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                                                                        TM
 AAAAA   SSSSS   PPPPP   EEEEE   NN    N   PPPPP   L       U   U   SSSSS
 A   A   S       P   P   E       N N   N   P   P   L       U   U   S    
 AAAAA   SSSSS   PPPPP   EEEEE   N   N N   PPPPP   L       U   U   SSSSS
 A   A       S   P       E       N    NN   P       L       U   U       S
 A   A   SSSSS   P       EEEEE   N     N   P       LLLLL   UUUUU   SSSSS

 ASPEN PLUS IS A TRADEMARK OF           HOTLINE:
 ASPEN TECHNOLOGY, INC.                 U.S.A. 888/996-7001
 TEN CANAL PARK                         EUROPE (32) 2/724-0100
 CAMBRIDGE, MASSACHUSETTS 02141                             
 617/949-1000

 PLATFORM: WIN32                                         NOVEMBER 18, 2016   
 VERSION: 11.1   Build 192                               FRIDAY      
 INSTALLATION: TEAM_EAT                                  7:41:40 A.M.        

 THIS COPY OF ASPEN PLUS LICENSED TO                                 


      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      TO BE "UNPUBLISHED" AND LICENSED WITH DISCLOSURE PROHIBITIONS.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                           NOVEMBER 18, 2016   
   7:41:40 A.M.                           FRIDAY      
   INPUT FILE: _5441dze.inm                                                                    
   RUN ID : _5441dze
     1    ;
     2    ;Input file created by Aspen Plus Rel. 11.1 at 07:41:39 Fri Nov 18, 2016
     3    ;Directory C:\Program Files (x86)\AspenTech\Working Folders\Aspen Plus 11.1  Runid SIMU
     4    ;
     5
     6
     7
     8    TITLE 'REACTOR COMPARISON'
     9
    10    IN-UNITS MET
    11
    12    DEF-STREAMS CONVEN ALL
    13
    14    ACCOUNT-INFO ACCOUNT=R PROJECT-ID=E PROJECT-NAME="1"  &
    15            USER-NAME="R"
    16
    17    DESCRIPTION "
    18        General Simulation with English Units :
    19        F, psi, lb/hr, lbmol/hr, Btu/hr, cuft/hr.
    20
    21        Property Method: None
    22
    23        Flow basis for input: Mole
    24
    25        Stream report composition: Mole flow
    26        "
    27
    28    DATABANKS PURE11  / AQUEOUS  / SOLIDS  / INORGANIC  /  &
    29            NOASPENPCD
    30
    31    PROP-SOURCES PURE11  / AQUEOUS  / SOLIDS  / INORGANIC
    32
    33    COMPONENTS
    34        ETHANOL C2H6O-2 /
    35        ACID C2H4O2-1 /
    36        ACETATE C4H8O2-3 /
    37        WATER H2O
    38
    39    FLOWSHEET
    40        BLOCK B1 IN=FEED OUT=F-STOIC F-GIBBS F-PLUG F-CSTR
    41        BLOCK RSTOIC IN=F-STOIC OUT=P-STOIC
    42        BLOCK RGIBBS IN=F-GIBBS OUT=P-GIBBS
    43        BLOCK RPLUG IN=F-PLUG OUT=P-PLUG
    44        BLOCK RCSTR IN=F-CSTR OUT=P-CSTR
    45
    46    PROPERTIES NRTL-HOC
    47        PROPERTIES NRTL
    48
    49    PROP-DATA HOCETA-1
    50        IN-UNITS ENG
    51        PROP-LIST HOCETA
    52        BPVAL ETHANOL ETHANOL 1.400000000
    53        BPVAL ETHANOL ACID 2.500000000
    54        BPVAL ETHANOL ACETATE 1.300000000
