takoradi interconnect (case 1)

TAKORADI INTERCONNECT (CASE 1)

Index

ReportIndex

Input FileInput ReprintSolution HistoryNode SummaryLink SummaryDevice SummaryStructure SummaryVelocity SummaryResults SummaryFlash SummaryPhaseDataL005L007L009

Input FileIndex

Input File: C:\USERS\EBERECHUKWU\DESKTOP\GHANA GAS\TAKORADI INTERCONNECT (CASE 1)

$ SIMSCI PIPEPHASE Version 9.0 keyword file...$$General Data Section$TITLE DATE=05/06/15$$DIMENSION TEMPERATURE=C, PRESSURE=BARG, LENGTH=KM,IN$CALCULATION NETWORK, Compositional, PRANDTL$DEFAULT IDPIPE=4.026, IDTUBING=4.026, IDRISER=4.026, * IDANNULUS=6.065, HAUSEN$PRINT INPUT=FULL, DEVICE=FULL, PLOT=FULL, * PROPERTY=FULL, MAP=TAITEL, DATABASE=FULL, * SIMULATOR=PART$SEGMENT AUTO=ON, DLHORIZ(KM)=0.6096, DLVERT(KM)=0.1524$$Component Data Section$COMPONENT DATA$LIBID 1, CO2 / * 2, N2 / * 3, H2S / * 4, C1 / * 5, C2 / * 6, C3 / * 7, IC4 / * 8, NC4 / * 9, IC5 / * 10, NC5 / * 11, NC6 / * 12, NC7 / * 13, NC8 / * 14, H2O$PHASE VL=1,14

$$Network Data Section$NETWORK DATA$SOLUTION PBALANCE, FLOWAL=2, STEP=1$TOLERANCE PRESSURE=0.1$$Thermodynamic Data Section$THERMODYNAMIC DATA$METHOD SET=SET01, SYSTEM=SRK$WATER PROPERTY=Super$KVALUE BANK=SimSci$$PVT Data Section$PVT PROPERTY DATA$SET SETNO=1, SET=SET01 $$Structure Data Section$STRUCTURE DATA$SOURCE NAME=GHANA, IDNAME=GHAN, PRIORITY=0, * PRES=50, TEMP=47, RATE(GV)=60, * XCORD=-111, YCORD=0, * COMP(M)=1, 1.67 / 2, 0.7099 / 4, 82.217 / * 5, 9.889 / 6, 4.419 / 7, 0.3399 / * 8, 0.5899 / 9, 0.07 / 10, 0.05 / * 11, 0.01 / 12, 0.01 / 13, 0.01 / * 14, 0.0156$SOURCE NAME=TEMA, IDNAME=TEMA, PRIORITY=0, * PRES(ESTI)=108, TEMP=27, RATE(GV)=60, * XCORD=-110, YCORD=411, * COMP(M)=1, 2.55 / 2, 0.66 / 4, 88.74 / * 5, 5.93 / 6, 1.28 / 7, 0.26 / * 8, 0.26 / 9, 0.09 / 10, 0.06 / * 11, 0.06 / 12, 0.1 / 14, 0.01$SINK NAME=D003, IDNAME=D003, PRES(ESTI)=108, * RATE(ESTI)=1.235e+006, XCORD=1244, YCORD=195$JUNCTION NAME=J004, IDNAME=J004, PRES(ESTI)= 108, * TROCK=25, XCORD=484, YCORD=215$LINK NAME=L005, FROM=GHANA, TO=J004, * IDNAME=L005, IDFROM=GHAN, IDTO=J004PIPE NAME=20 , LENGTH(KM)=1.000e-004, 1.5, * 6.500e-004, ECHG=0, 0, * 6.500e-004, NOMD=20, SCHED= 160, * U=1PIPE NAME=P016, LENGTH(KM)=1.000e-004, 0.2, * ECHG=1.000e-004, 0, NOMD=12, * SCHED= 160, U=1$LINK NAME=L007, FROM=TEMA, TO=J004, * IDNAME=L007, IDFROM=TEMA, IDTO=J004PIPE NAME=P005, LENGTH(KM)=1.000e-004, 0.02441, * ECHG=0, 0, NOMD=20, * SCHED= 160, U=1$LINK NAME=L009, FROM=J004, TO=D003, * IDNAME=L009, IDFROM=J004, IDTO=D003PIPE NAME=P007, LENGTH(KM)=1.000e-004, 0.07, * 1.500e-003, 9.140e-004, 1.500e-003, * ECHG=0, 0, 1.500e-003, * 0, -1.500e-003, NOMD=12, * SCHED= 160, U=1PIPE NAME=P017, LENGTH(KM)=1.000e-004, 7.326e-003, * ECHG=0, 0, NOMD=20, * SCHED= 160, U=1$$ End of keyword file...$END

Input ReprintIndex

Input Data

*** WARNING ***** PRESS: ESTIMATE AND FLOW DIRECTION INCONSISTENT FOR FOLLOWING LINKS LINK FROM NODE PRESSURE TO NODE PRESSURE 1 GHAN 739.9 J004 1581.1 CALCULATION OPTIONS RUN TYPE........ NETWORK FLUID TYPE...... COMPOSITIONAL DIMENSIONAL UNITS - PETROLEUM TEMPERATURE..... DEG C PRESSURE........ BARG MOLAR RATE...... MOLE/HR WEIGHT RATE..... LB/HR LIQUID RATE..... BBL/DAY VAPOR RATE...... MM FT3/DAY COARSE LENGTH... KM 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........ 26.67 DEG C 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 BEGGS-BRILL (MOODY) REYNOLDS NUMBER(LAMINAR)..... 3000.0000 RISER FLOW CODE IS BEGGS-BRILL (MOODY) TUBING FLOW CODE IS BEGGS-BRILL (MOODY) ANNULUS FLOW CODE IS BEGGS-BRILL (MOODY) BASE CONDITIONS STANDARD TEMPERATURE....... 15.56 DEG C STANDARD PRESSURE.......... 0.000 BARG

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 FLASH........... SUMMARY STREAM.......... SUMMARY SEGMENTATION OPTIONS LENGTH CHANGE - HORIZONTAL....... 0.6 KM VERTICAL......... 0.2 KM MAXIMUM NUMBER OF SEGMENTS....... 50 AUTOSEGMENT OPTION IS ................ ON TARGET SEGMENT PRESSURE CHANGE........ 1.3789E+00 BARG TARGET SEGMENT TEMPERATURE CHANGE..... -1.5000E+01 DEG C SEGMENT PRESSURE ERROR ............... 1.3789E-02 BARG SEGMENT ENTHALPY ERROR ............... 5.0000E-02 BTU/LB NUMBER OF INTERNAL SEGMENT ITERATIONS. 25 SOLUTION METHODS/TOLERANCES NETWORK SOLUTION METHOD IS PBAL MAXIMUM ITERATIONS..................... 20 MAXIMUM NUMBER OF INTERVAL HALVINGS.... 3 ABSOLUTE PRESSURE TOLERANCE............ 0.100 BARG RATE PERTURBATION...................... 0.010000 METHOD OF INITIAL SOLUTION ESTIMATION.. FLOW = 2 ZERO FLOW IN CHECK VALVES.............. OFF CHOKE CRITICAL FLOW MODEL (FORTUNATI) . EXPONENTIAL NEW ACCELERATION OPTION IS............. OFF SOURCE GHANA PHASE IS MIXED THIS SOURCE IS ON RATE...................... 60.0000 MM FT3/DAY PRESSURE.................. 49.9998 BARG TEMPERATURE............... 47.00 DEG C

