


                                     +
                                   + + +
                                   + + +
                                   + + +
                             +     + + +     +
                           + + +   + + +   + + +
                           + + +   + + +   + + +
                           + + +   + + +   + + +
                     +     + + +   + + +   + + +     +
                   + + +   + + +   + + +   + + +   + + +
                   + + +   + + +   + + +   + + +   + + +
                   + + +   + + +   + + +   + + +   + + +
             +     + + +   + + +   + + +   + + +   + + +     +
           + + +   + + +   + + +   + + +   + + +   + + +   + + +
           + + +   + + +   + + +   + + +   + + +   + + +   + + +
           + + +   + + +   + + +   + + +   + + +   + + +   + + +
           + + +   + + +   + + +   + + +   + + +   + + +   + + +
           + + +   + + +   + + +   + + +   + + +   + + +   + + +
           + + +   + + +   + + +   + + +   + + +   + + +   + + +
           + + +   + + +   + + +   + + +   + + +   + + +   + + +
           + + +   + + +   + + +   + + +   + + +   + + +   + + +
             +     + + +   + + +   + + +   + + +   + + +     +
                   + + +   + + +   + + +   + + +   + + +
                   + + +   + + +   + + +   + + +   + + +
                   + + +   + + +   + + +   + + +   + + +
                     +       +     + + +     +       +
                                   + + +
                                   + + +
                                   + + +
 ASPENTECH                         + + +
                                   + + +
 FLOWSHEET SIMULATION              + + +
 FOR THE PROCESS INDUSTRIES        + + +
                                     +


                                                                        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                                         OCTOBER 6, 2016     
 VERSION: 11.1   Build 192                               THURSDAY    
 INSTALLATION: TEAM_EAT                                  10:30:42 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                           OCTOBER 6, 2016     
   10:30:42 A.M.                          THURSDAY    
   INPUT FILE: _2518ony.inm                                                                    
   RUN ID : _2518ony
     1    ;
     2    ;Input file created by Aspen Plus Rel. 11.1 at 10:30:42 Thu Oct 6, 2016
     3    ;Directory E:\Aspen Plus\T2 - Copy  Runid t1
     4    ;
     5
     6
     7
     8    TITLE 'Tutorial'
     9
    10    IN-UNITS ENG
    11
    12    DEF-STREAMS CONVEN ALL
    13
    14    ACCOUNT-INFO ACCOUNT=1 PROJECT-ID=1  &
    15            PROJECT-NAME="HOS3124@GMAIL.COM"  &
    16            USER-NAME="HOSSEIN KHAKPOUR"
    17
    18    DESCRIPTION "
    19        General Simulation with English Units :
    20        F, psi, lb/hr, lbmol/hr, Btu/hr, cuft/hr.
    21
    22        Property Method: None
    23
    24        Flow basis for input: Mole
    25
    26        Stream report composition: Mole flow
    27        "
    28
    29    DATABANKS PURE11  / AQUEOUS  / SOLIDS  / INORGANIC  /  &
    30            NOASPENPCD
    31
    32    PROP-SOURCES PURE11  / AQUEOUS  / SOLIDS  / INORGANIC
    33
    34    COMPONENTS
    35        WATER H2O /
    36        ACETONE C3H6O-1 /
    37        MIBK C6H12O-2
    38
    39    FLOWSHEET
    40        BLOCK MIXER IN=FEED MIBK OUT=PRUDUCT
    41        BLOCK FLASH1 IN=PRUDUCT OUT=VAPOR1 MA1 WA1
    42        BLOCK B1 IN=WA1 MIBK2 OUT=PRDUCT2
    43        BLOCK B2 IN=PRDUCT2 OUT=VAPOR2 MA2 WATER
    44
    45    PROPERTIES NRTL FREE-WATER=STEAMNBS
    46        PROPERTIES IDEAL / SRK
    47
    48    PROP-DATA NRTL-1
    49        IN-UNITS ENG
    50        PROP-LIST NRTL
    51        BPVAL WATER ACETONE .0544000000 755.9488740 .3000000000 0.0  &
    52            0.0 0.0 68.00000346 203.1800024
    53        BPVAL ACETONE WATER 6.398100000 -3256.183774 .3000000000  &
    54            0.0 0.0 0.0 68.00000346 203.1800024
    55        BPVAL WATER MIBK 9.162943000 -2247.739182 .2000000000 0.0  &
    56            0.0 0.0 32.00000374 240.8000021
    57        BPVAL MIBK WATER -3.230481000 2175.978583 .2000000000 0.0  &
    58            0.0 0.0 32.00000374 240.8000021
    59        BPVAL ACETONE MIBK -5.445200000 3300.340834 .3000000000 0.0  &
    60            0.0 0.0 77.00000338 230.2340022
    61        BPVAL MIBK ACETONE 5.301300000 -3124.634735 .3000000000 0.0  &
    62            0.0 0.0 77.00000338 230.2340022
    63
    64    STREAM FEED
    65        SUBSTREAM MIXED TEMP=75. PRES=50. MASS-FLOW=100.
    66        MASS-FRAC WATER 0.5 / ACETONE 0.5
    67
    68    STREAM MIBK
    69        SUBSTREAM MIXED TEMP=75. PRES=50. MASS-FLOW=100.
    70        MOLE-FLOW MIBK 1.
    71
    72    STREAM MIBK2
    73        SUBSTREAM MIXED TEMP=75. PRES=50. MASS-FLOW=50.
    74        MASS-FRAC MIBK 1.
    75
    76    BLOCK B1 MIXER
    77
    78    BLOCK MIXER MIXER
    79        PARAM NPHASE=1 PHASE=L
    80        BLOCK-OPTION FREE-WATER=NO
    81
    82    BLOCK B2 FLASH3
    83        PARAM TEMP=75. PRES=50.
    84
    85    BLOCK FLASH1 FLASH3
    86        PARAM TEMP=75. PRES=50.
    87
    88    EO-CONV-OPTI
    89    ;
    90    ;
    91    ;
    92    ;
    93    ;
 *** INPUT TRANSLATOR MESSAGES ***