    55        BPVAL ETHANOL WATER 1.550000000
    56        BPVAL ACID ETHANOL 2.500000000
    57        BPVAL ACID ACID 4.500000000
    58        BPVAL ACID ACETATE 2.000000000
    59        BPVAL ACID WATER 2.500000000
    60        BPVAL ACETATE ETHANOL 1.300000000
    61        BPVAL ACETATE ACID 2.000000000
    62        BPVAL ACETATE ACETATE .5300000000
    63        BPVAL ACETATE WATER 1.300000000
    64        BPVAL WATER ETHANOL 1.550000000
    65        BPVAL WATER ACID 2.500000000
    66        BPVAL WATER ACETATE 1.300000000
    67        BPVAL WATER WATER 1.700000000
    68
    69    PROP-DATA NRTL-1
    70        IN-UNITS ENG
    71        PROP-LIST NRTL
    72        BPVAL ETHANOL ACETATE -1.151200000 943.9628324 .3000000000  &
    73            0.0 0.0 0.0 104.0000032 173.2100026
    74        BPVAL ACETATE ETHANOL -.2431000000 509.3204359 .3000000000  &
    75            0.0 0.0 0.0 104.0000032 173.2100026
    76        BPVAL ETHANOL WATER -.8009000000 443.1239965 .3000000000  &
    77            0.0 0.0 0.0 76.98200338 212.0000023
    78        BPVAL WATER ETHANOL 3.457800000 -1054.945612 .3000000000  &
    79            0.0 0.0 0.0 76.98200338 212.0000023
    80        BPVAL ACETATE WATER -3.719800000 2315.048921 .2000000000  &
    81            0.0 0.0 0.0 32.00000374 158.7200027
    82        BPVAL WATER ACETATE 9.463200000 -3070.229375 .2000000000  &
    83            0.0 0.0 0.0 32.00000374 158.7200027
    84
    85    STREAM FEED
    86        SUBSTREAM MIXED TEMP=70. <C> PRES=1.
    87        MOLE-FLOW ETHANOL 186.59 / ACID 192.6 / WATER 8.892
    88
    89    BLOCK RSTOIC RSTOIC
    90        PARAM TEMP=70. <C> PRES=1.
    91        STOIC 1 MIXED ACID -1. / ETHANOL -1. / ACETATE 1. /  &
    92            WATER 1.
    93        CONV 1 MIXED ETHANOL 0.7
    94
    95    BLOCK RGIBBS RGIBBS
    96        PARAM TEMP=70. <C> PRES=1.
    97
    98    BLOCK RCSTR RCSTR
    99        PARAM VOL=0.14 <cum> TEMP=70. <C> PRES=1. NPHASE=2
   100        BLOCK-OPTION FREE-WATER=NO
   101        REACTIONS RXN-IDS=R-1
   102
   103    BLOCK RPLUG RPLUG
   104        PARAM TYPE=T-SPEC LENGTH=2. <meter> DIAM=0.33 <meter>  &
   105            NPHASE=2
   106        T-SPEC 0.0 70. <C>
   107        BLOCK-OPTION FREE-WATER=NO
   108        REACTIONS RXN-IDS=R-1
   109
   110    BLOCK B1 DUPL
   111
   112    EO-CONV-OPTI
   113
   114    REACTIONS R-1 POWERLAW
   115        REAC-DATA 1
   116        REAC-DATA 2
   117        RATE-CON 1 PRE-EXP=190000000. ACT-ENERGY=59500000. <J/kmol>
   118        RATE-CON 2 PRE-EXP=50000000. ACT-ENERGY=50500000. <J/kmol>
   119        STOIC 1 MIXED ETHANOL -1. / ACID -1. / ACETATE 1. /  &
   120            WATER 1.
   121        STOIC 2 MIXED ACETATE -1. / WATER -1. / ETHANOL 1. /  &
   122            ACID 1.
   123        POWLAW-EXP 1 MIXED ETHANOL 1. / MIXED ACID 1. / MIXED  &
   124            ACETATE 0. / MIXED WATER 0.
   125        POWLAW-EXP 2 MIXED ACETATE 0. / MIXED WATER 0. / MIXED  &
   126            ETHANOL 0. / MIXED ACID 0.
   127    ;
   128    ;
   129    ;
   130    ;
   131    ;
 *** INPUT TRANSLATOR MESSAGES ***