SOURCE TEMA PHASE IS MIXED THIS SOURCE IS ON RATE...................... 60.0000 MM FT3/DAY ESTIMATED PRESSURE........ 108.0000 BARG TEMPERATURE............... 27.00 DEG C LINK L005 LINK IS FROM "GHANA " TO "J004 "

DEVICE SA001, 20 , IS A PIPE FLOW CODE IS BEGGS-BRILL (MOODY) INSIDE DIAMETER.............. 16.0630 IN LENGTH....................... 1.5 KM ELEVATION CHANGE............. 0.0 KM PIPELINE PROFILE IN KM LENGTH ELEVATION 0.0 0.0 1.5 0.0 0.0 0.0 FLOW EFFICIENCY.............. 100.00 PERCENT HEAT LOSS COEFFICIENT........ 1.00000 BTU/HR-FT2-F ROUGHNESS.................... 0.00180 IN AMBIENT TEMPERATURE.......... 26.67 DEG C

DEVICE SA002, P016, IS A PIPE FLOW CODE IS BEGGS-BRILL (MOODY) INSIDE DIAMETER.............. 10.1260 IN LENGTH....................... 0.2 KM ELEVATION CHANGE............. 0.0 KM PIPELINE PROFILE IN KM LENGTH ELEVATION 0.0 0.0 0.2 0.0 FLOW EFFICIENCY.............. 100.00 PERCENT HEAT LOSS COEFFICIENT........ 1.00000 BTU/HR-FT2-F ROUGHNESS.................... 0.00180 IN AMBIENT TEMPERATURE.......... 26.67 DEG C LINK L007 LINK IS FROM "TEMA " TO "J004 "

DEVICE SA003, P005, IS A PIPE FLOW CODE IS BEGGS-BRILL (MOODY) INSIDE DIAMETER.............. 16.0630 IN LENGTH....................... 0.0 KM ELEVATION CHANGE............. 0.0 KM PIPELINE PROFILE IN KM LENGTH ELEVATION 0.0 0.0 0.0 0.0 FLOW EFFICIENCY.............. 100.00 PERCENT HEAT LOSS COEFFICIENT........ 1.00000 BTU/HR-FT2-F ROUGHNESS.................... 0.00180 IN AMBIENT TEMPERATURE.......... 26.67 DEG C

LINK L009 LINK IS FROM "J004 " TO "D003 "

DEVICE SA004, P007, IS A PIPE FLOW CODE IS BEGGS-BRILL (MOODY) INSIDE DIAMETER.............. 10.1260 IN LENGTH....................... 0.1 KM ELEVATION CHANGE............. 0.0 KM PIPELINE PROFILE IN KM LENGTH ELEVATION 0.0 0.0 0.1 0.0 0.0 0.0 0.0 0.0 0.0 0.0 FLOW EFFICIENCY.............. 100.00 PERCENT HEAT LOSS COEFFICIENT........ 1.00000 BTU/HR-FT2-F ROUGHNESS.................... 0.00180 IN AMBIENT TEMPERATURE.......... 26.67 DEG C

DEVICE SA005, P017, IS A PIPE FLOW CODE IS BEGGS-BRILL (MOODY) INSIDE DIAMETER.............. 16.0630 IN LENGTH....................... 0.0 KM ELEVATION CHANGE............. 0.0 KM PIPELINE PROFILE IN KM LENGTH ELEVATION 0.0 0.0 0.0 0.0 FLOW EFFICIENCY.............. 100.00 PERCENT HEAT LOSS COEFFICIENT........ 1.00000 BTU/HR-FT2-F ROUGHNESS.................... 0.00180 IN AMBIENT TEMPERATURE.......... 26.67 DEG C JUNCTIONS AND SINKS

JUNCTION J004 ESTIMATED PRESSURE........ 108.0000 BARG

SINK D003 ESTIMATED RATE............ 1235000.0000 LB/HR ESTIMATED PRESSURE........ 108.0000 BARG NODE CONNECTIONS

---- CONNECTIONS ---- NODE NODE NAME NODE TYPE TO NODE VIA LINK ---- --------- --------- --------- --------- GHAN GHANA SOURCE J004 L005 TEMA TEMA SOURCE J004 L007 D003 D003 SINK J004 L009 J004 J004 JUNCTION GHANA L005 TEMA L007 D003 L009 LINK CONNECTIONS

