINGS.... 3
ABSOLUTE PRESSURE TOLERANCE............ 0.100 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
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 5
PROJECT INPUT
PROBLEM SOURCE DATA 05/16/12
==============================================================================
SOURCE P250
(P250)
THIS SOURCE IS ON
PVT SET NUMBER............ 1
RATE...................... 200000.0000 BBL/DAY
ESTIMATED PRESSURE........ 116.0001 PSIG
TEMPERATURE............... 100.00 DEG F
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 6
PROJECT INPUT
PROBLEM STRUCTURE DATA 05/16/12
==============================================================================
LINK L001
LINK IS FROM "P250 " TO "J001 "
"L001" FROM "P250" TO "J001"
DEVICE SA001, P000, IS A PIPE
FLOW CODE IS MOODY
INSIDE DIAMETER.............. 18.8110 IN
LENGTH....................... 3.3 FT
ELEVATION CHANGE............. 0.0 FT
FLOW EFFICIENCY.............. 100.00 PERCENT
HEAT LOSS COEFFICIENT........ 1.00000 BTU/HR-FT2-F
ROUGHNESS.................... 0.00180 IN
AMBIENT TEMPERATURE.......... 80.00 DEG F
LINK L003
LINK IS FROM "J001 " TO "J000 "
"L003" FROM "J001" TO "J000"
DEVICE SA002, P001, IS A PIPE
FLOW CODE IS MOODY
INSIDE DIAMETER.............. 18.8110 IN
LENGTH....................... 32.8 FT
ELEVATION CHANGE............. 0.0 FT
FLOW EFFICIENCY.............. 100.00 PERCENT
HEAT LOSS COEFFICIENT........ 1.00000 BTU/HR-FT2-F
ROUGHNESS.................... 0.00180 IN
AMBIENT TEMPERATURE.......... 80.00 DEG F
LINK L004
LINK IS FROM "J001 " TO "J002 "
"L004" FROM "J001" TO "J002"
DEVICE SA003, P002, IS A PIPE
FLOW CODE IS MOODY
INSIDE DIAMETER.............. 18.8110 IN
LENGTH....................... 32.8 FT
ELEVATION CHANGE............. 0.0 FT
FLOW EFFICIENCY.............. 100.00 PERCENT
HEAT LOSS COEFFICIENT........ 1.00000 BTU/HR-FT2-F
ROUGHNESS.................... 0.00180 IN
AMBIENT TEMPERATURE.......... 80.00 DEG F
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 7
PROJECT INPUT
PROBLEM STRUCTURE DATA 05/16/12
==============================================================================
LINK L006
LINK IS FROM "J021 " TO "D002 "
"L006" FROM "J021" TO "D002"
DEVICE SA004, P016, IS A PIPE
FLOW CODE IS MOODY
INSIDE DIAMETER.............. 17.9370 IN
LENGTH....................... 98.4 FT
ELEVATION CHANGE............. 0.0 FT
FLOW EFFICIENCY.............. 100.00 PERCENT
HEAT LOSS COEFFICIENT........ 1.00000 BTU/HR-FT2-F
ROUGHNESS.................... 0.00180 IN
AMBIENT TEMPERATURE.......... 80.00 DEG F
LINK L010
LINK IS FROM "J000 " TO "J004 "
"L010" FROM "J000" TO "J004"
DEVICE SA005, P004, IS A PIPE
FLOW CODE IS MOODY
INSIDE DIAMETER.............. 10.0197 IN
LENGTH....................... 19.7 FT
ELEVATION CHANGE............. 0.0 FT
FLOW EFFICIENCY.............. 100.00 PERCENT
HEAT LOSS COEFFICIENT........ 1.00000 BTU/HR-FT2-F
ROUGHNESS.................... 0.00180 IN
AMBIENT TEMPERATURE.......... 80.00 DEG F
DEVICE SA006, P005, IS A PIPE
FLOW CODE IS MOODY
INSIDE DIAMETER.............. 9.5591 IN
LENGTH....................... 19.7 FT
ELEVATION CHANGE............. 0.0 FT
FLOW EFFICIENCY.............. 100.00 PERCENT
HEAT LOSS COEFFICIENT........ 1.00000 BTU/HR-FT2-F
ROUGHNESS.................... 0.00180 IN
AMBIENT TEMPERATURE.......... 80.00 DEG F
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 8
PROJECT INPUT
PROBLEM STRUCTURE DATA 05/16/12
==============================================================================
LINK L018
LINK IS FROM "J004 " TO "J005 "
"L018" FROM "J004" TO "J005"
DEVICE SA007, P012, IS A PIPE
FLOW CODE IS MOODY
INSIDE DIAMETER.............. 17.9370 IN
LENGTH....................... 23.0 FT
ELEVATION CHANGE............. 0.0 FT
FLOW EFFICIENCY.............. 100.00 PERCENT
HEAT LOSS COEFFICIENT........ 1.00000 BTU/HR-FT2-F
ROUGHNESS.................... 0.00180 IN
AMBIENT TEMPERATURE.......... 80.00 DEG F
LINK L024
LINK IS FROM "J006 " TO "J021 "
"L024" FROM "J006" TO "J021"
DEVICE SA008, P015, IS A PIPE
FLOW CODE IS MOODY
INSIDE DIAMETER.............. 17.9370 IN
LENGTH....................... 196.9 FT
ELEVATION CHANGE............. 0.0 FT
FLOW EFFICIENCY.............. 100.00 PERCENT
HEAT LOSS COEFFICIENT........ 1.00000 BTU/HR-FT2-F
ROUGHNESS.................... 0.00180 IN
AMBIENT TEMPERATURE.......... 80.00 DEG F
LINK L030
LINK IS FROM "J005 " TO "J006 "
"L030" FROM "J005" TO "J006"
DEVICE SA009, P013, IS A PIPE
FLOW CODE IS MOODY
INSIDE DIAMETER.............. 17.9370 IN
LENGTH....................... 23.0 FT
ELEVATION CHANGE............. 0.0 FT
FLOW EFFICIENCY.............. 100.00 PERCENT
HEAT LOSS COEFFICIENT........ 1.00000 BTU/HR-FT2-F
ROUGHNESS.................... 0.00180 IN
AMBIENT TEMPERATURE.......... 80.00 DEG F
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 9
PROJECT INPUT
PROBLEM STRUCTURE DATA 05/16/12
==============================================================================
LINK L032
LINK IS FROM "J007 " TO "J006 "
"L032" FROM "J007" TO "J006"
DEVICE SA010, P014, IS A PIPE
FLOW CODE IS MOODY
INSIDE DIAMETER.............. 17.9370 IN
LENGTH....................... 19.7 FT
ELEVATION CHANGE............. 0.0 FT
FLOW EFFICIENCY.............. 100.00 PERCENT
HEAT LOSS COEFFICIENT........ 1.00000 BTU/HR-FT2-F
ROUGHNESS.................... 0.00180 IN
AMBIENT TEMPERATURE.......... 80.00 DEG F
LINK L075
LINK IS FROM "J021 " TO "MPG1154 "
"L075" FROM "J021" TO "MPG1"
DEVICE SA011, P027, IS A PIPE
FLOW CODE IS MOODY
INSIDE DIAMETER.............. 5.7638 IN
LENGTH....................... 1476.4 FT
ELEVATION CHANGE............. 0.0 FT
FLOW EFFICIENCY.............. 100.00 PERCENT
HEAT LOSS COEFFICIENT........ 1.00000 BTU/HR-FT2-F
ROUGHNESS.................... 0.00180 IN
AMBIENT TEMPERATURE.......... 80.00 DEG F
DEVICE SA012, R001, IS A SUBNETWORK REGULATOR
FLOW RATE........ ............. 16000.0 BBL/DAY
DEVICE SA013, P044, IS A PIPE
FLOW CODE IS MOODY
INSIDE DIAMETER.............. 5.7638 IN
LENGTH....................... 6.6 FT
ELEVATION CHANGE............. 0.0 FT
FLOW EFFICIENCY.............. 100.00 PERCENT
HEAT LOSS COEFFICIENT........ 1.00000 BTU/HR-FT2-F
ROUGHNESS.................... 0.00180 IN
AMBIENT TEMPERATURE.......... 80.00 DEG F
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 10
PROJECT INPUT
PROBLEM STRUCTURE DATA 05/16/12
==============================================================================
LINK L077
LINK IS FROM "J021 " TO "MPG10218 "
"L077" FROM "J021" TO "MPG2"
DEVICE SA014, P028, IS A PIPE
FLOW CODE IS MOODY
INSIDE DIAMETER.............. 5.7638 IN
LENGTH....................... 5085.3 FT
ELEVATION CHANGE............. 0.0 FT
FLOW EFFICIENCY.............. 100.00 PERCENT
HEAT LOSS COEFFICIENT........ 1.00000 BTU/HR-FT2-F
ROUGHNESS.................... 0.00180 IN
AMBIENT TEMPERATURE.......... 80.00 DEG F
DEVICE SA015, R002, IS A SUBNETWORK REGULATOR
FLOW RATE........ ............. 16000.0 BBL/DAY
DEVICE SA016, P043, IS A PIPE
FLOW CODE IS MOODY
INSIDE DIAMETER.............. 5.7638 IN
LENGTH....................... 6.6 FT
ELEVATION CHANGE............. 0.0 FT
FLOW EFFICIENCY.............. 100.00 PERCENT
HEAT LOSS COEFFICIENT........ 1.00000 BTU/HR-FT2-F
ROUGHNESS.................... 0.00180 IN
AMBIENT TEMPERATURE.......... 80.00 DEG F
LINK L079
LINK IS FROM "J021 " TO "MPG1035 "
"L079" FROM "J021" TO "MPG3"
DEVICE SA017, P029, IS A PIPE
FLOW CODE IS MOODY
INSIDE DIAMETER.............. 5.7638 IN
LENGTH....................... 4527.6 FT
ELEVATION CHANGE............. 0.0 FT
FLOW EFFICIENCY.............. 100.00 PERCENT
HEAT LOSS COEFFICIENT........ 1.00000 BTU/HR-FT2-F
ROUGHNESS.................... 0.00180 IN
AMBIENT TEMPERATURE.......... 80.00 DEG F
DEVICE SA018, R003, IS A SUBNETWORK REGULATOR
FLOW RATE........ ............. 16000.0 BBL/DAY
DEVICE SA019, P042, IS A PIPE
FLOW CODE IS MOODY
INSIDE DIAMETER.............. 5.7638 IN
LENGTH....................... 6.6 FT
ELEVATION CHANGE............. 0.0 FT
FLOW EFFICIENCY.............. 100.00 PERCENT
HEAT LOSS COEFFICIENT........ 1.00000 BTU/HR-FT2-F
ROUGHNESS.................... 0.00180 IN
AMBIENT TEMPERATURE.......... 80.00 DEG F
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 11
PROJECT INPUT
PROBLEM STRUCTURE DATA 05/16/12
==============================================================================
LINK L080
LINK IS FROM "J021 " TO "MPG716 "
"L080" FROM "J021" TO "MPG7"
DEVICE SA020, P030, IS A PIPE
FLOW CODE IS MOODY
INSIDE DIAMETER.............. 5.7638 IN
LENGTH....................... 5249.3 FT
ELEVATION CHANGE............. 0.0 FT
FLOW EFFICIENCY.............. 100.00 PERCENT
HEAT LOSS COEFFICIENT........ 1.00000 BTU/HR-FT2-F
ROUGHNESS.................... 0.00180 IN
AMBIENT TEMPERATURE.......... 80.00 DEG F
DEVICE SA021, R004, IS A SUBNETWORK REGULATOR
FLOW RATE........ ............. 16000.0 BBL/DAY
DEVICE SA022, P041, IS A PIPE
FLOW CODE IS MOODY
INSIDE DIAMETER.............. 5.7638 IN
LENGTH....................... 6.6 FT
ELEVATION CHANGE............. 0.0 FT
FLOW EFFICIENCY.............. 100.00 PERCENT
HEAT LOSS COEFFICIENT........ 1.00000 BTU/HR-FT2-F
ROUGHNESS.................... 0.00180 IN
AMBIENT TEMPERATURE.......... 80.00 DEG F
LINK L081
LINK IS FROM "J021 " TO "MPGBE "
"L081" FROM "J021" TO "MPGB"
DEVICE SA023, P031, IS A PIPE
FLOW CODE IS MOODY
INSIDE DIAMETER.............. 5.7638 IN
LENGTH....................... 14042.0 FT
ELEVATION CHANGE............. 0.0 FT
FLOW EFFICIENCY.............. 100.00 PERCENT
HEAT LOSS COEFFICIENT........ 1.00000 BTU/HR-FT2-F
ROUGHNESS.................... 0.00180 IN
AMBIENT TEMPERATURE.......... 80.00 DEG F
DEVICE SA024, R005, IS A SUBNETWORK REGULATOR
FLOW RATE........ ............. 16000.0 BBL/DAY
DEVICE SA025, P045, IS A PIPE
FLOW CODE IS MOODY
INSIDE DIAMETER.............. 5.7638 IN
LENGTH....................... 6.6 FT
ELEVATION CHANGE............. 0.0 FT
FLOW EFFICIENCY.............. 100.00 PERCENT
HEAT LOSS COEFFICIENT........ 1.00000 BTU/HR-FT2-F
ROUGHNESS.................... 0.00180 IN
AMBIENT TEMPERATURE.......... 80.00 DEG F
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 12
PROJECT INPUT
PROBLEM STRUCTURE DATA 05/16/12
==============================================================================
LINK L083
LINK IS FROM "J021 " TO "POZO1 "
"L083" FROM "J021" TO "POZO"
DEVICE SA026, P032, IS A PIPE
FLOW CODE IS MOODY
INSIDE DIAMETER.............. 5.7638 IN
LENGTH....................... 9842.5 FT
ELEVATION CHANGE............. 0.0 FT
FLOW EFFICIENCY.............. 100.00 PERCENT
HEAT LOSS COEFFICIENT........ 1.00000 BTU/HR-FT2-F
ROUGHNESS.................... 0.00180 IN
AMBIENT TEMPERATURE.......... 80.00 DEG F
LINK L084
LINK IS FROM "J021 " TO "POZO2 "
"L084" FROM "J021" TO "POZ1"
DEVICE SA027, P033, IS A PIPE
FLOW CODE IS MOODY
INSIDE DIAMETER.............. 5.7638 IN
LENGTH....................... 9842.5 FT
ELEVATION CHANGE............. 0.0 FT
FLOW EFFICIENCY.............. 100.00 PERCENT
HEAT LOSS COEFFICIENT........ 1.00000 BTU/HR-FT2-F
ROUGHNESS.................... 0.00180 IN
AMBIENT TEMPERATURE.......... 80.00 DEG F
LINK L086
LINK IS FROM "J021 " TO "POZO3 "
"L086" FROM "J021" TO "POZ2"
DEVICE SA028, P034, IS A PIPE
FLOW CODE IS MOODY
INSIDE DIAMETER.............. 5.7638 IN
LENGTH....................... 9842.5 FT
ELEVATION CHANGE............. 0.0 FT
FLOW EFFICIENCY.............. 100.00 PERCENT
HEAT LOSS COEFFICIENT........ 1.00000 BTU/HR-FT2-F
ROUGHNESS.................... 0.00180 IN
AMBIENT TEMPERATURE.......... 80.00 DEG F
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 13
PROJECT INPUT
PROBLEM STRUCTURE DATA 05/16/12
==============================================================================
LINK L088
LINK IS FROM "J021 " TO "POZO4 "
"L088" FROM "J021" TO "POZ3"
DEVICE SA029, P035, IS A PIPE
FLOW CODE IS MOODY
INSIDE DIAMETER.............. 5.7638 IN
LENGTH....................... 9842.5 FT
ELEVATION CHANGE............. 0.0 FT
FLOW EFFICIENCY.............. 100.00 PERCENT
HEAT LOSS COEFFICIENT........ 1.00000 BTU/HR-FT2-F
ROUGHNESS.................... 0.00180 IN
AMBIENT TEMPERATURE.......... 80.00 DEG F
LINK L099
LINK IS FROM "J000 " TO "J005 "
"L099" FROM "J000" TO "J005"
DEVICE SA030, P006, IS A PIPE
FLOW CODE IS MOODY
INSIDE DIAMETER.............. 10.0197 IN
LENGTH....................... 19.7 FT
ELEVATION CHANGE............. 0.0 FT
FLOW EFFICIENCY.............. 100.00 PERCENT
HEAT LOSS COEFFICIENT........ 1.00000 BTU/HR-FT2-F
ROUGHNESS.................... 0.00180 IN
AMBIENT TEMPERATURE.......... 80.00 DEG F
DEVICE SA031, P007, IS A PIPE
FLOW CODE IS MOODY
INSIDE DIAMETER.............. 9.0591 IN
LENGTH....................... 19.7 FT
ELEVATION CHANGE............. 0.0 FT
FLOW EFFICIENCY.............. 100.00 PERCENT
HEAT LOSS COEFFICIENT........ 1.00000 BTU/HR-FT2-F
ROUGHNESS.................... 0.00180 IN
AMBIENT TEMPERATURE.......... 80.00 DEG F
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 14
PROJECT INPUT
PROBLEM STRUCTURE DATA 05/16/12
==============================================================================
LINK L100
LINK IS FROM "J002 " TO "J006 "
"L100" FROM "J002" TO "J006"
DEVICE SA032, P008, IS A PIPE
FLOW CODE IS MOODY
INSIDE DIAMETER.............. 10.0197 IN
LENGTH....................... 19.7 FT
ELEVATION CHANGE............. 0.0 FT
FLOW EFFICIENCY.............. 100.00 PERCENT
HEAT LOSS COEFFICIENT........ 1.00000 BTU/HR-FT2-F
ROUGHNESS.................... 0.00180 IN
AMBIENT TEMPERATURE.......... 80.00 DEG F
DEVICE SA033, P009, IS A PIPE
FLOW CODE IS MOODY
INSIDE DIAMETER.............. 9.5591 IN
LENGTH....................... 19.7 FT
ELEVATION CHANGE............. 0.0 FT
FLOW EFFICIENCY.............. 100.00 PERCENT
HEAT LOSS COEFFICIENT........ 1.00000 BTU/HR-FT2-F
ROUGHNESS.................... 0.00180 IN
AMBIENT TEMPERATURE.......... 80.00 DEG F
LINK L101
LINK IS FROM "J002 " TO "J007 "
"L101" FROM "J002" TO "J007"
DEVICE SA034, P010, IS A PIPE
FLOW CODE IS MOODY
INSIDE DIAMETER.............. 10.0197 IN
LENGTH....................... 19.7 FT
ELEVATION CHANGE............. 0.0 FT
FLOW EFFICIENCY.............. 100.00 PERCENT
HEAT LOSS COEFFICIENT........ 1.00000 BTU/HR-FT2-F
ROUGHNESS.................... 0.00180 IN
AMBIENT TEMPERATURE.......... 80.00 DEG F
DEVICE SA035, P011, IS A PIPE
FLOW CODE IS MOODY
INSIDE DIAMETER.............. 9.5591 IN
LENGTH....................... 19.7 FT
ELEVATION CHANGE............. 0.0 FT
FLOW EFFICIENCY.............. 100.00 PERCENT
HEAT LOSS COEFFICIENT........ 1.00000 BTU/HR-FT2-F
ROUGHNESS.................... 0.00180 IN
AMBIENT TEMPERATURE.......... 80.00 DEG F
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 15
PROJECT INPUT
PROBLEM STRUCTURE DATA 05/16/12
==============================================================================
JUNCTIONS AND SINKS
JUNCTION J000
(J000)
ESTIMATED PRESSURE........ 1200.0041 PSIG
JUNCTION J001
(J001)
ESTIMATED PRESSURE........ 1200.0042 PSIG
JUNCTION J002
(J002)
ESTIMATED PRESSURE........ 766.4025 PSIG
JUNCTION J004
(J004)
ESTIMATED PRESSURE........ 983.2033 PSIG
JUNCTION J005
(J005)
ESTIMATED PRESSURE........ 549.6017 PSIG
JUNCTION J006
(J006)
ESTIMATED PRESSURE........ 116.0001 PSIG
JUNCTION J007
(J007)
ESTIMATED PRESSURE........ 332.8009 PSIG
JUNCTION J021
(J021)
ESTIMATED PRESSURE........ 1200.0041 PSIG
SINK D002
(D002)
RATE...................... 56000.0171 BBL/DAY
ESTIMATED PRESSURE........ 1200.0041 PSIG
SINK MPG1154
(MPG1)
ESTIMATED RATE............ 16000.0171 BBL/DAY
PRESSURE.................. 1200.0041 PSIG
SINK MPG10218
(MPG2)
ESTIMATED RATE............ 16000.0171 BBL/DAY
PRESSURE.................. 1200.0041 PSIG
SINK MPG1035
(MPG3)
ESTIMATED RATE............ 16000.0171 BBL/DAY
PRESSURE.................. 1200.0041 PSIG
SINK MPG716
(MPG7)
ESTIMATED RATE............ 16000.0171 BBL/DAY
PRESSURE.................. 1200.0041 PSIG
SINK MPGBE
(MPGB)
ESTIMATED RATE............ 16000.0171 BBL/DAY
PRESSURE.................. 1200.0041 PSIG
SINK POZO2
(POZ1)
ESTIMATED RATE............ 16000.0171 BBL/DAY
PRESSURE.................. 1200.0041 PSIG
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 16
PROJECT INPUT
PROBLEM STRUCTURE DATA 05/16/12
==============================================================================
JUNCTIONS AND SINKS (CONT)
SINK POZO3
(POZ2)
ESTIMATED RATE............ 16000.0171 BBL/DAY
PRESSURE.................. 1200.0041 PSIG
SINK POZO4
(POZ3)
ESTIMATED RATE............ 16000.0171 BBL/DAY
PRESSURE.................. 1200.0041 PSIG
SINK POZO1
(POZO)
ESTIMATED RATE............ 16000.0171 BBL/DAY
PRESSURE.................. 1200.0041 PSIG
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 17
PROJECT INPUT
PROBLEM NETWORK CONNECTIVITY 05/16/12
==============================================================================
NODE CONNECTIONS
---- CONNECTIONS ----
NODE NODE NAME NODE TYPE TO NODE VIA LINK
---- --------- --------- --------- ---------
P250 P250 SOURCE J001 L001
D002 D002 SINK J021 L006
MPG1 MPG1154 SINK J021 L075
MPG2 MPG10218 SINK J021 L077
MPG3 MPG1035 SINK J021 L079
MPG7 MPG716 SINK J021 L080
MPGB MPGBE SINK J021 L081
POZ1 POZO2 SINK J021 L084
POZ2 POZO3 SINK J021 L086
POZ3 POZO4 SINK J021 L088
POZO POZO1 SINK J021 L083
J000 J000 JUNCTION J001 L003
J004 L010
J005 L099
J001 J001 JUNCTION P250 L001
J000 L003
J002 L004
J002 J002 JUNCTION J001 L004
J006 L100
J007 L101
J004 J004 JUNCTION J000 L010
J005 L018
J005 J005 JUNCTION J004 L018
J006 L030
J000 L099
J006 J006 JUNCTION J021 L024
J005 L030
J007 L032
J002 L100
J007 J007 JUNCTION J006 L032
J002 L101
J021 J021 JUNCTION D002 L006
J006 L024
MPG1154 L075
MPG10218 L077
MPG1035 L079
MPG716 L080
MPGBE L081
POZO1 L083
POZO2 L084
POZO3 L086
POZO4 L088
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 18
PROJECT INPUT
PROBLEM NETWORK CONNECTIVITY 05/16/12
==============================================================================
LINK CONNECTIONS
LINK LINK NAME FROM NODE TO NODE
---- --------- --------- ----------
L001 L001 P250 J001
L003 L003 J001 J000
L004 L004 J001 J002
L006 L006 J021 D002
L010 L010 J000 J004
L018 L018 J004 J005
L024 L024 J006 J021
L030 L030 J005 J006
L032 L032 J007 J006
L075 L075 J021 MPG1154
L077 L077 J021 MPG10218
L079 L079 J021 MPG1035
L080 L080 J021 MPG716
L081 L081 J021 MPGBE
L083 L083 J021 POZO1
L084 L084 J021 POZO2
L086 L086 J021 POZO3
L088 L088 J021 POZO4
L099 L099 J000 J005
L100 L100 J002 J006
L101 L101 J002 J007
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 19
PROJECT INPUT
PROBLEM NETWORK CONNECTIVITY 05/16/12
==============================================================================
ROW 1, COLUMN 1
+-------------------------------------------------------------
|
| +----+ +----+ +----+ +----+ +----+ +----+
| |P250|----|J001|----|J000|----|J004|----|J005|----|J006|--
| |SRCE| |....| |....| |....| |....| |....|
| +----+ +----+ +----+ +----+ +----+ +----+
| | | | |
| | | | |
| | +-------------------+ |
| | |
| | |
| | |
| | |
| | |
| | |
| | |
| | |
| | |
| | |
| | |
| | |
| | |
| | |
| | |
| | |
| | |
| | |
| | |
| | |
| | |
| | |
| | |
| | |
| | |
| | |
| | |
| | |
| | |
| | |
| | |
| | |
| | |
| | |
| | |
| | |
| | |
| | |
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 20
PROJECT INPUT
PROBLEM NETWORK CONNECTIVITY 05/16/12
==============================================================================
ROW 2, COLUMN 1
| | |
| | |
| | |
| | |
| | |
| | |
| | |
| | -----
| | |
| | |
| | |
| | |
| +---------------------------------------[----
| |
| |
| |
| |
| +----
|
|
|
+-------------------------------------------------------------
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 21
PROJECT INPUT
PROBLEM NETWORK CONNECTIVITY 05/16/12
==============================================================================
ROW 1, COLUMN 2
---------------------+
|
+----+ +----+ |
--|J021|----|D002| |
|....| |SINK| |
|....| +----+ |
|....| |
|....| +----+ |
|....|----|MPG1| |
|....| |SINK| |
|....| +----+ |
|....| |
|....| +----+ |
|....|----|MPG2| |
|....| |SINK| |
|....| +----+ |
|....| |
|....| +----+ |
|....|----|MPG3| |
|....| |SINK| |
|....| +----+ |
|....| |
|....| +----+ |
|....|----|MPG7| |
|....| |SINK| |
|....| +----+ |
|....| |
|....| +----+ |
|....|----|MPGB| |
|....| |SINK| |
|....| +----+ |
|....| |
|....| +----+ |
|....|----|POZO| |
|....| |SINK| |
|....| +----+ |
|....| |
|....| +----+ |
|....|----|POZ1| |
|....| |SINK| |
|....| +----+ |
|....| |
|....| +----+ |
|J021|----|POZ2| |
|....| |SINK| |
+----+ +----+ |
| |
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 22
PROJECT INPUT
PROBLEM NETWORK CONNECTIVITY 05/16/12
==============================================================================
ROW 2, COLUMN 2
| |
+----+ |
|POZ3| |
|SINK| |
+----+ |
|
+----+ +----+ |
--|J007|----|J002| |
|....| |....| |
+----+ |....| |
|....| |
|....| |
------------|J002| |
|....| |
+----+ |
| |
| |
---------------+ |
|
|
|
---------------------+
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 23
PROJECT INPUT
PROBLEM ERROR SUMMARY 05/16/12
==============================================================================
END OF INPUT PROCESSING -- NO ERRORS
-- 1 WARNING
END OF INPUT CROSS-CHECKING -- NO ERRORS.