  *   WARNING IN THE "STREAM" PARAGRAPH WHICH BEGINS ON LINE 68                 
      STREAM NAME: MIBK                                        (STSTRM.28)      
      COMPONENT MOLE FLOWS OF SUBSTREAM: "MIXED"                                
      ARE NORMALIZED TO THE TOTAL MOLE FLOW VALUE.                              
 
 

 PDF updated                                                                      TIME =      0.12

 *** CALCULATION TRACE ***

 TUTORIAL                                                        

 *** FLOWSHEET ANALYSIS MESSAGES ***

 FLOWSHEET CONNECTIVITY BY STREAMS       

   STREAM     SOURCE     DEST           STREAM     SOURCE     DEST
   MIBK       ----       MIXER          FEED       ----       MIXER   
   MIBK2      ----       B1             PRUDUCT    MIXER      FLASH1  
   VAPOR1     FLASH1     ----           MA1        FLASH1     ----    
   WA1        FLASH1     B1             PRDUCT2    B1         B2      
   VAPOR2     B2         ----           MA2        B2         ----    
   WATER      B2         ----                                         

 FLOWSHEET CONNECTIVITY BY BLOCKS        

   BLOCK        INLETS                         OUTLETS
   MIXER        FEED MIBK                      PRUDUCT                     
   FLASH1       PRUDUCT                        VAPOR1 MA1 WA1              
   B1           WA1 MIBK2                      PRDUCT2                     
   B2           PRDUCT2                        VAPOR2 MA2 WATER            

      COMPUTATION ORDER FOR THE FLOWSHEET IS:
      MIXER FLASH1 B1 B2 

Calculations begin                                                              time      0.07


 SIMULATION CALCULATIONS BEGIN                                                    TIME =      0.07

      ENTHALPY CALCULATION FOR INLET STREAM FEED OF BLOCK MIXER                   TIME =      0.07
      KODE = 2  NTRIAL =   2  T =   297.04  P =  0.3447E+06  V =  0.0000E+00  Q =  0.0000E+00

      ENTHALPY CALCULATION FOR INLET STREAM MIBK OF BLOCK MIXER                   TIME =      0.07
      KODE = 2  NTRIAL =   1  T =   297.04  P =  0.3447E+06  V =  0.0000E+00  Q =  0.0000E+00

      UOS BLOCK MIXER    MODEL: MIXER                                             TIME =      0.07
      KODE = 1   NO. TEMP ITER =    5     TEMP =   291.65    
      KPHASE =    2 KODE =    1 T =   291.65     P =  0.34474E+06 Q =  0.00000E+00