LINK LINK NAME FROM NODE TO NODE ---- --------- --------- ---------- L005 L005 GHANA J004 L007 L007 TEMA J004 L009 L009 J004 D003 +------------------------------+ | | | +----+ +----+ +----+ | | |GHAN|----|J004|----|TEMA| | | |SRCE| |....| |SRCE| | | +----+ +----+ +----+ | | | | | +----+ | | |D003| | | |SINK| | | +----+ | | | +------------------------------+ END OF INPUT PROCESSING -- NO ERRORS -- 1 WARNING ============================================================================== VLE K-VALUE DATA FOR SET 'SET01' SRK PURE COMPONENT DATA COMP CRITICAL CRITICAL ALPHA C1 C2 C3 TEMPERATURE PRESSURE TYPE DEG C BAR(GA) ---- ---------- ---------- ----- ---------- ---------- ---------- 1 31.04 72.80 1 0.8342 N/A N/A 2 -146.90 32.93 1 0.5505 N/A N/A 3 100.40 89.06 1 0.6356 N/A N/A 4 -82.60 44.99 1 0.4964 N/A N/A 5 32.30 47.83 1 0.6335 N/A N/A 6 96.67 41.48 1 0.7165 N/A N/A 7 134.98 35.46 1 0.7534 N/A N/A 8 152.00 36.98 1 0.7897 N/A N/A 9 187.24 32.80 1 0.8312 N/A N/A 10 196.50 32.68 1 0.8634 N/A N/A 11 234.20 28.67 1 0.9280 N/A N/A 12 267.00 26.34 1 1.0092 N/A N/A 13 295.60 23.81 1 1.0781 N/A N/A 14 374.20 220.18 2 1.0000 0.6620 0.8000 SRK INTERACTION PARAMETERS KIJ = A(I,J) + B(I,J)/T + C(I,J)/T**2 I J KA(I,J) KB(I,J) KC(I,J) UNITS FROM --- --- ---------- ---------- ---------- ----- ---- 1 2 -0.0300 0.00 0.00 DEG K SIMSCI BANK 1 3 0.1000 0.00 0.00 DEG K SIMSCI BANK 1 4 0.0933 0.00 0.00 DEG K SIMSCI BANK 1 5 0.1363 0.00 0.00 DEG K SIMSCI BANK 1 6 0.1289 0.00 0.00 DEG K SIMSCI BANK 1 7 0.1285 0.00 0.00 DEG K SIMSCI BANK 1 8 0.1430 0.00 0.00 DEG K SIMSCI BANK 1 9 0.1310 0.00 0.00 DEG K SIMSCI BANK 1 10 0.1310 0.00 0.00 DEG K SIMSCI BANK 1 11 0.1120 0.00 0.00 DEG K SIMSCI BANK 1 12 0.1100 0.00 0.00 DEG K SIMSCI BANK 1 13 0.1200 0.00 0.00 DEG K SIMSCI BANK 1 14 0.2300 0.00 0.00 DEG K SIMSCI BANK 2 3 0.1700 0.00 0.00 DEG K SIMSCI BANK 2 4 0.0300 0.00 0.00 DEG K SIMSCI BANK 2 5 0.0600 0.00 0.00 DEG K SIMSCI BANK 2 6 0.0900 0.00 0.00 DEG K SIMSCI BANK 2 7 0.1130 0.00 0.00 DEG K SIMSCI BANK 2 8 0.1130 0.00 0.00 DEG K SIMSCI BANK 2 9 0.1400 0.00 0.00 DEG K SIMSCI BANK 2 10 0.1400 0.00 0.00 DEG K SIMSCI BANK 2 11 0.1660 0.00 0.00 DEG K SIMSCI BANK 2 12 0.2000 0.00 0.00 DEG K SIMSCI BANK ============================================================================== VLE K-VALUE DATA FOR SET 'SET01' (Cont) I J KA(I,J) KB(I,J) KC(I,J) UNITS FROM --- --- ---------- ---------- ---------- ----- ---- 2 13 0.2000 0.00 0.00 DEG K MW CORRELATION 2 14 0.5300 0.00 0.00 DEG K SIMSCI BANK 3 4 0.0900 0.00 0.00 DEG K SIMSCI BANK 3 5 0.0850 0.00 0.00 DEG K SIMSCI BANK 3 6 0.0760 0.00 0.00 DEG K SIMSCI BANK 3 7 0.0600 0.00 0.00 DEG K SIMSCI BANK 3 8 0.0600 0.00 0.00 DEG K SIMSCI BANK 3 9 0.0650 0.00 0.00 DEG K SIMSCI BANK 3 10 0.0680 0.00 0.00 DEG K SIMSCI BANK 3 11 0.0680 0.00 0.00 DEG K SIMSCI BANK 3 12 0.0680 0.00 0.00 DEG K SIMSCI BANK 3 13 0.0600 0.00 0.00 DEG K SIMSCI BANK 3 14 0.1350 0.00 0.00 DEG K SIMSCI BANK 4 5 -7.800E-03 0.00 0.00 DEG K SIMSCI BANK 4 6 9.000E-03 0.00 0.00 DEG K SIMSCI BANK 4 7 0.0241 0.00 0.00 DEG K SIMSCI BANK 4 8 5.600E-03 0.00 0.00 DEG K SIMSCI BANK 4 9 -7.800E-03 0.00 0.00 DEG K SIMSCI BANK 4 10 0.0190 0.00 0.00 DEG K SIMSCI BANK 4 11 0.0374 0.00 0.00 DEG K SIMSCI BANK 4 12 0.0307 0.00 0.00 DEG K SIMSCI BANK 4 13 0.0448 0.00 0.00 DEG K SIMSCI BANK 4 14 0.5200 0.00 0.00 DEG K SIMSCI BANK 5 6 -2.200E-03 0.00 0.00 DEG K SIMSCI BANK 5 7 -1.000E-02 0.00 0.00 DEG K SIMSCI BANK 5 8 6.700E-03 0.00 0.00 DEG K SIMSCI BANK 5 10 5.600E-03 0.00 0.00 DEG K SIMSCI BANK 5 11 -0.0156 0.00 0.00 DEG K SIMSCI BANK 5 12 4.100E-03 0.00 0.00 DEG K SIMSCI BANK 5 13 0.0170 0.00 0.00 DEG K SIMSCI BANK 5 14 0.5500 0.00 0.00 DEG K SIMSCI BANK 6 7 -1.000E-02 0.00 0.00 DEG K SIMSCI BANK 6 9 7.800E-03 0.00 0.00 DEG K SIMSCI BANK 6 10 0.0233 0.00 0.00 DEG K SIMSCI BANK 6 11 -2.200E-03 0.00 0.00 DEG K SIMSCI BANK 6 12 4.400E-03 0.00 0.00 DEG K SIMSCI BANK 6 14 0.5300 0.00 0.00 DEG K SIMSCI BANK 7 8 1.100E-03 0.00 0.00 DEG K SIMSCI BANK 7 14 0.5200 0.00 0.00 DEG K SIMSCI BANK 8 10 0.0204 0.00 0.00 DEG K SIMSCI BANK 8 11 -0.0111 0.00 0.00 DEG K SIMSCI BANK 8 12 -4.000E-04 0.00 0.00 DEG K SIMSCI BANK 8 14 0.5200 0.00 0.00 DEG K SIMSCI BANK 9 14 0.5000 0.00 0.00 DEG K SIMSCI BANK 10 12 1.900E-03 0.00 0.00 DEG K SIMSCI BANK 10 13 -2.200E-03 0.00 0.00 DEG K SIMSCI BANK 10 14 0.5000 0.00 0.00 DEG K SIMSCI BANK 11 12 -1.100E-03 0.00 0.00 DEG K SIMSCI BANK 11 14 0.5000 0.00 0.00 DEG K SIMSCI BANK ============================================================================== VLE K-VALUE DATA FOR SET 'SET01' (Cont) I J KA(I,J) KB(I,J) KC(I,J) UNITS FROM --- --- ---------- ---------- ---------- ----- ---- 12 14 0.5000 0.00 0.00 DEG K SIMSCI BANK 13 14 0.5000 0.00 0.00 DEG K SIMSCI BANK ALL PAIRS NOT PRINTED ARE DEFAULTED TO IDEAL ============================================================================== THERMODYNAMIC SETS USED FOR EACH UNIT OPERATION DEFAULT METHOD IS SET01 THERMODYNAMIC SET UNIT OPERATIONS ----------------- --------------- SET01 ============================================================================== THERMODYNAMIC METHODS USED FOR EACH SET THERMODYNAMIC SET SET01 (DEFAULT) PROPERTY METHOD -------- ------ KVALUE(VLE) SOAVE-REDLICH-KWONG KVALUE(LLE) UNSPECIFIED KVALUE(SLE) UNSPECIFIED LIQUID ENTHALPY SOAVE-REDLICH-KWONG VAPOR ENTHALPY SOAVE-REDLICH-KWONG LIQUID DENSITY API VAPOR DENSITY SOAVE-REDLICH-KWONG LIQUID ENTROPY SOAVE-REDLICH-KWONG VAPOR ENTROPY SOAVE-REDLICH-KWONG LIQUID VISCOSITY PETROLEUM VAPOR VISCOSITY PETROLEUM LIQUID CONDUCTIVITY PETROLEUM VAPOR CONDUCTIVITY PETROLEUM SURFACE TENSION PETROLEUM LIQUID DIFFUSIVITY UNSPECIFIED ============================================================================== COMPONENT COMP. TYPE PHASE MOL. WEIGHT API --------------------- ----------- ----------- ----------- ----------- 1 CO2 LIBRARY VAP/LIQ 44.010 39.600 2 N2 LIBRARY VAP/LIQ 28.013 43.600 3 H2S LIBRARY VAP/LIQ 34.079 47.600 4 C1 LIBRARY VAP/LIQ 16.043 340.167 5 C2 LIBRARY VAP/LIQ 30.070 265.526 6 C3 LIBRARY VAP/LIQ 44.097 147.208 7 IC4 LIBRARY VAP/LIQ 58.124 119.788 8 NC4 LIBRARY VAP/LIQ 58.124 110.629 9 IC5 LIBRARY VAP/LIQ 72.151 95.727 10 NC5 LIBRARY VAP/LIQ 72.151 92.747 11 NC6 LIBRARY VAP/LIQ 86.178 81.602 12 NC7 LIBRARY VAP/LIQ 100.206 74.109 13 NC8 LIBRARY VAP/LIQ 114.233 68.698 14 H2O LIBRARY VAP/LIQ 18.015 10.063 COMPONENT NBP CRIT. TEMP. CRIT. PRES. CRIT. VOLM. C C BAR(GA) BBL/LB-MOL --------------------- ----------- ----------- ----------- ----------- 1 CO2 -78.480 31.040 72.802 0.2682 2 N2 -195.800 -146.900 32.931 0.2571 3 H2S -60.340 100.400 89.065 0.2787 4 C1 -161.490 -82.600 44.988 0.2824 5 C2 -88.630 32.300 47.825 0.4222 6 C3 -42.070 96.670 41.482 0.5792 7 IC4 -11.730 134.980 35.464 0.7503 8 NC4 -0.500 152.000 36.984 0.7275 9 IC5 27.850 187.240 32.799 0.8730 10 NC5 36.074 196.500 32.677 0.8673 11 NC6 68.740 234.200 28.675 1.0556 12 NC7 98.430 267.000 26.344 1.2325 13 NC8 125.670 295.600 23.811 1.4037 14 H2O 100.000 374.200 220.179 0.1581 COMPONENT ACEN. FACT. HEAT FORM. G FORM. BTU/LB-MOL BTU/LB-MOL --------------------- ----------- ----------- ----------- 1 CO2 0.23100 -169171.97 -169565.78 2 N2 0.04500 0.00 0.00 3 H2S 0.10000 -8849.66 -14391.10 4 C1 0.01040 -32066.21 -21726.14 5 C2 0.09860 -36120.21 -13810.45 6 C3 0.15290 -44650.04 -10139.64 7 IC4 0.17720 -57870.16 -9121.45 8 NC4 0.20130 -54072.23 -7169.22 9 IC5 0.22900 -66411.44 -6372.53 10 NC5 0.25060 -62968.62 -3672.87 11 NC6 0.29430 -71771.28 -34.39 12 NC7 0.34990 -80693.47 3477.00 13 NC8 0.39770 -89773.43 6828.55 14 H2O 0.34800 -104039.98 -98364.58

