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U.S.A. 888/996-7100 200 WHEELER ROAD EUROPE (44) 1189-226555 BURLINGTON, MASSACHUSETTS 01803 781/221-6400 PLATFORM: WIN32 MAY 18, 2011 VERSION: 24.0 Build 63 WEDNESDAY INSTALLATION: 9:50:29 P.M. THIS COPY OF ASPEN PLUS LICENSED TO CO-LAN - CAPE OPEN LABOR ASPEN PLUS (R) IS A PROPRIETARY PRODUCT OF ASPEN TECHNOLOGY, INC. (ASPENTECH), AND MAY BE USED ONLY UNDER AGREEMENT WITH ASPENTECH. RESTRICTED RIGHTS LEGEND: USE, REPRODUCTION, OR DISCLOSURE BY THE U.S. GOVERNMENT IS SUBJECT TO RESTRICTIONS SET FORTH IN (i) FAR 52.227-14, Alt. III, (ii) FAR 52.227-19, (iii) DFARS 252.227-7013(c)(1)(ii), or (iv) THE ACCOMPANYING LICENSE AGREEMENT, AS APPLICABLE. FOR PURPOSES OF THE FAR, THIS SOFTWARE SHALL BE DEEMED TO BE "UNPUBLISHED" AND LICENSED WITH DISCLOSURE PROHIBITIONS. CONTRACTOR/SUBCONTRACTOR: ASPEN TECHNOLOGY, INC. 200 WHEELER ROAD, BURLINGTON, MA 01803. *** INPUT SUMMARY *** >>CURRENT RUN ORIGINAL RUN MAY 18, 2011 9:50:29 P.M. WEDNESDAY INPUT FILE: _4939qsy.inm RUN ID : _4939qsy 1 ; 2 ;Input file created by Aspen Plus Rel. 24.0 at 21:50:26 Wed May 18, 2011 3 ;Directory C:\Documents and Settings\MICHEL PONS\Mes documents\Input\CERE Runid UNCONNECTEDMIXERV72 4 ; 5 6 7 8 IN-UNITS MET VOLUME-FLOW='cum/hr' ENTHALPY-FLO='Gcal/hr' & 9 HEAT-TRANS-C='kcal/hr-sqm-K' PRESSURE=bar TEMPERATURE=C & 10 VOLUME=cum DELTA-T=C HEAD=meter MOLE-DENSITY='kmol/cum' & 11 MASS-DENSITY='kg/cum' MOLE-ENTHALP='kcal/mol' & 12 MASS-ENTHALP='kcal/kg' HEAT=Gcal MOLE-CONC='mol/l' & 13 PDROP=bar 14 15 DEF-STREAMS CONVEN ALL 16 17 SIM-OPTIONS OLD-DATABANK=NO 18 19 DESCRIPTION " 20 General Simulation with Metric Units : 21 C, bar, kg/hr, kmol/hr, Gcal/hr, cum/hr. 22 23 Property Method: None 24 25 Flow basis for input: Mole 26 27 Stream report composition: Mole flow 28 " 29 30 DATABANKS 'APV72 PURE20' / 'APV72 AQUEOUS' / 'APV72 SOLIDS' / & 31 'APV72 INORGANIC' / NOASPENPCD 32 33 PROP-SOURCES 'APV72 PURE20' / 'APV72 AQUEOUS' / 'APV72 SOLIDS' & 34 / 'APV72 INORGANIC' 35 36 COMPONENTS 37 ETHANE C2H6 / 38 PROPANE C3H8 / 39 N-BUTANE C4H10-1 / 40 N-PEN-01 C5H12-1 41 42 FLOWSHEET 43 BLOCK B1 IN=1 OUT=3 44 45 PROPERTIES PENG-ROB 46 47 PROP-DATA PRKBV-1 48 IN-UNITS MET VOLUME-FLOW='cum/hr' ENTHALPY-FLO='Gcal/hr' & 49 HEAT-TRANS-C='kcal/hr-sqm-K' PRESSURE=bar TEMPERATURE=C & 50 VOLUME=cum DELTA-T=C HEAD=meter MOLE-DENSITY='kmol/cum' & 51 MASS-DENSITY='kg/cum' MOLE-ENTHALP='kcal/mol' & 52 MASS-ENTHALP='kcal/kg' HEAT=Gcal MOLE-CONC='mol/l' & 53 PDROP=bar 