      UOS BLOCK FLASH1   MODEL: FLASH3                                            TIME =      0.07
      KODE = 2  NTRIAL =   9  T =   297.04  P =  0.3447E+06  V =  0.0000E+00  BETA =  0.5818      Q =   412.3    

      ENTHALPY CALCULATION FOR INLET STREAM MIBK2 OF BLOCK B1                     TIME =      0.07
      KODE = 2  NTRIAL =   1  T =   297.04  P =  0.3447E+06  V =  0.0000E+00  Q =  0.0000E+00

      UOS BLOCK B1       MODEL: MIXER                                             TIME =      0.07
      NO. TEMP ITER =    5     TEMP =   293.10    
      KODE = 1  NTRIAL =   2  T =   293.10  P =  0.3447E+06  V =  0.0000E+00  Q =  0.0000E+00

      UOS BLOCK B2       MODEL: FLASH3                                            TIME =      0.07
      KODE = 2  NTRIAL =   8  T =   297.04  P =  0.3447E+06  V =  0.0000E+00  BETA =  0.7730      Q =   123.0    

 Report Writer entered                                                            Time =      0.22

 Results generated                                                                Time =      0.24

RUN SAVED



 NO ERRORS OR WARNINGS GENERATED

RUN SAVED



 NO ERRORS OR WARNINGS GENERATED


*** INPUT SPECIFICATION MESSAGES ***

 RENAME       IS  NEW 10/06/2016   10:40:57:14 
 ;
 ;Input file created by Aspen Plus Rel. 11.1 at 10:40:54 Thu Oct 6, 2016
 ;Directory E:\Aspen Plus\T2 - Copy  Runid t1
 ;
 
 
 RENAME
     BLOCK B2 FLASH2 / B1 MIXER2 / MIXER MIXER1

 DESIGN-SPEC  DS-1     IS NEW 10/06/2016   10:40:57:14 
 DESIGN-SPEC DS-1
     DEFINE WATER MASS-FRAC STREAM=WATER SUBSTREAM=MIXED  &
         COMPONENT=WATER
     SPEC "WATER" TO ".9"
     TOL-SPEC ".0001"
     VARY MASS-FLOW STREAM=MIBK2 SUBSTREAM=MIXED COMPONENT=MIBK
     LIMITS "25" "100"

 PDF updated                                                                      TIME =    614.61
 THIS COPY OF ASPEN PLUS LICENSED TO                                 
 
 DESIGN SPEC: DS-1 WILL BE INTERPRETED 
 
 *** FLOWSHEET ANALYSIS MESSAGES ***

 FLOWSHEET CONNECTIVITY BY STREAMS       

   STREAM     SOURCE     DEST           STREAM     SOURCE     DEST
   MIBK       ----       MIXER1         FEED       ----       MIXER1  
   MIBK2      ----       MIXER2         PRUDUCT    MIXER1     FLASH1  
   VAPOR1     FLASH1     ----           MA1        FLASH1     ----    
   WA1        FLASH1     MIXER2         PRDUCT2    MIXER2     FLASH2  
   VAPOR2     FLASH2     ----           MA2        FLASH2     ----    
   WATER      FLASH2     ----                                         

 FLOWSHEET CONNECTIVITY BY BLOCKS        

   BLOCK        INLETS                         OUTLETS
   MIXER1       FEED MIBK                      PRUDUCT                     
   FLASH1       PRUDUCT                        VAPOR1 MA1 WA1              
   MIXER2       WA1 MIBK2                      PRDUCT2                     
   FLASH2       PRDUCT2                        VAPOR2 MA2 WATER            

      BLOCK $OLVER01 (METHOD: SECANT  ) HAS BEEN DEFINED TO CONVERGE
                SPECS : DS-1

      COMPUTATION ORDER FOR THE FLOWSHEET IS:
      MIXER1 FLASH1 
      $OLVER01 MIXER2 FLASH2 
      (RETURN $OLVER01) 


Calculations begin                                                              time    616.87


      CONVERGENCE BLOCK $OLVER01  METHOD: SECANT                                  TIME =    616.87
      ---FLASH STREAM MIBK2   :
      KODE = 2  NTRIAL =   1  T =   297.04  P =  0.3447E+06  V =  0.0000E+00  Q =  0.0000E+00