SUBNETWORK NUMBER 1
LINK FROM NODE TO NODE
1 22 21 MPG1
SUBNETWORK NUMBER 2
LINK FROM NODE TO NODE
1 L001 P250 J001
2 L003 J001 J000
3 L004 J001 J002
4 L006 J021 D002
5 L010 J000 J004
6 L018 J004 J005
7 L024 J006 J021
8 L030 J005 J006
9 L032 J007 J006
10 L075 J021 20
11 L077 J021 22
12 L079 J021 24
13 L080 J021 26
14 L081 J021 28
15 L083 J021 POZO
16 L084 J021 POZ1
17 L086 J021 POZ2
18 L088 J021 POZ3
19 L099 J000 J005
20 L100 J002 J006
21 L101 J002 J007
SUBNETWORK NUMBER 3
LINK FROM NODE TO NODE
1 23 23 MPG2
SUBNETWORK NUMBER 4
LINK FROM NODE TO NODE
1 24 25 MPG3
SUBNETWORK NUMBER 5
LINK FROM NODE TO NODE
1 25 27 MPG7
SUBNETWORK NUMBER 6
LINK FROM NODE TO NODE
1 26 29 MPGB
R
PIPEPHASE Version 9.1 NETWORK DIRECTORY
==============================================================================
PAGE CONTENTS
---- --------------------------------------------
1 SOLUTION DATA
6 NETWORK REPORT
131 ERROR SUMMARY
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 1
PROJECT OUTPUT
PROBLEM SOLUTION DATA 05/16/12
==============================================================================
CONVERGENCE TOLERANCE 0.10 PSI PRESSURE IMBALANCE AT SELECTED NODES
(RMS VALUE USED FOR STEP-SIZE SELECTION)
ITERATION NUMBER 0. 0
MAX PRESSURE IMBALANCE = -1173.987 PSI AT NODE POZO
RMS AVERAGE PRESSURE IMBALANCE = 887.451 PSI
ITERATION NUMBER 1. 0
MAX PRESSURE IMBALANCE = -0.013 PSI AT NODE POZO
RMS AVERAGE PRESSURE IMBALANCE = 0.011 PSI
********************************************
PBAL SOLUTION CONVERGED AFTER 1 ITERATIONS
********************************************
CONVERGENCE TOLERANCE 0.10 PSI PRESSURE IMBALANCE AT SELECTED NODES
(RMS VALUE USED FOR STEP-SIZE SELECTION)
ITERATION NUMBER 0. 0
MAX PRESSURE IMBALANCE = -1170.659 PSI AT NODE MPG1
ITERATION NUMBER 1. 0
MAX PRESSURE IMBALANCE = -1112.129 PSI AT NODE MPG1
ITERATION NUMBER 2. 0
** WARNING ** MREGULATOR OUTLET PRESSURE EXCEEDS
THE INLET PRESSURE: R001
MAX PRESSURE IMBALANCE = 111.213 PSI AT NODE MPG1
ITERATION NUMBER 3. 0
MAX PRESSURE IMBALANCE = -529.723 PSI AT NODE MPG1
ITERATION NUMBER 4. 0
MAX PRESSURE IMBALANCE = 0.000 PSI AT NODE MPG1
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 2
PROJECT OUTPUT
PROBLEM SOLUTION DATA 05/16/12
==============================================================================
********************************************
PBAL SOLUTION CONVERGED AFTER 4 ITERATIONS
********************************************
CONVERGENCE TOLERANCE 0.10 PSI PRESSURE IMBALANCE AT SELECTED NODES
(RMS VALUE USED FOR STEP-SIZE SELECTION)
ITERATION NUMBER 0. 0
MAX PRESSURE IMBALANCE = -1170.659 PSI AT NODE MPG2
ITERATION NUMBER 1. 0
MAX PRESSURE IMBALANCE = -1112.129 PSI AT NODE MPG2
ITERATION NUMBER 2. 0
** WARNING ** MREGULATOR OUTLET PRESSURE EXCEEDS
THE INLET PRESSURE: R002
MAX PRESSURE IMBALANCE = 111.213 PSI AT NODE MPG2
ITERATION NUMBER 3. 0
MAX PRESSURE IMBALANCE = -529.723 PSI AT NODE MPG2
ITERATION NUMBER 4. 0
MAX PRESSURE IMBALANCE = 0.000 PSI AT NODE MPG2
********************************************
PBAL SOLUTION CONVERGED AFTER 4 ITERATIONS
********************************************
CONVERGENCE TOLERANCE 0.10 PSI PRESSURE IMBALANCE AT SELECTED NODES
(RMS VALUE USED FOR STEP-SIZE SELECTION)
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 3
PROJECT OUTPUT
PROBLEM SOLUTION DATA 05/16/12
==============================================================================
ITERATION NUMBER 0. 0
MAX PRESSURE IMBALANCE = -1170.659 PSI AT NODE MPG3
ITERATION NUMBER 1. 0
MAX PRESSURE IMBALANCE = -1112.129 PSI AT NODE MPG3
ITERATION NUMBER 2. 0
** WARNING ** MREGULATOR OUTLET PRESSURE EXCEEDS
THE INLET PRESSURE: R003
MAX PRESSURE IMBALANCE = 111.213 PSI AT NODE MPG3
ITERATION NUMBER 3. 0
MAX PRESSURE IMBALANCE = -529.723 PSI AT NODE MPG3
ITERATION NUMBER 4. 0
MAX PRESSURE IMBALANCE = 0.000 PSI AT NODE MPG3
********************************************
PBAL SOLUTION CONVERGED AFTER 4 ITERATIONS
********************************************
CONVERGENCE TOLERANCE 0.10 PSI PRESSURE IMBALANCE AT SELECTED NODES
(RMS VALUE USED FOR STEP-SIZE SELECTION)
ITERATION NUMBER 0. 0
MAX PRESSURE IMBALANCE = -1170.659 PSI AT NODE MPG7
ITERATION NUMBER 1. 0
MAX PRESSURE IMBALANCE = -1112.129 PSI AT NODE MPG7
ITERATION NUMBER 2. 0
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 4
PROJECT OUTPUT
PROBLEM SOLUTION DATA 05/16/12
==============================================================================
** WARNING ** MREGULATOR OUTLET PRESSURE EXCEEDS
THE INLET PRESSURE: R004
MAX PRESSURE IMBALANCE = 111.213 PSI AT NODE MPG7
ITERATION NUMBER 3. 0
MAX PRESSURE IMBALANCE = -529.723 PSI AT NODE MPG7
ITERATION NUMBER 4. 0
MAX PRESSURE IMBALANCE = 0.000 PSI AT NODE MPG7
********************************************
PBAL SOLUTION CONVERGED AFTER 4 ITERATIONS
********************************************
CONVERGENCE TOLERANCE 0.10 PSI PRESSURE IMBALANCE AT SELECTED NODES
(RMS VALUE USED FOR STEP-SIZE SELECTION)
ITERATION NUMBER 0. 0
MAX PRESSURE IMBALANCE = -1170.659 PSI AT NODE MPGB
ITERATION NUMBER 1. 0
MAX PRESSURE IMBALANCE = -1112.129 PSI AT NODE MPGB
ITERATION NUMBER 2. 0
** WARNING ** MREGULATOR OUTLET PRESSURE EXCEEDS
THE INLET PRESSURE: R005
MAX PRESSURE IMBALANCE = 111.213 PSI AT NODE MPGB
ITERATION NUMBER 3. 0
MAX PRESSURE IMBALANCE = -529.723 PSI AT NODE MPGB
ITERATION NUMBER 4. 0
** WARNING ** MREGULATOR OUTLET PRESSURE EXCEEDS
THE INLET PRESSURE: R005
MAX PRESSURE IMBALANCE = 0.000 PSI AT NODE MPGB
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 5
PROJECT OUTPUT
PROBLEM SOLUTION DATA 05/16/12
==============================================================================
********************************************
PBAL SOLUTION CONVERGED AFTER 4 ITERATIONS
********************************************
** WARNING ** MREGULATOR OUTLET PRESSURE EXCEEDS
THE INLET PRESSURE: R005
***** PROBLEM SOLUTION REACHED *****
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 6
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
LINK SUMMARY
RATE, PRESSURE AND TEMPERATURE SUMMARY
--------------------------------------
FROM(F)
AND
TO(T) ----ACTUAL FLOW RATES***-- PRESS: ---HOLDUP**---
LINK NODE GAS OIL WATER PRESS: DROP TEMP: GAS LIQ
(MMCFD) (BPD) (BPD) (PSIG) (PSIG) (F) (MM (STB)
SCF)
---- ------- -------- -------- -------- -------- ------- ----- ------- -------
L001 P250(F) 0.0000 0.0 200510.4 1289.7 100.0
J001(T) 0.0000 0.0 200510.4 1289.7 9.53E-3 100.0 0.0000 1.1
L003 J001(F) 0.0000 0.0 97171.0 1289.7 100.0
J000(T) 0.0000 0.0 97170.9 1289.7 2.49E-2 100.0 0.0000 11.2
L004 J001(F) 0.0000 0.0 103339.4 1289.7 100.0
J002(T) 0.0000 0.0 103339.4 1289.7 2.78E-2 100.0 0.0000 11.2
L006 J021(F) 0.0000 0.0 56142.9 1288.7 100.0
D002(T) 0.0000 0.0 56142.8 1288.7 3.45E-2 100.0 0.0000 30.7
L010 J000(F) 0.0000 0.0 49684.7 1289.7 100.0
J004(T) 0.0000 0.0 49684.7 1289.5 0.2 100.0 0.0000 3.7
L018 J004(F) 0.0000 0.0 49684.7 1289.5 100.0
J005(T) 0.0000 0.0 49684.7 1289.5 6.44E-3 100.0 0.0000 7.2
L024 J006(F) 0.0000 0.0 200510.2 1289.5 100.0
J021(T) 0.0000 0.0 200510.4 1288.7 0.7 100.0 0.0000 61.4
L030 J005(F) 0.0000 0.0 97170.9 1289.5 100.0
J006(T) 0.0000 0.0 97170.9 1289.5 2.20E-2 100.0 0.0000 7.2
L032 J007(F) 0.0000 0.0 51485.5 1289.5 100.0
J006(T) 0.0000 0.0 51485.5 1289.5 1.07E-2 100.0 0.0000 6.1
L075 J021(F) 0.0000 0.0 16040.8 1288.7 100.0
MPG1(T) 0.0000 0.0 16044.5 1200.0* 88.7 99.8 0.0000 47.7
L077 J021(F) 0.0000 0.0 16040.8 1288.7 100.0
MPG2(T) 0.0000 0.0 16043.0 1200.0* 88.7 99.3 0.0000 163.9
L079 J021(F) 0.0000 0.0 16040.8 1288.7 100.0
MPG3(T) 0.0000 0.0 16043.2 1200.0* 88.7 99.4 0.0000 146.0
L080 J021(F) 0.0000 0.0 16040.8 1288.7 100.0
MPG7(T) 0.0000 0.0 16042.9 1200.0* 88.7 99.3 0.0000 169.2
L081 J021(F) 0.0000 0.0 16040.8 1288.7 100.0
MPGB(T) 0.0000 0.0 16039.5 1200.0* 88.7 98.3 0.0000 452.2
L083 J021(F) 0.0000 0.0 16040.8 1288.7 100.0
POZO(T) 0.0000 0.0 16041.1 1200.0* 88.7 98.8 0.0000 316.8
L084 J021(F) 0.0000 0.0 16040.8 1288.7 100.0
POZ1(T) 0.0000 0.0 16041.1 1200.0* 88.7 98.8 0.0000 316.8
L086 J021(F) 0.0000 0.0 16040.8 1288.7 100.0
POZ2(T) 0.0000 0.0 16041.1 1200.0* 88.7 98.8 0.0000 316.8
L088 J021(F) 0.0000 0.0 16040.8 1288.7 100.0
POZ3(T) 0.0000 0.0 16041.1 1200.0* 88.7 98.8 0.0000 316.8
* - INDICATES KNOWN PRESSURE
** VOLUME REPORTED AT USER STANDARD CONDITIONS
*** RATE REPORTED AT ACTUAL TEMPERATURE AND PRESSURE CONDITIONS
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 7
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
LINK SUMMARY
RATE, PRESSURE AND TEMPERATURE SUMMARY
--------------------------------------
FROM(F)
AND
TO(T) ----ACTUAL FLOW RATES***-- PRESS: ---HOLDUP**---
LINK NODE GAS OIL WATER PRESS: DROP TEMP: GAS LIQ
(MMCFD) (BPD) (BPD) (PSIG) (PSIG) (F) (MM (STB)
SCF)
---- ------- -------- -------- -------- -------- ------- ----- ------- -------
**********************************CONTINUED**************************
L099 J000(F) 0.0000 0.0 47486.2 1289.7 100.0
J005(T) 0.0000 0.0 47486.2 1289.5 0.2 100.0 0.0000 3.5
L100 J002(F) 0.0000 0.0 51853.8 1289.7 100.0
J006(T) 0.0000 0.0 51853.8 1289.5 0.2 100.0 0.0000 3.7
L101 J002(F) 0.0000 0.0 51485.5 1289.7 100.0
J007(T) 0.0000 0.0 51485.5 1289.5 0.2 100.0 0.0000 3.7
* - INDICATES KNOWN PRESSURE
** VOLUME REPORTED AT USER STANDARD CONDITIONS
*** RATE REPORTED AT ACTUAL TEMPERATURE AND PRESSURE CONDITIONS
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 8
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
NODE SUMMARY
---STANDARD FLOW RATES ---**
NODE PRES. GAS OIL WATER TEMP.
(PSIG) (MMCFD) (BPD) (BPD) (F)
---- ------- -------- -------- -------- -------
P250 1289.7 0.0000 0.0 200000.0* 100.0
J001 1289.7 0.0000 0.0 0.0* 100.0
J021 1288.7 0.0000 0.0 0.0* 100.0
J000 1289.7 0.0000 0.0 0.0* 100.0
J004 1289.5 0.0000 0.0 0.0* 100.0
J006 1289.5 0.0000 0.0 0.0* 100.0
J005 1289.5 0.0000 0.0 0.0* 100.0
J007 1289.5 0.0000 0.0 0.0* 100.0
J002 1289.7 0.0000 0.0 0.0* 100.0
D002 1288.7 0.0000 0.0 -56000.0* 100.0
POZO 1200.0* 0.0000 0.0 -16000.0 98.8
POZ1 1200.0* 0.0000 0.0 -16000.0 98.8
POZ2 1200.0* 0.0000 0.0 -16000.0 98.8
POZ3 1200.0* 0.0000 0.0 -16000.0 98.8
MPG1 1200.0* 0.0000 0.0 -16000.0 99.8
MPG2 1200.0* 0.0000 0.0 -16000.0 99.3
MPG3 1200.0* 0.0000 0.0 -16000.0 99.4
MPG7 1200.0* 0.0000 0.0 -16000.0 99.3
MPGB 1200.0* 0.0000 0.0 -16000.0 98.3
* INDICATES KNOWN PRESSURE OR FLOW
** STANDARD FLOW RATES REPORTED AT USER STD CONDITION
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 9
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
NODE CONTAMINANT AND GAS SUMMARY
NODE N2(%) CO2(%) H2S(%)
---- ----------- ----------- -----------
P250 0.0000 0.0000 0.0000
J001 0.0000 0.0000 0.0000
J021 0.0000 0.0000 0.0000
J000 0.0000 0.0000 0.0000
J004 0.0000 0.0000 0.0000
J006 0.0000 0.0000 0.0000
J005 0.0000 0.0000 0.0000
J007 0.0000 0.0000 0.0000
J002 0.0000 0.0000 0.0000
D002 0.0000 0.0000 0.0000
POZO 0.0000 0.0000 0.0000
POZ1 0.0000 0.0000 0.0000
POZ2 0.0000 0.0000 0.0000
POZ3 0.0000 0.0000 0.0000
MPG1 0.0000 0.0000 0.0000
MPG2 0.0000 0.0000 0.0000
MPG3 0.0000 0.0000 0.0000
MPG7 0.0000 0.0000 0.0000
MPGB 0.0000 0.0000 0.0000
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 10
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
DEVICE SUMMARY
C
O ------- OUTLET ------ AVG.
LINK DEVI DEVI R INSIDE MEAS ELEV INSITU LIQ
NAME NAME TYPE R DIAM LENGTH CHNG PRESS: TEMP: LGR HOLDUP
(IN) (FT) (FT) (PSIG) (F) (CFBBL)
---- ---- ---- ---- -------- --------- ------- ------- ------ ------- ------
L001 ***SOURCE*** RATE= 2.000E5 (BPD) 1289.7 100.0
P250 1289.7 100.0
P000 PIPE DW 18.811 3.3 0.0 1289.7 100.0
J001**JUNCTION** PRES= 1289.7 (PSIG) TEMP= 100.0 (F)
L003 **JUNCTION** RATE= 96923.6 (BPD) 1289.7 100.0
J001 1289.7 100.0
P001 PIPE DW 18.811 32.8 0.0 1289.7 100.0
J000**JUNCTION** PRES= 1289.7 (PSIG) TEMP= 100.0 (F)
L004 **JUNCTION** RATE= 1.030E5 (BPD) 1289.7 100.0
J001 1289.7 100.0
P002 PIPE DW 18.811 32.8 0.0 1289.7 100.0
J002**JUNCTION** PRES= 1289.7 (PSIG) TEMP= 100.0 (F)
L006 **JUNCTION** RATE= 56000.0 (BPD) 1288.7 100.0
J021 1288.7 100.0
P016 PIPE DW 17.937 98.4 0.0 1288.7 100.0
D002 *** SINK *** PRES= 1288.7 (PSIG) TEMP= 100.0 (F)
L010 **JUNCTION** RATE= 49558.3 (BPD) 1289.7 100.0
J000 1289.7 100.0
P004 PIPE DW 10.020 19.7 0.0 1289.6 100.0
P005 PIPE DW 9.559 19.7 0.0 1289.5 100.0
J004**JUNCTION** PRES= 1289.5 (PSIG) TEMP= 100.0 (F)
L018 **JUNCTION** RATE= 49558.3 (BPD) 1289.5 100.0
J004 1289.5 100.0
P012 PIPE DW 17.937 23.0 0.0 1289.5 100.0
J005**JUNCTION** PRES= 1289.5 (PSIG) TEMP= 100.0 (F)
L024 **JUNCTION** RATE= 2.000E5 (BPD) 1289.5 100.0
J006 1289.5 100.0
P015 PIPE DW 17.937 196.9 0.0 1288.7 100.0
J021**JUNCTION** PRES= 1288.7 (PSIG) TEMP= 100.0 (F)
L030 **JUNCTION** RATE= 96923.6 (BPD) 1289.5 100.0
J005 1289.5 100.0
P013 PIPE DW 17.937 23.0 0.0 1289.5 100.0
J006**JUNCTION** PRES= 1289.5 (PSIG) TEMP= 100.0 (F)
L032 **JUNCTION** RATE= 51354.5 (BPD) 1289.5 100.0
J007 1289.5 100.0
P014 PIPE DW 17.937 19.7 0.0 1289.5 100.0
J006**JUNCTION** PRES= 1289.5 (PSIG) TEMP= 100.0 (F)
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 11
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
DEVICE SUMMARY
C
O ------- OUTLET ------ AVG.
LINK DEVI DEVI R INSIDE MEAS ELEV INSITU LIQ
NAME NAME TYPE R DIAM LENGTH CHNG PRESS: TEMP: LGR HOLDUP
(IN) (FT) (FT) (PSIG) (F) (CFBBL)
---- ---- ---- ---- -------- --------- ------- ------- ------ ------- ------
**********************************CONTINUED**************************
L075 **JUNCTION** RATE= 16000.0 (BPD) 1288.7 100.0
J021 1288.7 100.0
P027 PIPE DW 5.764 1476.4 0.0 1275.4 99.8
R001 MREG 0.000 0.0 0.0 1200.1 99.8
P044 PIPE DW 5.764 6.6 0.0 1200.0 99.8
MPG1 *** SINK *** PRES= 1200.0 (PSIG) TEMP= 99.8 (F)
L077 **JUNCTION** RATE= 16000.0 (BPD) 1288.7 100.0
J021 1288.7 100.0
P028 PIPE DW 5.764 5085.3 0.0 1242.9 99.4
R002 MREG 0.000 0.0 0.0 1200.1 99.4
P043 PIPE DW 5.764 6.6 0.0 1200.0 99.3
MPG2 *** SINK *** PRES= 1200.0 (PSIG) TEMP= 99.3 (F)
L079 **JUNCTION** RATE= 16000.0 (BPD) 1288.7 100.0
J021 1288.7 100.0
P029 PIPE DW 5.764 4527.6 0.0 1247.9 99.4
R003 MREG 0.000 0.0 0.0 1200.1 99.4
P042 PIPE DW 5.764 6.6 0.0 1200.0 99.4
MPG3 *** SINK *** PRES= 1200.0 (PSIG) TEMP= 99.4 (F)
L080 **JUNCTION** RATE= 16000.0 (BPD) 1288.7 100.0
J021 1288.7 100.0
P030 PIPE DW 5.764 5249.3 0.0 1241.4 99.3
R004 MREG 0.000 0.0 0.0 1200.1 99.3
P041 PIPE DW 5.764 6.6 0.0 1200.0 99.3
MPG7 *** SINK *** PRES= 1200.0 (PSIG) TEMP= 99.3 (F)
L081 **JUNCTION** RATE= 16000.0 (BPD) 1288.7 100.0
J021 1288.7 100.0
P031 PIPE DW 5.764 14042.0 0.0 1162.1 98.3
R005 MREG 0.000 0.0 0.0 1200.1 98.3
P045 PIPE DW 5.764 6.6 0.0 1200.0 98.3
MPGB *** SINK *** PRES= 1200.0 (PSIG) TEMP= 98.3 (F)
L083 **JUNCTION** RATE= 16000.0 (BPD) 1288.7 100.0
J021 1288.7 100.0
P032 PIPE DW 5.764 9842.5 0.0 1200.0 98.8
POZO *** SINK *** PRES= 1200.0 (PSIG) TEMP= 98.8 (F)
L084 **JUNCTION** RATE= 16000.0 (BPD) 1288.7 100.0
J021 1288.7 100.0
P033 PIPE DW 5.764 9842.5 0.0 1200.0 98.8
POZ1 *** SINK *** PRES= 1200.0 (PSIG) TEMP= 98.8 (F)
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 12
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
DEVICE SUMMARY
C
O ------- OUTLET ------ AVG.
LINK DEVI DEVI R INSIDE MEAS ELEV INSITU LIQ
NAME NAME TYPE R DIAM LENGTH CHNG PRESS: TEMP: LGR HOLDUP
(IN) (FT) (FT) (PSIG) (F) (CFBBL)
---- ---- ---- ---- -------- --------- ------- ------- ------ ------- ------
**********************************CONTINUED**************************
L086 **JUNCTION** RATE= 16000.0 (BPD) 1288.7 100.0
J021 1288.7 100.0
P034 PIPE DW 5.764 9842.5 0.0 1200.0 98.8
POZ2 *** SINK *** PRES= 1200.0 (PSIG) TEMP= 98.8 (F)
L088 **JUNCTION** RATE= 16000.0 (BPD) 1288.7 100.0
J021 1288.7 100.0
P035 PIPE DW 5.764 9842.5 0.0 1200.0 98.8
POZ3 *** SINK *** PRES= 1200.0 (PSIG) TEMP= 98.8 (F)
L099 **JUNCTION** RATE= 47365.4 (BPD) 1289.7 100.0
J000 1289.7 100.0
P006 PIPE DW 10.020 19.7 0.0 1289.6 100.0
P007 PIPE DW 9.059 19.7 0.0 1289.5 100.0
J005**JUNCTION** PRES= 1289.5 (PSIG) TEMP= 100.0 (F)
L100 **JUNCTION** RATE= 51721.9 (BPD) 1289.7 100.0
J002 1289.7 100.0
P008 PIPE DW 10.020 19.7 0.0 1289.6 100.0
P009 PIPE DW 9.559 19.7 0.0 1289.5 100.0
J006**JUNCTION** PRES= 1289.5 (PSIG) TEMP= 100.0 (F)
L101 **JUNCTION** RATE= 51354.5 (BPD) 1289.7 100.0
J002 1289.7 100.0
P010 PIPE DW 10.020 19.7 0.0 1289.6 100.0
P011 PIPE DW 9.559 19.7 0.0 1289.5 100.0
J007**JUNCTION** PRES= 1289.5 (PSIG) TEMP= 100.0 (F)
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 13
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
STRUCTURE DATA SUMMARY
DEVICE DEVICE INLET DIA OUTLET DIA ELEVATION KMUL OR
LINK NAME TYPE (NOM/ID) (NOM/ID) LENGTH CHANGE K FACTOR
(IN) (IN) (FT) (FT)
---- ------ ------ --------------- --------------- --------- --------- --------
L001 P000 PIPE 20.000 18.811 20.000 18.811 3.3 0.0
L003 P001 PIPE 20.000 18.811 20.000 18.811 32.8 0.0
L004 P002 PIPE 20.000 18.811 20.000 18.811 32.8 0.0
L006 P016 PIPE 20.000 17.937 20.000 17.937 98.4 0.0
L010 P004 PIPE 10.000 10.020 10.000 10.020 19.7 0.0
L010 P005 PIPE 10.000 9.559 10.000 9.559 19.7 0.0
L018 P012 PIPE 20.000 17.937 20.000 17.937 23.0 0.0
L024 P015 PIPE 20.000 17.937 20.000 17.937 196.9 0.0
L030 P013 PIPE 20.000 17.937 20.000 17.937 23.0 0.0
L032 P014 PIPE 20.000 17.937 20.000 17.937 19.7 0.0
L075 P027 PIPE 6.000 5.764 6.000 5.764 1476.4 0.0
L075 R001 MREG 0.0 0.0
L075 P044 PIPE 6.000 5.764 6.000 5.764 6.6 0.0
L077 P028 PIPE 6.000 5.764 6.000 5.764 5085.3 0.0
L077 R002 MREG 0.0 0.0
L077 P043 PIPE 6.000 5.764 6.000 5.764 6.6 0.0
L079 P029 PIPE 6.000 5.764 6.000 5.764 4527.6 0.0
L079 R003 MREG 0.0 0.0
L079 P042 PIPE 6.000 5.764 6.000 5.764 6.6 0.0
L080 P030 PIPE 6.000 5.764 6.000 5.764 5249.3 0.0
L080 R004 MREG 0.0 0.0
L080 P041 PIPE 6.000 5.764 6.000 5.764 6.6 0.0
L081 P031 PIPE 6.000 5.764 6.000 5.764 14042.0 0.0
L081 R005 MREG 0.0 0.0
L081 P045 PIPE 6.000 5.764 6.000 5.764 6.6 0.0
L083 P032 PIPE 6.000 5.764 6.000 5.764 9842.5 0.0
L084 P033 PIPE 6.000 5.764 6.000 5.764 9842.5 0.0
L086 P034 PIPE 6.000 5.764 6.000 5.764 9842.5 0.0
L088 P035 PIPE 6.000 5.764 6.000 5.764 9842.5 0.0
L099 P006 PIPE 10.000 10.020 10.000 10.020 19.7 0.0
L099 P007 PIPE 10.000 9.059 10.000 9.059 19.7 0.0
L100 P008 PIPE 10.000 10.020 10.000 10.020 19.7 0.0
L100 P009 PIPE 10.000 9.559 10.000 9.559 19.7 0.0
L101 P010 PIPE 10.000 10.020 10.000 10.020 19.7 0.0
L101 P011 PIPE 10.000 9.559 10.000 9.559 19.7 0.0
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 14
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
VELOCITY SUMMARY
PRESSURE
DEVICE DEVICE MIXTURE VELOCITY CRITICAL GRADIENT PRESSURE
LINK NAME TYPE (INLET/OUTLET) VELOCITY (INLET/OUTLET) DROP
(FPS) (FPS) (PSIFT) (PSIG)
---- ------ ------ ---------------- -------- -------------- --------
L001 P000 PIPE 6.75 6.75 0.00 -2.9E-3 -2.9E-3 -9.531E-3
L003 P001 PIPE 3.27 3.27 0.00 -7.6E-4 -7.6E-4 -2.487E-2
L004 P002 PIPE 3.48 3.48 0.00 -8.5E-4 -8.5E-4 -2.785E-2
L006 P016 PIPE 2.08 2.08 0.00 -3.5E-4 -3.5E-4 -3.446E-2
L010 P004 PIPE 5.90 5.90 0.00 -4.8E-3 -4.8E-3 -9.481E-2
L010 P005 PIPE 6.48 6.48 0.00 -6.1E-3 -6.1E-3 -0.1
L018 P012 PIPE 1.84 1.84 0.00 -2.8E-4 -2.8E-4 -6.439E-3
L024 P015 PIPE 7.43 7.43 0.00 -3.7E-3 -3.7E-3 -0.7
L030 P013 PIPE 3.60 3.60 0.00 -9.6E-4 -9.6E-4 -2.196E-2
L032 P014 PIPE 1.91 1.91 0.00 -3.0E-4 -3.0E-4 -5.888E-3
L075 P027 PIPE 5.75 5.75 0.00 -9.0E-3 -9.0E-3 -13.3
L075 R001 MREG -75.4
L075 P044 PIPE 5.75 5.75 0.00 -9.0E-3 -9.0E-3 -5.917E-2
L077 P028 PIPE 5.75 5.75 0.00 -9.0E-3 -9.0E-3 -45.8
L077 R002 MREG -42.8
L077 P043 PIPE 5.75 5.75 0.00 -9.0E-3 -9.0E-3 -5.917E-2
L079 P029 PIPE 5.75 5.75 0.00 -9.0E-3 -9.0E-3 -40.8
L079 R003 MREG -47.9
L079 P042 PIPE 5.75 5.75 0.00 -9.0E-3 -9.0E-3 -5.917E-2
L080 P030 PIPE 5.75 5.75 0.00 -9.0E-3 -9.0E-3 -47.3
L080 R004 MREG -41.3
L080 P041 PIPE 5.75 5.75 0.00 -9.0E-3 -9.0E-3 -5.917E-2
L081 P031 PIPE 5.75 5.75 0.00 -9.0E-3 -9.0E-3 -126.6
L081 R005 MREG 37.9
L081 P045 PIPE 5.75 5.75 0.00 -9.0E-3 -9.0E-3 -5.918E-2
L083 P032 PIPE 5.75 5.75 0.00 -9.0E-3 -9.0E-3 -88.7
L084 P033 PIPE 5.75 5.75 0.00 -9.0E-3 -9.0E-3 -88.7
L086 P034 PIPE 5.75 5.75 0.00 -9.0E-3 -9.0E-3 -88.7
L088 P035 PIPE 5.75 5.75 0.00 -9.0E-3 -9.0E-3 -88.7
L099 P006 PIPE 5.64 5.64 0.00 -4.4E-3 -4.4E-3 -8.716E-2
L099 P007 PIPE 6.89 6.89 0.00 -7.3E-3 -7.3E-3 -0.1
L100 P008 PIPE 6.15 6.15 0.00 -5.2E-3 -5.2E-3 -0.1
L100 P009 PIPE 6.76 6.76 0.00 -6.6E-3 -6.6E-3 -0.1
L101 P010 PIPE 6.11 6.11 0.00 -5.1E-3 -5.1E-3 -0.1
L101 P011 PIPE 6.71 6.71 0.00 -6.5E-3 -6.5E-3 -0.1
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 15
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
RESULTS SUMMARY
DEVICE DEVICE MIXTURE PRESSURE TEMPERATURE QUALITY
LINK NAME TYPE FLOW RATE INLET/OUTLET INLET/OUTLET INLET/OUTLET
(BPD) (PSIG) (F) (FRAC)
---- ------ ------ --------- ----------------- ----------------- ------------
L001 P000 PIPE 200510.22 1289.7 1289.7 100.00 100.00 0.000 0.000
L003 P001 PIPE 97170.91 1289.7 1289.7 100.00 100.00 0.000 0.000
L004 P002 PIPE 103339.31 1289.7 1289.7 100.00 100.00 0.000 0.000
L006 P016 PIPE 56142.86 1288.7 1288.7 99.99 99.98 0.000 0.000
L010 P004 PIPE 49684.67 1289.7 1289.6 100.00 100.00 0.000 0.000
L010 P005 PIPE 49684.67 1289.6 1289.5 100.00 99.99 0.000 0.000
L018 P012 PIPE 49684.67 1289.5 1289.5 99.99 99.99 0.000 0.000
L024 P015 PIPE 200510.12 1289.5 1288.7 99.99 99.99 0.000 0.000
L030 P013 PIPE 97170.85 1289.5 1289.5 99.99 99.99 0.000 0.000
L032 P014 PIPE 51485.48 1289.5 1289.5 100.00 99.99 0.000 0.000
L075 P027 PIPE 16040.82 1288.7 1275.4 99.99 99.80 0.000 0.000
L075 R001 MREG 0.00 1275.4 1200.1 99.80 99.80 0.000
L075 P044 PIPE 16044.45 1200.1 1200.0 99.80 99.80 0.000 0.000
L077 P028 PIPE 16040.83 1288.7 1242.9 99.99 99.35 0.000 0.000
L077 R002 MREG 0.00 1242.9 1200.1 99.35 99.35 0.000
L077 P043 PIPE 16042.96 1200.1 1200.0 99.35 99.35 0.000 0.000
L079 P029 PIPE 16040.83 1288.7 1247.9 99.99 99.42 0.000 0.000
L079 R003 MREG 0.00 1247.9 1200.1 99.42 99.42 0.000
L079 P042 PIPE 16043.19 1200.1 1200.0 99.42 99.42 0.000 0.000
L080 P030 PIPE 16040.83 1288.7 1241.4 99.99 99.33 0.000 0.000
L080 R004 MREG 0.00 1241.4 1200.1 99.33 99.33 0.000
L080 P041 PIPE 16042.90 1200.1 1200.0 99.33 99.33 0.000 0.000
L081 P031 PIPE 16040.83 1288.7 1162.1 99.99 98.28 0.000 0.000
L081 R005 MREG 0.00 1162.1 1200.1 98.28 98.28 0.000
L081 P045 PIPE 16039.44 1200.1 1200.0 98.28 98.28 0.000 0.000
L083 P032 PIPE 16040.83 1288.7 1200.0 99.99 98.77 0.000 0.000
L084 P033 PIPE 16040.83 1288.7 1200.0 99.99 98.77 0.000 0.000
L086 P034 PIPE 16040.83 1288.7 1200.0 99.99 98.77 0.000 0.000
L088 P035 PIPE 16040.83 1288.7 1200.0 99.99 98.77 0.000 0.000
L099 P006 PIPE 47486.20 1289.7 1289.6 100.00 100.00 0.000 0.000
L099 P007 PIPE 47486.20 1289.6 1289.5 100.00 99.99 0.000 0.000
L100 P008 PIPE 51853.80 1289.7 1289.6 100.00 100.00 0.000 0.000
L100 P009 PIPE 51853.80 1289.6 1289.5 100.00 100.00 0.000 0.000
L101 P010 PIPE 51485.48 1289.7 1289.6 100.00 100.00 0.000 0.000
L101 P011 PIPE 51485.48 1289.6 1289.5 100.00 100.00 0.000 0.000
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 16
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
LINK "L001" DEVICE DETAIL REPORT
PRESSURE AND TEMPERATURE REPORT
-------------------------------
DEVICE MWD OR TVD
NAME LENGTH I OR
AND SEGM INSIDE FROM & ELEV CALC CALC OVERALL AMB
TYPE NO DIAM. INLET O CHNG PRESS TEMP U-FACT TEMP
(IN) (FT) (FT) (PSIG) (F) (BTU/ (F)
HRFT2F)
------ ---- ------ --------- - -------- ------- ------ ------- ------
P000 0000 18.811 0.0 I 0.0 1289.7 100.0 80.0
(PIPE) 0001 0.8 0.0 1289.7 100.0 1.000 80.0
0002 1.6 0.0 1289.7 100.0 1.000 80.0
0003 2.5 0.0 1289.7 100.0 1.000 80.0
0004 3.3 O 0.0 1289.7 100.0 1.000 80.0
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 17
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
SURFACE PRESSURE PLOT FOR LINK
1295. +-----+-----+-----+-----+-----+-----+-----+-----+-----+-----+
| | | | | |
| | | | | |
| | | | | |
1294. + | | | | +
| | | | | |
| | | | | |
| | | | | |
1293. +-----------+-----------+-----------+-----------+-----------+
| | | | | |
| | | | | |
| | | | | |
P 1292. + | | | | +
R | | | | | |
E | | | | | |
S | | | | | |
S 1291. +-----------+-----------+-----------+-----------+-----------+
U | | | | | |
R | | | | | |
E | | | | | |
1290. + | | | | +
PPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPP |
| | | | | |
| | | | | |
P 1289. +-----------+-----------+-----------+-----------+-----------+
S | | | | | |
I | | | | | |
G | | | | | |
1288. + | | | | +
| | | | | |
| | | | | |
| | | | | |
1287. +-----------+-----------+-----------+-----------+-----------+
| | | | | |
| | | | | |
| | | | | |
1286. + | | | | +
| | | | | |
| | | | | |
| | | | | |
1285. +-----+-----+-----+-----+-----+-----+-----+-----+-----+-----+
0.0 0.8 1.6 2.4 3.2 4.0
DIST. FROM 1ST SURFACE DEVICE INLET FT
KEY... P - P - FLUID PRESS.