Solution HistoryIndex

Solution History

R PIPEPHASE Version 9.0 - INPUT MODULE ========================================== *** SCANNING GENERAL DATA COMPONENT DATA METHODS DATA THERMODYNAMIC DATA PROPERTY DATA STRUCTURE DATA END OF PRE-PROCESSING -- NO ERRORS R PIPEPHASE Version 9.0 - CROSS CHECKING MODULE =================================================== *** CHECKING GENERAL DATA STRUCTURE DATA CASE STUDY DATA PVTG DATA METHODS DATA *** INPUT REPRINT GENERAL DATA METHODS DATA STRUCTURE DATA NETWORK DATA *** FORMATTING DATA END OF INPUT PROCESSING -- NO ERRORS -- 1 WARNING END OF INPUT CROSS-CHECKING -- NO ERRORS. R PIPEPHASE Version 9.0 - CALCULATION MODULE ================================================ ITERATION NUMBER 0. 0 MAX PRESSURE IMBALANCE = 844.283 PSI AT NODE J004 RMS AVERAGE PRESSURE IMBALANCE = 844.283 PSI ITERATION NUMBER 1. 0 MAX PRESSURE IMBALANCE = -0.006 PSI AT NODE J004 RMS AVERAGE PRESSURE IMBALANCE = 0.006 PSI END OF NETWORK PROCESSING -- NO ERRORS -- 1 WARNING *** BASE CASE SOLVED *** *** NETWORK SIMULATION SOLVED CALCULATION STARTED 08:30:06 05/08/15 CALCULATION FINISHED 08:30:06 05/08/15 CALCULATION RUN TIME 0 HR 0 MIN 0 SEC NETWORK SIMULATION SOLVED

Node SummaryIndex

Node Summary - Base Case

NodePressureTemperatureGas Weight RateOil Weight RateWater Weight RateTotal Weight RateGas GV RateOil LV RateWater LV RateGas Specific GravityOil Specific GravityWater Specific GravityBARGDEG CLB/HRLB/HRLB/HRLB/HRMM FT3/DAYBBL/DAYBBL/DAYGHANA50.0047.00129,821.2270.000.00129,821.2359.820.000.000.680.000.00TEMA49.7927.00121,582.8750.000.00121,582.8859.850.000.000.640.000.00J00449.7934.56.0000.000.000.000.000.000.000.660.000.00D00349.6234.44-251,404.1020.000.00-251,404.10-119.670.000.000.660.000.00Rates reported at standard conditions. Specified values are underlined.

Link SummaryIndex

Link Summary - Base Case

Link NameInlet / OutletNode NameGas GV RateOil LV RateWater LV RatePressurePressure DropTemperatureGas HoldupLiquid HoldupMM FT3/DAYBBL/DAYBBL/DAYBARGBARGDEG CMM SCFABBLSL005InGHANA1.19330.000.0050.0047.00OutJ0041.16980.000.0049.790.2141.730.38300.00L007InTEMA1.11630.000.0049.7927.000.00OutJ0041.11630.000.0049.790.0027.000.00610.00L009InJ0042.28810.000.0049.7934.560.00OutD0032.29540.000.0049.620.1734.440.00890.00Rates reported at actual conditions. Gas holdup reported at standard conditions. Specified pressures are underlined.

Device SummaryIndex

Device Summary - Base Case

Link NameDevice NameDevice TypeInside DiameterMeasured LengthElevation ChangeOutlet PressureOutlet TemperatureOutlet In-Situ QualityOutlet Liquid HoldupTotal Mass RateINKMKMBARGDEG CLB/HRL00520PIPE16.061.500.0049.9142.131.000.00129,821.L005P016PIPE10.130.200.0049.7941.731.000.00129,821.L007P005PIPE16.060.020.0049.7927.001.000.00121,583.L009P007PIPE10.130.070.0049.6234.451.000.00251,404.L009P017PIPE16.060.010.0049.6234.441.000.00251,404.

Structure SummaryIndex

Structure Summary - Base Case

Link NameDevice NameDevice TypeInlet Inside DiameterOutlet Inside DiameterMeasured LengthElevation ChangeININKMKML00520PIPE16.0616.061.50.0L005P016PIPE10.1310.130.20.0L007P005PIPE16.0616.060.00.0L009P007PIPE10.1310.130.10.0L009P017PIPE16.0616.060.00.0

Velocity SummaryIndex

Velocity Summary - Base Case

Link NameDevice NameDevice TypeInlet Mixture VelocityOutlet Mixture VelocityCritical VelocityInlet Pressure GradientOutlet Pressure GradientPressure DropFT/SECFT/SECFT/SECPSI/FTPSI/FTBARGL00520PIPE9.819.611,356.28-0.0003-0.0188-0.09L005P016PIPE24.1924.201,341.17-0.0212-0.0027-0.12L007P005PIPE9.189.181,352.70-0.0002-0.0002-0.00L009P007PIPE47.3547.511,346.78-0.01020.0080-0.17L009P017PIPE18.8818.881,346.65-0.0009-0.0009-0.00

Results SummaryIndex

Results Summary - Base Case

Link NameDevice NameDevice TypeSeg 1 Mixture Flow RateInlet PressureOutlet PressureInlet TemperatureOutlet TemperatureInlet QualityOutlet QualityLB/HRBARGBARGDEG CDEG CFractionFractionL00520PIPE129,821.2350.0049.9147.0042.131.00001.0000L005P016PIPE129,821.2349.9149.7942.1341.731.00001.0000L007P005PIPE121,582.8849.7949.7927.0027.001.00001.0000L009P007PIPE251,404.0949.7949.6234.5634.451.00001.0000L009P017PIPE251,404.0949.6249.6234.4534.441.00001.0000