      UOS BLOCK MIXER2   MODEL: MIXER                                             TIME =    616.95
      NO. TEMP ITER =    5     TEMP =   293.10    
      KODE = 1  NTRIAL =   2  T =   293.10  P =  0.3447E+06  V =  0.0000E+00  Q =  0.0000E+00

      UOS BLOCK FLASH2   MODEL: FLASH3                                            TIME =    616.95
      KODE = 2  NTRIAL =   8  T =   297.04  P =  0.3447E+06  V =  0.0000E+00  BETA =  0.7730      Q =   123.0    

      CONVERGENCE BLOCK $OLVER01  METHOD: SECANT                                  TIME =    616.95
      ---FLASH STREAM MIBK2   :
      KODE = 2  NTRIAL =   1  T =   297.04  P =  0.3447E+06  V =  0.0000E+00  Q =  0.0000E+00
      SPEC   1 ERROR = -0.31950E-01 OLD X =  0.62898E-04 NEW X =  0.63841E-04

  LOOP $OLVER01 ITER    1:  1 VARS NOT CONVERGED, MAX ERR/TOL     -319.50         TIME =    616.96

      UOS BLOCK MIXER2   MODEL: MIXER                                             TIME =    616.96
      NO. TEMP ITER =    5     TEMP =   293.04    
      KODE = 1  NTRIAL =   2  T =   293.04  P =  0.3447E+06  V =  0.0000E+00  Q =  0.0000E+00

      UOS BLOCK FLASH2   MODEL: FLASH3                                            TIME =    616.97
      KODE = 2  NTRIAL =   8  T =   297.04  P =  0.3447E+06  V =  0.0000E+00  BETA =  0.7706      Q =   124.2    

      CONVERGENCE BLOCK $OLVER01  METHOD: SECANT                                  TIME =    616.97
      ---FLASH STREAM MIBK2   :
      KODE = 2  NTRIAL =   1  T =   297.04  P =  0.3447E+06  V =  0.0000E+00  Q =  0.0000E+00
      SPEC   1 ERROR = -0.31118E-01 OLD X =  0.63841E-04 NEW X =  0.99136E-04

  LOOP $OLVER01 ITER    2:  1 VARS NOT CONVERGED, MAX ERR/TOL     -311.18         TIME =    616.97

      UOS BLOCK MIXER2   MODEL: MIXER                                             TIME =    616.97
      NO. TEMP ITER =    5     TEMP =   291.21    
      KODE = 1  NTRIAL =   2  T =   291.21  P =  0.3447E+06  V =  0.0000E+00  Q =  0.0000E+00

      UOS BLOCK FLASH2   MODEL: FLASH3                                            TIME =    616.97
      KODE = 2  NTRIAL =   7  T =   297.04  P =  0.3447E+06  V =  0.0000E+00  BETA =  0.6923      Q =   165.1    

      CONVERGENCE BLOCK $OLVER01  METHOD: SECANT                                  TIME =    616.97
      ---FLASH STREAM MIBK2   :
      KODE = 2  NTRIAL =   1  T =   297.04  P =  0.3447E+06  V =  0.0000E+00  Q =  0.0000E+00
      SPEC   1 ERROR = -0.70207E-02 OLD X =  0.99136E-04 NEW X =  0.11713E-03

  LOOP $OLVER01 ITER    3:  1 VARS NOT CONVERGED, MAX ERR/TOL     -70.207         TIME =    616.97

      UOS BLOCK MIXER2   MODEL: MIXER                                             TIME =    616.97
      NO. TEMP ITER =    5     TEMP =   290.45    
      KODE = 1  NTRIAL =   2  T =   290.45  P =  0.3447E+06  V =  0.0000E+00  Q =  0.0000E+00

      UOS BLOCK FLASH2   MODEL: FLASH3                                            TIME =    616.97
      KODE = 2  NTRIAL =   7  T =   297.04  P =  0.3447E+06  V =  0.0000E+00  BETA =  0.6583      Q =   184.2    

      CONVERGENCE BLOCK $OLVER01  METHOD: SECANT                                  TIME =    616.97
      ---FLASH STREAM MIBK2   :
      KODE = 2  NTRIAL =   1  T =   297.04  P =  0.3447E+06  V =  0.0000E+00  Q =  0.0000E+00
      SPEC   1 ERROR =  0.16269E-02 OLD X =  0.11713E-03 NEW X =  0.11332E-03