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 18
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
SURFACE TEMPERATURE PLOT FOR LINK
100.0 TTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTT----+-----+
| | | | | |
| | | | | |
| | | | | |
98.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
96.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
T | | | | | |
E | | | | | |
M 94.0 + | | | | +
P | | | | | |
E | | | | | |
R | | | | | |
A 92.0 +-----------+-----------+-----------+-----------+-----------+
T | | | | | |
U | | | | | |
R | | | | | |
E 90.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
88.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
D | | | | | |
E | | | | | |
G 86.0 + | | | | +
| | | | | |
F | | | | | |
| | | | | |
84.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
| | | | | |
| | | | | |
82.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
80.0 AAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAA----+-----+
0.0 0.8 1.6 2.4 3.2 4.0
DIST. FROM 1ST SURFACE DEVICE INLET FT
KEY... T - T - FLUID TEMP. A - A - AMB. TEMP.
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 19
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
***************************CONTINUED****************************
LINK "L001" DEVICE DETAIL REPORT
HOLDUP AND VELOCITY DETAIL REPORT
---------------------------------
DEVICE
NAME ---LIQUID HOLDUP--- SUPERFICIAL T-D
AND SEG. NO LIQ GAS MIX . FLOW FLOW SONIC
TYPE NO. SLIP SLIP TOTAL VEL VEL VEL REGM REGM VEL
(ABBL) (FPS) (FPS) (FPS) (FPS)
------ ---- ----- ----- -------- ------- ------- ------- ---- ---- -------
P000 0000
(PIPE) 0001 1.00 1.00 0.3 6.75 0.00 6.75 ---- 1-PH 0.00
0002 1.00 1.00 0.6 6.75 0.00 6.75 ---- 1-PH 0.00
0003 1.00 1.00 0.8 6.75 0.00 6.75 ---- 1-PH 0.00
0004 1.00 1.00 1.1 6.75 0.00 6.75 ---- 1-PH 0.00
PRESSURE GRADIENT DETAIL REPORT
-------------------------------
DEVICE
NAME
AND SEGM. --PRESSURE GRADIENT---- --PRESSURE CHANGE--
TYPE NO: FRIC ELEV TOTAL FRIC ELEV
(PSIFT) (PSIFT) (PSIFT) (PSIG) (PSIG)
------ ---- -------- -------- -------- -------- --------
P000 0000
(PIPE) 0001 -0.0029 0.0000 -0.0029 -2.38E-3 0.0
0002 -0.0029 0.0000 -0.0029 -2.38E-3 0.0
0003 -0.0029 0.0000 -0.0029 -2.38E-3 0.0
0004 -0.0029 0.0000 -0.0029 -2.38E-3 0.0
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 20
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
LINK "L001" PROPERTY DETAIL REPORT
VISCOSITY AND DENSITY RESULTS
-----------------------------
DEVICE
NAME
AND SEGM ----------VISCOSITY---------- ------------DENSITY------------
TYPE NO OIL LIQ VAP LIQ VAP SLIP NO-SLIP
(CP) (CP) (CP) (LB/CF) (LB/CF) (LB/CF) (LB/CF)
------ ---- --------- --------- --------- ------- ------- ------- -------
P000 0000
(PIPE) 0001 0.000 2.320 0.000 63.216 0.000 63.216 63.216
0002 0.000 2.320 0.000 63.216 0.000 63.216 63.216
0003 0.000 2.320 0.000 63.216 0.000 63.216 63.216
0004 0.000 2.320 0.000 63.216 0.000 63.216 63.216
FRICTION AND SURFACE TENSION RESULTS
------------------------------------
DEVICE
NAME LIQ
AND SEGM --------------FRICTION------------ FRIC. REYNOLDS SURFACE
TYPE NUM. DENSITY VELO ID. VISCOSITY FACTOR NUMBER TENSION
(LB/CF) (FPS) (IN) (CP) (DN/CM)
------ ---- ------- ------- -------- --------- -------- -------- --------
P000 0000
(PIPE) 0001 63.216 6.75 18.811 2.320 0.0147 4.2910E5 0.00
0002 63.216 6.75 18.811 2.320 0.0147 4.2910E5 0.00
0003 63.216 6.75 18.811 2.320 0.0147 4.2910E5 0.00
0004 63.216 6.75 18.811 2.320 0.0147 4.2910E5 0.00
HEAT TRANSFER CALCULATIONS
--------------------------
DEVICE FLUID
NAME THERMAL ----------THERMAL RESISTANCE-------
AND SEGM CONDUCT- INSIDE INSULAT- SURROUN-
(TYPE) NO: IVITY FILM PIPE ION DING
(BTUFTF) (HR-FT2- (HR-FT2- (HR-FT2- (HR-FT2-
F/BTU) F/BTU) F/BTU) F/BTU)
------ ---- -------- -------- -------- -------- --------
P000 0000
(PIPE) 0001 0.000 0.000 0.000 0.000 0.000
0002 0.000 0.000 0.000 0.000 0.000
0003 0.000 0.000 0.000 0.000 0.000
0004 0.000 0.000 0.000 0.000 0.000
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 21
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
LINK "L003" DEVICE DETAIL REPORT
PRESSURE AND TEMPERATURE REPORT
-------------------------------
DEVICE MWD OR TVD
NAME LENGTH I OR
AND SEGM INSIDE FROM & ELEV CALC CALC OVERALL AMB
TYPE NO DIAM. INLET O CHNG PRESS TEMP U-FACT TEMP
(IN) (FT) (FT) (PSIG) (F) (BTU/ (F)
HRFT2F)
------ ---- ------ --------- - -------- ------- ------ ------- ------
P001 0000 18.811 0.0 I 0.0 1289.7 100.0 80.0
(PIPE) 0001 8.2 0.0 1289.7 100.0 1.000 80.0
0002 16.4 0.0 1289.7 100.0 1.000 80.0
0003 24.6 0.0 1289.7 100.0 1.000 80.0
0004 32.8 O 0.0 1289.7 100.0 1.000 80.0
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 22
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
SURFACE PRESSURE PLOT FOR LINK
1295. +-----+-----+-----+-----+-----+-----+-----+-----+-----+-----+
| | | | | |
| | | | | |
| | | | | |
1294. + | | | | +
| | | | | |
| | | | | |
| | | | | |
1293. +-----------+-----------+-----------+-----------+-----------+
| | | | | |
| | | | | |
| | | | | |
P 1292. + | | | | +
R | | | | | |
E | | | | | |
S | | | | | |
S 1291. +-----------+-----------+-----------+-----------+-----------+
U | | | | | |
R | | | | | |
E | | | | | |
1290. + | | | | +
PPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPP |
| | | | | |
| | | | | |
P 1289. +-----------+-----------+-----------+-----------+-----------+
S | | | | | |
I | | | | | |
G | | | | | |
1288. + | | | | +
| | | | | |
| | | | | |
| | | | | |
1287. +-----------+-----------+-----------+-----------+-----------+
| | | | | |
| | | | | |
| | | | | |
1286. + | | | | +
| | | | | |
| | | | | |
| | | | | |
1285. +-----+-----+-----+-----+-----+-----+-----+-----+-----+-----+
0.0 8.0 16.0 24.0 32.0 40.0
DIST. FROM 1ST SURFACE DEVICE INLET FT
KEY... P - P - FLUID PRESS.
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 23
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
SURFACE TEMPERATURE PLOT FOR LINK
100.0 TTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTT----+-----+
| | | | | |
| | | | | |
| | | | | |
98.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
96.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
T | | | | | |
E | | | | | |
M 94.0 + | | | | +
P | | | | | |
E | | | | | |
R | | | | | |
A 92.0 +-----------+-----------+-----------+-----------+-----------+
T | | | | | |
U | | | | | |
R | | | | | |
E 90.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
88.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
D | | | | | |
E | | | | | |
G 86.0 + | | | | +
| | | | | |
F | | | | | |
| | | | | |
84.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
| | | | | |
| | | | | |
82.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
80.0 AAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAA----+-----+
0.0 8.0 16.0 24.0 32.0 40.0
DIST. FROM 1ST SURFACE DEVICE INLET FT
KEY... T - T - FLUID TEMP. A - A - AMB. TEMP.
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 24
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
***************************CONTINUED****************************
LINK "L003" DEVICE DETAIL REPORT
HOLDUP AND VELOCITY DETAIL REPORT
---------------------------------
DEVICE
NAME ---LIQUID HOLDUP--- SUPERFICIAL T-D
AND SEG. NO LIQ GAS MIX . FLOW FLOW SONIC
TYPE NO. SLIP SLIP TOTAL VEL VEL VEL REGM REGM VEL
(ABBL) (FPS) (FPS) (FPS) (FPS)
------ ---- ----- ----- -------- ------- ------- ------- ---- ---- -------
P001 0000
(PIPE) 0001 1.00 1.00 2.8 3.27 0.00 3.27 ---- 1-PH 0.00
0002 1.00 1.00 5.6 3.27 0.00 3.27 ---- 1-PH 0.00
0003 1.00 1.00 8.5 3.27 0.00 3.27 ---- 1-PH 0.00
0004 1.00 1.00 11.3 3.27 0.00 3.27 ---- 1-PH 0.00
PRESSURE GRADIENT DETAIL REPORT
-------------------------------
DEVICE
NAME
AND SEGM. --PRESSURE GRADIENT---- --PRESSURE CHANGE--
TYPE NO: FRIC ELEV TOTAL FRIC ELEV
(PSIFT) (PSIFT) (PSIFT) (PSIG) (PSIG)
------ ---- -------- -------- -------- -------- --------
P001 0000
(PIPE) 0001 -0.0008 0.0000 -0.0008 -6.22E-3 0.0
0002 -0.0008 0.0000 -0.0008 -6.22E-3 0.0
0003 -0.0008 0.0000 -0.0008 -6.22E-3 0.0
0004 -0.0008 0.0000 -0.0008 -6.22E-3 0.0
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 25
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
LINK "L003" PROPERTY DETAIL REPORT
VISCOSITY AND DENSITY RESULTS
-----------------------------
DEVICE
NAME
AND SEGM ----------VISCOSITY---------- ------------DENSITY------------
TYPE NO OIL LIQ VAP LIQ VAP SLIP NO-SLIP
(CP) (CP) (CP) (LB/CF) (LB/CF) (LB/CF) (LB/CF)
------ ---- --------- --------- --------- ------- ------- ------- -------
P001 0000
(PIPE) 0001 0.000 2.320 0.000 63.216 0.000 63.216 63.216
0002 0.000 2.320 0.000 63.216 0.000 63.216 63.216
0003 0.000 2.320 0.000 63.217 0.000 63.217 63.217
0004 0.000 2.320 0.000 63.217 0.000 63.217 63.217
FRICTION AND SURFACE TENSION RESULTS
------------------------------------
DEVICE
NAME LIQ
AND SEGM --------------FRICTION------------ FRIC. REYNOLDS SURFACE
TYPE NUM. DENSITY VELO ID. VISCOSITY FACTOR NUMBER TENSION
(LB/CF) (FPS) (IN) (CP) (DN/CM)
------ ---- ------- ------- -------- --------- -------- -------- --------
P001 0000
(PIPE) 0001 63.216 3.27 18.811 2.320 0.0163 2.0795E5 0.00
0002 63.216 3.27 18.811 2.320 0.0163 2.0795E5 0.00
0003 63.217 3.27 18.811 2.320 0.0163 2.0795E5 0.00
0004 63.217 3.27 18.811 2.320 0.0163 2.0795E5 0.00
HEAT TRANSFER CALCULATIONS
--------------------------
DEVICE FLUID
NAME THERMAL ----------THERMAL RESISTANCE-------
AND SEGM CONDUCT- INSIDE INSULAT- SURROUN-
(TYPE) NO: IVITY FILM PIPE ION DING
(BTUFTF) (HR-FT2- (HR-FT2- (HR-FT2- (HR-FT2-
F/BTU) F/BTU) F/BTU) F/BTU)
------ ---- -------- -------- -------- -------- --------
P001 0000
(PIPE) 0001 0.000 0.000 0.000 0.000 0.000
0002 0.000 0.000 0.000 0.000 0.000
0003 0.000 0.000 0.000 0.000 0.000
0004 0.000 0.000 0.000 0.000 0.000
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 26
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
LINK "L004" DEVICE DETAIL REPORT
PRESSURE AND TEMPERATURE REPORT
-------------------------------
DEVICE MWD OR TVD
NAME LENGTH I OR
AND SEGM INSIDE FROM & ELEV CALC CALC OVERALL AMB
TYPE NO DIAM. INLET O CHNG PRESS TEMP U-FACT TEMP
(IN) (FT) (FT) (PSIG) (F) (BTU/ (F)
HRFT2F)
------ ---- ------ --------- - -------- ------- ------ ------- ------
P002 0000 18.811 0.0 I 0.0 1289.7 100.0 80.0
(PIPE) 0001 8.2 0.0 1289.7 100.0 1.000 80.0
0002 16.4 0.0 1289.7 100.0 1.000 80.0
0003 24.6 0.0 1289.7 100.0 1.000 80.0
0004 32.8 O 0.0 1289.7 100.0 1.000 80.0
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 27
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
SURFACE PRESSURE PLOT FOR LINK
1295. +-----+-----+-----+-----+-----+-----+-----+-----+-----+-----+
| | | | | |
| | | | | |
| | | | | |
1294. + | | | | +
| | | | | |
| | | | | |
| | | | | |
1293. +-----------+-----------+-----------+-----------+-----------+
| | | | | |
| | | | | |
| | | | | |
P 1292. + | | | | +
R | | | | | |
E | | | | | |
S | | | | | |
S 1291. +-----------+-----------+-----------+-----------+-----------+
U | | | | | |
R | | | | | |
E | | | | | |
1290. + | | | | +
PPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPP |
| | | | | |
| | | | | |
P 1289. +-----------+-----------+-----------+-----------+-----------+
S | | | | | |
I | | | | | |
G | | | | | |
1288. + | | | | +
| | | | | |
| | | | | |
| | | | | |
1287. +-----------+-----------+-----------+-----------+-----------+
| | | | | |
| | | | | |
| | | | | |
1286. + | | | | +
| | | | | |
| | | | | |
| | | | | |
1285. +-----+-----+-----+-----+-----+-----+-----+-----+-----+-----+
0.0 8.0 16.0 24.0 32.0 40.0
DIST. FROM 1ST SURFACE DEVICE INLET FT
KEY... P - P - FLUID PRESS.
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 28
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
SURFACE TEMPERATURE PLOT FOR LINK
100.0 TTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTT----+-----+
| | | | | |
| | | | | |
| | | | | |
98.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
96.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
T | | | | | |
E | | | | | |
M 94.0 + | | | | +
P | | | | | |
E | | | | | |
R | | | | | |
A 92.0 +-----------+-----------+-----------+-----------+-----------+
T | | | | | |
U | | | | | |
R | | | | | |
E 90.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
88.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
D | | | | | |
E | | | | | |
G 86.0 + | | | | +
| | | | | |
F | | | | | |
| | | | | |
84.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
| | | | | |
| | | | | |
82.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
80.0 AAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAA----+-----+
0.0 8.0 16.0 24.0 32.0 40.0
DIST. FROM 1ST SURFACE DEVICE INLET FT
KEY... T - T - FLUID TEMP. A - A - AMB. TEMP.
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 29
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
***************************CONTINUED****************************
LINK "L004" DEVICE DETAIL REPORT
HOLDUP AND VELOCITY DETAIL REPORT
---------------------------------
DEVICE
NAME ---LIQUID HOLDUP--- SUPERFICIAL T-D
AND SEG. NO LIQ GAS MIX . FLOW FLOW SONIC
TYPE NO. SLIP SLIP TOTAL VEL VEL VEL REGM REGM VEL
(ABBL) (FPS) (FPS) (FPS) (FPS)
------ ---- ----- ----- -------- ------- ------- ------- ---- ---- -------
P002 0000
(PIPE) 0001 1.00 1.00 2.8 3.48 0.00 3.48 ---- 1-PH 0.00
0002 1.00 1.00 5.6 3.48 0.00 3.48 ---- 1-PH 0.00
0003 1.00 1.00 8.5 3.48 0.00 3.48 ---- 1-PH 0.00
0004 1.00 1.00 11.3 3.48 0.00 3.48 ---- 1-PH 0.00
PRESSURE GRADIENT DETAIL REPORT
-------------------------------
DEVICE
NAME
AND SEGM. --PRESSURE GRADIENT---- --PRESSURE CHANGE--
TYPE NO: FRIC ELEV TOTAL FRIC ELEV
(PSIFT) (PSIFT) (PSIFT) (PSIG) (PSIG)
------ ---- -------- -------- -------- -------- --------
P002 0000
(PIPE) 0001 -0.0008 0.0000 -0.0008 -6.96E-3 0.0
0002 -0.0008 0.0000 -0.0008 -6.96E-3 0.0
0003 -0.0008 0.0000 -0.0008 -6.96E-3 0.0
0004 -0.0008 0.0000 -0.0008 -6.96E-3 0.0
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 30
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
LINK "L004" PROPERTY DETAIL REPORT
VISCOSITY AND DENSITY RESULTS
-----------------------------
DEVICE
NAME
AND SEGM ----------VISCOSITY---------- ------------DENSITY------------
TYPE NO OIL LIQ VAP LIQ VAP SLIP NO-SLIP
(CP) (CP) (CP) (LB/CF) (LB/CF) (LB/CF) (LB/CF)
------ ---- --------- --------- --------- ------- ------- ------- -------
P002 0000
(PIPE) 0001 0.000 2.320 0.000 63.216 0.000 63.216 63.216
0002 0.000 2.320 0.000 63.216 0.000 63.216 63.216
0003 0.000 2.320 0.000 63.217 0.000 63.217 63.217
0004 0.000 2.320 0.000 63.217 0.000 63.217 63.217
FRICTION AND SURFACE TENSION RESULTS
------------------------------------
DEVICE
NAME LIQ
AND SEGM --------------FRICTION------------ FRIC. REYNOLDS SURFACE
TYPE NUM. DENSITY VELO ID. VISCOSITY FACTOR NUMBER TENSION
(LB/CF) (FPS) (IN) (CP) (DN/CM)
------ ---- ------- ------- -------- --------- -------- -------- --------
P002 0000
(PIPE) 0001 63.216 3.48 18.811 2.320 0.0161 2.2115E5 0.00
0002 63.216 3.48 18.811 2.320 0.0161 2.2115E5 0.00
0003 63.217 3.48 18.811 2.320 0.0161 2.2115E5 0.00
0004 63.217 3.48 18.811 2.320 0.0161 2.2115E5 0.00
HEAT TRANSFER CALCULATIONS
--------------------------
DEVICE FLUID
NAME THERMAL ----------THERMAL RESISTANCE-------
AND SEGM CONDUCT- INSIDE INSULAT- SURROUN-
(TYPE) NO: IVITY FILM PIPE ION DING
(BTUFTF) (HR-FT2- (HR-FT2- (HR-FT2- (HR-FT2-
F/BTU) F/BTU) F/BTU) F/BTU)
------ ---- -------- -------- -------- -------- --------
P002 0000
(PIPE) 0001 0.000 0.000 0.000 0.000 0.000
0002 0.000 0.000 0.000 0.000 0.000
0003 0.000 0.000 0.000 0.000 0.000
0004 0.000 0.000 0.000 0.000 0.000
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 31
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
LINK "L006" DEVICE DETAIL REPORT
PRESSURE AND TEMPERATURE REPORT
-------------------------------
DEVICE MWD OR TVD
NAME LENGTH I OR
AND SEGM INSIDE FROM & ELEV CALC CALC OVERALL AMB
TYPE NO DIAM. INLET O CHNG PRESS TEMP U-FACT TEMP
(IN) (FT) (FT) (PSIG) (F) (BTU/ (F)
HRFT2F)
------ ---- ------ --------- - -------- ------- ------ ------- ------
P016 0000 17.937 0.0 I 0.0 1288.7 100.0 80.0
(PIPE) 0001 24.6 0.0 1288.7 100.0 1.000 80.0
0002 49.2 0.0 1288.7 100.0 1.000 80.0
0003 73.8 0.0 1288.7 100.0 1.000 80.0
0004 98.4 O 0.0 1288.7 100.0 1.000 80.0
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 32
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
SURFACE PRESSURE PLOT FOR LINK
1294. +-----+-----+-----+-----+-----+-----+-----+-----+-----+-----+
| | | | | |
| | | | | |
| | | | | |
1293. + | | | | +
| | | | | |
| | | | | |
| | | | | |
1292. +-----------+-----------+-----------+-----------+-----------+
| | | | | |
| | | | | |
| | | | | |
P 1291. + | | | | +
R | | | | | |
E | | | | | |
S | | | | | |
S 1290. +-----------+-----------+-----------+-----------+-----------+
U | | | | | |
R | | | | | |
E | | | | | |
1289. + | | | | +
PPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPP|
| | | | | |
| | | | | |
P 1288. +-----------+-----------+-----------+-----------+-----------+
S | | | | | |
I | | | | | |
G | | | | | |
1287. + | | | | +
| | | | | |
| | | | | |
| | | | | |
1286. +-----------+-----------+-----------+-----------+-----------+
| | | | | |
| | | | | |
| | | | | |
1285. + | | | | +
| | | | | |
| | | | | |
| | | | | |
1284. +-----+-----+-----+-----+-----+-----+-----+-----+-----+-----+
0.0 20.0 40.0 60.0 80.0 100.0
DIST. FROM 1ST SURFACE DEVICE INLET FT
KEY... P - P - FLUID PRESS.
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 33
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
SURFACE TEMPERATURE PLOT FOR LINK
100.0 TTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTT+
| | | | | |
| | | | | |
| | | | | |
98.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
96.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
T | | | | | |
E | | | | | |
M 94.0 + | | | | +
P | | | | | |
E | | | | | |
R | | | | | |
A 92.0 +-----------+-----------+-----------+-----------+-----------+
T | | | | | |
U | | | | | |
R | | | | | |
E 90.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
88.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
D | | | | | |
E | | | | | |
G 86.0 + | | | | +
| | | | | |
F | | | | | |
| | | | | |
84.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
| | | | | |
| | | | | |
82.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
80.0 AAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAA+
0.0 20.0 40.0 60.0 80.0 100.0
DIST. FROM 1ST SURFACE DEVICE INLET FT
KEY... T - T - FLUID TEMP. A - A - AMB. TEMP.
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 34
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
***************************CONTINUED****************************
LINK "L006" DEVICE DETAIL REPORT
HOLDUP AND VELOCITY DETAIL REPORT
---------------------------------
DEVICE
NAME ---LIQUID HOLDUP--- SUPERFICIAL T-D
AND SEG. NO LIQ GAS MIX . FLOW FLOW SONIC
TYPE NO. SLIP SLIP TOTAL VEL VEL VEL REGM REGM VEL
(ABBL) (FPS) (FPS) (FPS) (FPS)
------ ---- ----- ----- -------- ------- ------- ------- ---- ---- -------
P016 0000
(PIPE) 0001 1.00 1.00 7.7 2.08 0.00 2.08 ---- 1-PH 0.00
0002 1.00 1.00 15.4 2.08 0.00 2.08 ---- 1-PH 0.00
0003 1.00 1.00 23.1 2.08 0.00 2.08 ---- 1-PH 0.00
0004 1.00 1.00 30.8 2.08 0.00 2.08 ---- 1-PH 0.00
PRESSURE GRADIENT DETAIL REPORT
-------------------------------
DEVICE
NAME
AND SEGM. --PRESSURE GRADIENT---- --PRESSURE CHANGE--
TYPE NO: FRIC ELEV TOTAL FRIC ELEV
(PSIFT) (PSIFT) (PSIFT) (PSIG) (PSIG)
------ ---- -------- -------- -------- -------- --------
P016 0000
(PIPE) 0001 -0.0004 0.0000 -0.0004 -8.62E-3 0.0
0002 -0.0004 0.0000 -0.0004 -8.62E-3 0.0
0003 -0.0004 0.0000 -0.0004 -8.62E-3 0.0
0004 -0.0004 0.0000 -0.0004 -8.62E-3 0.0
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 35
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
LINK "L006" PROPERTY DETAIL REPORT
VISCOSITY AND DENSITY RESULTS
-----------------------------
DEVICE
NAME
AND SEGM ----------VISCOSITY---------- ------------DENSITY------------
TYPE NO OIL LIQ VAP LIQ VAP SLIP NO-SLIP
(CP) (CP) (CP) (LB/CF) (LB/CF) (LB/CF) (LB/CF)
------ ---- --------- --------- --------- ------- ------- ------- -------
P016 0000
(PIPE) 0001 0.000 2.320 0.000 63.216 0.000 63.216 63.216
0002 0.000 2.320 0.000 63.217 0.000 63.217 63.217
0003 0.000 2.320 0.000 63.217 0.000 63.217 63.217
0004 0.000 2.320 0.000 63.217 0.000 63.217 63.217
FRICTION AND SURFACE TENSION RESULTS
------------------------------------
DEVICE
NAME LIQ
AND SEGM --------------FRICTION------------ FRIC. REYNOLDS SURFACE
TYPE NUM. DENSITY VELO ID. VISCOSITY FACTOR NUMBER TENSION
(LB/CF) (FPS) (IN) (CP) (DN/CM)
------ ---- ------- ------- -------- --------- -------- -------- --------
P016 0000
(PIPE) 0001 63.216 2.08 17.937 2.320 0.0178 1.2600E5 0.00
0002 63.217 2.08 17.937 2.320 0.0178 1.2600E5 0.00
0003 63.217 2.08 17.937 2.320 0.0178 1.2600E5 0.00
0004 63.217 2.08 17.937 2.320 0.0178 1.2600E5 0.00
HEAT TRANSFER CALCULATIONS
--------------------------
DEVICE FLUID
NAME THERMAL ----------THERMAL RESISTANCE-------
AND SEGM CONDUCT- INSIDE INSULAT- SURROUN-
(TYPE) NO: IVITY FILM PIPE ION DING
(BTUFTF) (HR-FT2- (HR-FT2- (HR-FT2- (HR-FT2-
F/BTU) F/BTU) F/BTU) F/BTU)
------ ---- -------- -------- -------- -------- --------
P016 0000
(PIPE) 0001 0.000 0.000 0.000 0.000 0.000
0002 0.000 0.000 0.000 0.000 0.000
0003 0.000 0.000 0.000 0.000 0.000
0004 0.000 0.000 0.000 0.000 0.000
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 36
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
LINK "L010" DEVICE DETAIL REPORT
PRESSURE AND TEMPERATURE REPORT
-------------------------------
DEVICE MWD OR TVD
NAME LENGTH I OR
AND SEGM INSIDE FROM & ELEV CALC CALC OVERALL AMB
TYPE NO DIAM. INLET O CHNG PRESS TEMP U-FACT TEMP
(IN) (FT) (FT) (PSIG) (F) (BTU/ (F)
HRFT2F)
------ ---- ------ --------- - -------- ------- ------ ------- ------
P004 0000 10.020 0.0 I 0.0 1289.7 100.0 80.0
(PIPE) 0001 4.9 0.0 1289.7 100.0 1.000 80.0
0002 9.8 0.0 1289.7 100.0 1.000 80.0
0003 14.8 0.0 1289.6 100.0 1.000 80.0
0004 19.7 O 0.0 1289.6 100.0 1.000 80.0
P005 0000 9.559 0.0 I 0.0 1289.6 100.0 80.0
(PIPE) 0001 4.9 0.0 1289.6 100.0 1.000 80.0
0002 9.8 0.0 1289.6 100.0 1.000 80.0
0003 14.8 0.0 1289.5 100.0 1.000 80.0
0004 19.7 O 0.0 1289.5 100.0 1.000 80.0
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 37
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
SURFACE PRESSURE PLOT FOR LINK
1295. +-----+-----+-----+-----+-----+-----+-----+-----+-----+-----+
| | | | | |
| | | | | |
| | | | | |
1294. + | | | | +
| | | | | |
| | | | | |
| | | | | |
1293. +-----------+-----------+-----------+-----------+-----------+
| | | | | |
| | | | | |
| | | | | |
P 1292. + | | | | +
R | | | | | |
E | | | | | |
S | | | | | |
S 1291. +-----------+-----------+-----------+-----------+-----------+
U | | | | | |
R | | | | | |
E | | | | | |
1290. + | | | | +
PPPPPPPPPPPPPPPPPPPPPPPPPPP | | |
| | | PPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPP|
| | | | | |
P 1289. +-----------+-----------+-----------+-----------+-----------+
S | | | | | |
I | | | | | |
G | | | | | |
1288. + | | | | +
| | | | | |
| | | | | |
| | | | | |
1287. +-----------+-----------+-----------+-----------+-----------+
| | | | | |
| | | | | |
| | | | | |
1286. + | | | | +
| | | | | |
| | | | | |
| | | | | |
1285. +-----+-----+-----+-----+-----+-----+-----+-----+-----+-----+
0.0 8.0 16.0 24.0 32.0 40.0
DIST. FROM 1ST SURFACE DEVICE INLET FT
KEY... P - P - FLUID PRESS.