Flash SummaryIndex

Flash Report for Node GHANA - Base Case

VaporLiquid1Vap+Liq1Liquid2TotalTemp DEG C47.00Pressure BARG50.00

COMPONENTMole FractionCO2 0.0167000.0000000.0167000.0000000.016700N2 0.0070990.0000000.0070990.0000000.007099H2S 0.0000000.0000000.0000000.0000000.000000C1 0.8221680.0000000.8221680.0000000.822168C2 0.0988900.0000000.0988900.0000000.098890C3 0.0441900.0000000.0441900.0000000.044190IC4 0.0033990.0000000.0033990.0000000.003399NC4 0.0058990.0000000.0058990.0000000.005899IC5 0.0007000.0000000.0007000.0000000.000700NC5 0.0005000.0000000.0005000.0000000.000500NC6 0.0001000.0000000.0001000.0000000.000100NC7 0.0001000.0000000.0001000.0000000.000100NC8 0.0001000.0000000.0001000.0000000.000100H2O 0.0001560.0000000.0001560.0000000.000156

TOTAL RATESWeight Rate LB/HR 129,821.230.00129,821.230.00129,821.23Molar Rate MOLE/HR 6,587.900.006,587.900.006,587.90

PHASE PROPERTIESMass Fraction 1.0000000.0000001.0000000.0000001.000000Volume Fraction 1.0000000.0000001.0000000.0000001.000000Density LB/FT3 2.610.000.00Actual SPGR 0.68020.00000.0000Viscosity CP 0.01270.00000.0000Enthalpy BTU/LB 124.3780.0000.000124.378Surface Tension DYNES/CM 0.0000.000Molecular Wt 19.7060.00019.7060.00019.706

Flash Report for Node TEMA - Base Case





Flash Report for Node J004 - Base Case





Flash Report for Node D003 - Base Case





PhaseDataIndex

Phase Envelope for - L005 Base Case

Link NamePressureTemperatureidCodeBARGDEG CL005 -2.55E-04-40.02215204192L005 1.7407850303-29.18177550742L005 3.0954103885-24.6193898942L005 5.1162739539-19.99442921452L005 8.1310481313-15.40280840352L005 12.6285627069-11.01147583682L005 19.3380660289-7.11264637872L005 29.3474687935-4.24101263312L005 39.9573173942-3.37567960144L005 44.2797430463-3.49921818822L005 49.7882797568-3.99938300760L005 50.000027262-4.02639110270L005 54.3077919629-4.70307801612L005 63.9832802289-7.1836285732L005 72.4547746266-10.86311826472L005 78.9270493594-15.6190017962L005 82.7851904157-21.30544138962L005 83.7431085768-26.35123987135L005 79.9354033666-37.78339255322L005 78.1531294927-40.45429898752L005 77.2102451195-41.72903402453L005 72.7892991851-46.98675658221L005 68.9183401791-51.03865722331L005 64.9413820956-54.9251624971L005 60.9138318081-58.70490627081L005 56.872835038-62.42197659241L005 52.8486793956-66.10767720951L005 50.000027579-68.733284510L005 49.7882800894-68.92950596410L005 44.9637742734-73.46018592661L005 41.1581734228-77.14595632961L005 37.4787864061-80.84170411021L005 33.9491801608-84.54538290161L005 30.5897704636-88.25234555891L005 27.4172066451-91.95612480621L005 24.4440077215-95.64906415811L005 21.6784446008-99.3228293361L005 19.1246398749-102.9688215921L005 16.7828447089-106.57850838241L005 14.6498475499-110.14368303761L005 12.7194695372-113.65666277461L005 10.9831050474-117.11043304651L005 9.4302715344-120.49874543381L005 8.0491397504-123.81617577871L005 6.8270227341-127.05814887271L005 5.7508089921-130.22093564391L005 4.8073316362-133.30162837471L005 3.9836705744-136.29809902651L005 3.2673890683-139.20894522761L005 2.6467090554-142.03342793071L005 2.1106316712-144.77140417361L005 1.6490105387-147.42325781031L005 1.252585795-149.98983053121L005 0.6227098513-154.87239135041L005 0.1641993462-159.43252906231L005 -0.996056655315.559L005 -0.994916819316.53356655829L005 -0.993712511317.51713311659L005 -0.992440683418.50069967479L005 -0.991098174419.48426623299L005 -0.989681706920.46783279119L005 -0.988187884621.45139934949L005 -0.986613189122.43496590769L005 -0.984953977223.41853246589L005 -0.983206477524.40209902419L005 50.000027579478L005 50.000021786146.9996302148L005 50.000021786146.9996302148L005 49.95679489644.40366908388L005 49.914062063242.13975004398L005 49.914062063242.13975004398L005 49.911304976942.13414330458L005 49.910825080642.13334757118L005 49.910825080642.13334757118L005 49.788280089441.73002176978


Link NamePressureTemperatureidCodeBARGDEG CL007 -2.55E-04-35.2529628492L007 1.7407850303-22.99453656532L007 3.0954103885-17.87029971112L007 5.1162739539-12.71324027012L007 8.1310481313-7.65144745072L007 12.6285627069-2.9037326852L007 19.33806602891.15116948092L007 29.34746879353.82707322682L007 36.21906734554.27492995144L007 44.27974304633.73814991832L007 49.78828008942.86210072390L007 49.78912454252.86193464060L007 66.5560785687-2.87437625972L007 73.6624331713-7.00928394292L007 83.183379528-16.35032686542L007 85.3087691349-20.34595046062L007 86.7943248394-27.79525295015L007 81.5941701781-42.42941494252L007 75.987814355-49.15421498212L007 71.4811887029-53.47005979442L007 68.3517966784-56.23370206062L007 65.9442213437-58.33617087352L007 65.0240119744-59.14176112613L007 62.3404100486-61.49162341051L007 59.7387361719-63.76120490081L007 56.5745200104-66.50655915341L007 53.2010609878-69.42786990891L007 49.7891245425-72.39937854030L007 49.7882800894-72.40011821210L007 46.0057283772-75.74567865011L007 42.2893512578-79.11910069861L007 38.5688122366-82.61796707151L007 34.8990783682-86.22644868161L007 31.3307511924-89.92679417711L007 27.9079760344-93.69985797971L007 24.6670504803-97.5257181521L007 21.6357172142-101.38428954151L007 18.8330703013-105.25588142791L007 16.2699682906-109.12167338271L007 13.9498291218-112.96409757231L007 11.8696783205-116.76712496731L007 10.0213303953-120.51645909341L007 8.3926002156-124.19964514071L007 6.9684628689-127.80610494151L007 5.7321037746-131.32710982741L007 4.6658230538-134.75570388881L007 3.7517774848-138.08658989491L007 2.9725588154-141.31598926161L007 2.3116184347-144.44148618151L007 1.7535556599-147.46186452011L007 1.2842907184-150.37694448021L007 0.8911446342-153.18742446291L007 0.289493795-158.50088710621L007 -0.1256821469-163.42005060871L007 -0.996056655315.559L007 -0.993879862617.38363428639L007 -0.991469783919.21726857279L007 -0.9888057121.0509028599L007 -0.985865503122.88453714539L007 -0.982625530824.71817143169L007 -0.979060598626.5518057189L007 -0.975143881728.38544000439L007 -0.970846855830.21907429069L007 -0.966139227332.05270857699L007 49.7891245425278L007 49.789119462626.99999123648L007 49.789119462626.99999123648L007 49.787879445326.99785617488