  LOOP $OLVER01 ITER    4:  1 VARS NOT CONVERGED, MAX ERR/TOL      16.269         TIME =    616.97

      UOS BLOCK MIXER2   MODEL: MIXER                                             TIME =    616.97
      NO. TEMP ITER =    5     TEMP =   290.60    
      KODE = 1  NTRIAL =   2  T =   290.60  P =  0.3447E+06  V =  0.0000E+00  Q =  0.0000E+00

      UOS BLOCK FLASH2   MODEL: FLASH3                                            TIME =    616.97
      KODE = 2  NTRIAL =   7  T =   297.04  P =  0.3447E+06  V =  0.0000E+00  BETA =  0.6653      Q =   180.2    

      CONVERGENCE BLOCK $OLVER01  METHOD: SECANT                                  TIME =    616.97
      ---FLASH STREAM MIBK2   :
      KODE = 2  NTRIAL =   1  T =   297.04  P =  0.3447E+06  V =  0.0000E+00  Q =  0.0000E+00
      SPEC   1 ERROR = -0.58010E-04                          X =  0.11332E-03

  LOOP $OLVER01 ITER    5:    *** CONVERGED *** , MAX ERR/TOL    -0.58010         TIME =    616.97

 Report Writer entered                                                            Time =    618.33

 Results generated                                                                Time =    618.36

RUN SAVED



 NO ERRORS OR WARNINGS GENERATED


 NO ERRORS OR WARNINGS GENERATED

RUN SAVED



 NO ERRORS OR WARNINGS GENERATED

 *** CALCULATION TRACE ***

 TUTORIAL                                                        


RUN SAVED



 NO ERRORS OR WARNINGS GENERATED

 *** CALCULATION TRACE ***

 TUTORIAL                                                        


RUN SAVED



 NO ERRORS OR WARNINGS GENERATED

 *** CALCULATION TRACE ***

 TUTORIAL                                                        


RUN SAVED



 NO ERRORS OR WARNINGS GENERATED

 *** CALCULATION TRACE ***

 TUTORIAL                                                        



*** INPUT SPECIFICATION MESSAGES ***

 OUT-UNITS    IS  NEW 11/09/2016   12:12:35:95 
 OUT-UNITS ENG

 STREAM-REPOR IS  NEW 11/09/2016   12:12:35:95 
 STREAM-REPOR NOMOLEFLOW MASSFRAC

 PDF updated                                                                      TIME =      0.04
 THIS COPY OF ASPEN PLUS LICENSED TO                                 
 
 DESIGN SPEC: DS-1 WILL BE INTERPRETED 
 

Calculations begin                                                              time      0.16


 Report Writer entered                                                            Time =      0.17

 Results generated                                                                Time =      0.19

RUN SAVED



 NO ERRORS OR WARNINGS GENERATED

 *** CALCULATION TRACE ***

 TUTORIAL                                                        



*** INPUT SPECIFICATION MESSAGES ***

 REPORT       IS  NEW 11/09/2016   12:42:23:94 
 ;
 ;Input file created by Aspen Plus Rel. 11.1 at 12:42:23 Wed Nov 9, 2016
 ;Directory E:\Aspen Plus\T2 -sensitivity  Runid t1
 ;
 
 
 
 REPORT NOREPORT

 PDF updated                                                                      TIME =     93.06
 THIS COPY OF ASPEN PLUS LICENSED TO                                 
 
 DESIGN SPEC: DS-1 WILL BE INTERPRETED 
 

Calculations begin                                                              time     93.20



*** INPUT SPECIFICATION MESSAGES ***

 CHANGES WERE MADE TO REPORT       11/09/2016   12:43:52:96 
 ;
 ;Input file created by Aspen Plus Rel. 11.1 at 12:43:52 Wed Nov 9, 2016
 ;Directory E:\Aspen Plus\T2 -sensitivity  Runid t1
 ;
 
 
 
 REPORT NOINSERT

 PDF updated                                                                      TIME =    182.08
 THIS COPY OF ASPEN PLUS LICENSED TO                                 
 
 DESIGN SPEC: DS-1 WILL BE INTERPRETED 
 


Calculations begin                                                              time    182.19


 Report Writer entered                                                            Time =    182.20

 Results generated                                                                Time =    182.22