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 38
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
SURFACE TEMPERATURE PLOT FOR LINK
100.0 TTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTT+
| | | | | |
| | | | | |
| | | | | |
98.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
96.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
T | | | | | |
E | | | | | |
M 94.0 + | | | | +
P | | | | | |
E | | | | | |
R | | | | | |
A 92.0 +-----------+-----------+-----------+-----------+-----------+
T | | | | | |
U | | | | | |
R | | | | | |
E 90.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
88.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
D | | | | | |
E | | | | | |
G 86.0 + | | | | +
| | | | | |
F | | | | | |
| | | | | |
84.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
| | | | | |
| | | | | |
82.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
80.0 AAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAA+
0.0 8.0 16.0 24.0 32.0 40.0
DIST. FROM 1ST SURFACE DEVICE INLET FT
KEY... T - T - FLUID TEMP. A - A - AMB. TEMP.
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 39
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
***************************CONTINUED****************************
LINK "L010" DEVICE DETAIL REPORT
HOLDUP AND VELOCITY DETAIL REPORT
---------------------------------
DEVICE
NAME ---LIQUID HOLDUP--- SUPERFICIAL T-D
AND SEG. NO LIQ GAS MIX . FLOW FLOW SONIC
TYPE NO. SLIP SLIP TOTAL VEL VEL VEL REGM REGM VEL
(ABBL) (FPS) (FPS) (FPS) (FPS)
------ ---- ----- ----- -------- ------- ------- ------- ---- ---- -------
P004 0000
(PIPE) 0001 1.00 1.00 0.5 5.90 0.00 5.90 ---- 1-PH 0.00
0002 1.00 1.00 1.0 5.90 0.00 5.90 ---- 1-PH 0.00
0003 1.00 1.00 1.4 5.90 0.00 5.90 ---- 1-PH 0.00
0004 1.00 1.00 1.9 5.90 0.00 5.90 ---- 1-PH 0.00
P005 0000
(PIPE) 0001 1.00 1.00 2.4 6.48 0.00 6.48 ---- 1-PH 0.00
0002 1.00 1.00 2.8 6.48 0.00 6.48 ---- 1-PH 0.00
0003 1.00 1.00 3.2 6.48 0.00 6.48 ---- 1-PH 0.00
0004 1.00 1.00 3.7 6.48 0.00 6.48 ---- 1-PH 0.00
PRESSURE GRADIENT DETAIL REPORT
-------------------------------
DEVICE
NAME
AND SEGM. --PRESSURE GRADIENT---- --PRESSURE CHANGE--
TYPE NO: FRIC ELEV TOTAL FRIC ELEV
(PSIFT) (PSIFT) (PSIFT) (PSIG) (PSIG)
------ ---- -------- -------- -------- -------- --------
P004 0000
(PIPE) 0001 -0.0048 0.0000 -0.0048 -2.37E-2 0.0
0002 -0.0048 0.0000 -0.0048 -2.37E-2 0.0
0003 -0.0048 0.0000 -0.0048 -2.37E-2 0.0
0004 -0.0048 0.0000 -0.0048 -2.37E-2 0.0
P005 0000
(PIPE) 0001 -0.0061 0.0000 -0.0061 -2.99E-2 0.0
0002 -0.0061 0.0000 -0.0061 -2.99E-2 0.0
0003 -0.0061 0.0000 -0.0061 -2.99E-2 0.0
0004 -0.0061 0.0000 -0.0061 -2.99E-2 0.0
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 40
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
LINK "L010" PROPERTY DETAIL REPORT
VISCOSITY AND DENSITY RESULTS
-----------------------------
DEVICE
NAME
AND SEGM ----------VISCOSITY---------- ------------DENSITY------------
TYPE NO OIL LIQ VAP LIQ VAP SLIP NO-SLIP
(CP) (CP) (CP) (LB/CF) (LB/CF) (LB/CF) (LB/CF)
------ ---- --------- --------- --------- ------- ------- ------- -------
P004 0000
(PIPE) 0001 0.000 2.320 0.000 63.217 0.000 63.217 63.217
0002 0.000 2.320 0.000 63.217 0.000 63.217 63.217
0003 0.000 2.320 0.000 63.217 0.000 63.217 63.217
0004 0.000 2.320 0.000 63.217 0.000 63.217 63.217
P005 0000
(PIPE) 0001 0.000 2.320 0.000 63.217 0.000 63.217 63.217
0002 0.000 2.320 0.000 63.217 0.000 63.217 63.217
0003 0.000 2.320 0.000 63.217 0.000 63.217 63.217
0004 0.000 2.320 0.000 63.217 0.000 63.217 63.217
FRICTION AND SURFACE TENSION RESULTS
------------------------------------
DEVICE
NAME LIQ
AND SEGM --------------FRICTION------------ FRIC. REYNOLDS SURFACE
TYPE NUM. DENSITY VELO ID. VISCOSITY FACTOR NUMBER TENSION
(LB/CF) (FPS) (IN) (CP) (DN/CM)
------ ---- ------- ------- -------- --------- -------- -------- --------
P004 0000
(PIPE) 0001 63.217 5.90 10.020 2.320 0.0170 1.9962E5 0.00
0002 63.217 5.90 10.020 2.320 0.0170 1.9962E5 0.00
0003 63.217 5.90 10.020 2.320 0.0170 1.9962E5 0.00
0004 63.217 5.90 10.020 2.320 0.0170 1.9962E5 0.00
P005 0000
(PIPE) 0001 63.217 6.48 9.559 2.320 0.0169 2.0924E5 0.00
0002 63.217 6.48 9.559 2.320 0.0169 2.0924E5 0.00
0003 63.217 6.48 9.559 2.320 0.0169 2.0924E5 0.00
0004 63.217 6.48 9.559 2.320 0.0169 2.0924E5 0.00
HEAT TRANSFER CALCULATIONS
--------------------------
DEVICE FLUID
NAME THERMAL ----------THERMAL RESISTANCE-------
AND SEGM CONDUCT- INSIDE INSULAT- SURROUN-
(TYPE) NO: IVITY FILM PIPE ION DING
(BTUFTF) (HR-FT2- (HR-FT2- (HR-FT2- (HR-FT2-
F/BTU) F/BTU) F/BTU) F/BTU)
------ ---- -------- -------- -------- -------- --------
P004 0000
Heat Transfer Resistances based on pipe ID
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 41
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
***************************CONTINUED****************************
LINK "L010" PROPERTY DETAIL REPORT
HEAT TRANSFER CALCULATIONS
--------------------------
DEVICE FLUID
NAME THERMAL ----------THERMAL RESISTANCE-------
AND SEGM CONDUCT- INSIDE INSULAT- SURROUN-
(TYPE) NO: IVITY FILM PIPE ION DING
(BTUFTF) (HR-FT2- (HR-FT2- (HR-FT2- (HR-FT2-
F/BTU) F/BTU) F/BTU) F/BTU)
------ ---- -------- -------- -------- -------- --------
(PIPE) 0001 0.000 0.000 0.000 0.000 0.000
0002 0.000 0.000 0.000 0.000 0.000
0003 0.000 0.000 0.000 0.000 0.000
0004 0.000 0.000 0.000 0.000 0.000
P005 0000
(PIPE) 0001 0.000 0.000 0.000 0.000 0.000
0002 0.000 0.000 0.000 0.000 0.000
0003 0.000 0.000 0.000 0.000 0.000
0004 0.000 0.000 0.000 0.000 0.000
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 42
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
LINK "L018" DEVICE DETAIL REPORT
PRESSURE AND TEMPERATURE REPORT
-------------------------------
DEVICE MWD OR TVD
NAME LENGTH I OR
AND SEGM INSIDE FROM & ELEV CALC CALC OVERALL AMB
TYPE NO DIAM. INLET O CHNG PRESS TEMP U-FACT TEMP
(IN) (FT) (FT) (PSIG) (F) (BTU/ (F)
HRFT2F)
------ ---- ------ --------- - -------- ------- ------ ------- ------
P012 0000 17.937 0.0 I 0.0 1289.5 100.0 80.0
(PIPE) 0001 5.7 0.0 1289.5 100.0 1.000 80.0
0002 11.5 0.0 1289.5 100.0 1.000 80.0
0003 17.2 0.0 1289.5 100.0 1.000 80.0
0004 23.0 O 0.0 1289.5 100.0 1.000 80.0
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 43
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
SURFACE PRESSURE PLOT FOR LINK
1294. +-----+-----+-----+-----+-----+-----+-----+-----+-----+-----+
| | | | | |
| | | | | |
| | | | | |
1293. + | | | | +
| | | | | |
| | | | | |
| | | | | |
1292. +-----------+-----------+-----------+-----------+-----------+
| | | | | |
| | | | | |
| | | | | |
P 1291. + | | | | +
R | | | | | |
E | | | | | |
S | | | | | |
S 1290. +-----------+-----------+-----------+-----------+-----------+
U | | | | | |
R PPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPP |
E | | | | | |
1289. + | | | | +
| | | | | |
| | | | | |
| | | | | |
P 1288. +-----------+-----------+-----------+-----------+-----------+
S | | | | | |
I | | | | | |
G | | | | | |
1287. + | | | | +
| | | | | |
| | | | | |
| | | | | |
1286. +-----------+-----------+-----------+-----------+-----------+
| | | | | |
| | | | | |
| | | | | |
1285. + | | | | +
| | | | | |
| | | | | |
| | | | | |
1284. +-----+-----+-----+-----+-----+-----+-----+-----+-----+-----+
0.0 5.0 10.0 15.0 20.0 25.0
DIST. FROM 1ST SURFACE DEVICE INLET FT
KEY... P - P - FLUID PRESS.
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 44
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
SURFACE TEMPERATURE PLOT FOR LINK
100.0 TTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTT----+
| | | | | |
| | | | | |
| | | | | |
98.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
96.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
T | | | | | |
E | | | | | |
M 94.0 + | | | | +
P | | | | | |
E | | | | | |
R | | | | | |
A 92.0 +-----------+-----------+-----------+-----------+-----------+
T | | | | | |
U | | | | | |
R | | | | | |
E 90.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
88.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
D | | | | | |
E | | | | | |
G 86.0 + | | | | +
| | | | | |
F | | | | | |
| | | | | |
84.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
| | | | | |
| | | | | |
82.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
80.0 AAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAA----+
0.0 5.0 10.0 15.0 20.0 25.0
DIST. FROM 1ST SURFACE DEVICE INLET FT
KEY... T - T - FLUID TEMP. A - A - AMB. TEMP.
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 45
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
***************************CONTINUED****************************
LINK "L018" DEVICE DETAIL REPORT
HOLDUP AND VELOCITY DETAIL REPORT
---------------------------------
DEVICE
NAME ---LIQUID HOLDUP--- SUPERFICIAL T-D
AND SEG. NO LIQ GAS MIX . FLOW FLOW SONIC
TYPE NO. SLIP SLIP TOTAL VEL VEL VEL REGM REGM VEL
(ABBL) (FPS) (FPS) (FPS) (FPS)
------ ---- ----- ----- -------- ------- ------- ------- ---- ---- -------
P012 0000
(PIPE) 0001 1.00 1.00 1.8 1.84 0.00 1.84 ---- 1-PH 0.00
0002 1.00 1.00 3.6 1.84 0.00 1.84 ---- 1-PH 0.00
0003 1.00 1.00 5.4 1.84 0.00 1.84 ---- 1-PH 0.00
0004 1.00 1.00 7.2 1.84 0.00 1.84 ---- 1-PH 0.00
PRESSURE GRADIENT DETAIL REPORT
-------------------------------
DEVICE
NAME
AND SEGM. --PRESSURE GRADIENT---- --PRESSURE CHANGE--
TYPE NO: FRIC ELEV TOTAL FRIC ELEV
(PSIFT) (PSIFT) (PSIFT) (PSIG) (PSIG)
------ ---- -------- -------- -------- -------- --------
P012 0000
(PIPE) 0001 -0.0003 0.0000 -0.0003 -1.61E-3 0.0
0002 -0.0003 0.0000 -0.0003 -1.61E-3 0.0
0003 -0.0003 0.0000 -0.0003 -1.61E-3 0.0
0004 -0.0003 0.0000 -0.0003 -1.61E-3 0.0
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 46
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
LINK "L018" PROPERTY DETAIL REPORT
VISCOSITY AND DENSITY RESULTS
-----------------------------
DEVICE
NAME
AND SEGM ----------VISCOSITY---------- ------------DENSITY------------
TYPE NO OIL LIQ VAP LIQ VAP SLIP NO-SLIP
(CP) (CP) (CP) (LB/CF) (LB/CF) (LB/CF) (LB/CF)
------ ---- --------- --------- --------- ------- ------- ------- -------
P012 0000
(PIPE) 0001 0.000 2.320 0.000 63.217 0.000 63.217 63.217
0002 0.000 2.320 0.000 63.217 0.000 63.217 63.217
0003 0.000 2.320 0.000 63.217 0.000 63.217 63.217
0004 0.000 2.320 0.000 63.217 0.000 63.217 63.217
FRICTION AND SURFACE TENSION RESULTS
------------------------------------
DEVICE
NAME LIQ
AND SEGM --------------FRICTION------------ FRIC. REYNOLDS SURFACE
TYPE NUM. DENSITY VELO ID. VISCOSITY FACTOR NUMBER TENSION
(LB/CF) (FPS) (IN) (CP) (DN/CM)
------ ---- ------- ------- -------- --------- -------- -------- --------
P012 0000
(PIPE) 0001 63.217 1.84 17.937 2.320 0.0182 1.1150E5 0.00
0002 63.217 1.84 17.937 2.320 0.0182 1.1150E5 0.00
0003 63.217 1.84 17.937 2.320 0.0182 1.1150E5 0.00
0004 63.217 1.84 17.937 2.320 0.0182 1.1150E5 0.00
HEAT TRANSFER CALCULATIONS
--------------------------
DEVICE FLUID
NAME THERMAL ----------THERMAL RESISTANCE-------
AND SEGM CONDUCT- INSIDE INSULAT- SURROUN-
(TYPE) NO: IVITY FILM PIPE ION DING
(BTUFTF) (HR-FT2- (HR-FT2- (HR-FT2- (HR-FT2-
F/BTU) F/BTU) F/BTU) F/BTU)
------ ---- -------- -------- -------- -------- --------
P012 0000
(PIPE) 0001 0.000 0.000 0.000 0.000 0.000
0002 0.000 0.000 0.000 0.000 0.000
0003 0.000 0.000 0.000 0.000 0.000
0004 0.000 0.000 0.000 0.000 0.000
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 47
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
LINK "L024" DEVICE DETAIL REPORT
PRESSURE AND TEMPERATURE REPORT
-------------------------------
DEVICE MWD OR TVD
NAME LENGTH I OR
AND SEGM INSIDE FROM & ELEV CALC CALC OVERALL AMB
TYPE NO DIAM. INLET O CHNG PRESS TEMP U-FACT TEMP
(IN) (FT) (FT) (PSIG) (F) (BTU/ (F)
HRFT2F)
------ ---- ------ --------- - -------- ------- ------ ------- ------
P015 0000 17.937 0.0 I 0.0 1289.5 100.0 80.0
(PIPE) 0001 49.2 0.0 1289.3 100.0 1.000 80.0
0002 98.4 0.0 1289.1 100.0 1.000 80.0
0003 147.6 0.0 1288.9 100.0 1.000 80.0
0004 196.9 O 0.0 1288.7 100.0 1.000 80.0
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 48
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
SURFACE PRESSURE PLOT FOR LINK
1294. +-----+-----+-----+-----+-----+-----+-----+-----+-----+-----+
| | | | | |
| | | | | |
| | | | | |
1293. + | | | | +
| | | | | |
| | | | | |
| | | | | |
1292. +-----------+-----------+-----------+-----------+-----------+
| | | | | |
| | | | | |
| | | | | |
P 1291. + | | | | +
R | | | | | |
E | | | | | |
S | | | | | |
S 1290. +-----------+-----------+-----------+-----------+-----------+
U | | | | | |
R PPPPPPPP | | | | |
E | PPPPPPPPPPPPPPP | | | |
1289. + | PPPPPPPPPPPPPPPPPPPPPPPPPPPPP +
| | | | | PPPPPPPP|
| | | | | |
| | | | | |
P 1288. +-----------+-----------+-----------+-----------+-----------+
S | | | | | |
I | | | | | |
G | | | | | |
1287. + | | | | +
| | | | | |
| | | | | |
| | | | | |
1286. +-----------+-----------+-----------+-----------+-----------+
| | | | | |
| | | | | |
| | | | | |
1285. + | | | | +
| | | | | |
| | | | | |
| | | | | |
1284. +-----+-----+-----+-----+-----+-----+-----+-----+-----+-----+
0.0 40.0 80.0 120.0 160.0 200.0
DIST. FROM 1ST SURFACE DEVICE INLET FT
KEY... P - P - FLUID PRESS.
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 49
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
SURFACE TEMPERATURE PLOT FOR LINK
100.0 TTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTT+
| | | | | |
| | | | | |
| | | | | |
98.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
96.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
T | | | | | |
E | | | | | |
M 94.0 + | | | | +
P | | | | | |
E | | | | | |
R | | | | | |
A 92.0 +-----------+-----------+-----------+-----------+-----------+
T | | | | | |
U | | | | | |
R | | | | | |
E 90.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
88.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
D | | | | | |
E | | | | | |
G 86.0 + | | | | +
| | | | | |
F | | | | | |
| | | | | |
84.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
| | | | | |
| | | | | |
82.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
80.0 AAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAA+
0.0 40.0 80.0 120.0 160.0 200.0
DIST. FROM 1ST SURFACE DEVICE INLET FT
KEY... T - T - FLUID TEMP. A - A - AMB. TEMP.
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 50
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
***************************CONTINUED****************************
LINK "L024" DEVICE DETAIL REPORT
HOLDUP AND VELOCITY DETAIL REPORT
---------------------------------
DEVICE
NAME ---LIQUID HOLDUP--- SUPERFICIAL T-D
AND SEG. NO LIQ GAS MIX . FLOW FLOW SONIC
TYPE NO. SLIP SLIP TOTAL VEL VEL VEL REGM REGM VEL
(ABBL) (FPS) (FPS) (FPS) (FPS)
------ ---- ----- ----- -------- ------- ------- ------- ---- ---- -------
P015 0000
(PIPE) 0001 1.00 1.00 15.4 7.43 0.00 7.43 ---- 1-PH 0.00
0002 1.00 1.00 30.8 7.43 0.00 7.43 ---- 1-PH 0.00
0003 1.00 1.00 46.1 7.43 0.00 7.43 ---- 1-PH 0.00
0004 1.00 1.00 61.5 7.43 0.00 7.43 ---- 1-PH 0.00
PRESSURE GRADIENT DETAIL REPORT
-------------------------------
DEVICE
NAME
AND SEGM. --PRESSURE GRADIENT---- --PRESSURE CHANGE--
TYPE NO: FRIC ELEV TOTAL FRIC ELEV
(PSIFT) (PSIFT) (PSIFT) (PSIG) (PSIG)
------ ---- -------- -------- -------- -------- --------
P015 0000
(PIPE) 0001 -0.0037 0.0000 -0.0037 -0.2 0.0
0002 -0.0037 0.0000 -0.0037 -0.2 0.0
0003 -0.0037 0.0000 -0.0037 -0.2 0.0
0004 -0.0037 0.0000 -0.0037 -0.2 0.0
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 51
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
LINK "L024" PROPERTY DETAIL REPORT
VISCOSITY AND DENSITY RESULTS
-----------------------------
DEVICE
NAME
AND SEGM ----------VISCOSITY---------- ------------DENSITY------------
TYPE NO OIL LIQ VAP LIQ VAP SLIP NO-SLIP
(CP) (CP) (CP) (LB/CF) (LB/CF) (LB/CF) (LB/CF)
------ ---- --------- --------- --------- ------- ------- ------- -------
P015 0000
(PIPE) 0001 0.000 2.320 0.000 63.217 0.000 63.217 63.217
0002 0.000 2.320 0.000 63.217 0.000 63.217 63.217
0003 0.000 2.320 0.000 63.216 0.000 63.216 63.216
0004 0.000 2.320 0.000 63.216 0.000 63.216 63.216
FRICTION AND SURFACE TENSION RESULTS
------------------------------------
DEVICE
NAME LIQ
AND SEGM --------------FRICTION------------ FRIC. REYNOLDS SURFACE
TYPE NUM. DENSITY VELO ID. VISCOSITY FACTOR NUMBER TENSION
(LB/CF) (FPS) (IN) (CP) (DN/CM)
------ ---- ------- ------- -------- --------- -------- -------- --------
P015 0000
(PIPE) 0001 63.217 7.43 17.937 2.320 0.0146 4.5000E5 0.00
0002 63.217 7.43 17.937 2.320 0.0146 4.5000E5 0.00
0003 63.216 7.43 17.937 2.320 0.0146 4.5000E5 0.00
0004 63.216 7.43 17.937 2.320 0.0146 4.5000E5 0.00
HEAT TRANSFER CALCULATIONS
--------------------------
DEVICE FLUID
NAME THERMAL ----------THERMAL RESISTANCE-------
AND SEGM CONDUCT- INSIDE INSULAT- SURROUN-
(TYPE) NO: IVITY FILM PIPE ION DING
(BTUFTF) (HR-FT2- (HR-FT2- (HR-FT2- (HR-FT2-
F/BTU) F/BTU) F/BTU) F/BTU)
------ ---- -------- -------- -------- -------- --------
P015 0000
(PIPE) 0001 0.000 0.000 0.000 0.000 0.000
0002 0.000 0.000 0.000 0.000 0.000
0003 0.000 0.000 0.000 0.000 0.000
0004 0.000 0.000 0.000 0.000 0.000
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 52
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
LINK "L030" DEVICE DETAIL REPORT
PRESSURE AND TEMPERATURE REPORT
-------------------------------
DEVICE MWD OR TVD
NAME LENGTH I OR
AND SEGM INSIDE FROM & ELEV CALC CALC OVERALL AMB
TYPE NO DIAM. INLET O CHNG PRESS TEMP U-FACT TEMP
(IN) (FT) (FT) (PSIG) (F) (BTU/ (F)
HRFT2F)
------ ---- ------ --------- - -------- ------- ------ ------- ------
P013 0000 17.937 0.0 I 0.0 1289.5 100.0 80.0
(PIPE) 0001 5.7 0.0 1289.5 100.0 1.000 80.0
0002 11.5 0.0 1289.5 100.0 1.000 80.0
0003 17.2 0.0 1289.5 100.0 1.000 80.0
0004 23.0 O 0.0 1289.5 100.0 1.000 80.0
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 53
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
SURFACE PRESSURE PLOT FOR LINK
1294. +-----+-----+-----+-----+-----+-----+-----+-----+-----+-----+
| | | | | |
| | | | | |
| | | | | |
1293. + | | | | +
| | | | | |
| | | | | |
| | | | | |
1292. +-----------+-----------+-----------+-----------+-----------+
| | | | | |
| | | | | |
| | | | | |
P 1291. + | | | | +
R | | | | | |
E | | | | | |
S | | | | | |
S 1290. +-----------+-----------+-----------+-----------+-----------+
U | | | | | |
R PPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPP |
E | | | | | |
1289. + | | | | +
| | | | | |
| | | | | |
| | | | | |
P 1288. +-----------+-----------+-----------+-----------+-----------+
S | | | | | |
I | | | | | |
G | | | | | |
1287. + | | | | +
| | | | | |
| | | | | |
| | | | | |
1286. +-----------+-----------+-----------+-----------+-----------+
| | | | | |
| | | | | |
| | | | | |
1285. + | | | | +
| | | | | |
| | | | | |
| | | | | |
1284. +-----+-----+-----+-----+-----+-----+-----+-----+-----+-----+
0.0 5.0 10.0 15.0 20.0 25.0
DIST. FROM 1ST SURFACE DEVICE INLET FT
KEY... P - P - FLUID PRESS.
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 54
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
SURFACE TEMPERATURE PLOT FOR LINK
100.0 TTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTT----+
| | | | | |
| | | | | |
| | | | | |
98.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
96.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
T | | | | | |
E | | | | | |
M 94.0 + | | | | +
P | | | | | |
E | | | | | |
R | | | | | |
A 92.0 +-----------+-----------+-----------+-----------+-----------+
T | | | | | |
U | | | | | |
R | | | | | |
E 90.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
88.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
D | | | | | |
E | | | | | |
G 86.0 + | | | | +
| | | | | |
F | | | | | |
| | | | | |
84.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
| | | | | |
| | | | | |
82.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
80.0 AAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAA----+
0.0 5.0 10.0 15.0 20.0 25.0
DIST. FROM 1ST SURFACE DEVICE INLET FT
KEY... T - T - FLUID TEMP. A - A - AMB. TEMP.