Link NamePressureTemperatureidCodeBARGDEG CL009 -2.55E-04-37.50037659752L009 1.7407850303-25.83591757612L009 3.0954103885-20.93975816062L009 5.1162739539-15.99526654062L009 8.1310481313-11.11935145892L009 12.6285627069-6.51409591272L009 19.3380660289-2.53279629682L009 29.34746879350.17724888592L009 36.98470819530.70658476694L009 44.27974304630.28448846542L009 49.6154884993-0.51367168430L009 49.7882800894-0.54650348710L009 54.3077919629-1.56250428692L009 69.3136453783-7.45759421652L009 79.630387201-15.80269299772L009 83.8480404832-24.99598034522L009 84.037905038-27.55180980175L009 80.2067595112-39.60893480982L009 77.0135211543-44.24303345212L009 73.8228378184-48.06660220592L009 71.7282253596-50.34070754973L009 67.3919017766-54.69423933231L009 64.0739649458-57.82400147021L009 60.6695292453-60.93149187371L009 57.1859411936-64.05317988131L009 53.6411749536-67.21059642261L009 50.06022955-70.41587757211L009 49.7882800894-70.66084590940L009 49.6154884993-70.81664235610L009 46.472416786-73.67469391411L009 42.9091662579-76.98797772021L009 39.4021821607-80.3530718921L009 35.9819014416-83.76458078381L009 32.6762484959-87.21505136281L009 29.5096908951-90.69554477221L009 26.5025938299-94.19612682531L009 23.6708586914-97.70629122351L009 21.0258188958-101.2153224821L009 18.5743561939-104.71260260681L009 16.3191943979-108.1878645321L009 14.259324871-111.63139524591L009 12.3905189261-115.03419188141L009 10.7058858516-118.38807454161L009 9.1964408246-121.68576011191L009 7.8516536892-124.92090168261L009 6.6599567276-128.08809842791L009 5.6091965106-131.18288084071L009 4.6870212278-134.20167611331L009 3.8812002647-137.14175820441L009 3.1798770696-140.00118677051L009 2.5717595079-142.77873869311L009 2.0462540179-145.47383544171L009 1.5935510855-148.08646899881L009 1.2046700131-150.61712856521L009 0.586640852-155.43654779391L009 0.1367655198-159.94336406651L009 -0.996056655315.559L009 -0.994369628716.9871514889L009 -0.992541960618.42430297619L009 -0.990563898219.86145446419L009 -0.988425159821.29860595229L009 -0.986114916522.73575744029L009 -0.983621771524.17290892829L009 -0.980933740925.61006041639L009 -0.978038233127.04721190439L009 -0.974922028928.48436339249L009 49.788280089434.55937529248L009 49.788049132534.55922153058L009 49.788049132534.55922153058L009 49.707153269834.50541670858L009 49.626135504234.45161188658L009 49.626135504234.45161188658L009 49.616459129334.44053225368L009 49.616459129334.44053225368L009 49.614341432734.43912839028L009 49.614341432734.43912839028L009 49.617066619434.44578537518L009 49.617045368234.44570302558L009 49.617045368234.44570302558L009 49.615488499334.43975849348

L005Index

L005 - Base Case

Temperature Pressure Report - Base Case

NameDevice TypeDevice SegMWD Or Total LengthTVD Or Total ElevationInside DiameterPressureTemperatureAmbient TemperatureU FactorQualityDevice DomainKMKMINBARGDEG CDEG CBTU/HR-FT-F20PIPE Inlet 0.000.0016.0650.0047.0026.670.001.00X 20PIPE Seg 1 0.000.0016.0650.0047.0026.671.001.00X 20PIPE Seg 2 0.000.0016.0650.0047.0026.670.001.00X 20PIPE Seg 3 0.750.0016.0649.9644.4026.671.001.00X 20PIPE Seg 4 1.500.0016.0649.9142.1426.671.001.00X 20PIPE Seg 5 1.500.0016.0649.9142.1426.670.001.00X 20PIPE Outlet 1.500.0016.0649.9142.1326.671.001.00X P016PIPE Inlet 1.500.0010.1349.9142.1326.670.001.00X P016PIPE Seg 1 1.500.0010.1349.9142.1326.671.001.00X P016PIPE Seg 2 1.500.0010.1349.9142.1326.670.001.00X P016PIPE Outlet 1.700.0010.1349.7941.7326.671.001.00X

Holdup and Velocity Report - Base Case

NameDevice TypeDevice SegNo Slip Liquid HoldupSlip Liquid HoldupTotal Liquid HoldupLiquid Superficial VelocityGas Superficial VelocityMixture VelocitySonic VelocityFlow Regime Corr / T-DABBLSFT/SECFT/SECFT/SECFT/SEC20PIPE Inlet 0.0000.0000.0000.0000.000---- ----20PIPE Seg 1 0.0000.0000.0000.0009.8149.8141,356.2841-PH 1-PH20PIPE Seg 2 0.0000.0000.0000.0009.8149.8141,356.2841-PH 1-PH20PIPE Seg 3 0.0000.0000.0000.0009.7609.7601,351.9971-PH 1-PH20PIPE Seg 4 0.0000.0000.0000.0009.6609.6601,344.4541-PH 1-PH20PIPE Seg 5 0.0000.0000.0000.0009.6609.6601,344.4541-PH 1-PH20PIPE Outlet 0.0000.0000.0000.0009.6139.6131,341.1611-PH 1-PHP016PIPE Inlet 0.0000.0000.0000.0009.6139.6131,341.1611-PH 1-PHP016PIPE Seg 1 0.0000.0000.0000.00024.19124.1911,341.1681-PH 1-PHP016PIPE Seg 2 0.0000.0000.0000.00024.19124.1911,341.1681-PH 1-PHP016PIPE Outlet 0.0000.0000.0000.00024.20024.2001,339.8091-PH 1-PH

Pressure Gradient Report - L005 Base Case

NameDevice TypeDevice SegFriction Pressure GradientElevation Pressure GradientTotal Pressure GradientFriction Pressure DropElevation Pressure DropPSI/FTPSI/FTPSI/FTBARGBARG20PIPE Inlet 20PIPE Seg 1 -0.0000.000-0.000-0.0000.00020PIPE Seg 2 -0.0000.000-0.000-0.0000.00020PIPE Seg 3 -0.0000.000-0.000-0.0430.00020PIPE Seg 4 -0.0000.000-0.000-0.0430.00020PIPE Seg 5 -0.0000.000-0.000-0.0430.00020PIPE Outlet -0.000-0.018-0.019-0.000-0.003P016PIPE Inlet -0.000-0.018-0.019-0.000-0.003P016PIPE Seg 1 -0.003-0.018-0.021-0.000-0.000P016PIPE Seg 2 -0.003-0.018-0.021-0.000-0.000P016PIPE Outlet -0.0030.000-0.003-0.1220.000

Viscosity Density Report - Base Case

NameDevice TypeDevice SegOil ViscosityLiquid ViscosityVapor ViscosityLiquid DensityVapor DensitySlip DensityNo Slip DensityCPCPCPKG/M3KG/M3KG/M3KG/M320PIPE Inlet 20PIPE Seg 1 0.0000.0000.0130.00041.8252.6112.61120PIPE Seg 2 0.0000.0000.0130.00041.8252.6112.61120PIPE Seg 3 0.0000.0000.0130.00042.0552.6252.62520PIPE Seg 4 0.0000.0000.0130.00042.4922.6532.65320PIPE Seg 5 0.0000.0000.0130.00042.4922.6532.65320PIPE Outlet 0.0000.0000.0130.00042.6992.6662.666P016PIPE Inlet 0.0000.0000.0130.00042.6992.6662.666P016PIPE Seg 1 0.0000.0000.0130.00042.6982.6662.666P016PIPE Seg 2 0.0000.0000.0130.00042.6982.6662.666P016PIPE Outlet 0.0000.0000.0130.00042.6822.6652.665