54 PROP-LIST PRKBV 55 BPVAL ETHANE PROPANE 1.10000000E-3 0.0 0.0 -273.1500000 & 56 726.8500000 57 BPVAL PROPANE ETHANE 1.10000000E-3 0.0 0.0 -273.1500000 & 58 726.8500000 59 BPVAL ETHANE N-BUTANE 9.60000000E-3 0.0 0.0 -273.1500000 & 60 726.8500000 61 BPVAL N-BUTANE ETHANE 9.60000000E-3 0.0 0.0 -273.1500000 & 62 726.8500000 63 BPVAL ETHANE N-PEN-01 7.80000000E-3 0.0 0.0 -273.1500000 & 64 726.8500000 65 BPVAL N-PEN-01 ETHANE 7.80000000E-3 0.0 0.0 -273.1500000 & 66 726.8500000 67 BPVAL PROPANE N-BUTANE 3.30000000E-3 0.0 0.0 -273.1500000 & 68 726.8500000 69 BPVAL N-BUTANE PROPANE 3.30000000E-3 0.0 0.0 -273.1500000 & 70 726.8500000 71 BPVAL PROPANE N-PEN-01 .0267000000 0.0 0.0 -273.1500000 & 72 726.8500000 73 BPVAL N-PEN-01 PROPANE .0267000000 0.0 0.0 -273.1500000 & 74 726.8500000 75 BPVAL N-BUTANE N-PEN-01 .0174000000 0.0 0.0 -273.1500000 & 76 726.8500000 77 BPVAL N-PEN-01 N-BUTANE .0174000000 0.0 0.0 -273.1500000 & 78 726.8500000 79 80 STREAM 1 81 SUBSTREAM MIXED TEMP=25. PRES=16. 82 MOLE-FLOW ETHANE 0.1 / PROPANE 0.3 / & 83 N-BUTANE 0.5 / N-PEN-01 0.1 84 85 BLOCK B1 CAPE-OPEN 86 PARAMETERS BYPASS-USER=YES NCHAR=1 87 CHAR CHAR-LIST="{CBA52F41-EA91-4761-A2BC-87169AC37320}" 88 CONNECT STREAM=1 PORT="IN" 89 CONNECT STREAM=3 PORT="OUT" 90 91 EO-CONV-OPTI 92 ; 93 ; 94 ; 95 ; 96 ; *** INPUT TRANSLATOR MESSAGES *** *** THIS RUN USES THE PROPERTIES ENTERPRISE DATABASE *** CO-BF9A7BB49918\SQLEXPRESS.APV72 : (DATAVERSION - 24.0.0.63) CO-BF9A7BB49918\SQLEXPRESS.FACTV72 : (DATAVERSION - 24.0.0.63) CO-BF9A7BB49918\SQLEXPRESS.NISTV72 : (DATAVERSION - 24.0.0.63) PDF updated TIME = 10.96 *** CALCULATION TRACE *** *** FLOWSHEET ANALYSIS MESSAGES *** FLOWSHEET CONNECTIVITY BY STREAMS STREAM SOURCE DEST STREAM SOURCE DEST 1 ---- B1 3 B1 ---- FLOWSHEET CONNECTIVITY BY BLOCKS BLOCK INLETS OUTLETS B1 1 3 COMPUTATION ORDER FOR THE FLOWSHEET IS: B1 Calculations begin time 0.38 SIMULATION CALCULATIONS BEGIN TIME = 0.41 ENTHALPY CALCULATION FOR INLET STREAM 1 OF BLOCK B1 TIME = 0.43 KODE = 2 NTRIAL = 4 T = 298.1500 P = 1.600000E+06 V = 0.00000 Q = 0.00000 UOS BLOCK B1 MODEL: CAPE-OPEN TIME = 0.78 KODE = 2 NTRIAL = 4 T = 298.1500 P = 1.600000E+06 V = 0.00000 Q = 0.00000 KODE = 2 NTRIAL = 4 T = 298.1500 P = 1.600000E+06 V = 0.00000 Q = 0.00000 * WARNING WHILE EXECUTING UNIT OPERATIONS BLOCK: "B1" (MODEL: "CAPE-OPEN") (BALMAS.1) BLOCK B1 IS NOT IN MASS BALANCE: MASS INLET FLOW = 0.52512648E+02, MASS OUTLET FLOW = 0.52512648E+37 RELATIVE DIFFERENCE = 0.10000000E+36 CHECK USER SUBROUTINE