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 55
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
***************************CONTINUED****************************
LINK "L030" DEVICE DETAIL REPORT
HOLDUP AND VELOCITY DETAIL REPORT
---------------------------------
DEVICE
NAME ---LIQUID HOLDUP--- SUPERFICIAL T-D
AND SEG. NO LIQ GAS MIX . FLOW FLOW SONIC
TYPE NO. SLIP SLIP TOTAL VEL VEL VEL REGM REGM VEL
(ABBL) (FPS) (FPS) (FPS) (FPS)
------ ---- ----- ----- -------- ------- ------- ------- ---- ---- -------
P013 0000
(PIPE) 0001 1.00 1.00 1.8 3.60 0.00 3.60 ---- 1-PH 0.00
0002 1.00 1.00 3.6 3.60 0.00 3.60 ---- 1-PH 0.00
0003 1.00 1.00 5.4 3.60 0.00 3.60 ---- 1-PH 0.00
0004 1.00 1.00 7.2 3.60 0.00 3.60 ---- 1-PH 0.00
PRESSURE GRADIENT DETAIL REPORT
-------------------------------
DEVICE
NAME
AND SEGM. --PRESSURE GRADIENT---- --PRESSURE CHANGE--
TYPE NO: FRIC ELEV TOTAL FRIC ELEV
(PSIFT) (PSIFT) (PSIFT) (PSIG) (PSIG)
------ ---- -------- -------- -------- -------- --------
P013 0000
(PIPE) 0001 -0.0010 0.0000 -0.0010 -5.49E-3 0.0
0002 -0.0010 0.0000 -0.0010 -5.49E-3 0.0
0003 -0.0010 0.0000 -0.0010 -5.49E-3 0.0
0004 -0.0010 0.0000 -0.0010 -5.49E-3 0.0
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 56
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
LINK "L030" PROPERTY DETAIL REPORT
VISCOSITY AND DENSITY RESULTS
-----------------------------
DEVICE
NAME
AND SEGM ----------VISCOSITY---------- ------------DENSITY------------
TYPE NO OIL LIQ VAP LIQ VAP SLIP NO-SLIP
(CP) (CP) (CP) (LB/CF) (LB/CF) (LB/CF) (LB/CF)
------ ---- --------- --------- --------- ------- ------- ------- -------
P013 0000
(PIPE) 0001 0.000 2.320 0.000 63.217 0.000 63.217 63.217
0002 0.000 2.320 0.000 63.217 0.000 63.217 63.217
0003 0.000 2.320 0.000 63.217 0.000 63.217 63.217
0004 0.000 2.320 0.000 63.217 0.000 63.217 63.217
FRICTION AND SURFACE TENSION RESULTS
------------------------------------
DEVICE
NAME LIQ
AND SEGM --------------FRICTION------------ FRIC. REYNOLDS SURFACE
TYPE NUM. DENSITY VELO ID. VISCOSITY FACTOR NUMBER TENSION
(LB/CF) (FPS) (IN) (CP) (DN/CM)
------ ---- ------- ------- -------- --------- -------- -------- --------
P013 0000
(PIPE) 0001 63.217 3.60 17.937 2.320 0.0162 2.1808E5 0.00
0002 63.217 3.60 17.937 2.320 0.0162 2.1808E5 0.00
0003 63.217 3.60 17.937 2.320 0.0162 2.1808E5 0.00
0004 63.217 3.60 17.937 2.320 0.0162 2.1808E5 0.00
HEAT TRANSFER CALCULATIONS
--------------------------
DEVICE FLUID
NAME THERMAL ----------THERMAL RESISTANCE-------
AND SEGM CONDUCT- INSIDE INSULAT- SURROUN-
(TYPE) NO: IVITY FILM PIPE ION DING
(BTUFTF) (HR-FT2- (HR-FT2- (HR-FT2- (HR-FT2-
F/BTU) F/BTU) F/BTU) F/BTU)
------ ---- -------- -------- -------- -------- --------
P013 0000
(PIPE) 0001 0.000 0.000 0.000 0.000 0.000
0002 0.000 0.000 0.000 0.000 0.000
0003 0.000 0.000 0.000 0.000 0.000
0004 0.000 0.000 0.000 0.000 0.000
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 57
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
LINK "L032" DEVICE DETAIL REPORT
PRESSURE AND TEMPERATURE REPORT
-------------------------------
DEVICE MWD OR TVD
NAME LENGTH I OR
AND SEGM INSIDE FROM & ELEV CALC CALC OVERALL AMB
TYPE NO DIAM. INLET O CHNG PRESS TEMP U-FACT TEMP
(IN) (FT) (FT) (PSIG) (F) (BTU/ (F)
HRFT2F)
------ ---- ------ --------- - -------- ------- ------ ------- ------
P014 0000 17.937 0.0 I 0.0 1289.5 100.0 80.0
(PIPE) 0001 4.9 0.0 1289.5 100.0 1.000 80.0
0002 9.8 0.0 1289.5 100.0 1.000 80.0
0003 14.8 0.0 1289.5 100.0 1.000 80.0
0004 19.7 O 0.0 1289.5 100.0 1.000 80.0
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 58
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
SURFACE PRESSURE PLOT FOR LINK
1294. +-----+-----+-----+-----+-----+-----+-----+-----+-----+-----+
| | | | | |
| | | | | |
| | | | | |
1293. + | | | | +
| | | | | |
| | | | | |
| | | | | |
1292. +-----------+-----------+-----------+-----------+-----------+
| | | | | |
| | | | | |
| | | | | |
P 1291. + | | | | +
R | | | | | |
E | | | | | |
S | | | | | |
S 1290. +-----------+-----------+-----------+-----------+-----------+
U | | | | | |
R PPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPP|
E | | | | | |
1289. + | | | | +
| | | | | |
| | | | | |
| | | | | |
P 1288. +-----------+-----------+-----------+-----------+-----------+
S | | | | | |
I | | | | | |
G | | | | | |
1287. + | | | | +
| | | | | |
| | | | | |
| | | | | |
1286. +-----------+-----------+-----------+-----------+-----------+
| | | | | |
| | | | | |
| | | | | |
1285. + | | | | +
| | | | | |
| | | | | |
| | | | | |
1284. +-----+-----+-----+-----+-----+-----+-----+-----+-----+-----+
0.0 4.0 8.0 12.0 16.0 20.0
DIST. FROM 1ST SURFACE DEVICE INLET FT
KEY... P - P - FLUID PRESS.
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 59
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
SURFACE TEMPERATURE PLOT FOR LINK
100.0 TTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTT+
| | | | | |
| | | | | |
| | | | | |
98.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
96.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
T | | | | | |
E | | | | | |
M 94.0 + | | | | +
P | | | | | |
E | | | | | |
R | | | | | |
A 92.0 +-----------+-----------+-----------+-----------+-----------+
T | | | | | |
U | | | | | |
R | | | | | |
E 90.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
88.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
D | | | | | |
E | | | | | |
G 86.0 + | | | | +
| | | | | |
F | | | | | |
| | | | | |
84.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
| | | | | |
| | | | | |
82.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
80.0 AAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAA+
0.0 4.0 8.0 12.0 16.0 20.0
DIST. FROM 1ST SURFACE DEVICE INLET FT
KEY... T - T - FLUID TEMP. A - A - AMB. TEMP.
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 60
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
***************************CONTINUED****************************
LINK "L032" DEVICE DETAIL REPORT
HOLDUP AND VELOCITY DETAIL REPORT
---------------------------------
DEVICE
NAME ---LIQUID HOLDUP--- SUPERFICIAL T-D
AND SEG. NO LIQ GAS MIX . FLOW FLOW SONIC
TYPE NO. SLIP SLIP TOTAL VEL VEL VEL REGM REGM VEL
(ABBL) (FPS) (FPS) (FPS) (FPS)
------ ---- ----- ----- -------- ------- ------- ------- ---- ---- -------
P014 0000
(PIPE) 0001 1.00 1.00 1.5 1.91 0.00 1.91 ---- 1-PH 0.00
0002 1.00 1.00 3.1 1.91 0.00 1.91 ---- 1-PH 0.00
0003 1.00 1.00 4.6 1.91 0.00 1.91 ---- 1-PH 0.00
0004 1.00 1.00 6.2 1.91 0.00 1.91 ---- 1-PH 0.00
PRESSURE GRADIENT DETAIL REPORT
-------------------------------
DEVICE
NAME
AND SEGM. --PRESSURE GRADIENT---- --PRESSURE CHANGE--
TYPE NO: FRIC ELEV TOTAL FRIC ELEV
(PSIFT) (PSIFT) (PSIFT) (PSIG) (PSIG)
------ ---- -------- -------- -------- -------- --------
P014 0000
(PIPE) 0001 -0.0003 0.0000 -0.0003 -1.47E-3 0.0
0002 -0.0003 0.0000 -0.0003 -1.47E-3 0.0
0003 -0.0003 0.0000 -0.0003 -1.47E-3 0.0
0004 -0.0003 0.0000 -0.0003 -1.47E-3 0.0
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 61
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
LINK "L032" PROPERTY DETAIL REPORT
VISCOSITY AND DENSITY RESULTS
-----------------------------
DEVICE
NAME
AND SEGM ----------VISCOSITY---------- ------------DENSITY------------
TYPE NO OIL LIQ VAP LIQ VAP SLIP NO-SLIP
(CP) (CP) (CP) (LB/CF) (LB/CF) (LB/CF) (LB/CF)
------ ---- --------- --------- --------- ------- ------- ------- -------
P014 0000
(PIPE) 0001 0.000 2.320 0.000 63.217 0.000 63.217 63.217
0002 0.000 2.320 0.000 63.217 0.000 63.217 63.217
0003 0.000 2.320 0.000 63.217 0.000 63.217 63.217
0004 0.000 2.320 0.000 63.217 0.000 63.217 63.217
FRICTION AND SURFACE TENSION RESULTS
------------------------------------
DEVICE
NAME LIQ
AND SEGM --------------FRICTION------------ FRIC. REYNOLDS SURFACE
TYPE NUM. DENSITY VELO ID. VISCOSITY FACTOR NUMBER TENSION
(LB/CF) (FPS) (IN) (CP) (DN/CM)
------ ---- ------- ------- -------- --------- -------- -------- --------
P014 0000
(PIPE) 0001 63.217 1.91 17.937 2.320 0.0181 1.1555E5 0.00
0002 63.217 1.91 17.937 2.320 0.0181 1.1555E5 0.00
0003 63.217 1.91 17.937 2.320 0.0181 1.1555E5 0.00
0004 63.217 1.91 17.937 2.320 0.0181 1.1555E5 0.00
HEAT TRANSFER CALCULATIONS
--------------------------
DEVICE FLUID
NAME THERMAL ----------THERMAL RESISTANCE-------
AND SEGM CONDUCT- INSIDE INSULAT- SURROUN-
(TYPE) NO: IVITY FILM PIPE ION DING
(BTUFTF) (HR-FT2- (HR-FT2- (HR-FT2- (HR-FT2-
F/BTU) F/BTU) F/BTU) F/BTU)
------ ---- -------- -------- -------- -------- --------
P014 0000
(PIPE) 0001 0.000 0.000 0.000 0.000 0.000
0002 0.000 0.000 0.000 0.000 0.000
0003 0.000 0.000 0.000 0.000 0.000
0004 0.000 0.000 0.000 0.000 0.000
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 62
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
LINK "L075" DEVICE DETAIL REPORT
PRESSURE AND TEMPERATURE REPORT
-------------------------------
DEVICE MWD OR TVD
NAME LENGTH I OR
AND SEGM INSIDE FROM & ELEV CALC CALC OVERALL AMB
TYPE NO DIAM. INLET O CHNG PRESS TEMP U-FACT TEMP
(IN) (FT) (FT) (PSIG) (F) (BTU/ (F)
HRFT2F)
------ ---- ------ --------- - -------- ------- ------ ------- ------
P027 0000 5.764 0.0 I 0.0 1288.7 100.0 80.0
(PIPE) 0001 369.1 0.0 1285.4 99.9 1.000 80.0
0002 738.2 0.0 1282.1 99.9 1.000 80.0
0003 1107.3 0.0 1278.8 99.8 1.000 80.0
0004 1476.4 O 0.0 1275.4 99.8 1.000 80.0
R001 0000 0.000 0.0 I 0.0 1275.4 99.8
(MREG) 0001 0.0 O 0.0 1200.1 99.8 0.000
P044 0000 5.764 0.0 I 0.0 1200.1 99.8 80.0
(PIPE) 0001 1.6 0.0 1200.0 99.8 1.000 80.0
0002 3.3 0.0 1200.0 99.8 1.000 80.0
0003 4.9 0.0 1200.0 99.8 1.000 80.0
0004 6.6 O 0.0 1200.0 99.8 1.000 80.0
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 63
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
SURFACE PRESSURE PLOT FOR LINK
1290. +-----+-----+-----+-----+-----+-----+-----+-----+-----+-----+
PPPPPPPP | | | | |
| PPPPPPPPPPPPPPP | | | |
| | PPPPPPPPPPPPPPP | |
1280. + | | | PPPPPPPPPP| +
| | | | PPPPPPPP |
| | | | | PPPP|
| | | | | P|
1270. +-----------+-----------+-----------+-----------+----------P+
| | | | | P|
| | | | | P|
| | | | | P|
P 1260. + | | | | P+
R | | | | | P|
E | | | | | P|
S | | | | | P|
S 1250. +-----------+-----------+-----------+-----------+----------P+
U | | | | | P|
R | | | | | P|
E | | | | | P|
1240. + | | | | P+
| | | | | P|
| | | | | P|
| | | | | P|
P 1230. +-----------+-----------+-----------+-----------+----------P+
S | | | | | P|
I | | | | | P|
G | | | | | P|
1220. + | | | | P+
| | | | | P|
| | | | | P|
| | | | | P|
1210. +-----------+-----------+-----------+-----------+----------P+
| | | | | P|
| | | | | P|
| | | | | P|
1200. + | | | | P+
| | | | | |
| | | | | |
| | | | | |
1190. +-----+-----+-----+-----+-----+-----+-----+-----+-----+-----+
0. 300. 600. 900. 1200. 1500.
DIST. FROM 1ST SURFACE DEVICE INLET FT
KEY... P - P - FLUID PRESS.
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 64
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
SURFACE TEMPERATURE PLOT FOR LINK
100.0 TTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTT+
| | | | | |
| | | | | |
| | | | | |
98.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
96.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
T | | | | | |
E | | | | | |
M 94.0 + | | | | +
P | | | | | |
E | | | | | |
R | | | | | |
A 92.0 +-----------+-----------+-----------+-----------+-----------+
T | | | | | |
U | | | | | |
R | | | | | |
E 90.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
88.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
D | | | | | |
E | | | | | |
G 86.0 + | | | | +
| | | | | |
F | | | | | |
| | | | | |
84.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
| | | | | |
| | | | | |
82.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
80.0 AAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAA+
0. 300. 600. 900. 1200. 1500.
DIST. FROM 1ST SURFACE DEVICE INLET FT
KEY... T - T - FLUID TEMP. A - A - AMB. TEMP.
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 65
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
***************************CONTINUED****************************
LINK "L075" DEVICE DETAIL REPORT
HOLDUP AND VELOCITY DETAIL REPORT
---------------------------------
DEVICE
NAME ---LIQUID HOLDUP--- SUPERFICIAL T-D
AND SEG. NO LIQ GAS MIX . FLOW FLOW SONIC
TYPE NO. SLIP SLIP TOTAL VEL VEL VEL REGM REGM VEL
(ABBL) (FPS) (FPS) (FPS) (FPS)
------ ---- ----- ----- -------- ------- ------- ------- ---- ---- -------
P027 0000
(PIPE) 0001 1.00 1.00 11.9 5.75 0.00 5.75 ---- 1-PH 0.00
0002 1.00 1.00 23.8 5.75 0.00 5.75 ---- 1-PH 0.00
0003 1.00 1.00 35.7 5.75 0.00 5.75 ---- 1-PH 0.00
0004 1.00 1.00 47.6 5.75 0.00 5.75 ---- 1-PH 0.00
(MREG) 0000
R001 0001
P044 0000
(PIPE) 0001 1.00 1.00 5.294E-2 5.75 0.00 5.75 ---- 1-PH 0.00
0002 1.00 1.00 0.1 5.75 0.00 5.75 ---- 1-PH 0.00
0003 1.00 1.00 0.2 5.75 0.00 5.75 ---- 1-PH 0.00
0004 1.00 1.00 0.2 5.75 0.00 5.75 ---- 1-PH 0.00
PRESSURE GRADIENT DETAIL REPORT
-------------------------------
DEVICE
NAME
AND SEGM. --PRESSURE GRADIENT---- --PRESSURE CHANGE--
TYPE NO: FRIC ELEV TOTAL FRIC ELEV
(PSIFT) (PSIFT) (PSIFT) (PSIG) (PSIG)
------ ---- -------- -------- -------- -------- --------
P027 0000
(PIPE) 0001 -0.0090 0.0000 -0.0090 -3.3 0.0
0002 -0.0090 0.0000 -0.0090 -3.3 0.0
0003 -0.0090 0.0000 -0.0090 -3.3 0.0
0004 -0.0090 0.0000 -0.0090 -3.3 0.0
(MREG) 0000
R001 0001
P044 0000
(PIPE) 0001 -0.0090 0.0000 -0.0090 -1.48E-2 0.0
0002 -0.0090 0.0000 -0.0090 -1.48E-2 0.0
0003 -0.0090 0.0000 -0.0090 -1.48E-2 0.0
0004 -0.0090 0.0000 -0.0090 -1.48E-2 0.0
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 66
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
LINK "L075" PROPERTY DETAIL REPORT
VISCOSITY AND DENSITY RESULTS
-----------------------------
DEVICE
NAME
AND SEGM ----------VISCOSITY---------- ------------DENSITY------------
TYPE NO OIL LIQ VAP LIQ VAP SLIP NO-SLIP
(CP) (CP) (CP) (LB/CF) (LB/CF) (LB/CF) (LB/CF)
------ ---- --------- --------- --------- ------- ------- ------- -------
P027 0000
(PIPE) 0001 0.000 2.320 0.000 63.216 0.000 63.216 63.216
0002 0.000 2.320 0.000 63.216 0.000 63.216 63.216
0003 0.000 2.320 0.000 63.216 0.000 63.216 63.216
0004 0.000 2.321 0.000 63.216 0.000 63.216 63.216
R001 0000
(MREG) 0001
P044 0000
(PIPE) 0001 0.000 2.321 0.000 63.202 0.000 63.202 63.202
0002 0.000 2.321 0.000 63.202 0.000 63.202 63.202
0003 0.000 2.321 0.000 63.202 0.000 63.202 63.202
0004 0.000 2.321 0.000 63.202 0.000 63.202 63.202
FRICTION AND SURFACE TENSION RESULTS
------------------------------------
DEVICE
NAME LIQ
AND SEGM --------------FRICTION------------ FRIC. REYNOLDS SURFACE
TYPE NUM. DENSITY VELO ID. VISCOSITY FACTOR NUMBER TENSION
(LB/CF) (FPS) (IN) (CP) (DN/CM)
------ ---- ------- ------- -------- --------- -------- -------- --------
P027 0000
(PIPE) 0001 63.216 5.75 5.764 2.320 0.0192 1.1203E5 0.00
0002 63.216 5.75 5.764 2.320 0.0192 1.1202E5 0.00
0003 63.216 5.75 5.764 2.320 0.0192 1.1201E5 0.00
0004 63.216 5.75 5.764 2.321 0.0192 1.1200E5 0.00
R001 0000
(MREG) 0001
P044 0000
(PIPE) 0001 63.202 5.75 5.764 2.321 0.0192 1.1200E5 0.00
0002 63.202 5.75 5.764 2.321 0.0192 1.1200E5 0.00
0003 63.202 5.75 5.764 2.321 0.0192 1.1200E5 0.00
0004 63.202 5.75 5.764 2.321 0.0192 1.1200E5 0.00
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 67
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
***************************CONTINUED****************************
LINK "L075" PROPERTY DETAIL REPORT
HEAT TRANSFER CALCULATIONS
--------------------------
DEVICE FLUID
NAME THERMAL ----------THERMAL RESISTANCE-------
AND SEGM CONDUCT- INSIDE INSULAT- SURROUN-
(TYPE) NO: IVITY FILM PIPE ION DING
(BTUFTF) (HR-FT2- (HR-FT2- (HR-FT2- (HR-FT2-
F/BTU) F/BTU) F/BTU) F/BTU)
------ ---- -------- -------- -------- -------- --------
P027 0000
(PIPE) 0001 0.000 0.000 0.000 0.000 0.000
0002 0.000 0.000 0.000 0.000 0.000
0003 0.000 0.000 0.000 0.000 0.000
0004 0.000 0.000 0.000 0.000 0.000
R001 0000
(MREG) 0001
P044 0000
(PIPE) 0001 0.000 0.000 0.000 0.000 0.000
0002 0.000 0.000 0.000 0.000 0.000
0003 0.000 0.000 0.000 0.000 0.000
0004 0.000 0.000 0.000 0.000 0.000
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 68
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
LINK "L077" DEVICE DETAIL REPORT
PRESSURE AND TEMPERATURE REPORT
-------------------------------
DEVICE MWD OR TVD
NAME LENGTH I OR
AND SEGM INSIDE FROM & ELEV CALC CALC OVERALL AMB
TYPE NO DIAM. INLET O CHNG PRESS TEMP U-FACT TEMP
(IN) (FT) (FT) (PSIG) (F) (BTU/ (F)
HRFT2F)
------ ---- ------ --------- - -------- ------- ------ ------- ------
P028 0000 5.764 0.0 I 0.0 1288.7 100.0 80.0
(PIPE) 0001 1271.3 0.0 1277.3 99.8 1.000 80.0
0002 2542.7 0.0 1265.8 99.7 1.000 80.0
0003 3814.0 0.0 1254.4 99.5 1.000 80.0
0004 5085.3 O 0.0 1242.9 99.4 1.000 80.0
R002 0000 0.000 0.0 I 0.0 1242.9 99.4
(MREG) 0001 0.0 O 0.0 1200.1 99.4 0.000
P043 0000 5.764 0.0 I 0.0 1200.1 99.4 80.0
(PIPE) 0001 1.6 0.0 1200.0 99.4 1.000 80.0
0002 3.3 0.0 1200.0 99.4 1.000 80.0
0003 4.9 0.0 1200.0 99.3 1.000 80.0
0004 6.6 O 0.0 1200.0 99.3 1.000 80.0
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 69
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
SURFACE PRESSURE PLOT FOR LINK
1290. +-----+-----+-----+-----+-----+-----+-----+-----+-----+-----+
PP | | | | |
| PPP | | | | |
| PPPP | | | | |
1280. + PPP| | | | +
| PPP | | | |
| | PP | | | |
| | PPP | | | |
1270. +-----------+-------PP--+-----------+-----------+-----------+
| | PP| | | |
| | PPP | | |
| | | PPP | | |
P 1260. + | | PPPP | | +
R | | | PPP | |
E | | | |PPP | |
S | | | | PP | |
S 1250. +-----------+-----------+-----------+-----PPP---+-----------+
U | | | | PPP| |
R | | | | PP |
E | | | | | PP |
1240. + | | | | P +
| | | | | P |
| | | | | P |
| | | | | P |
P 1230. +-----------+-----------+-----------+-----------+--P--------+
S | | | | | P |
I | | | | | P |
G | | | | | P |
1220. + | | | | P +
| | | | | P |
| | | | | P |
| | | | | P |
1210. +-----------+-----------+-----------+-----------+--P--------+
| | | | | P |
| | | | | P |
| | | | | P |
1200. + | | | | P +
| | | | | |
| | | | | |
| | | | | |
1190. +-----+-----+-----+-----+-----+-----+-----+-----+-----+-----+
0. 1200. 2400. 3600. 4800. 6000.
DIST. FROM 1ST SURFACE DEVICE INLET FT
KEY... P - P - FLUID PRESS.
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 70
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
SURFACE TEMPERATURE PLOT FOR LINK
100.0 TTTTTTTTTTTTTTTTTTTT----+-----+-----+-----+-----+-----+-----+
| | TTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTT |
| | | | | |
| | | | | |
98.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
96.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
T | | | | | |
E | | | | | |
M 94.0 + | | | | +
P | | | | | |
E | | | | | |
R | | | | | |
A 92.0 +-----------+-----------+-----------+-----------+-----------+
T | | | | | |
U | | | | | |
R | | | | | |
E 90.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
88.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
D | | | | | |
E | | | | | |
G 86.0 + | | | | +
| | | | | |
F | | | | | |
| | | | | |
84.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
| | | | | |
| | | | | |
82.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
80.0 AAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAA--+-----+
0. 1200. 2400. 3600. 4800. 6000.
DIST. FROM 1ST SURFACE DEVICE INLET FT
KEY... T - T - FLUID TEMP. A - A - AMB. TEMP.
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 71
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
***************************CONTINUED****************************
LINK "L077" DEVICE DETAIL REPORT
HOLDUP AND VELOCITY DETAIL REPORT
---------------------------------
DEVICE
NAME ---LIQUID HOLDUP--- SUPERFICIAL T-D
AND SEG. NO LIQ GAS MIX . FLOW FLOW SONIC
TYPE NO. SLIP SLIP TOTAL VEL VEL VEL REGM REGM VEL
(ABBL) (FPS) (FPS) (FPS) (FPS)
------ ---- ----- ----- -------- ------- ------- ------- ---- ---- -------
P028 0000
(PIPE) 0001 1.00 1.00 41.0 5.75 0.00 5.75 ---- 1-PH 0.00
0002 1.00 1.00 82.1 5.75 0.00 5.75 ---- 1-PH 0.00
0003 1.00 1.00 123.1 5.75 0.00 5.75 ---- 1-PH 0.00
0004 1.00 1.00 164.1 5.75 0.00 5.75 ---- 1-PH 0.00
(MREG) 0000
R002 0001
P043 0000
(PIPE) 0001 1.00 1.00 5.294E-2 5.75 0.00 5.75 ---- 1-PH 0.00
0002 1.00 1.00 0.1 5.75 0.00 5.75 ---- 1-PH 0.00
0003 1.00 1.00 0.2 5.75 0.00 5.75 ---- 1-PH 0.00
0004 1.00 1.00 0.2 5.75 0.00 5.75 ---- 1-PH 0.00
PRESSURE GRADIENT DETAIL REPORT
-------------------------------
DEVICE
NAME
AND SEGM. --PRESSURE GRADIENT---- --PRESSURE CHANGE--
TYPE NO: FRIC ELEV TOTAL FRIC ELEV
(PSIFT) (PSIFT) (PSIFT) (PSIG) (PSIG)
------ ---- -------- -------- -------- -------- --------
P028 0000
(PIPE) 0001 -0.0090 0.0000 -0.0090 -11.5 0.0
0002 -0.0090 0.0000 -0.0090 -11.5 0.0
0003 -0.0090 0.0000 -0.0090 -11.5 0.0
0004 -0.0090 0.0000 -0.0090 -11.5 0.0
(MREG) 0000
R002 0001
P043 0000
(PIPE) 0001 -0.0090 0.0000 -0.0090 -1.48E-2 0.0
0002 -0.0090 0.0000 -0.0090 -1.48E-2 0.0
0003 -0.0090 0.0000 -0.0090 -1.48E-2 0.0
0004 -0.0090 0.0000 -0.0090 -1.48E-2 0.0
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 72
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
LINK "L077" PROPERTY DETAIL REPORT
VISCOSITY AND DENSITY RESULTS
-----------------------------
DEVICE
NAME
AND SEGM ----------VISCOSITY---------- ------------DENSITY------------
TYPE NO OIL LIQ VAP LIQ VAP SLIP NO-SLIP
(CP) (CP) (CP) (LB/CF) (LB/CF) (LB/CF) (LB/CF)
------ ---- --------- --------- --------- ------- ------- ------- -------
P028 0000
(PIPE) 0001 0.000 2.320 0.000 63.216 0.000 63.216 63.216
0002 0.000 2.321 0.000 63.216 0.000 63.216 63.216
0003 0.000 2.322 0.000 63.216 0.000 63.216 63.216
0004 0.000 2.322 0.000 63.216 0.000 63.216 63.216
R002 0000
(MREG) 0001
P043 0000
(PIPE) 0001 0.000 2.322 0.000 63.208 0.000 63.208 63.208
0002 0.000 2.322 0.000 63.208 0.000 63.208 63.208
0003 0.000 2.322 0.000 63.208 0.000 63.208 63.208
0004 0.000 2.322 0.000 63.208 0.000 63.208 63.208
FRICTION AND SURFACE TENSION RESULTS
------------------------------------
DEVICE
NAME LIQ
AND SEGM --------------FRICTION------------ FRIC. REYNOLDS SURFACE
TYPE NUM. DENSITY VELO ID. VISCOSITY FACTOR NUMBER TENSION
(LB/CF) (FPS) (IN) (CP) (DN/CM)
------ ---- ------- ------- -------- --------- -------- -------- --------
P028 0000
(PIPE) 0001 63.216 5.75 5.764 2.320 0.0192 1.1202E5 0.00
0002 63.216 5.75 5.764 2.321 0.0192 1.1199E5 0.00
0003 63.216 5.75 5.764 2.322 0.0192 1.1196E5 0.00
0004 63.216 5.75 5.764 2.322 0.0192 1.1193E5 0.00
R002 0000
(MREG) 0001
P043 0000
(PIPE) 0001 63.208 5.75 5.764 2.322 0.0192 1.1191E5 0.00
0002 63.208 5.75 5.764 2.322 0.0192 1.1191E5 0.00
0003 63.208 5.75 5.764 2.322 0.0192 1.1191E5 0.00
0004 63.208 5.75 5.764 2.322 0.0192 1.1191E5 0.00
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 73
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
***************************CONTINUED****************************
LINK "L077" PROPERTY DETAIL REPORT
HEAT TRANSFER CALCULATIONS
--------------------------
DEVICE FLUID
NAME THERMAL ----------THERMAL RESISTANCE-------
AND SEGM CONDUCT- INSIDE INSULAT- SURROUN-
(TYPE) NO: IVITY FILM PIPE ION DING
(BTUFTF) (HR-FT2- (HR-FT2- (HR-FT2- (HR-FT2-
F/BTU) F/BTU) F/BTU) F/BTU)
------ ---- -------- -------- -------- -------- --------
P028 0000
(PIPE) 0001 0.000 0.000 0.000 0.000 0.000
0002 0.000 0.000 0.000 0.000 0.000
0003 0.000 0.000 0.000 0.000 0.000
0004 0.000 0.000 0.000 0.000 0.000
R002 0000
(MREG) 0001
P043 0000
(PIPE) 0001 0.000 0.000 0.000 0.000 0.000
0002 0.000 0.000 0.000 0.000 0.000
0003 0.000 0.000 0.000 0.000 0.000
0004 0.000 0.000 0.000 0.000 0.000
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 74
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
LINK "L079" DEVICE DETAIL REPORT
PRESSURE AND TEMPERATURE REPORT
-------------------------------
DEVICE MWD OR TVD
NAME LENGTH I OR
AND SEGM INSIDE FROM & ELEV CALC CALC OVERALL AMB
TYPE NO DIAM. INLET O CHNG PRESS TEMP U-FACT TEMP
(IN) (FT) (FT) (PSIG) (F) (BTU/ (F)
HRFT2F)
------ ---- ------ --------- - -------- ------- ------ ------- ------
P029 0000 5.764 0.0 I 0.0 1288.7 100.0 80.0
(PIPE) 0001 1131.9 0.0 1278.5 99.8 1.000 80.0
0002 2263.8 0.0 1268.3 99.7 1.000 80.0
0003 3395.7 0.0 1258.1 99.6 1.000 80.0
0004 4527.6 O 0.0 1247.9 99.4 1.000 80.0
R003 0000 0.000 0.0 I 0.0 1247.9 99.4
(MREG) 0001 0.0 O 0.0 1200.1 99.4 0.000
P042 0000 5.764 0.0 I 0.0 1200.1 99.4 80.0
(PIPE) 0001 1.6 0.0 1200.0 99.4 1.000 80.0
0002 3.3 0.0 1200.0 99.4 1.000 80.0
0003 4.9 0.0 1200.0 99.4 1.000 80.0
0004 6.6 O 0.0 1200.0 99.4 1.000 80.0
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 75
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
SURFACE PRESSURE PLOT FOR LINK
1290. +-----+-----+-----+-----+-----+-----+-----+-----+-----+-----+
PP | | | | |
| PPPP | | | | |
| PPP | | | | |
1280. + PPPP | | | +
| |PPP | | | |
| | PPP | | | |
| | PPPP | | | |
1270. +-----------+----------PPP----------+-----------+-----------+
| | | PPP | | |
| | | PPPP | | |
| | | PPP| | |
P 1260. + | | PPPP | +
R | | | | PPP | |
E | | | | PPP | |
S | | | | PPPP |
S 1250. +-----------+-----------+-----------+-----------+-PPP-------+
U | | | | | PP |
R | | | | | P |
E | | | | | P |
1240. + | | | | P +
| | | | | P |
| | | | | P |
| | | | | P |
P 1230. +-----------+-----------+-----------+-----------+-----P-----+
S | | | | | P |
I | | | | | P |
G | | | | | P |
1220. + | | | | P +
| | | | | P |
| | | | | P |
| | | | | P |
1210. +-----------+-----------+-----------+-----------+-----P-----+
| | | | | P |
| | | | | P |
| | | | | P |
1200. + | | | | P +
| | | | | |
| | | | | |
| | | | | |
1190. +-----+-----+-----+-----+-----+-----+-----+-----+-----+-----+
0. 1000. 2000. 3000. 4000. 5000.