RUN SAVED



 NO ERRORS OR WARNINGS GENERATED

 *** CALCULATION TRACE ***

 TUTORIAL                                                        



*** INPUT SPECIFICATION MESSAGES ***

 CHANGES WERE MADE TO DESIGN-SPEC  DS-1     12/08/2016   11:28:12:59 
 ;
 ;Input file created by Aspen Plus Rel. 11.1 at 11:28:12 Thu Dec 8, 2016
 ;Directory D:\FaraDars.Org\T1173\FVCHE9506\FVCHE9506-S3\Files And Codes\T4 -sensitivity  Runid t1
 ;
 
 
 
 DESIGN-SPEC DS-1
     DEFINE WATER MASS-FRAC STREAM=WATER SUBSTREAM=MIXED  &
         COMPONENT=WATER
     SPEC "WATER" TO "0.9"
     TOL-SPEC "0.0001"
     VARY MASS-FLOW STREAM=MIBK2 SUBSTREAM=MIXED COMPONENT=MIBK
     LIMITS "25" "100"

 PDF updated                                                                      TIME =    748.55
 THIS COPY OF ASPEN PLUS LICENSED TO                                 
 
 DESIGN SPEC: DS-1 WILL BE INTERPRETED 
 
 *** FLOWSHEET ANALYSIS MESSAGES ***
 CONVERGENCE BLOCK $OLVER01 FOR DESIGN SPEC DS-1     IS DELETED

 FLOWSHEET CONNECTIVITY BY STREAMS       

   STREAM     SOURCE     DEST           STREAM     SOURCE     DEST
   MIBK       ----       MIXER1         FEED       ----       MIXER1  
   MIBK2      ----       MIXER2         PRUDUCT    MIXER1     FLASH1  
   VAPOR1     FLASH1     ----           MA1        FLASH1     ----    
   WA1        FLASH1     MIXER2         PRDUCT2    MIXER2     FLASH2  
   VAPOR2     FLASH2     ----           MA2        FLASH2     ----    
   WATER      FLASH2     ----                                         

 FLOWSHEET CONNECTIVITY BY BLOCKS        

   BLOCK        INLETS                         OUTLETS
   MIXER1       FEED MIBK                      PRUDUCT                     
   FLASH1       PRUDUCT                        VAPOR1 MA1 WA1              
   MIXER2       WA1 MIBK2                      PRDUCT2                     
   FLASH2       PRDUCT2                        VAPOR2 MA2 WATER            

      BLOCK $OLVER02 (METHOD: SECANT  ) HAS BEEN DEFINED TO CONVERGE
                SPECS : DS-1

      COMPUTATION ORDER FOR THE FLOWSHEET IS:
      MIXER1 FLASH1 
      $OLVER02 MIXER2 FLASH2 
      (RETURN $OLVER02) 

Calculations begin                                                              time    748.70


      CONVERGENCE BLOCK $OLVER02  METHOD: SECANT                                  TIME =    748.70
      ---FLASH STREAM MIBK2   :
      KODE = 2  NTRIAL =   1  T =   297.04  P =  0.3447E+06  V =  0.0000E+00  Q =  0.0000E+00

      UOS BLOCK MIXER2   MODEL: MIXER                                             TIME =    748.70
      NO. TEMP ITER =    5     TEMP =   290.60    
      KODE = 1  NTRIAL =   2  T =   290.60  P =  0.3447E+06  V =  0.0000E+00  Q =  0.0000E+00

      UOS BLOCK FLASH2   MODEL: FLASH3                                            TIME =    748.70
      KODE = 2  NTRIAL =   7  T =   297.04  P =  0.3447E+06  V =  0.0000E+00  BETA =  0.6653      Q =   180.2    

      CONVERGENCE BLOCK $OLVER02  METHOD: SECANT                                  TIME =    748.70
      ---FLASH STREAM MIBK2   :
      KODE = 2  NTRIAL =   1  T =   297.04  P =  0.3447E+06  V =  0.0000E+00  Q =  0.0000E+00
      SPEC   1 ERROR = -0.58010E-04                          X =  0.11332E-03

  LOOP $OLVER02 ITER    1:    *** CONVERGED *** , MAX ERR/TOL    -0.58010         TIME =    748.70

 Report Writer entered                                                            Time =    748.86

 Results generated                                                                Time =    748.87

RUN SAVED



 NO ERRORS OR WARNINGS GENERATED