Friction Report - Base Case

NameDevice TypeDevice SegFriction DensityFriction VelocityFriction DiameterFriction ViscosityFriction FactorReynolds NumberLiquid Surface TensionKG/M3FT/SECINCPDYNES/CM20PIPE Inlet 0.00020PIPE Seg 1 2.6119.81416.0630.0130.0134.008E+060.00020PIPE Seg 2 2.6119.8140.0000.0130.0134.008E+060.00020PIPE Seg 3 2.6259.76016.0630.0130.0134.018E+060.00020PIPE Seg 4 2.6539.66016.0630.0130.0134.037E+060.00020PIPE Seg 5 2.6539.6600.0000.0130.0134.037E+060.00020PIPE Outlet 2.6669.61316.0630.0130.0134.046E+060.000P016PIPE Inlet 2.6669.6130.0000.0130.0134.046E+060.000P016PIPE Seg 1 2.66624.19110.1260.0130.0146.419E+060.000P016PIPE Seg 2 2.66624.1910.0000.0130.0146.419E+060.000P016PIPE Outlet 2.66524.20010.1260.0130.0146.423E+060.000

Heat Transfer Report - Base Case

NameDevice TypeDevice SegFluid Thermal Conduct.Inside Film Thermal ResistancePipe Thermal ResistanceInsulation Thermal ResistanceSurrounding Thermal ResistanceLiquid EnthalpyVapor EnthalpyHydrate FormationBTU/HR-FT-FHR-FT2-F/BTUHR-FT2-F/BTUHR-FT2-F/BTUHR-FT2-F/BTUBTU/LBBTU/LB20PIPE Inlet 0.00000.00000.00000.0000 20PIPE Seg 1 0.00000.00000.00000.00000.000124.378N 20PIPE Seg 2 0.00000.00000.00000.00000.000124.378N 20PIPE Seg 3 0.00000.00000.00000.00000.000123.013N 20PIPE Seg 4 0.00000.00000.00000.00000.000120.457N 20PIPE Seg 5 0.00000.00000.00000.00000.000120.457N 20PIPE Outlet 0.00000.00000.00000.00000.000119.264N P016PIPE Inlet 0.00000.00000.00000.00000.000119.264N P016PIPE Seg 1 0.00000.00000.00000.00000.000119.262N P016PIPE Seg 2 0.00000.00000.00000.00000.000119.262N P016PIPE Outlet 0.00000.00000.00000.00000.000119.078N

L007Index

L007 - Base Case


NameDevice TypeDevice SegMWD Or Total LengthTVD Or Total ElevationInside DiameterPressureTemperatureAmbient TemperatureU FactorQualityDevice DomainKMKMINBARGDEG CDEG CBTU/HR-FT-FP005PIPE Inlet 0.000.0016.0649.7927.0026.670.001.00X P005PIPE Seg 1 0.000.0016.0649.7927.0026.671.001.00X P005PIPE Seg 2 0.000.0016.0649.7927.0026.670.001.00X P005PIPE Outlet 0.020.0016.0649.7927.0026.671.001.00X


NameDevice TypeDevice SegNo Slip Liquid HoldupSlip Liquid HoldupTotal Liquid HoldupLiquid Superficial VelocityGas Superficial VelocityMixture VelocitySonic VelocityFlow Regime Corr / T-DABBLSFT/SECFT/SECFT/SECFT/SECP005PIPE Inlet 0.0000.0000.0000.0000.000---- ----P005PIPE Seg 1 0.0000.0000.0000.0009.1819.1811,352.7001-PH 1-PHP005PIPE Seg 2 0.0000.0000.0000.0009.1819.1811,352.7001-PH 1-PHP005PIPE Outlet 0.0000.0000.0000.0009.1819.1811,352.6901-PH 1-PH


NameDevice TypeDevice SegFriction Pressure GradientElevation Pressure GradientTotal Pressure GradientFriction Pressure DropElevation Pressure DropPSI/FTPSI/FTPSI/FTBARGBARGP005PIPE Inlet P005PIPE Seg 1 -0.0000.000-0.000-0.0000.000P005PIPE Seg 2 -0.0000.000-0.000-0.0000.000P005PIPE Outlet -0.0000.000-0.000-0.0010.000


NameDevice TypeDevice SegOil ViscosityLiquid ViscosityVapor ViscosityLiquid DensityVapor DensitySlip DensityNo Slip DensityCPCPCPKG/M3KG/M3KG/M3KG/M3P005PIPE Inlet P005PIPE Seg 1 0.0000.0000.0120.00041.8732.6142.614P005PIPE Seg 2 0.0000.0000.0120.00041.8732.6142.614P005PIPE Outlet 0.0000.0000.0120.00041.8722.6142.614


NameDevice TypeDevice SegFriction DensityFriction VelocityFriction DiameterFriction ViscosityFriction FactorReynolds NumberLiquid Surface TensionKG/M3FT/SECINCPDYNES/CMP005PIPE Inlet 0.000P005PIPE Seg 1 2.6149.18116.0630.0120.0133.884E+060.000P005PIPE Seg 2 2.6149.1810.0000.0120.0133.884E+060.000P005PIPE Outlet 2.6149.18116.0630.0120.0133.884E+060.000


NameDevice TypeDevice SegFluid Thermal Conduct.Inside Film Thermal ResistancePipe Thermal ResistanceInsulation Thermal ResistanceSurrounding Thermal ResistanceLiquid EnthalpyVapor EnthalpyHydrate FormationBTU/HR-FT-FHR-FT2-F/BTUHR-FT2-F/BTUHR-FT2-F/BTUHR-FT2-F/BTUBTU/LBBTU/LBP005PIPE Inlet 0.00000.00000.00000.0000 P005PIPE Seg 1 0.00000.00000.00000.00000.00096.729N P005PIPE Seg 2 0.00000.00000.00000.00000.00096.729N P005PIPE Outlet 0.00000.00000.00000.00000.00096.728N

L009Index

L009 - Base Case


NameDevice TypeDevice SegMWD Or Total LengthTVD Or Total ElevationInside DiameterPressureTemperatureAmbient TemperatureU FactorQualityDevice DomainKMKMINBARGDEG CDEG CBTU/HR-FT-FP007PIPE Inlet 0.000.0010.1349.7934.5626.670.001.00X P007PIPE Seg 1 0.000.0010.1349.7934.5626.671.001.00X P007PIPE Seg 2 0.000.0010.1349.7934.5626.670.001.00X P007PIPE Seg 3 0.040.0010.1349.7134.5126.671.001.00X P007PIPE Seg 4 0.070.0010.1349.6334.4526.671.001.00X P007PIPE Seg 5 0.070.0010.1349.6334.4526.670.001.00X P007PIPE Seg 6 0.070.0010.1349.6234.4426.671.001.00X P007PIPE Seg 7 0.070.0010.1349.6234.4426.670.001.00X P007PIPE Seg 8 0.070.0010.1349.6134.4426.671.001.00X P007PIPE Seg 9 0.070.0010.1349.6134.4426.670.001.00X P007PIPE Outlet 0.070.0010.1349.6234.4526.671.001.00X P017PIPE Inlet 0.070.0016.0649.6234.4526.670.001.00X P017PIPE Seg 1 0.070.0016.0649.6234.4526.671.001.00X P017PIPE Seg 2 0.070.0016.0649.6234.4526.670.001.00X P017PIPE Outlet 0.080.0016.0649.6234.4426.671.001.00X