DIST. FROM 1ST SURFACE DEVICE INLET FT
KEY... P - P - FLUID PRESS.
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 76
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
SURFACE TEMPERATURE PLOT FOR LINK
100.0 TTTTTTTTTTTTTTTTTTTTT---+-----+-----+-----+-----+-----+-----+
| | TTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTT |
| | | | | |
| | | | | |
98.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
96.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
T | | | | | |
E | | | | | |
M 94.0 + | | | | +
P | | | | | |
E | | | | | |
R | | | | | |
A 92.0 +-----------+-----------+-----------+-----------+-----------+
T | | | | | |
U | | | | | |
R | | | | | |
E 90.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
88.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
D | | | | | |
E | | | | | |
G 86.0 + | | | | +
| | | | | |
F | | | | | |
| | | | | |
84.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
| | | | | |
| | | | | |
82.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
80.0 AAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAA-----+
0. 1000. 2000. 3000. 4000. 5000.
DIST. FROM 1ST SURFACE DEVICE INLET FT
KEY... T - T - FLUID TEMP. A - A - AMB. TEMP.
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 77
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
***************************CONTINUED****************************
LINK "L079" DEVICE DETAIL REPORT
HOLDUP AND VELOCITY DETAIL REPORT
---------------------------------
DEVICE
NAME ---LIQUID HOLDUP--- SUPERFICIAL T-D
AND SEG. NO LIQ GAS MIX . FLOW FLOW SONIC
TYPE NO. SLIP SLIP TOTAL VEL VEL VEL REGM REGM VEL
(ABBL) (FPS) (FPS) (FPS) (FPS)
------ ---- ----- ----- -------- ------- ------- ------- ---- ---- -------
P029 0000
(PIPE) 0001 1.00 1.00 36.5 5.75 0.00 5.75 ---- 1-PH 0.00
0002 1.00 1.00 73.1 5.75 0.00 5.75 ---- 1-PH 0.00
0003 1.00 1.00 109.6 5.75 0.00 5.75 ---- 1-PH 0.00
0004 1.00 1.00 146.1 5.75 0.00 5.75 ---- 1-PH 0.00
(MREG) 0000
R003 0001
P042 0000
(PIPE) 0001 1.00 1.00 5.294E-2 5.75 0.00 5.75 ---- 1-PH 0.00
0002 1.00 1.00 0.1 5.75 0.00 5.75 ---- 1-PH 0.00
0003 1.00 1.00 0.2 5.75 0.00 5.75 ---- 1-PH 0.00
0004 1.00 1.00 0.2 5.75 0.00 5.75 ---- 1-PH 0.00
PRESSURE GRADIENT DETAIL REPORT
-------------------------------
DEVICE
NAME
AND SEGM. --PRESSURE GRADIENT---- --PRESSURE CHANGE--
TYPE NO: FRIC ELEV TOTAL FRIC ELEV
(PSIFT) (PSIFT) (PSIFT) (PSIG) (PSIG)
------ ---- -------- -------- -------- -------- --------
P029 0000
(PIPE) 0001 -0.0090 0.0000 -0.0090 -10.2 0.0
0002 -0.0090 0.0000 -0.0090 -10.2 0.0
0003 -0.0090 0.0000 -0.0090 -10.2 0.0
0004 -0.0090 0.0000 -0.0090 -10.2 0.0
(MREG) 0000
R003 0001
P042 0000
(PIPE) 0001 -0.0090 0.0000 -0.0090 -1.48E-2 0.0
0002 -0.0090 0.0000 -0.0090 -1.48E-2 0.0
0003 -0.0090 0.0000 -0.0090 -1.48E-2 0.0
0004 -0.0090 0.0000 -0.0090 -1.48E-2 0.0
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 78
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
LINK "L079" PROPERTY DETAIL REPORT
VISCOSITY AND DENSITY RESULTS
-----------------------------
DEVICE
NAME
AND SEGM ----------VISCOSITY---------- ------------DENSITY------------
TYPE NO OIL LIQ VAP LIQ VAP SLIP NO-SLIP
(CP) (CP) (CP) (LB/CF) (LB/CF) (LB/CF) (LB/CF)
------ ---- --------- --------- --------- ------- ------- ------- -------
P029 0000
(PIPE) 0001 0.000 2.320 0.000 63.216 0.000 63.216 63.216
0002 0.000 2.321 0.000 63.216 0.000 63.216 63.216
0003 0.000 2.321 0.000 63.216 0.000 63.216 63.216
0004 0.000 2.322 0.000 63.216 0.000 63.216 63.216
R003 0000
(MREG) 0001
P042 0000
(PIPE) 0001 0.000 2.322 0.000 63.207 0.000 63.207 63.207
0002 0.000 2.322 0.000 63.207 0.000 63.207 63.207
0003 0.000 2.322 0.000 63.207 0.000 63.207 63.207
0004 0.000 2.322 0.000 63.207 0.000 63.207 63.207
FRICTION AND SURFACE TENSION RESULTS
------------------------------------
DEVICE
NAME LIQ
AND SEGM --------------FRICTION------------ FRIC. REYNOLDS SURFACE
TYPE NUM. DENSITY VELO ID. VISCOSITY FACTOR NUMBER TENSION
(LB/CF) (FPS) (IN) (CP) (DN/CM)
------ ---- ------- ------- -------- --------- -------- -------- --------
P029 0000
(PIPE) 0001 63.216 5.75 5.764 2.320 0.0192 1.1202E5 0.00
0002 63.216 5.75 5.764 2.321 0.0192 1.1199E5 0.00
0003 63.216 5.75 5.764 2.321 0.0192 1.1197E5 0.00
0004 63.216 5.75 5.764 2.322 0.0192 1.1194E5 0.00
R003 0000
(MREG) 0001
P042 0000
(PIPE) 0001 63.207 5.75 5.764 2.322 0.0192 1.1193E5 0.00
0002 63.207 5.75 5.764 2.322 0.0192 1.1193E5 0.00
0003 63.207 5.75 5.764 2.322 0.0192 1.1193E5 0.00
0004 63.207 5.75 5.764 2.322 0.0192 1.1193E5 0.00
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 79
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
***************************CONTINUED****************************
LINK "L079" PROPERTY DETAIL REPORT
HEAT TRANSFER CALCULATIONS
--------------------------
DEVICE FLUID
NAME THERMAL ----------THERMAL RESISTANCE-------
AND SEGM CONDUCT- INSIDE INSULAT- SURROUN-
(TYPE) NO: IVITY FILM PIPE ION DING
(BTUFTF) (HR-FT2- (HR-FT2- (HR-FT2- (HR-FT2-
F/BTU) F/BTU) F/BTU) F/BTU)
------ ---- -------- -------- -------- -------- --------
P029 0000
(PIPE) 0001 0.000 0.000 0.000 0.000 0.000
0002 0.000 0.000 0.000 0.000 0.000
0003 0.000 0.000 0.000 0.000 0.000
0004 0.000 0.000 0.000 0.000 0.000
R003 0000
(MREG) 0001
P042 0000
(PIPE) 0001 0.000 0.000 0.000 0.000 0.000
0002 0.000 0.000 0.000 0.000 0.000
0003 0.000 0.000 0.000 0.000 0.000
0004 0.000 0.000 0.000 0.000 0.000
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 80
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
LINK "L080" DEVICE DETAIL REPORT
PRESSURE AND TEMPERATURE REPORT
-------------------------------
DEVICE MWD OR TVD
NAME LENGTH I OR
AND SEGM INSIDE FROM & ELEV CALC CALC OVERALL AMB
TYPE NO DIAM. INLET O CHNG PRESS TEMP U-FACT TEMP
(IN) (FT) (FT) (PSIG) (F) (BTU/ (F)
HRFT2F)
------ ---- ------ --------- - -------- ------- ------ ------- ------
P030 0000 5.764 0.0 I 0.0 1288.7 100.0 80.0
(PIPE) 0001 1312.3 0.0 1276.9 99.8 1.000 80.0
0002 2624.7 0.0 1265.1 99.7 1.000 80.0
0003 3937.0 0.0 1253.2 99.5 1.000 80.0
0004 5249.3 O 0.0 1241.4 99.3 1.000 80.0
R004 0000 0.000 0.0 I 0.0 1241.4 99.3
(MREG) 0001 0.0 O 0.0 1200.1 99.3 0.000
P041 0000 5.764 0.0 I 0.0 1200.1 99.3 80.0
(PIPE) 0001 1.6 0.0 1200.0 99.3 1.000 80.0
0002 3.3 0.0 1200.0 99.3 1.000 80.0
0003 4.9 0.0 1200.0 99.3 1.000 80.0
0004 6.6 O 0.0 1200.0 99.3 1.000 80.0
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 81
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
SURFACE PRESSURE PLOT FOR LINK
1290. +-----+-----+-----+-----+-----+-----+-----+-----+-----+-----+
PP | | | | |
| PPP | | | | |
| PPPP | | | | |
1280. + PPP| | | | +
| PPP | | | |
| | PP | | | |
| | PPP | | | |
1270. +-----------+-------PPP-+-----------+-----------+-----------+
| | PP | | |
| | |PPP | | |
| | | PP | | |
P 1260. + | | PPP | | +
R | | | PPP| | |
E | | | PP | |
S | | | | PPP | |
S 1250. +-----------+-----------+-----------+----PPP----+-----------+
U | | | | PPPP| |
R | | | | PPP |
E | | | | | PP |
1240. + | | | | P +
| | | | | P |
| | | | | P |
| | | | | P |
P 1230. +-----------+-----------+-----------+-----------+---P-------+
S | | | | | P |
I | | | | | P |
G | | | | | P |
1220. + | | | | P +
| | | | | P |
| | | | | P |
| | | | | P |
1210. +-----------+-----------+-----------+-----------+---P-------+
| | | | | P |
| | | | | P |
| | | | | P |
1200. + | | | | PP +
| | | | | |
| | | | | |
| | | | | |
1190. +-----+-----+-----+-----+-----+-----+-----+-----+-----+-----+
0. 1200. 2400. 3600. 4800. 6000.
DIST. FROM 1ST SURFACE DEVICE INLET FT
KEY... P - P - FLUID PRESS.
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 82
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
SURFACE TEMPERATURE PLOT FOR LINK
100.0 TTTTTTTTTTTTTTTTTTTT----+-----+-----+-----+-----+-----+-----+
| | TTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTT |
| | | | | |
| | | | | |
98.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
96.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
T | | | | | |
E | | | | | |
M 94.0 + | | | | +
P | | | | | |
E | | | | | |
R | | | | | |
A 92.0 +-----------+-----------+-----------+-----------+-----------+
T | | | | | |
U | | | | | |
R | | | | | |
E 90.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
88.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
D | | | | | |
E | | | | | |
G 86.0 + | | | | +
| | | | | |
F | | | | | |
| | | | | |
84.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
| | | | | |
| | | | | |
82.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
80.0 AAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAA+-----+
0. 1200. 2400. 3600. 4800. 6000.
DIST. FROM 1ST SURFACE DEVICE INLET FT
KEY... T - T - FLUID TEMP. A - A - AMB. TEMP.
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 83
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
***************************CONTINUED****************************
LINK "L080" DEVICE DETAIL REPORT
HOLDUP AND VELOCITY DETAIL REPORT
---------------------------------
DEVICE
NAME ---LIQUID HOLDUP--- SUPERFICIAL T-D
AND SEG. NO LIQ GAS MIX . FLOW FLOW SONIC
TYPE NO. SLIP SLIP TOTAL VEL VEL VEL REGM REGM VEL
(ABBL) (FPS) (FPS) (FPS) (FPS)
------ ---- ----- ----- -------- ------- ------- ------- ---- ---- -------
P030 0000
(PIPE) 0001 1.00 1.00 42.4 5.75 0.00 5.75 ---- 1-PH 0.00
0002 1.00 1.00 84.7 5.75 0.00 5.75 ---- 1-PH 0.00
0003 1.00 1.00 127.1 5.75 0.00 5.75 ---- 1-PH 0.00
0004 1.00 1.00 169.4 5.75 0.00 5.75 ---- 1-PH 0.00
(MREG) 0000
R004 0001
P041 0000
(PIPE) 0001 1.00 1.00 5.294E-2 5.75 0.00 5.75 ---- 1-PH 0.00
0002 1.00 1.00 0.1 5.75 0.00 5.75 ---- 1-PH 0.00
0003 1.00 1.00 0.2 5.75 0.00 5.75 ---- 1-PH 0.00
0004 1.00 1.00 0.2 5.75 0.00 5.75 ---- 1-PH 0.00
PRESSURE GRADIENT DETAIL REPORT
-------------------------------
DEVICE
NAME
AND SEGM. --PRESSURE GRADIENT---- --PRESSURE CHANGE--
TYPE NO: FRIC ELEV TOTAL FRIC ELEV
(PSIFT) (PSIFT) (PSIFT) (PSIG) (PSIG)
------ ---- -------- -------- -------- -------- --------
P030 0000
(PIPE) 0001 -0.0090 0.0000 -0.0090 -11.8 0.0
0002 -0.0090 0.0000 -0.0090 -11.8 0.0
0003 -0.0090 0.0000 -0.0090 -11.8 0.0
0004 -0.0090 0.0000 -0.0090 -11.8 0.0
(MREG) 0000
R004 0001
P041 0000
(PIPE) 0001 -0.0090 0.0000 -0.0090 -1.48E-2 0.0
0002 -0.0090 0.0000 -0.0090 -1.48E-2 0.0
0003 -0.0090 0.0000 -0.0090 -1.48E-2 0.0
0004 -0.0090 0.0000 -0.0090 -1.48E-2 0.0
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 84
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
LINK "L080" PROPERTY DETAIL REPORT
VISCOSITY AND DENSITY RESULTS
-----------------------------
DEVICE
NAME
AND SEGM ----------VISCOSITY---------- ------------DENSITY------------
TYPE NO OIL LIQ VAP LIQ VAP SLIP NO-SLIP
(CP) (CP) (CP) (LB/CF) (LB/CF) (LB/CF) (LB/CF)
------ ---- --------- --------- --------- ------- ------- ------- -------
P030 0000
(PIPE) 0001 0.000 2.320 0.000 63.216 0.000 63.216 63.216
0002 0.000 2.321 0.000 63.216 0.000 63.216 63.216
0003 0.000 2.322 0.000 63.216 0.000 63.216 63.216
0004 0.000 2.322 0.000 63.216 0.000 63.216 63.216
R004 0000
(MREG) 0001
P041 0000
(PIPE) 0001 0.000 2.323 0.000 63.208 0.000 63.208 63.208
0002 0.000 2.323 0.000 63.208 0.000 63.208 63.208
0003 0.000 2.323 0.000 63.208 0.000 63.208 63.208
0004 0.000 2.323 0.000 63.208 0.000 63.208 63.208
FRICTION AND SURFACE TENSION RESULTS
------------------------------------
DEVICE
NAME LIQ
AND SEGM --------------FRICTION------------ FRIC. REYNOLDS SURFACE
TYPE NUM. DENSITY VELO ID. VISCOSITY FACTOR NUMBER TENSION
(LB/CF) (FPS) (IN) (CP) (DN/CM)
------ ---- ------- ------- -------- --------- -------- -------- --------
P030 0000
(PIPE) 0001 63.216 5.75 5.764 2.320 0.0192 1.1201E5 0.00
0002 63.216 5.75 5.764 2.321 0.0192 1.1198E5 0.00
0003 63.216 5.75 5.764 2.322 0.0192 1.1196E5 0.00
0004 63.216 5.75 5.764 2.322 0.0192 1.1193E5 0.00
R004 0000
(MREG) 0001
P041 0000
(PIPE) 0001 63.208 5.75 5.764 2.323 0.0192 1.1191E5 0.00
0002 63.208 5.75 5.764 2.323 0.0192 1.1191E5 0.00
0003 63.208 5.75 5.764 2.323 0.0192 1.1191E5 0.00
0004 63.208 5.75 5.764 2.323 0.0192 1.1191E5 0.00
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 85
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
***************************CONTINUED****************************
LINK "L080" PROPERTY DETAIL REPORT
HEAT TRANSFER CALCULATIONS
--------------------------
DEVICE FLUID
NAME THERMAL ----------THERMAL RESISTANCE-------
AND SEGM CONDUCT- INSIDE INSULAT- SURROUN-
(TYPE) NO: IVITY FILM PIPE ION DING
(BTUFTF) (HR-FT2- (HR-FT2- (HR-FT2- (HR-FT2-
F/BTU) F/BTU) F/BTU) F/BTU)
------ ---- -------- -------- -------- -------- --------
P030 0000
(PIPE) 0001 0.000 0.000 0.000 0.000 0.000
0002 0.000 0.000 0.000 0.000 0.000
0003 0.000 0.000 0.000 0.000 0.000
0004 0.000 0.000 0.000 0.000 0.000
R004 0000
(MREG) 0001
P041 0000
(PIPE) 0001 0.000 0.000 0.000 0.000 0.000
0002 0.000 0.000 0.000 0.000 0.000
0003 0.000 0.000 0.000 0.000 0.000
0004 0.000 0.000 0.000 0.000 0.000
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 86
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
LINK "L081" DEVICE DETAIL REPORT
PRESSURE AND TEMPERATURE REPORT
-------------------------------
DEVICE MWD OR TVD
NAME LENGTH I OR
AND SEGM INSIDE FROM & ELEV CALC CALC OVERALL AMB
TYPE NO DIAM. INLET O CHNG PRESS TEMP U-FACT TEMP
(IN) (FT) (FT) (PSIG) (F) (BTU/ (F)
HRFT2F)
------ ---- ------ --------- - -------- ------- ------ ------- ------
P031 0000 5.764 0.0 I 0.0 1288.7 100.0 80.0
(PIPE) 0001 2000.0 0.0 1270.7 99.7 1.000 80.0
0002 4000.0 0.0 1252.7 99.5 1.000 80.0
0003 6000.0 0.0 1234.6 99.2 1.000 80.0
0004 8000.0 0.0 1216.6 99.0 1.000 80.0
0005 10000.0 0.0 1198.6 98.8 1.000 80.0
0006 12000.0 0.0 1180.5 98.5 1.000 80.0
0007 14000.0 0.0 1162.5 98.3 1.000 80.0
0008 14042.0 O 0.0 1162.1 98.3 1.000 80.0
R005 0000 0.000 0.0 I 0.0 1162.1 98.3
(MREG) 0001 0.0 O 0.0 1200.1 98.3 0.000
P045 0000 5.764 0.0 I 0.0 1200.1 98.3 80.0
(PIPE) 0001 1.6 0.0 1200.0 98.3 1.000 80.0
0002 3.3 0.0 1200.0 98.3 1.000 80.0
0003 4.9 0.0 1200.0 98.3 1.000 80.0
0004 6.6 O 0.0 1200.0 98.3 1.000 80.0
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 87
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
SURFACE PRESSURE PLOT FOR LINK
1305. +-----+-----+-----+-----+-----+-----+-----+-----+-----+-----+
| | | | | |
| | | | | |
| | | | | |
1290. P | | | | +
|PP | | | | |
| PP | | | | |
| P | | | | |
1275. +-----PP----+-----------+-----------+-----------+-----------+
| P | | | | |
| PP | | | | |
| PP | | | |
P 1260. + |P | | | +
R | | PP | | | |
E | | P | | | |
S | | PP | | | |
S 1245. +-----------+------PP---+-----------+-----------+-----------+
U | | P | | | |
R | | PP| | | |
E | | P | | |
1230. + | |PP | | +
| | | PP | | |
| | | P | | |
| | | PP | | |
P 1215. +-----------+-----------+-------PP--+-----------+-----------+
S | | | PP| | |
I | | | PP | |
G | | | | PP | |
1200. + | | | P | P +
| | | | PP | P |
| | | | PP | P |
| | | | P | P |
1185. +-----------+-----------+-----------+---------PP+-------P---+
| | | | P P |
| | | | |PP P |
| | | | | PP P |
1170. + | | | | P P +
| | | | | PPP |
| | | | | P |
| | | | | |
1155. +-----+-----+-----+-----+-----+-----+-----+-----+-----+-----+
0.0 3.0 6.0 9.0 12.0 15.0
DIST. FROM 1ST SURFACE DEVICE INLET FT (10**3)
KEY... P - P - FLUID PRESS.
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 88
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
SURFACE TEMPERATURE PLOT FOR LINK
100.0 TTTTT-+-----+-----+-----+-----+-----+-----+-----+-----+-----+
| TTTTTTTTTTTTTTTT | | | |
| | TTTTTTTTTTTTTTTTTTTTTTTT | |
| | | | TTTTTTTTTTTT |
98.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
96.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
T | | | | | |
E | | | | | |
M 94.0 + | | | | +
P | | | | | |
E | | | | | |
R | | | | | |
A 92.0 +-----------+-----------+-----------+-----------+-----------+
T | | | | | |
U | | | | | |
R | | | | | |
E 90.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
88.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
D | | | | | |
E | | | | | |
G 86.0 + | | | | +
| | | | | |
F | | | | | |
| | | | | |
84.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
| | | | | |
| | | | | |
82.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
80.0 AAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAA---+
0.0 3.0 6.0 9.0 12.0 15.0
DIST. FROM 1ST SURFACE DEVICE INLET FT (10**3)
KEY... T - T - FLUID TEMP. A - A - AMB. TEMP.
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 89
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
***************************CONTINUED****************************
LINK "L081" DEVICE DETAIL REPORT
HOLDUP AND VELOCITY DETAIL REPORT
---------------------------------
DEVICE
NAME ---LIQUID HOLDUP--- SUPERFICIAL T-D
AND SEG. NO LIQ GAS MIX . FLOW FLOW SONIC
TYPE NO. SLIP SLIP TOTAL VEL VEL VEL REGM REGM VEL
(ABBL) (FPS) (FPS) (FPS) (FPS)
------ ---- ----- ----- -------- ------- ------- ------- ---- ---- -------
P031 0000
(PIPE) 0001 1.00 1.00 64.5 5.75 0.00 5.75 ---- 1-PH 0.00
0002 1.00 1.00 129.1 5.75 0.00 5.75 ---- 1-PH 0.00
0003 1.00 1.00 193.6 5.75 0.00 5.75 ---- 1-PH 0.00
0004 1.00 1.00 258.2 5.75 0.00 5.75 ---- 1-PH 0.00
0005 1.00 1.00 322.7 5.75 0.00 5.75 ---- 1-PH 0.00
0006 1.00 1.00 387.3 5.75 0.00 5.75 ---- 1-PH 0.00
0007 1.00 1.00 451.8 5.75 0.00 5.75 ---- 1-PH 0.00
0008 1.00 1.00 453.2 5.75 0.00 5.75 ---- 1-PH 0.00
(MREG) 0000
R005 0001
P045 0000
(PIPE) 0001 1.00 1.00 5.294E-2 5.75 0.00 5.75 ---- 1-PH 0.00
0002 1.00 1.00 0.1 5.75 0.00 5.75 ---- 1-PH 0.00
0003 1.00 1.00 0.2 5.75 0.00 5.75 ---- 1-PH 0.00
0004 1.00 1.00 0.2 5.75 0.00 5.75 ---- 1-PH 0.00
PRESSURE GRADIENT DETAIL REPORT
-------------------------------
DEVICE
NAME
AND SEGM. --PRESSURE GRADIENT---- --PRESSURE CHANGE--
TYPE NO: FRIC ELEV TOTAL FRIC ELEV
(PSIFT) (PSIFT) (PSIFT) (PSIG) (PSIG)
------ ---- -------- -------- -------- -------- --------
P031 0000
(PIPE) 0001 -0.0090 0.0000 -0.0090 -18.0 0.0
0002 -0.0090 0.0000 -0.0090 -18.0 0.0
0003 -0.0090 0.0000 -0.0090 -18.0 0.0
0004 -0.0090 0.0000 -0.0090 -18.0 0.0
0005 -0.0090 0.0000 -0.0090 -18.0 0.0
0006 -0.0090 0.0000 -0.0090 -18.0 0.0
0007 -0.0090 0.0000 -0.0090 -18.0 0.0
0008 -0.0090 0.0000 -0.0090 -0.4 0.0
(MREG) 0000
R005 0001
P045 0000
(PIPE) 0001 -0.0090 0.0000 -0.0090 -1.48E-2 0.0
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 90
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
**************************CONTINUED****************************
LINK "L081" DEVICE DETAIL REPORT
PRESSURE GRADIENT DETAIL REPORT
-------------------------------
DEVICE
NAME
AND SEGM. --PRESSURE GRADIENT---- --PRESSURE CHANGE--
TYPE NO: FRIC ELEV TOTAL FRIC ELEV
(PSIFT) (PSIFT) (PSIFT) (PSIG) (PSIG)
------ ---- -------- -------- -------- -------- --------
0002 -0.0090 0.0000 -0.0090 -1.48E-2 0.0
0003 -0.0090 0.0000 -0.0090 -1.48E-2 0.0
0004 -0.0090 0.0000 -0.0090 -1.48E-2 0.0
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 91
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
LINK "L081" PROPERTY DETAIL REPORT
VISCOSITY AND DENSITY RESULTS
-----------------------------
DEVICE
NAME
AND SEGM ----------VISCOSITY---------- ------------DENSITY------------
TYPE NO OIL LIQ VAP LIQ VAP SLIP NO-SLIP
(CP) (CP) (CP) (LB/CF) (LB/CF) (LB/CF) (LB/CF)
------ ---- --------- --------- --------- ------- ------- ------- -------
P031 0000
(PIPE) 0001 0.000 2.321 0.000 63.216 0.000 63.216 63.216
0002 0.000 2.321 0.000 63.216 0.000 63.216 63.216
0003 0.000 2.322 0.000 63.216 0.000 63.216 63.216
0004 0.000 2.323 0.000 63.216 0.000 63.216 63.216
0005 0.000 2.324 0.000 63.216 0.000 63.216 63.216
0006 0.000 2.325 0.000 63.215 0.000 63.215 63.215
0007 0.000 2.326 0.000 63.215 0.000 63.215 63.215
0008 0.000 2.326 0.000 63.215 0.000 63.215 63.215
R005 0000
(MREG) 0001
P045 0000
(PIPE) 0001 0.000 2.326 0.000 63.222 0.000 63.222 63.222
0002 0.000 2.326 0.000 63.222 0.000 63.222 63.222
0003 0.000 2.326 0.000 63.222 0.000 63.222 63.222
0004 0.000 2.326 0.000 63.222 0.000 63.222 63.222
FRICTION AND SURFACE TENSION RESULTS
------------------------------------
DEVICE
NAME LIQ
AND SEGM --------------FRICTION------------ FRIC. REYNOLDS SURFACE
TYPE NUM. DENSITY VELO ID. VISCOSITY FACTOR NUMBER TENSION
(LB/CF) (FPS) (IN) (CP) (DN/CM)
------ ---- ------- ------- -------- --------- -------- -------- --------
P031 0000
(PIPE) 0001 63.216 5.75 5.764 2.321 0.0192 1.1201E5 0.00
0002 63.216 5.75 5.764 2.321 0.0192 1.1196E5 0.00
0003 63.216 5.75 5.764 2.322 0.0192 1.1192E5 0.00
0004 63.216 5.75 5.764 2.323 0.0192 1.1187E5 0.00
0005 63.216 5.75 5.764 2.324 0.0192 1.1183E5 0.00
0006 63.215 5.75 5.764 2.325 0.0192 1.1179E5 0.00
0007 63.215 5.75 5.764 2.326 0.0192 1.1174E5 0.00
0008 63.215 5.75 5.764 2.326 0.0192 1.1172E5 0.00
R005 0000
(MREG) 0001
P045 0000
(PIPE) 0001 63.222 5.75 5.764 2.326 0.0192 1.1172E5 0.00
0002 63.222 5.75 5.764 2.326 0.0192 1.1172E5 0.00
0003 63.222 5.75 5.764 2.326 0.0192 1.1172E5 0.00
0004 63.222 5.75 5.764 2.326 0.0192 1.1172E5 0.00
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 92
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
***************************CONTINUED****************************
LINK "L081" PROPERTY DETAIL REPORT
HEAT TRANSFER CALCULATIONS
--------------------------
DEVICE FLUID
NAME THERMAL ----------THERMAL RESISTANCE-------
AND SEGM CONDUCT- INSIDE INSULAT- SURROUN-
(TYPE) NO: IVITY FILM PIPE ION DING
(BTUFTF) (HR-FT2- (HR-FT2- (HR-FT2- (HR-FT2-
F/BTU) F/BTU) F/BTU) F/BTU)
------ ---- -------- -------- -------- -------- --------
P031 0000
(PIPE) 0001 0.000 0.000 0.000 0.000 0.000
0002 0.000 0.000 0.000 0.000 0.000
0003 0.000 0.000 0.000 0.000 0.000
0004 0.000 0.000 0.000 0.000 0.000
0005 0.000 0.000 0.000 0.000 0.000
0006 0.000 0.000 0.000 0.000 0.000
0007 0.000 0.000 0.000 0.000 0.000
0008 0.000 0.000 0.000 0.000 0.000
R005 0000
(MREG) 0001
P045 0000
(PIPE) 0001 0.000 0.000 0.000 0.000 0.000
0002 0.000 0.000 0.000 0.000 0.000
0003 0.000 0.000 0.000 0.000 0.000
0004 0.000 0.000 0.000 0.000 0.000
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 93
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
LINK "L083" DEVICE DETAIL REPORT
PRESSURE AND TEMPERATURE REPORT
-------------------------------
DEVICE MWD OR TVD
NAME LENGTH I OR
AND SEGM INSIDE FROM & ELEV CALC CALC OVERALL AMB
TYPE NO DIAM. INLET O CHNG PRESS TEMP U-FACT TEMP
(IN) (FT) (FT) (PSIG) (F) (BTU/ (F)
HRFT2F)
------ ---- ------ --------- - -------- ------- ------ ------- ------
P032 0000 5.764 0.0 I 0.0 1288.7 100.0 80.0
(PIPE) 0001 2000.0 0.0 1270.7 99.7 1.000 80.0
0002 4000.0 0.0 1252.7 99.5 1.000 80.0
0003 6000.0 0.0 1234.6 99.2 1.000 80.0
0004 8000.0 0.0 1216.6 99.0 1.000 80.0
0005 9842.5 O 0.0 1200.0 98.8 1.000 80.0
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 94
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
SURFACE PRESSURE PLOT FOR LINK
1290. +-----+-----+-----+-----+-----+-----+-----+-----+-----+-----+
P | | | | |
|PP | | | | |
| PP | | | | |
1280. + PP | | | | +
| P | | | | |
| PP | | | | |
| PP| | | | |
1270. +-----------P-----------+-----------+-----------+-----------+
| |PP | | | |
| | PP | | | |
| | PP | | | |
P 1260. + | P | | | +
R | | PP | | | |
E | | PP| | | |
S | | P | | |
S 1250. +-----------+-----------+PP---------+-----------+-----------+
U | | | PP | | |
R | | | PP | | |
E | | | P | | |
1240. + | | PP | | +
| | | PP| | |
| | | P | |
| | | |PP | |
P 1230. +-----------+-----------+-----------+--PP-------+-----------+
S | | | | PP | |
I | | | | P | |
G | | | | PP | |
1220. + | | | PP| +
| | | | P |
| | | | |PP |
| | | | | P |
1210. +-----------+-----------+-----------+-----------+---PP------+
| | | | | PP |
| | | | | P |
| | | | | PP |
1200. + | | | | P+
| | | | | |
| | | | | |
| | | | | |
1190. +-----+-----+-----+-----+-----+-----+-----+-----+-----+-----+
0.0 2.0 4.0 6.0 8.0 10.0
DIST. FROM 1ST SURFACE DEVICE INLET FT (10**3)
KEY... P - P - FLUID PRESS.
