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U.S.A. 888/996-7100 TEN CANAL PARK EUROPE (32) 2/701-9555 CAMBRIDGE, MASSACHUSETTS 02141 617/949-1000 PLATFORM: WIN32 DECEMBER 2, 2008 VERSION: 21.0 Build 52 TUESDAY INSTALLATION: 9:39:19 P.M. THIS COPY OF ASPEN PLUS LICENSED TO UNIV OF UTAH 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 FOR PURPOSES OF THE FAR, THIS SOFTWARE SHALL BE DEEMED TO BE "UNPUBLISHED" AND LICENSED WITH DISCLOSURE PROHIBITIONS.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. TEN CANAL PARK, CAMBRIDGE, MA 02141. *** INPUT SUMMARY *** >>CURRENT RUN ORIGINAL RUN DECEMBER 2, 2008 9:39:19 P.M. TUESDAY INPUT FILE: _3435yfk.inm RUN ID : _3435yfk 1 ; 2 ;Input file created by Aspen Plus Rel. 21.0 at 21:38:35 Tue Dec 2, 2008 3 ;Directory Z:\public_html\Aspen2803\Oblad Thermo Runid THERMO - EXAMPLE 13.3 4 ; 5 6 7 DYNAMICS 8 DYNAMICS RESULTS=ON 9 10 TITLE 'Methan hydration' 11 12 IN-UNITS MET VOLUME-FLOW='cum/hr' ENTHALPY-FLO='Gcal/hr' & 13 HEAT-TRANS-C='kcal/hr-sqm-K' PRESSURE=bar TEMPERATURE=C & 14 VOLUME=cum DELTA-T=C HEAD=meter MOLE-DENSITY='kmol/cum' & 15 MASS-DENSITY='kg/cum' MOLE-ENTHALP='kcal/mol' & 16 MASS-ENTHALP='kcal/kg' HEAT=Gcal MOLE-CONC='mol/l' & 17 PDROP=bar 18 19 DEF-STREAMS CONVEN ALL 20 21 DESCRIPTION " 22 General Simulation with Metric Units : 23 C, bar, kg/hr, kmol/hr, Gcal/hr, cum/hr. 24 25 Property Method: None 26 27 Flow basis for input: Mole 28 29 Stream report composition: Mole flow 30 " 31 32 DATABANKS PURE20 / AQUEOUS / SOLIDS / INORGANIC / & 33 NOASPENPCD 34 35 PROP-SOURCES PURE20 / AQUEOUS / SOLIDS / INORGANIC 36 37 COMPONENTS 38 METHANE CH4 / 39 WATER H2O / 40 CO CO / 41 CO2 CO2 / 42 H2 H2 43 44 FLOWSHEET 45 BLOCK GIBBS IN=1 OUT=2 46 BLOCK EQUILIB IN=4 OUT=3 5 47 48 PROPERTIES IDEAL 49 50 STREAM 1 51 SUBSTREAM MIXED TEMP=1000. PRES=1. 52 MOLE-FLOW METHANE 2. / WATER 3. 53 54 STREAM 4 55 SUBSTREAM MIXED TEMP=1000. PRES=1. 56 MOLE-FLOW METHANE 2. / WATER 3. 57 58 BLOCK EQUILIB REQUIL 59 PARAM NREAC=2 TEMP=1000. PRES=100. 60 STOIC 1 METHANE -1. * / WATER -1. * / CO 1. * / H2 & 61 3. * 62 STOIC 2 METHANE -1. * / WATER -2. * / CO2 1. * / H2 & 63 4. * 64 TAPP-SPEC 1 0.0 / 2 0.0 65 66 BLOCK GIBBS RGIBBS 67 PARAM TEMP=1000. PRES=100. 68 69 EO-CONV-OPTI 70 71 STREAM-REPOR MOLEFLOW 72 ; 73 ; 74 ; 75 ; 76 ; *** INPUT TRANSLATOR MESSAGES *** PDF updated TIME = 10.07 *** CALCULATION TRACE *** METHAN HYDRATION *** FLOWSHEET ANALYSIS MESSAGES *** FLOWSHEET CONNECTIVITY BY STREAMS STREAM SOURCE DEST STREAM SOURCE DEST 1 ---- GIBBS 4 ---- EQUILIB 2 GIBBS ---- 3 EQUILIB ---- 5 EQUILIB ---- FLOWSHEET CONNECTIVITY BY BLOCKS BLOCK INLETS OUTLETS GIBBS 1 2 EQUILIB 4 3 5 COMPUTATION ORDER FOR THE FLOWSHEET IS: EQUILIB GIBBS Calculations begin time 4.05 SIMULATION CALCULATIONS BEGIN TIME = 4.05 ENTHALPY CALCULATION FOR INLET STREAM 4 OF BLOCK EQUILIB TIME = 4.05 KODE = 2 NTRIAL = 1 T =1273.1500 P = 100000. V = 1.00000 Q = 0.00000 UOS BLOCK EQUILIB MODEL: REQUIL TIME = 4.05 EQUILK CONVERGED IN 9 ITERATIONS. KODE = 2 T = 1273. P = 0.1000E+08 V = 1.000 Q = 0.7512E+05 REACTION EXTENTS (KGMOL/SEC) = 0.2756D-03 0.6545D-04 ENTHALPY CALCULATION FOR INLET STREAM 1 OF BLOCK GIBBS TIME = 4.08 KODE = 2 NTRIAL = 1 T =1273.1500 P = 100000. V = 1.00000 Q = 0.00000 UOS BLOCK GIBBS MODEL: RGIBBS TIME = 4.25 ITER = 9 T = 1273.1500 P = 1.000000E+07 PHASES = VAPOR STREAM 2 WILL BE FLASHED FOR PROPERTY CALCULATIONS. KODE = 2 NO. TEMP ITER = 1 TEMP = 1273.15 KPHASE = 1 KODE = 2 T = 1273.15 P = 1.000000E+07 Q = 1.542953E-11 STREAM 2 WILL BE FLASHED FOR PROPERTY CALCULATIONS. KODE = 2 NO. TEMP ITER = 1 TEMP = 1273.15 KPHASE = 1 KODE = 2 T = 1273.15 P = 1.000000E+07 Q = 1.542953E-11 STREAM 2 WILL BE FLASHED FOR PROPERTY CALCULATIONS. KODE = 2 NO. TEMP ITER = 1 TEMP = 1273.15 KPHASE = 1 KODE = 2 T = 1273.15 P = 1.000000E+07 Q = 1.542953E-11 STREAM 2 WILL BE FLASHED FOR PROPERTY CALCULATIONS. KODE = 2 NO. TEMP ITER = 1 TEMP = 1273.15 KPHASE = 1 KODE = 2 T = 1273.15 P = 1.000000E+07 Q = 1.542953E-11 Report Writer entered Time = 193.16 STREAM 2 WILL BE FLASHED FOR PROPERTY CALCULATIONS. KODE = 2 NO. TEMP ITER = 1 TEMP = 1273.15 KPHASE = 1 KODE = 2 T = 1273.15 P = 1.000000E+07 Q = 1.542953E-11 Results generated Time = 193.63 Report Writer entered Time = 202.75 STREAM 2 WILL BE FLASHED FOR PROPERTY CALCULATIONS. KODE = 2 NO. TEMP ITER = 1 TEMP = 1273.15 KPHASE = 1 KODE = 2 T = 1273.15 P = 1.000000E+07 Q = 1.542953E-11 Results generated Time = 203.10 RUN SAVED NO ERRORS OR WARNINGS GENERATED