NameDevice TypeDevice SegNo Slip Liquid HoldupSlip Liquid HoldupTotal Liquid HoldupLiquid Superficial VelocityGas Superficial VelocityMixture VelocitySonic VelocityFlow Regime Corr / T-DABBLSFT/SECFT/SECFT/SECFT/SECP007PIPE Inlet 0.0000.0000.0000.0000.000---- ----P007PIPE Seg 1 0.0000.0000.0000.00047.35447.3541,346.7811-PH 1-PHP007PIPE Seg 2 0.0000.0000.0000.00047.35447.3541,346.7811-PH 1-PHP007PIPE Seg 3 0.0000.0000.0000.00047.38947.3891,346.2141-PH 1-PHP007PIPE Seg 4 0.0000.0000.0000.00047.46147.4611,346.1501-PH 1-PHP007PIPE Seg 5 0.0000.0000.0000.00047.46147.4611,346.1501-PH 1-PHP007PIPE Seg 6 0.0000.0000.0000.00047.50047.5001,346.5821-PH 1-PHP007PIPE Seg 7 0.0000.0000.0000.00047.50047.5001,346.5821-PH 1-PHP007PIPE Seg 8 0.0000.0000.0000.00047.50547.5051,346.6201-PH 1-PHP007PIPE Seg 9 0.0000.0000.0000.00047.50547.5051,346.6201-PH 1-PHP007PIPE Outlet 0.0000.0000.0000.00047.50547.5051,346.6601-PH 1-PHP017PIPE Inlet 0.0000.0000.0000.00047.50547.5051,346.6601-PH 1-PHP017PIPE Seg 1 0.0000.0000.0000.00018.87818.8781,346.6511-PH 1-PHP017PIPE Seg 2 0.0000.0000.0000.00018.87818.8781,346.6511-PH 1-PHP017PIPE Outlet 0.0000.0000.0000.00018.87818.8781,346.6321-PH 1-PH


NameDevice TypeDevice SegFriction Pressure GradientElevation Pressure GradientTotal Pressure GradientFriction Pressure DropElevation Pressure DropPSI/FTPSI/FTPSI/FTBARGBARGP007PIPE Inlet P007PIPE Seg 1 -0.0100.000-0.010-0.0000.000P007PIPE Seg 2 -0.0100.000-0.010-0.0000.000P007PIPE Seg 3 -0.0100.000-0.010-0.0810.000P007PIPE Seg 4 -0.0100.000-0.010-0.0810.000P007PIPE Seg 5 -0.0100.000-0.010-0.0810.000P007PIPE Seg 6 -0.010-0.018-0.029-0.003-0.006P007PIPE Seg 7 -0.010-0.018-0.029-0.003-0.006P007PIPE Seg 8 -0.0100.000-0.010-0.0020.000P007PIPE Seg 9 -0.0100.000-0.010-0.0020.000P007PIPE Outlet -0.0100.0180.008-0.0030.006P017PIPE Inlet -0.0100.0180.008-0.0030.006P017PIPE Seg 1 -0.0010.000-0.001-0.0000.000P017PIPE Seg 2 -0.0010.000-0.001-0.0000.000P017PIPE Outlet -0.0010.000-0.001-0.0020.000


NameDevice TypeDevice SegOil ViscosityLiquid ViscosityVapor ViscosityLiquid DensityVapor DensitySlip DensityNo Slip DensityCPCPCPKG/M3KG/M3KG/M3KG/M3P007PIPE Inlet P007PIPE Seg 1 0.0000.0000.0120.00042.2412.6372.637P007PIPE Seg 2 0.0000.0000.0120.00042.2412.6372.637P007PIPE Seg 3 0.0000.0000.0120.00042.2092.6352.635P007PIPE Seg 4 0.0000.0000.0120.00042.1462.6312.631P007PIPE Seg 5 0.0000.0000.0120.00042.1462.6312.631P007PIPE Seg 6 0.0000.0000.0120.00042.1112.6292.629P007PIPE Seg 7 0.0000.0000.0120.00042.1112.6292.629P007PIPE Seg 8 0.0000.0000.0120.00042.1062.6292.629P007PIPE Seg 9 0.0000.0000.0120.00042.1062.6292.629P007PIPE Outlet 0.0000.0000.0120.00042.1062.6292.629P017PIPE Inlet 0.0000.0000.0120.00042.1062.6292.629P017PIPE Seg 1 0.0000.0000.0120.00042.1072.6292.629P017PIPE Seg 2 0.0000.0000.0120.00042.1072.6292.629P017PIPE Outlet 0.0000.0000.0120.00042.1072.6292.629


NameDevice TypeDevice SegFriction DensityFriction VelocityFriction DiameterFriction ViscosityFriction FactorReynolds NumberLiquid Surface TensionKG/M3FT/SECINCPDYNES/CMP007PIPE Inlet 0.000P007PIPE Seg 1 2.63747.35410.1260.0120.0131.258E+070.000P007PIPE Seg 2 2.63747.3540.0000.0120.0131.258E+070.000P007PIPE Seg 3 2.63547.38910.1260.0120.0131.259E+070.000P007PIPE Seg 4 2.63147.46110.1260.0120.0131.259E+070.000P007PIPE Seg 5 2.63147.4610.0000.0120.0131.259E+070.000P007PIPE Seg 6 2.62947.50010.1260.0120.0131.259E+070.000P007PIPE Seg 7 2.62947.5000.0000.0120.0131.259E+070.000P007PIPE Seg 8 2.62947.50510.1260.0120.0131.259E+070.000P007PIPE Seg 9 2.62947.5050.0000.0120.0131.259E+070.000P007PIPE Outlet 2.62947.50510.1260.0120.0131.259E+070.000P017PIPE Inlet 2.62947.5050.0000.0120.0131.259E+070.000P017PIPE Seg 1 2.62918.87816.0630.0120.0127.938E+060.000P017PIPE Seg 2 2.62918.8780.0000.0120.0127.938E+060.000P017PIPE Outlet 2.62918.87816.0630.0120.0127.938E+060.000


NameDevice TypeDevice SegFluid Thermal Conduct.Inside Film Thermal ResistancePipe Thermal ResistanceInsulation Thermal ResistanceSurrounding Thermal ResistanceLiquid EnthalpyVapor EnthalpyHydrate FormationBTU/HR-FT-FHR-FT2-F/BTUHR-FT2-F/BTUHR-FT2-F/BTUHR-FT2-F/BTUBTU/LBBTU/LBP007PIPE Inlet 0.00000.00000.00000.0000 P007PIPE Seg 1 0.00000.00000.00000.00000.000108.174N P007PIPE Seg 2 0.00000.00000.00000.00000.000108.174N P007PIPE Seg 3 0.00000.00000.00000.00000.000108.165N P007PIPE Seg 4 0.00000.00000.00000.00000.000108.148N P007PIPE Seg 5 0.00000.00000.00000.00000.000108.148N P007PIPE Seg 6 0.00000.00000.00000.00000.000108.136N P007PIPE Seg 7 0.00000.00000.00000.00000.000108.136N P007PIPE Seg 8 0.00000.00000.00000.00000.000108.132N P007PIPE Seg 9 0.00000.00000.00000.00000.000108.132N P007PIPE Outlet 0.00000.00000.00000.00000.000108.135N P017PIPE Inlet 0.00000.00000.00000.00000.000108.135N P017PIPE Seg 1 0.00000.00000.00000.00000.000108.138N P017PIPE Seg 2 0.00000.00000.00000.00000.000108.138N P017PIPE Outlet 0.00000.00000.00000.00000.000108.135N

takoradi interconnect (case 1)

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