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 95
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
SURFACE TEMPERATURE PLOT FOR LINK
100.0 TTTTTTT-----+-----+-----+-----+-----+-----+-----+-----+-----+
| TTTTTTTTTTTTTTTTTTTTTTTT | | |
| | | TTTTTTTTTTTTTTTTTTTTTTTTTTTTT|
| | | | | |
98.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
96.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
T | | | | | |
E | | | | | |
M 94.0 + | | | | +
P | | | | | |
E | | | | | |
R | | | | | |
A 92.0 +-----------+-----------+-----------+-----------+-----------+
T | | | | | |
U | | | | | |
R | | | | | |
E 90.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
88.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
D | | | | | |
E | | | | | |
G 86.0 + | | | | +
| | | | | |
F | | | | | |
| | | | | |
84.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
| | | | | |
| | | | | |
82.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
80.0 AAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAA+
0.0 2.0 4.0 6.0 8.0 10.0
DIST. FROM 1ST SURFACE DEVICE INLET FT (10**3)
KEY... T - T - FLUID TEMP. A - A - AMB. TEMP.
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 96
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
***************************CONTINUED****************************
LINK "L083" DEVICE DETAIL REPORT
HOLDUP AND VELOCITY DETAIL REPORT
---------------------------------
DEVICE
NAME ---LIQUID HOLDUP--- SUPERFICIAL T-D
AND SEG. NO LIQ GAS MIX . FLOW FLOW SONIC
TYPE NO. SLIP SLIP TOTAL VEL VEL VEL REGM REGM VEL
(ABBL) (FPS) (FPS) (FPS) (FPS)
------ ---- ----- ----- -------- ------- ------- ------- ---- ---- -------
P032 0000
(PIPE) 0001 1.00 1.00 64.5 5.75 0.00 5.75 ---- 1-PH 0.00
0002 1.00 1.00 129.1 5.75 0.00 5.75 ---- 1-PH 0.00
0003 1.00 1.00 193.6 5.75 0.00 5.75 ---- 1-PH 0.00
0004 1.00 1.00 258.2 5.75 0.00 5.75 ---- 1-PH 0.00
0005 1.00 1.00 317.6 5.75 0.00 5.75 ---- 1-PH 0.00
PRESSURE GRADIENT DETAIL REPORT
-------------------------------
DEVICE
NAME
AND SEGM. --PRESSURE GRADIENT---- --PRESSURE CHANGE--
TYPE NO: FRIC ELEV TOTAL FRIC ELEV
(PSIFT) (PSIFT) (PSIFT) (PSIG) (PSIG)
------ ---- -------- -------- -------- -------- --------
P032 0000
(PIPE) 0001 -0.0090 0.0000 -0.0090 -18.0 0.0
0002 -0.0090 0.0000 -0.0090 -18.0 0.0
0003 -0.0090 0.0000 -0.0090 -18.0 0.0
0004 -0.0090 0.0000 -0.0090 -18.0 0.0
0005 -0.0090 0.0000 -0.0090 -16.6 0.0
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 97
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
LINK "L083" PROPERTY DETAIL REPORT
VISCOSITY AND DENSITY RESULTS
-----------------------------
DEVICE
NAME
AND SEGM ----------VISCOSITY---------- ------------DENSITY------------
TYPE NO OIL LIQ VAP LIQ VAP SLIP NO-SLIP
(CP) (CP) (CP) (LB/CF) (LB/CF) (LB/CF) (LB/CF)
------ ---- --------- --------- --------- ------- ------- ------- -------
P032 0000
(PIPE) 0001 0.000 2.321 0.000 63.216 0.000 63.216 63.216
0002 0.000 2.321 0.000 63.216 0.000 63.216 63.216
0003 0.000 2.322 0.000 63.216 0.000 63.216 63.216
0004 0.000 2.323 0.000 63.216 0.000 63.216 63.216
0005 0.000 2.324 0.000 63.216 0.000 63.216 63.216
FRICTION AND SURFACE TENSION RESULTS
------------------------------------
DEVICE
NAME LIQ
AND SEGM --------------FRICTION------------ FRIC. REYNOLDS SURFACE
TYPE NUM. DENSITY VELO ID. VISCOSITY FACTOR NUMBER TENSION
(LB/CF) (FPS) (IN) (CP) (DN/CM)
------ ---- ------- ------- -------- --------- -------- -------- --------
P032 0000
(PIPE) 0001 63.216 5.75 5.764 2.321 0.0192 1.1201E5 0.00
0002 63.216 5.75 5.764 2.321 0.0192 1.1196E5 0.00
0003 63.216 5.75 5.764 2.322 0.0192 1.1192E5 0.00
0004 63.216 5.75 5.764 2.323 0.0192 1.1187E5 0.00
0005 63.216 5.75 5.764 2.324 0.0192 1.1183E5 0.00
HEAT TRANSFER CALCULATIONS
--------------------------
DEVICE FLUID
NAME THERMAL ----------THERMAL RESISTANCE-------
AND SEGM CONDUCT- INSIDE INSULAT- SURROUN-
(TYPE) NO: IVITY FILM PIPE ION DING
(BTUFTF) (HR-FT2- (HR-FT2- (HR-FT2- (HR-FT2-
F/BTU) F/BTU) F/BTU) F/BTU)
------ ---- -------- -------- -------- -------- --------
P032 0000
(PIPE) 0001 0.000 0.000 0.000 0.000 0.000
0002 0.000 0.000 0.000 0.000 0.000
0003 0.000 0.000 0.000 0.000 0.000
0004 0.000 0.000 0.000 0.000 0.000
0005 0.000 0.000 0.000 0.000 0.000
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 98
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
LINK "L084" DEVICE DETAIL REPORT
PRESSURE AND TEMPERATURE REPORT
-------------------------------
DEVICE MWD OR TVD
NAME LENGTH I OR
AND SEGM INSIDE FROM & ELEV CALC CALC OVERALL AMB
TYPE NO DIAM. INLET O CHNG PRESS TEMP U-FACT TEMP
(IN) (FT) (FT) (PSIG) (F) (BTU/ (F)
HRFT2F)
------ ---- ------ --------- - -------- ------- ------ ------- ------
P033 0000 5.764 0.0 I 0.0 1288.7 100.0 80.0
(PIPE) 0001 2000.0 0.0 1270.7 99.7 1.000 80.0
0002 4000.0 0.0 1252.7 99.5 1.000 80.0
0003 6000.0 0.0 1234.6 99.2 1.000 80.0
0004 8000.0 0.0 1216.6 99.0 1.000 80.0
0005 9842.5 O 0.0 1200.0 98.8 1.000 80.0
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 99
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
SURFACE PRESSURE PLOT FOR LINK
1290. +-----+-----+-----+-----+-----+-----+-----+-----+-----+-----+
P | | | | |
|PP | | | | |
| PP | | | | |
1280. + PP | | | | +
| P | | | | |
| PP | | | | |
| PP| | | | |
1270. +-----------P-----------+-----------+-----------+-----------+
| |PP | | | |
| | PP | | | |
| | PP | | | |
P 1260. + | P | | | +
R | | PP | | | |
E | | PP| | | |
S | | P | | |
S 1250. +-----------+-----------+PP---------+-----------+-----------+
U | | | PP | | |
R | | | PP | | |
E | | | P | | |
1240. + | | PP | | +
| | | PP| | |
| | | P | |
| | | |PP | |
P 1230. +-----------+-----------+-----------+--PP-------+-----------+
S | | | | PP | |
I | | | | P | |
G | | | | PP | |
1220. + | | | PP| +
| | | | P |
| | | | |PP |
| | | | | P |
1210. +-----------+-----------+-----------+-----------+---PP------+
| | | | | PP |
| | | | | P |
| | | | | PP |
1200. + | | | | P+
| | | | | |
| | | | | |
| | | | | |
1190. +-----+-----+-----+-----+-----+-----+-----+-----+-----+-----+
0.0 2.0 4.0 6.0 8.0 10.0
DIST. FROM 1ST SURFACE DEVICE INLET FT (10**3)
KEY... P - P - FLUID PRESS.
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 100
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
SURFACE TEMPERATURE PLOT FOR LINK
100.0 TTTTTTT-----+-----+-----+-----+-----+-----+-----+-----+-----+
| TTTTTTTTTTTTTTTTTTTTTTTT | | |
| | | TTTTTTTTTTTTTTTTTTTTTTTTTTTTT|
| | | | | |
98.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
96.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
T | | | | | |
E | | | | | |
M 94.0 + | | | | +
P | | | | | |
E | | | | | |
R | | | | | |
A 92.0 +-----------+-----------+-----------+-----------+-----------+
T | | | | | |
U | | | | | |
R | | | | | |
E 90.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
88.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
D | | | | | |
E | | | | | |
G 86.0 + | | | | +
| | | | | |
F | | | | | |
| | | | | |
84.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
| | | | | |
| | | | | |
82.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
80.0 AAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAA+
0.0 2.0 4.0 6.0 8.0 10.0
DIST. FROM 1ST SURFACE DEVICE INLET FT (10**3)
KEY... T - T - FLUID TEMP. A - A - AMB. TEMP.
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 101
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
***************************CONTINUED****************************
LINK "L084" DEVICE DETAIL REPORT
HOLDUP AND VELOCITY DETAIL REPORT
---------------------------------
DEVICE
NAME ---LIQUID HOLDUP--- SUPERFICIAL T-D
AND SEG. NO LIQ GAS MIX . FLOW FLOW SONIC
TYPE NO. SLIP SLIP TOTAL VEL VEL VEL REGM REGM VEL
(ABBL) (FPS) (FPS) (FPS) (FPS)
------ ---- ----- ----- -------- ------- ------- ------- ---- ---- -------
P033 0000
(PIPE) 0001 1.00 1.00 64.5 5.75 0.00 5.75 ---- 1-PH 0.00
0002 1.00 1.00 129.1 5.75 0.00 5.75 ---- 1-PH 0.00
0003 1.00 1.00 193.6 5.75 0.00 5.75 ---- 1-PH 0.00
0004 1.00 1.00 258.2 5.75 0.00 5.75 ---- 1-PH 0.00
0005 1.00 1.00 317.6 5.75 0.00 5.75 ---- 1-PH 0.00
PRESSURE GRADIENT DETAIL REPORT
-------------------------------
DEVICE
NAME
AND SEGM. --PRESSURE GRADIENT---- --PRESSURE CHANGE--
TYPE NO: FRIC ELEV TOTAL FRIC ELEV
(PSIFT) (PSIFT) (PSIFT) (PSIG) (PSIG)
------ ---- -------- -------- -------- -------- --------
P033 0000
(PIPE) 0001 -0.0090 0.0000 -0.0090 -18.0 0.0
0002 -0.0090 0.0000 -0.0090 -18.0 0.0
0003 -0.0090 0.0000 -0.0090 -18.0 0.0
0004 -0.0090 0.0000 -0.0090 -18.0 0.0
0005 -0.0090 0.0000 -0.0090 -16.6 0.0
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 102
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
LINK "L084" PROPERTY DETAIL REPORT
VISCOSITY AND DENSITY RESULTS
-----------------------------
DEVICE
NAME
AND SEGM ----------VISCOSITY---------- ------------DENSITY------------
TYPE NO OIL LIQ VAP LIQ VAP SLIP NO-SLIP
(CP) (CP) (CP) (LB/CF) (LB/CF) (LB/CF) (LB/CF)
------ ---- --------- --------- --------- ------- ------- ------- -------
P033 0000
(PIPE) 0001 0.000 2.321 0.000 63.216 0.000 63.216 63.216
0002 0.000 2.321 0.000 63.216 0.000 63.216 63.216
0003 0.000 2.322 0.000 63.216 0.000 63.216 63.216
0004 0.000 2.323 0.000 63.216 0.000 63.216 63.216
0005 0.000 2.324 0.000 63.216 0.000 63.216 63.216
FRICTION AND SURFACE TENSION RESULTS
------------------------------------
DEVICE
NAME LIQ
AND SEGM --------------FRICTION------------ FRIC. REYNOLDS SURFACE
TYPE NUM. DENSITY VELO ID. VISCOSITY FACTOR NUMBER TENSION
(LB/CF) (FPS) (IN) (CP) (DN/CM)
------ ---- ------- ------- -------- --------- -------- -------- --------
P033 0000
(PIPE) 0001 63.216 5.75 5.764 2.321 0.0192 1.1201E5 0.00
0002 63.216 5.75 5.764 2.321 0.0192 1.1196E5 0.00
0003 63.216 5.75 5.764 2.322 0.0192 1.1192E5 0.00
0004 63.216 5.75 5.764 2.323 0.0192 1.1187E5 0.00
0005 63.216 5.75 5.764 2.324 0.0192 1.1183E5 0.00
HEAT TRANSFER CALCULATIONS
--------------------------
DEVICE FLUID
NAME THERMAL ----------THERMAL RESISTANCE-------
AND SEGM CONDUCT- INSIDE INSULAT- SURROUN-
(TYPE) NO: IVITY FILM PIPE ION DING
(BTUFTF) (HR-FT2- (HR-FT2- (HR-FT2- (HR-FT2-
F/BTU) F/BTU) F/BTU) F/BTU)
------ ---- -------- -------- -------- -------- --------
P033 0000
(PIPE) 0001 0.000 0.000 0.000 0.000 0.000
0002 0.000 0.000 0.000 0.000 0.000
0003 0.000 0.000 0.000 0.000 0.000
0004 0.000 0.000 0.000 0.000 0.000
0005 0.000 0.000 0.000 0.000 0.000
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 103
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
LINK "L086" DEVICE DETAIL REPORT
PRESSURE AND TEMPERATURE REPORT
-------------------------------
DEVICE MWD OR TVD
NAME LENGTH I OR
AND SEGM INSIDE FROM & ELEV CALC CALC OVERALL AMB
TYPE NO DIAM. INLET O CHNG PRESS TEMP U-FACT TEMP
(IN) (FT) (FT) (PSIG) (F) (BTU/ (F)
HRFT2F)
------ ---- ------ --------- - -------- ------- ------ ------- ------
P034 0000 5.764 0.0 I 0.0 1288.7 100.0 80.0
(PIPE) 0001 2000.0 0.0 1270.7 99.7 1.000 80.0
0002 4000.0 0.0 1252.7 99.5 1.000 80.0
0003 6000.0 0.0 1234.6 99.2 1.000 80.0
0004 8000.0 0.0 1216.6 99.0 1.000 80.0
0005 9842.5 O 0.0 1200.0 98.8 1.000 80.0
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 104
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
SURFACE PRESSURE PLOT FOR LINK
1290. +-----+-----+-----+-----+-----+-----+-----+-----+-----+-----+
P | | | | |
|PP | | | | |
| PP | | | | |
1280. + PP | | | | +
| P | | | | |
| PP | | | | |
| PP| | | | |
1270. +-----------P-----------+-----------+-----------+-----------+
| |PP | | | |
| | PP | | | |
| | PP | | | |
P 1260. + | P | | | +
R | | PP | | | |
E | | PP| | | |
S | | P | | |
S 1250. +-----------+-----------+PP---------+-----------+-----------+
U | | | PP | | |
R | | | PP | | |
E | | | P | | |
1240. + | | PP | | +
| | | PP| | |
| | | P | |
| | | |PP | |
P 1230. +-----------+-----------+-----------+--PP-------+-----------+
S | | | | PP | |
I | | | | P | |
G | | | | PP | |
1220. + | | | PP| +
| | | | P |
| | | | |PP |
| | | | | P |
1210. +-----------+-----------+-----------+-----------+---PP------+
| | | | | PP |
| | | | | P |
| | | | | PP |
1200. + | | | | P+
| | | | | |
| | | | | |
| | | | | |
1190. +-----+-----+-----+-----+-----+-----+-----+-----+-----+-----+
0.0 2.0 4.0 6.0 8.0 10.0
DIST. FROM 1ST SURFACE DEVICE INLET FT (10**3)
KEY... P - P - FLUID PRESS.
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 105
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
SURFACE TEMPERATURE PLOT FOR LINK
100.0 TTTTTTT-----+-----+-----+-----+-----+-----+-----+-----+-----+
| TTTTTTTTTTTTTTTTTTTTTTTT | | |
| | | TTTTTTTTTTTTTTTTTTTTTTTTTTTTT|
| | | | | |
98.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
96.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
T | | | | | |
E | | | | | |
M 94.0 + | | | | +
P | | | | | |
E | | | | | |
R | | | | | |
A 92.0 +-----------+-----------+-----------+-----------+-----------+
T | | | | | |
U | | | | | |
R | | | | | |
E 90.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
88.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
D | | | | | |
E | | | | | |
G 86.0 + | | | | +
| | | | | |
F | | | | | |
| | | | | |
84.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
| | | | | |
| | | | | |
82.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
80.0 AAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAA+
0.0 2.0 4.0 6.0 8.0 10.0
DIST. FROM 1ST SURFACE DEVICE INLET FT (10**3)
KEY... T - T - FLUID TEMP. A - A - AMB. TEMP.
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 106
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
***************************CONTINUED****************************
LINK "L086" DEVICE DETAIL REPORT
HOLDUP AND VELOCITY DETAIL REPORT
---------------------------------
DEVICE
NAME ---LIQUID HOLDUP--- SUPERFICIAL T-D
AND SEG. NO LIQ GAS MIX . FLOW FLOW SONIC
TYPE NO. SLIP SLIP TOTAL VEL VEL VEL REGM REGM VEL
(ABBL) (FPS) (FPS) (FPS) (FPS)
------ ---- ----- ----- -------- ------- ------- ------- ---- ---- -------
P034 0000
(PIPE) 0001 1.00 1.00 64.5 5.75 0.00 5.75 ---- 1-PH 0.00
0002 1.00 1.00 129.1 5.75 0.00 5.75 ---- 1-PH 0.00
0003 1.00 1.00 193.6 5.75 0.00 5.75 ---- 1-PH 0.00
0004 1.00 1.00 258.2 5.75 0.00 5.75 ---- 1-PH 0.00
0005 1.00 1.00 317.6 5.75 0.00 5.75 ---- 1-PH 0.00
PRESSURE GRADIENT DETAIL REPORT
-------------------------------
DEVICE
NAME
AND SEGM. --PRESSURE GRADIENT---- --PRESSURE CHANGE--
TYPE NO: FRIC ELEV TOTAL FRIC ELEV
(PSIFT) (PSIFT) (PSIFT) (PSIG) (PSIG)
------ ---- -------- -------- -------- -------- --------
P034 0000
(PIPE) 0001 -0.0090 0.0000 -0.0090 -18.0 0.0
0002 -0.0090 0.0000 -0.0090 -18.0 0.0
0003 -0.0090 0.0000 -0.0090 -18.0 0.0
0004 -0.0090 0.0000 -0.0090 -18.0 0.0
0005 -0.0090 0.0000 -0.0090 -16.6 0.0
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 107
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
LINK "L086" PROPERTY DETAIL REPORT
VISCOSITY AND DENSITY RESULTS
-----------------------------
DEVICE
NAME
AND SEGM ----------VISCOSITY---------- ------------DENSITY------------
TYPE NO OIL LIQ VAP LIQ VAP SLIP NO-SLIP
(CP) (CP) (CP) (LB/CF) (LB/CF) (LB/CF) (LB/CF)
------ ---- --------- --------- --------- ------- ------- ------- -------
P034 0000
(PIPE) 0001 0.000 2.321 0.000 63.216 0.000 63.216 63.216
0002 0.000 2.321 0.000 63.216 0.000 63.216 63.216
0003 0.000 2.322 0.000 63.216 0.000 63.216 63.216
0004 0.000 2.323 0.000 63.216 0.000 63.216 63.216
0005 0.000 2.324 0.000 63.216 0.000 63.216 63.216
FRICTION AND SURFACE TENSION RESULTS
------------------------------------
DEVICE
NAME LIQ
AND SEGM --------------FRICTION------------ FRIC. REYNOLDS SURFACE
TYPE NUM. DENSITY VELO ID. VISCOSITY FACTOR NUMBER TENSION
(LB/CF) (FPS) (IN) (CP) (DN/CM)
------ ---- ------- ------- -------- --------- -------- -------- --------
P034 0000
(PIPE) 0001 63.216 5.75 5.764 2.321 0.0192 1.1201E5 0.00
0002 63.216 5.75 5.764 2.321 0.0192 1.1196E5 0.00
0003 63.216 5.75 5.764 2.322 0.0192 1.1192E5 0.00
0004 63.216 5.75 5.764 2.323 0.0192 1.1187E5 0.00
0005 63.216 5.75 5.764 2.324 0.0192 1.1183E5 0.00
HEAT TRANSFER CALCULATIONS
--------------------------
DEVICE FLUID
NAME THERMAL ----------THERMAL RESISTANCE-------
AND SEGM CONDUCT- INSIDE INSULAT- SURROUN-
(TYPE) NO: IVITY FILM PIPE ION DING
(BTUFTF) (HR-FT2- (HR-FT2- (HR-FT2- (HR-FT2-
F/BTU) F/BTU) F/BTU) F/BTU)
------ ---- -------- -------- -------- -------- --------
P034 0000
(PIPE) 0001 0.000 0.000 0.000 0.000 0.000
0002 0.000 0.000 0.000 0.000 0.000
0003 0.000 0.000 0.000 0.000 0.000
0004 0.000 0.000 0.000 0.000 0.000
0005 0.000 0.000 0.000 0.000 0.000
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 108
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
LINK "L088" DEVICE DETAIL REPORT
PRESSURE AND TEMPERATURE REPORT
-------------------------------
DEVICE MWD OR TVD
NAME LENGTH I OR
AND SEGM INSIDE FROM & ELEV CALC CALC OVERALL AMB
TYPE NO DIAM. INLET O CHNG PRESS TEMP U-FACT TEMP
(IN) (FT) (FT) (PSIG) (F) (BTU/ (F)
HRFT2F)
------ ---- ------ --------- - -------- ------- ------ ------- ------
P035 0000 5.764 0.0 I 0.0 1288.7 100.0 80.0
(PIPE) 0001 2000.0 0.0 1270.7 99.7 1.000 80.0
0002 4000.0 0.0 1252.7 99.5 1.000 80.0
0003 6000.0 0.0 1234.6 99.2 1.000 80.0
0004 8000.0 0.0 1216.6 99.0 1.000 80.0
0005 9842.5 O 0.0 1200.0 98.8 1.000 80.0
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 109
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
SURFACE PRESSURE PLOT FOR LINK
1290. +-----+-----+-----+-----+-----+-----+-----+-----+-----+-----+
P | | | | |
|PP | | | | |
| PP | | | | |
1280. + PP | | | | +
| P | | | | |
| PP | | | | |
| PP| | | | |
1270. +-----------P-----------+-----------+-----------+-----------+
| |PP | | | |
| | PP | | | |
| | PP | | | |
P 1260. + | P | | | +
R | | PP | | | |
E | | PP| | | |
S | | P | | |
S 1250. +-----------+-----------+PP---------+-----------+-----------+
U | | | PP | | |
R | | | PP | | |
E | | | P | | |
1240. + | | PP | | +
| | | PP| | |
| | | P | |
| | | |PP | |
P 1230. +-----------+-----------+-----------+--PP-------+-----------+
S | | | | PP | |
I | | | | P | |
G | | | | PP | |
1220. + | | | PP| +
| | | | P |
| | | | |PP |
| | | | | P |
1210. +-----------+-----------+-----------+-----------+---PP------+
| | | | | PP |
| | | | | P |
| | | | | PP |
1200. + | | | | P+
| | | | | |
| | | | | |
| | | | | |
1190. +-----+-----+-----+-----+-----+-----+-----+-----+-----+-----+
0.0 2.0 4.0 6.0 8.0 10.0
DIST. FROM 1ST SURFACE DEVICE INLET FT (10**3)
KEY... P - P - FLUID PRESS.
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 110
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
SURFACE TEMPERATURE PLOT FOR LINK
100.0 TTTTTTT-----+-----+-----+-----+-----+-----+-----+-----+-----+
| TTTTTTTTTTTTTTTTTTTTTTTT | | |
| | | TTTTTTTTTTTTTTTTTTTTTTTTTTTTT|
| | | | | |
98.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
96.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
T | | | | | |
E | | | | | |
M 94.0 + | | | | +
P | | | | | |
E | | | | | |
R | | | | | |
A 92.0 +-----------+-----------+-----------+-----------+-----------+
T | | | | | |
U | | | | | |
R | | | | | |
E 90.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
88.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
D | | | | | |
E | | | | | |
G 86.0 + | | | | +
| | | | | |
F | | | | | |
| | | | | |
84.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
| | | | | |
| | | | | |
82.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
80.0 AAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAA+
0.0 2.0 4.0 6.0 8.0 10.0
DIST. FROM 1ST SURFACE DEVICE INLET FT (10**3)
KEY... T - T - FLUID TEMP. A - A - AMB. TEMP.
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 111
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
***************************CONTINUED****************************
LINK "L088" DEVICE DETAIL REPORT
HOLDUP AND VELOCITY DETAIL REPORT
---------------------------------
DEVICE
NAME ---LIQUID HOLDUP--- SUPERFICIAL T-D
AND SEG. NO LIQ GAS MIX . FLOW FLOW SONIC
TYPE NO. SLIP SLIP TOTAL VEL VEL VEL REGM REGM VEL
(ABBL) (FPS) (FPS) (FPS) (FPS)
------ ---- ----- ----- -------- ------- ------- ------- ---- ---- -------
P035 0000
(PIPE) 0001 1.00 1.00 64.5 5.75 0.00 5.75 ---- 1-PH 0.00
0002 1.00 1.00 129.1 5.75 0.00 5.75 ---- 1-PH 0.00
0003 1.00 1.00 193.6 5.75 0.00 5.75 ---- 1-PH 0.00
0004 1.00 1.00 258.2 5.75 0.00 5.75 ---- 1-PH 0.00
0005 1.00 1.00 317.6 5.75 0.00 5.75 ---- 1-PH 0.00
PRESSURE GRADIENT DETAIL REPORT
-------------------------------
DEVICE
NAME
AND SEGM. --PRESSURE GRADIENT---- --PRESSURE CHANGE--
TYPE NO: FRIC ELEV TOTAL FRIC ELEV
(PSIFT) (PSIFT) (PSIFT) (PSIG) (PSIG)
------ ---- -------- -------- -------- -------- --------
P035 0000
(PIPE) 0001 -0.0090 0.0000 -0.0090 -18.0 0.0
0002 -0.0090 0.0000 -0.0090 -18.0 0.0
0003 -0.0090 0.0000 -0.0090 -18.0 0.0
0004 -0.0090 0.0000 -0.0090 -18.0 0.0
0005 -0.0090 0.0000 -0.0090 -16.6 0.0
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 112
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
LINK "L088" PROPERTY DETAIL REPORT
VISCOSITY AND DENSITY RESULTS
-----------------------------
DEVICE
NAME
AND SEGM ----------VISCOSITY---------- ------------DENSITY------------
TYPE NO OIL LIQ VAP LIQ VAP SLIP NO-SLIP
(CP) (CP) (CP) (LB/CF) (LB/CF) (LB/CF) (LB/CF)
------ ---- --------- --------- --------- ------- ------- ------- -------
P035 0000
(PIPE) 0001 0.000 2.321 0.000 63.216 0.000 63.216 63.216
0002 0.000 2.321 0.000 63.216 0.000 63.216 63.216
0003 0.000 2.322 0.000 63.216 0.000 63.216 63.216
0004 0.000 2.323 0.000 63.216 0.000 63.216 63.216
0005 0.000 2.324 0.000 63.216 0.000 63.216 63.216
FRICTION AND SURFACE TENSION RESULTS
------------------------------------
DEVICE
NAME LIQ
AND SEGM --------------FRICTION------------ FRIC. REYNOLDS SURFACE
TYPE NUM. DENSITY VELO ID. VISCOSITY FACTOR NUMBER TENSION
(LB/CF) (FPS) (IN) (CP) (DN/CM)
------ ---- ------- ------- -------- --------- -------- -------- --------
P035 0000
(PIPE) 0001 63.216 5.75 5.764 2.321 0.0192 1.1201E5 0.00
0002 63.216 5.75 5.764 2.321 0.0192 1.1196E5 0.00
0003 63.216 5.75 5.764 2.322 0.0192 1.1192E5 0.00
0004 63.216 5.75 5.764 2.323 0.0192 1.1187E5 0.00
0005 63.216 5.75 5.764 2.324 0.0192 1.1183E5 0.00
HEAT TRANSFER CALCULATIONS
--------------------------
DEVICE FLUID
NAME THERMAL ----------THERMAL RESISTANCE-------
AND SEGM CONDUCT- INSIDE INSULAT- SURROUN-
(TYPE) NO: IVITY FILM PIPE ION DING
(BTUFTF) (HR-FT2- (HR-FT2- (HR-FT2- (HR-FT2-
F/BTU) F/BTU) F/BTU) F/BTU)
------ ---- -------- -------- -------- -------- --------
P035 0000
(PIPE) 0001 0.000 0.000 0.000 0.000 0.000
0002 0.000 0.000 0.000 0.000 0.000
0003 0.000 0.000 0.000 0.000 0.000
0004 0.000 0.000 0.000 0.000 0.000
0005 0.000 0.000 0.000 0.000 0.000
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 113
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
LINK "L099" DEVICE DETAIL REPORT
PRESSURE AND TEMPERATURE REPORT
-------------------------------
DEVICE MWD OR TVD
NAME LENGTH I OR
AND SEGM INSIDE FROM & ELEV CALC CALC OVERALL AMB
TYPE NO DIAM. INLET O CHNG PRESS TEMP U-FACT TEMP
(IN) (FT) (FT) (PSIG) (F) (BTU/ (F)
HRFT2F)
------ ---- ------ --------- - -------- ------- ------ ------- ------
P006 0000 10.020 0.0 I 0.0 1289.7 100.0 80.0
(PIPE) 0001 4.9 0.0 1289.7 100.0 1.000 80.0
0002 9.8 0.0 1289.7 100.0 1.000 80.0
0003 14.8 0.0 1289.6 100.0 1.000 80.0
0004 19.7 O 0.0 1289.6 100.0 1.000 80.0
P007 0000 9.059 0.0 I 0.0 1289.6 100.0 80.0
(PIPE) 0001 4.9 0.0 1289.6 100.0 1.000 80.0
0002 9.8 0.0 1289.5 100.0 1.000 80.0
0003 14.8 0.0 1289.5 100.0 1.000 80.0
0004 19.7 O 0.0 1289.5 100.0 1.000 80.0
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 114
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
SURFACE PRESSURE PLOT FOR LINK
1295. +-----+-----+-----+-----+-----+-----+-----+-----+-----+-----+
| | | | | |
| | | | | |
| | | | | |
1294. + | | | | +
| | | | | |
| | | | | |
| | | | | |
1293. +-----------+-----------+-----------+-----------+-----------+
| | | | | |
| | | | | |
| | | | | |
P 1292. + | | | | +
R | | | | | |
E | | | | | |
S | | | | | |
S 1291. +-----------+-----------+-----------+-----------+-----------+
U | | | | | |
R | | | | | |
E | | | | | |
1290. + | | | | +
PPPPPPPPPPPPPPPPPPPPPPPPPPP | | |
| | | PPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPP|
| | | | | |
P 1289. +-----------+-----------+-----------+-----------+-----------+
S | | | | | |
I | | | | | |
G | | | | | |
1288. + | | | | +
| | | | | |
| | | | | |
| | | | | |
1287. +-----------+-----------+-----------+-----------+-----------+
| | | | | |
| | | | | |
| | | | | |
1286. + | | | | +
| | | | | |
| | | | | |
| | | | | |
1285. +-----+-----+-----+-----+-----+-----+-----+-----+-----+-----+
0.0 8.0 16.0 24.0 32.0 40.0
DIST. FROM 1ST SURFACE DEVICE INLET FT
KEY... P - P - FLUID PRESS.