      INFORMATION                                              (ESBPLD.1)       
      BINARY PARAMETERS HOCETA (DATA SET 1) FOR MODEL ESHOC                     
      ARE RETRIEVED FROM SDF TABLE.  TABLE NAME = ESHOC                         
 
 

 PDF updated                                                                      TIME =      2.05

 *** CALCULATION TRACE ***

 REACTOR COMPARISON                                              

 *** FLOWSHEET ANALYSIS MESSAGES ***

 FLOWSHEET CONNECTIVITY BY STREAMS       

   STREAM     SOURCE     DEST           STREAM     SOURCE     DEST
   FEED       ----       B1             F-STOIC    B1         RSTOIC  
   F-GIBBS    B1         RGIBBS         F-PLUG     B1         RPLUG   
   F-CSTR     B1         RCSTR          P-STOIC    RSTOIC     ----    
   P-GIBBS    RGIBBS     ----           P-PLUG     RPLUG      ----    
   P-CSTR     RCSTR      ----                                         

 FLOWSHEET CONNECTIVITY BY BLOCKS        

   BLOCK        INLETS                         OUTLETS
   B1           FEED                           F-STOIC F-GIBBS F-PLUG      
                                               F-CSTR                      
   RSTOIC       F-STOIC                        P-STOIC                     
   RGIBBS       F-GIBBS                        P-GIBBS                     
   RPLUG        F-PLUG                         P-PLUG                      
   RCSTR        F-CSTR                         P-CSTR                      

      COMPUTATION ORDER FOR THE FLOWSHEET IS:
      B1 RSTOIC RGIBBS RPLUG RCSTR 

Calculations begin                                                              time      0.12


 SIMULATION CALCULATIONS BEGIN                                                    TIME =      0.12

      ENTHALPY CALCULATION FOR INLET STREAM FEED OF BLOCK B1                      TIME =      0.12
      KODE = 2  NTRIAL =   5  T =   343.15  P =  0.1013E+06  V =  0.0000E+00  Q =  0.0000E+00

      UOS BLOCK B1       MODEL: DUPL                                              TIME =      0.17

      UOS BLOCK RSTOIC   MODEL: RSTOIC                                            TIME =      0.17
      KODE = 2  NTRIAL =   4  T =   343.15  P =  0.1013E+06  V =  0.0000E+00  Q = -0.4133E+05

      UOS BLOCK RGIBBS   MODEL: RGIBBS                                            TIME =      0.17
      ITER =  15  T =   343.15  P =  0.1013E+06  PHASES = VAPOR

      UOS BLOCK RPLUG    MODEL: RPLUG                                             TIME =      0.22
        AT REACTOR EXIT :
        LENGTH =   2.0000      DIAMETER =  0.33000      RESIDENCE TIME =   26.369    
        PROCESS STREAM T =    343.15     P =   0.10132E+06 H =  -0.40387E+08 V =   0.00000E+00

      UOS BLOCK RCSTR    MODEL: RCSTR                                             TIME =      0.30
      REACTOR DUTY =  -39466.     VOLUME =  0.14000     RES TIME =   21.572    

 Report Writer entered                                                            Time =    453.32

 Results generated                                                                Time =    453.40

 Report Writer entered                                                            Time =    453.47

 Results generated                                                                Time =    453.50

RUN SAVED



 NO ERRORS OR WARNINGS GENERATED

 Report Writer entered                                                            Time =    461.29

 Results generated                                                                Time =    461.33

 Report Writer entered                                                            Time =    461.37

 Results generated                                                                Time =    461.40

RUN SAVED



 NO ERRORS OR WARNINGS GENERATED