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 115
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
SURFACE TEMPERATURE PLOT FOR LINK
100.0 TTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTT+
| | | | | |
| | | | | |
| | | | | |
98.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
96.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
T | | | | | |
E | | | | | |
M 94.0 + | | | | +
P | | | | | |
E | | | | | |
R | | | | | |
A 92.0 +-----------+-----------+-----------+-----------+-----------+
T | | | | | |
U | | | | | |
R | | | | | |
E 90.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
88.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
D | | | | | |
E | | | | | |
G 86.0 + | | | | +
| | | | | |
F | | | | | |
| | | | | |
84.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
| | | | | |
| | | | | |
82.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
80.0 AAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAA+
0.0 8.0 16.0 24.0 32.0 40.0
DIST. FROM 1ST SURFACE DEVICE INLET FT
KEY... T - T - FLUID TEMP. A - A - AMB. TEMP.
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 116
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
***************************CONTINUED****************************
LINK "L099" DEVICE DETAIL REPORT
HOLDUP AND VELOCITY DETAIL REPORT
---------------------------------
DEVICE
NAME ---LIQUID HOLDUP--- SUPERFICIAL T-D
AND SEG. NO LIQ GAS MIX . FLOW FLOW SONIC
TYPE NO. SLIP SLIP TOTAL VEL VEL VEL REGM REGM VEL
(ABBL) (FPS) (FPS) (FPS) (FPS)
------ ---- ----- ----- -------- ------- ------- ------- ---- ---- -------
P006 0000
(PIPE) 0001 1.00 1.00 0.5 5.64 0.00 5.64 ---- 1-PH 0.00
0002 1.00 1.00 1.0 5.64 0.00 5.64 ---- 1-PH 0.00
0003 1.00 1.00 1.4 5.64 0.00 5.64 ---- 1-PH 0.00
0004 1.00 1.00 1.9 5.64 0.00 5.64 ---- 1-PH 0.00
P007 0000
(PIPE) 0001 1.00 1.00 2.3 6.89 0.00 6.89 ---- 1-PH 0.00
0002 1.00 1.00 2.7 6.89 0.00 6.89 ---- 1-PH 0.00
0003 1.00 1.00 3.1 6.89 0.00 6.89 ---- 1-PH 0.00
0004 1.00 1.00 3.5 6.89 0.00 6.89 ---- 1-PH 0.00
PRESSURE GRADIENT DETAIL REPORT
-------------------------------
DEVICE
NAME
AND SEGM. --PRESSURE GRADIENT---- --PRESSURE CHANGE--
TYPE NO: FRIC ELEV TOTAL FRIC ELEV
(PSIFT) (PSIFT) (PSIFT) (PSIG) (PSIG)
------ ---- -------- -------- -------- -------- --------
P006 0000
(PIPE) 0001 -0.0044 0.0000 -0.0044 -2.18E-2 0.0
0002 -0.0044 0.0000 -0.0044 -2.18E-2 0.0
0003 -0.0044 0.0000 -0.0044 -2.18E-2 0.0
0004 -0.0044 0.0000 -0.0044 -2.18E-2 0.0
P007 0000
(PIPE) 0001 -0.0073 0.0000 -0.0073 -3.58E-2 0.0
0002 -0.0073 0.0000 -0.0073 -3.58E-2 0.0
0003 -0.0073 0.0000 -0.0073 -3.58E-2 0.0
0004 -0.0073 0.0000 -0.0073 -3.58E-2 0.0
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 117
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
LINK "L099" PROPERTY DETAIL REPORT
VISCOSITY AND DENSITY RESULTS
-----------------------------
DEVICE
NAME
AND SEGM ----------VISCOSITY---------- ------------DENSITY------------
TYPE NO OIL LIQ VAP LIQ VAP SLIP NO-SLIP
(CP) (CP) (CP) (LB/CF) (LB/CF) (LB/CF) (LB/CF)
------ ---- --------- --------- --------- ------- ------- ------- -------
P006 0000
(PIPE) 0001 0.000 2.320 0.000 63.217 0.000 63.217 63.217
0002 0.000 2.320 0.000 63.217 0.000 63.217 63.217
0003 0.000 2.320 0.000 63.217 0.000 63.217 63.217
0004 0.000 2.320 0.000 63.217 0.000 63.217 63.217
P007 0000
(PIPE) 0001 0.000 2.320 0.000 63.217 0.000 63.217 63.217
0002 0.000 2.320 0.000 63.217 0.000 63.217 63.217
0003 0.000 2.320 0.000 63.217 0.000 63.217 63.217
0004 0.000 2.320 0.000 63.217 0.000 63.217 63.217
FRICTION AND SURFACE TENSION RESULTS
------------------------------------
DEVICE
NAME LIQ
AND SEGM --------------FRICTION------------ FRIC. REYNOLDS SURFACE
TYPE NUM. DENSITY VELO ID. VISCOSITY FACTOR NUMBER TENSION
(LB/CF) (FPS) (IN) (CP) (DN/CM)
------ ---- ------- ------- -------- --------- -------- -------- --------
P006 0000
(PIPE) 0001 63.217 5.64 10.020 2.320 0.0171 1.9078E5 0.00
0002 63.217 5.64 10.020 2.320 0.0171 1.9078E5 0.00
0003 63.217 5.64 10.020 2.320 0.0171 1.9078E5 0.00
0004 63.217 5.64 10.020 2.320 0.0171 1.9078E5 0.00
P007 0000
(PIPE) 0001 63.217 6.89 9.059 2.320 0.0170 2.1101E5 0.00
0002 63.217 6.89 9.059 2.320 0.0170 2.1101E5 0.00
0003 63.217 6.89 9.059 2.320 0.0170 2.1101E5 0.00
0004 63.217 6.89 9.059 2.320 0.0170 2.1101E5 0.00
HEAT TRANSFER CALCULATIONS
--------------------------
DEVICE FLUID
NAME THERMAL ----------THERMAL RESISTANCE-------
AND SEGM CONDUCT- INSIDE INSULAT- SURROUN-
(TYPE) NO: IVITY FILM PIPE ION DING
(BTUFTF) (HR-FT2- (HR-FT2- (HR-FT2- (HR-FT2-
F/BTU) F/BTU) F/BTU) F/BTU)
------ ---- -------- -------- -------- -------- --------
P006 0000
Heat Transfer Resistances based on pipe ID
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 118
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
***************************CONTINUED****************************
LINK "L099" PROPERTY DETAIL REPORT
HEAT TRANSFER CALCULATIONS
--------------------------
DEVICE FLUID
NAME THERMAL ----------THERMAL RESISTANCE-------
AND SEGM CONDUCT- INSIDE INSULAT- SURROUN-
(TYPE) NO: IVITY FILM PIPE ION DING
(BTUFTF) (HR-FT2- (HR-FT2- (HR-FT2- (HR-FT2-
F/BTU) F/BTU) F/BTU) F/BTU)
------ ---- -------- -------- -------- -------- --------
(PIPE) 0001 0.000 0.000 0.000 0.000 0.000
0002 0.000 0.000 0.000 0.000 0.000
0003 0.000 0.000 0.000 0.000 0.000
0004 0.000 0.000 0.000 0.000 0.000
P007 0000
(PIPE) 0001 0.000 0.000 0.000 0.000 0.000
0002 0.000 0.000 0.000 0.000 0.000
0003 0.000 0.000 0.000 0.000 0.000
0004 0.000 0.000 0.000 0.000 0.000
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 119
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
LINK "L100" DEVICE DETAIL REPORT
PRESSURE AND TEMPERATURE REPORT
-------------------------------
DEVICE MWD OR TVD
NAME LENGTH I OR
AND SEGM INSIDE FROM & ELEV CALC CALC OVERALL AMB
TYPE NO DIAM. INLET O CHNG PRESS TEMP U-FACT TEMP
(IN) (FT) (FT) (PSIG) (F) (BTU/ (F)
HRFT2F)
------ ---- ------ --------- - -------- ------- ------ ------- ------
P008 0000 10.020 0.0 I 0.0 1289.7 100.0 80.0
(PIPE) 0001 4.9 0.0 1289.7 100.0 1.000 80.0
0002 9.8 0.0 1289.7 100.0 1.000 80.0
0003 14.8 0.0 1289.6 100.0 1.000 80.0
0004 19.7 O 0.0 1289.6 100.0 1.000 80.0
P009 0000 9.559 0.0 I 0.0 1289.6 100.0 80.0
(PIPE) 0001 4.9 0.0 1289.6 100.0 1.000 80.0
0002 9.8 0.0 1289.5 100.0 1.000 80.0
0003 14.8 0.0 1289.5 100.0 1.000 80.0
0004 19.7 O 0.0 1289.5 100.0 1.000 80.0
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 120
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
SURFACE PRESSURE PLOT FOR LINK
1295. +-----+-----+-----+-----+-----+-----+-----+-----+-----+-----+
| | | | | |
| | | | | |
| | | | | |
1294. + | | | | +
| | | | | |
| | | | | |
| | | | | |
1293. +-----------+-----------+-----------+-----------+-----------+
| | | | | |
| | | | | |
| | | | | |
P 1292. + | | | | +
R | | | | | |
E | | | | | |
S | | | | | |
S 1291. +-----------+-----------+-----------+-----------+-----------+
U | | | | | |
R | | | | | |
E | | | | | |
1290. + | | | | +
PPPPPPPPPPPPPPPPPPPPPPPPPPP | | |
| | | PPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPP|
| | | | | |
P 1289. +-----------+-----------+-----------+-----------+-----------+
S | | | | | |
I | | | | | |
G | | | | | |
1288. + | | | | +
| | | | | |
| | | | | |
| | | | | |
1287. +-----------+-----------+-----------+-----------+-----------+
| | | | | |
| | | | | |
| | | | | |
1286. + | | | | +
| | | | | |
| | | | | |
| | | | | |
1285. +-----+-----+-----+-----+-----+-----+-----+-----+-----+-----+
0.0 8.0 16.0 24.0 32.0 40.0
DIST. FROM 1ST SURFACE DEVICE INLET FT
KEY... P - P - FLUID PRESS.
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 121
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
SURFACE TEMPERATURE PLOT FOR LINK
100.0 TTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTT+
| | | | | |
| | | | | |
| | | | | |
98.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
96.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
T | | | | | |
E | | | | | |
M 94.0 + | | | | +
P | | | | | |
E | | | | | |
R | | | | | |
A 92.0 +-----------+-----------+-----------+-----------+-----------+
T | | | | | |
U | | | | | |
R | | | | | |
E 90.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
88.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
D | | | | | |
E | | | | | |
G 86.0 + | | | | +
| | | | | |
F | | | | | |
| | | | | |
84.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
| | | | | |
| | | | | |
82.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
80.0 AAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAA+
0.0 8.0 16.0 24.0 32.0 40.0
DIST. FROM 1ST SURFACE DEVICE INLET FT
KEY... T - T - FLUID TEMP. A - A - AMB. TEMP.
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 122
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
***************************CONTINUED****************************
LINK "L100" DEVICE DETAIL REPORT
HOLDUP AND VELOCITY DETAIL REPORT
---------------------------------
DEVICE
NAME ---LIQUID HOLDUP--- SUPERFICIAL T-D
AND SEG. NO LIQ GAS MIX . FLOW FLOW SONIC
TYPE NO. SLIP SLIP TOTAL VEL VEL VEL REGM REGM VEL
(ABBL) (FPS) (FPS) (FPS) (FPS)
------ ---- ----- ----- -------- ------- ------- ------- ---- ---- -------
P008 0000
(PIPE) 0001 1.00 1.00 0.5 6.15 0.00 6.15 ---- 1-PH 0.00
0002 1.00 1.00 1.0 6.15 0.00 6.15 ---- 1-PH 0.00
0003 1.00 1.00 1.4 6.15 0.00 6.15 ---- 1-PH 0.00
0004 1.00 1.00 1.9 6.15 0.00 6.15 ---- 1-PH 0.00
P009 0000
(PIPE) 0001 1.00 1.00 2.4 6.76 0.00 6.76 ---- 1-PH 0.00
0002 1.00 1.00 2.8 6.76 0.00 6.76 ---- 1-PH 0.00
0003 1.00 1.00 3.2 6.76 0.00 6.76 ---- 1-PH 0.00
0004 1.00 1.00 3.7 6.76 0.00 6.76 ---- 1-PH 0.00
PRESSURE GRADIENT DETAIL REPORT
-------------------------------
DEVICE
NAME
AND SEGM. --PRESSURE GRADIENT---- --PRESSURE CHANGE--
TYPE NO: FRIC ELEV TOTAL FRIC ELEV
(PSIFT) (PSIFT) (PSIFT) (PSIG) (PSIG)
------ ---- -------- -------- -------- -------- --------
P008 0000
(PIPE) 0001 -0.0052 0.0000 -0.0052 -2.57E-2 0.0
0002 -0.0052 0.0000 -0.0052 -2.57E-2 0.0
0003 -0.0052 0.0000 -0.0052 -2.57E-2 0.0
0004 -0.0052 0.0000 -0.0052 -2.57E-2 0.0
P009 0000
(PIPE) 0001 -0.0066 0.0000 -0.0066 -3.24E-2 0.0
0002 -0.0066 0.0000 -0.0066 -3.24E-2 0.0
0003 -0.0066 0.0000 -0.0066 -3.24E-2 0.0
0004 -0.0066 0.0000 -0.0066 -3.24E-2 0.0
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 123
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
LINK "L100" PROPERTY DETAIL REPORT
VISCOSITY AND DENSITY RESULTS
-----------------------------
DEVICE
NAME
AND SEGM ----------VISCOSITY---------- ------------DENSITY------------
TYPE NO OIL LIQ VAP LIQ VAP SLIP NO-SLIP
(CP) (CP) (CP) (LB/CF) (LB/CF) (LB/CF) (LB/CF)
------ ---- --------- --------- --------- ------- ------- ------- -------
P008 0000
(PIPE) 0001 0.000 2.320 0.000 63.217 0.000 63.217 63.217
0002 0.000 2.320 0.000 63.217 0.000 63.217 63.217
0003 0.000 2.320 0.000 63.217 0.000 63.217 63.217
0004 0.000 2.320 0.000 63.217 0.000 63.217 63.217
P009 0000
(PIPE) 0001 0.000 2.320 0.000 63.217 0.000 63.217 63.217
0002 0.000 2.320 0.000 63.217 0.000 63.217 63.217
0003 0.000 2.320 0.000 63.217 0.000 63.217 63.217
0004 0.000 2.320 0.000 63.217 0.000 63.217 63.217
FRICTION AND SURFACE TENSION RESULTS
------------------------------------
DEVICE
NAME LIQ
AND SEGM --------------FRICTION------------ FRIC. REYNOLDS SURFACE
TYPE NUM. DENSITY VELO ID. VISCOSITY FACTOR NUMBER TENSION
(LB/CF) (FPS) (IN) (CP) (DN/CM)
------ ---- ------- ------- -------- --------- -------- -------- --------
P008 0000
(PIPE) 0001 63.217 6.15 10.020 2.320 0.0169 2.0833E5 0.00
0002 63.217 6.15 10.020 2.320 0.0169 2.0833E5 0.00
0003 63.217 6.15 10.020 2.320 0.0169 2.0833E5 0.00
0004 63.217 6.15 10.020 2.320 0.0169 2.0833E5 0.00
P009 0000
(PIPE) 0001 63.217 6.76 9.559 2.320 0.0168 2.1837E5 0.00
0002 63.217 6.76 9.559 2.320 0.0168 2.1837E5 0.00
0003 63.217 6.76 9.559 2.320 0.0168 2.1837E5 0.00
0004 63.217 6.76 9.559 2.320 0.0168 2.1837E5 0.00
HEAT TRANSFER CALCULATIONS
--------------------------
DEVICE FLUID
NAME THERMAL ----------THERMAL RESISTANCE-------
AND SEGM CONDUCT- INSIDE INSULAT- SURROUN-
(TYPE) NO: IVITY FILM PIPE ION DING
(BTUFTF) (HR-FT2- (HR-FT2- (HR-FT2- (HR-FT2-
F/BTU) F/BTU) F/BTU) F/BTU)
------ ---- -------- -------- -------- -------- --------
P008 0000
Heat Transfer Resistances based on pipe ID
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 124
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
***************************CONTINUED****************************
LINK "L100" PROPERTY DETAIL REPORT
HEAT TRANSFER CALCULATIONS
--------------------------
DEVICE FLUID
NAME THERMAL ----------THERMAL RESISTANCE-------
AND SEGM CONDUCT- INSIDE INSULAT- SURROUN-
(TYPE) NO: IVITY FILM PIPE ION DING
(BTUFTF) (HR-FT2- (HR-FT2- (HR-FT2- (HR-FT2-
F/BTU) F/BTU) F/BTU) F/BTU)
------ ---- -------- -------- -------- -------- --------
(PIPE) 0001 0.000 0.000 0.000 0.000 0.000
0002 0.000 0.000 0.000 0.000 0.000
0003 0.000 0.000 0.000 0.000 0.000
0004 0.000 0.000 0.000 0.000 0.000
P009 0000
(PIPE) 0001 0.000 0.000 0.000 0.000 0.000
0002 0.000 0.000 0.000 0.000 0.000
0003 0.000 0.000 0.000 0.000 0.000
0004 0.000 0.000 0.000 0.000 0.000
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 125
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
LINK "L101" DEVICE DETAIL REPORT
PRESSURE AND TEMPERATURE REPORT
-------------------------------
DEVICE MWD OR TVD
NAME LENGTH I OR
AND SEGM INSIDE FROM & ELEV CALC CALC OVERALL AMB
TYPE NO DIAM. INLET O CHNG PRESS TEMP U-FACT TEMP
(IN) (FT) (FT) (PSIG) (F) (BTU/ (F)
HRFT2F)
------ ---- ------ --------- - -------- ------- ------ ------- ------
P010 0000 10.020 0.0 I 0.0 1289.7 100.0 80.0
(PIPE) 0001 4.9 0.0 1289.7 100.0 1.000 80.0
0002 9.8 0.0 1289.7 100.0 1.000 80.0
0003 14.8 0.0 1289.6 100.0 1.000 80.0
0004 19.7 O 0.0 1289.6 100.0 1.000 80.0
P011 0000 9.559 0.0 I 0.0 1289.6 100.0 80.0
(PIPE) 0001 4.9 0.0 1289.6 100.0 1.000 80.0
0002 9.8 0.0 1289.5 100.0 1.000 80.0
0003 14.8 0.0 1289.5 100.0 1.000 80.0
0004 19.7 O 0.0 1289.5 100.0 1.000 80.0
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 126
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
SURFACE PRESSURE PLOT FOR LINK
1295. +-----+-----+-----+-----+-----+-----+-----+-----+-----+-----+
| | | | | |
| | | | | |
| | | | | |
1294. + | | | | +
| | | | | |
| | | | | |
| | | | | |
1293. +-----------+-----------+-----------+-----------+-----------+
| | | | | |
| | | | | |
| | | | | |
P 1292. + | | | | +
R | | | | | |
E | | | | | |
S | | | | | |
S 1291. +-----------+-----------+-----------+-----------+-----------+
U | | | | | |
R | | | | | |
E | | | | | |
1290. + | | | | +
PPPPPPPPPPPPPPPPPPPPPPPPPPP | | |
| | | PPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPPP|
| | | | | |
P 1289. +-----------+-----------+-----------+-----------+-----------+
S | | | | | |
I | | | | | |
G | | | | | |
1288. + | | | | +
| | | | | |
| | | | | |
| | | | | |
1287. +-----------+-----------+-----------+-----------+-----------+
| | | | | |
| | | | | |
| | | | | |
1286. + | | | | +
| | | | | |
| | | | | |
| | | | | |
1285. +-----+-----+-----+-----+-----+-----+-----+-----+-----+-----+
0.0 8.0 16.0 24.0 32.0 40.0
DIST. FROM 1ST SURFACE DEVICE INLET FT
KEY... P - P - FLUID PRESS.
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 127
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
SURFACE TEMPERATURE PLOT FOR LINK
100.0 TTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTTT+
| | | | | |
| | | | | |
| | | | | |
98.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
96.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
T | | | | | |
E | | | | | |
M 94.0 + | | | | +
P | | | | | |
E | | | | | |
R | | | | | |
A 92.0 +-----------+-----------+-----------+-----------+-----------+
T | | | | | |
U | | | | | |
R | | | | | |
E 90.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
88.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
D | | | | | |
E | | | | | |
G 86.0 + | | | | +
| | | | | |
F | | | | | |
| | | | | |
84.0 +-----------+-----------+-----------+-----------+-----------+
| | | | | |
| | | | | |
| | | | | |
82.0 + | | | | +
| | | | | |
| | | | | |
| | | | | |
80.0 AAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAAA+
0.0 8.0 16.0 24.0 32.0 40.0
DIST. FROM 1ST SURFACE DEVICE INLET FT
KEY... T - T - FLUID TEMP. A - A - AMB. TEMP.
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 128
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
***************************CONTINUED****************************
LINK "L101" DEVICE DETAIL REPORT
HOLDUP AND VELOCITY DETAIL REPORT
---------------------------------
DEVICE
NAME ---LIQUID HOLDUP--- SUPERFICIAL T-D
AND SEG. NO LIQ GAS MIX . FLOW FLOW SONIC
TYPE NO. SLIP SLIP TOTAL VEL VEL VEL REGM REGM VEL
(ABBL) (FPS) (FPS) (FPS) (FPS)
------ ---- ----- ----- -------- ------- ------- ------- ---- ---- -------
P010 0000
(PIPE) 0001 1.00 1.00 0.5 6.11 0.00 6.11 ---- 1-PH 0.00
0002 1.00 1.00 1.0 6.11 0.00 6.11 ---- 1-PH 0.00
0003 1.00 1.00 1.4 6.11 0.00 6.11 ---- 1-PH 0.00
0004 1.00 1.00 1.9 6.11 0.00 6.11 ---- 1-PH 0.00
P011 0000
(PIPE) 0001 1.00 1.00 2.4 6.71 0.00 6.71 ---- 1-PH 0.00
0002 1.00 1.00 2.8 6.71 0.00 6.71 ---- 1-PH 0.00
0003 1.00 1.00 3.2 6.71 0.00 6.71 ---- 1-PH 0.00
0004 1.00 1.00 3.7 6.71 0.00 6.71 ---- 1-PH 0.00
PRESSURE GRADIENT DETAIL REPORT
-------------------------------
DEVICE
NAME
AND SEGM. --PRESSURE GRADIENT---- --PRESSURE CHANGE--
TYPE NO: FRIC ELEV TOTAL FRIC ELEV
(PSIFT) (PSIFT) (PSIFT) (PSIG) (PSIG)
------ ---- -------- -------- -------- -------- --------
P010 0000
(PIPE) 0001 -0.0051 0.0000 -0.0051 -2.53E-2 0.0
0002 -0.0051 0.0000 -0.0051 -2.53E-2 0.0
0003 -0.0051 0.0000 -0.0051 -2.53E-2 0.0
0004 -0.0051 0.0000 -0.0051 -2.53E-2 0.0
P011 0000
(PIPE) 0001 -0.0065 0.0000 -0.0065 -3.19E-2 0.0
0002 -0.0065 0.0000 -0.0065 -3.19E-2 0.0
0003 -0.0065 0.0000 -0.0065 -3.19E-2 0.0
0004 -0.0065 0.0000 -0.0065 -3.19E-2 0.0
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 129
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
LINK "L101" PROPERTY DETAIL REPORT
VISCOSITY AND DENSITY RESULTS
-----------------------------
DEVICE
NAME
AND SEGM ----------VISCOSITY---------- ------------DENSITY------------
TYPE NO OIL LIQ VAP LIQ VAP SLIP NO-SLIP
(CP) (CP) (CP) (LB/CF) (LB/CF) (LB/CF) (LB/CF)
------ ---- --------- --------- --------- ------- ------- ------- -------
P010 0000
(PIPE) 0001 0.000 2.320 0.000 63.217 0.000 63.217 63.217
0002 0.000 2.320 0.000 63.217 0.000 63.217 63.217
0003 0.000 2.320 0.000 63.217 0.000 63.217 63.217
0004 0.000 2.320 0.000 63.217 0.000 63.217 63.217
P011 0000
(PIPE) 0001 0.000 2.320 0.000 63.217 0.000 63.217 63.217
0002 0.000 2.320 0.000 63.217 0.000 63.217 63.217
0003 0.000 2.320 0.000 63.217 0.000 63.217 63.217
0004 0.000 2.320 0.000 63.217 0.000 63.217 63.217
FRICTION AND SURFACE TENSION RESULTS
------------------------------------
DEVICE
NAME LIQ
AND SEGM --------------FRICTION------------ FRIC. REYNOLDS SURFACE
TYPE NUM. DENSITY VELO ID. VISCOSITY FACTOR NUMBER TENSION
(LB/CF) (FPS) (IN) (CP) (DN/CM)
------ ---- ------- ------- -------- --------- -------- -------- --------
P010 0000
(PIPE) 0001 63.217 6.11 10.020 2.320 0.0169 2.0685E5 0.00
0002 63.217 6.11 10.020 2.320 0.0169 2.0685E5 0.00
0003 63.217 6.11 10.020 2.320 0.0169 2.0685E5 0.00
0004 63.217 6.11 10.020 2.320 0.0169 2.0685E5 0.00
P011 0000
(PIPE) 0001 63.217 6.71 9.559 2.320 0.0168 2.1682E5 0.00
0002 63.217 6.71 9.559 2.320 0.0168 2.1682E5 0.00
0003 63.217 6.71 9.559 2.320 0.0168 2.1682E5 0.00
0004 63.217 6.71 9.559 2.320 0.0168 2.1682E5 0.00
HEAT TRANSFER CALCULATIONS
--------------------------
DEVICE FLUID
NAME THERMAL ----------THERMAL RESISTANCE-------
AND SEGM CONDUCT- INSIDE INSULAT- SURROUN-
(TYPE) NO: IVITY FILM PIPE ION DING
(BTUFTF) (HR-FT2- (HR-FT2- (HR-FT2- (HR-FT2-
F/BTU) F/BTU) F/BTU) F/BTU)
------ ---- -------- -------- -------- -------- --------
P010 0000
Heat Transfer Resistances based on pipe ID
VERSION 9.1 R
SIMULATION SCIENCES, INC. PIPEPHASE PAGE 130
PROJECT OUTPUT
PROBLEM NETWORK REPORT 05/16/12
==============================================================================
BASE CASE
***************************CONTINUED****************************
LINK "L101" PROPERTY DETAIL REPORT
HEAT TRANSFER CALCULATIONS
--------------------------
DEVICE FLUID
NAME THERMAL ----------THERMAL RESISTANCE-------
AND SEGM CONDUCT- INSIDE INSULAT- SURROUN-
(TYPE) NO: IVITY FILM PIPE ION DING
(BTUFTF) (HR-FT2- (HR-FT2- (HR-FT2- (HR-FT2-
F/BTU) F/BTU) F/BTU) F/BTU)
------ ---- -------- -------- -------- -------- --------
(PIPE) 0001 0.000 0.000 0.000 0.000 0.000
0002 0.000 0.000 0.000 0.000 0.000
0003 0.000 0.000 0.000 0.000 0.000
0004 0.000 0.000 0.000 0.000 0.000
P011 0000
(PIPE) 0001 0.000 0.000 0.000 0.000 0.000
0002 0.000 0.000 0.000 0.000 0.000
0003 0.000 0.000 0.000 0.000 0.000
0004 0.000 0.000 0.000 0.000 0.000
