MM \FLAVOR \VERSION \DATETIME \Nov 29 08:46:25 2005\MACHINE \startlibrary version1 NumLibs = 1 Built-In NumCats = 9
Mixers/Splitters active
Separators active
Heat Exchangers active Columns active Reactors active
Pressure Changers active
Manipulators active Solids active
User Models active
endlibrary ; 8
>VERSION 0 YT-501 RadFrac Built-In RADFRAC >VERSION 0 YD-501 Decanter Built-In DECANTER >VERSION 0 YT-511 RadFrac Built-In RADFRAC >VERSION 0
YE-500 Heater Built-In HEATER
>VERSION 0 YE-513 Heater Built-In HEATER
>VERSION 0 M1
FSplit Built-In FSPLIT
>VERSION 0 M2
FSplit Built-In FSPLIT
>VERSION 0 M3
FSplit Built-In FSPLIT
? SETUP MAIN ? \\ \RUN-CLASS = FLOWSHEET \\ \\ SIMULATE INTERACTIVE
= NO MOLEFLOW = MOLEFLOW MASSFLOW = MASSFLOW MOLEFRAC = MOLEFRAC MASSFRAC =
MASSFRAC TFFFILE = \VISITED = 1 \\ ? SETUP GLOBAL ? \\ \INSET
= METCBAR \\ \\ \SCLASS = CONVEN \\ ? SETUP DIAGNOSTICS ? ? SETUP
\DESCRIPTION DESCRIPTION = \CUM\
MMLOCAL \\ \\ UNITSET BASESET = MET ( 3 3 3 3 3 3 3 3 3 3 3 7 7 3 3 5 3 3 3 5 3
4 3 3 3 3 1 3 3 3 4 3 7 3 3 3 1 1 4 4 3 3 3 3 3 3 3 3 3 3 3 3 5 3 3 3 3 3 3 3
3 3 3 4 3 3 3 3 3 3 3 3 3 3 5 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3
3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 ) \\ ? SETUP \METCKGCM ? \\
DESCRIPTION DESCRIPTION = \
and CUM\
\\ \\ MMLOCAL \\ \\ UNITSET BASESET = MET ( 3 3 3 3 3 3 3 3 3 3 3 7 7 3 3 5 3 3 3
8 3 4 3 3 3 3 1 3 3 3 4 3 7 3 3 3 3 3 4 4 3 3 3 3 3 3 3 3 3 3 3 3 5 3 3 3 3 3
3 3 3 3 3 4 3 3 3 3 3 3 3 3 3 3 8 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 ) \\ ? SETUP \\? \\ DESCRIPTION DESCRIPTION = \and /HR\
\\ \\ MMLOCAL \\ \\ UNITSET BASESET = SI ( 1 1 1 1 1 1 1 1 1 3 3 7 1 1 1 1 1 1 1
5 1 4 1 1 1 1 1 1 1 1 4 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1
1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 4 5 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1
1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 ) \\ ? SETUP \SETUP
\? \\ ACCOUNT USER-NAME = \\\ ? SETUP \? ? SETUP DESCRIPTION ? \\ DESCRIP DESCRIP = ( \\bar, kg/hr, kmol/hr, MMKcal/hr, cum/hr.\\\\Method: None\\\basis for input: Mole\\\\report composition: Mole flow\) \\ ?
DATABANKS ? \\ DATABANKS \\ ? COMPONENTS MAIN ? \\ COMPONENTS CID = H2O ANAME =
H2O OUTNAME = H2O TYPE = CONV DBNAME1 = \= NBA ANAME = C6H12O2-1 OUTNAME = NBA TYPE = CONV DBNAME1 = \ANAME1 = \= CONV DBNAME1 = \ANAME1 = \/ CID = MA ANAME = C3H6O2-3 OUTNAME = MA TYPE = CONV DBNAME1 = \ANAME1 = \/
CID = PX ANAME = C8H10-3 OUTNAME = PX TYPE = CONV DBNAME1 = \ANAME1
= \\\ ? COMPONENTS \GLOBAL ? ? SOLVE ? ? FLOWSHEET GLOBAL
? \\ BLOCK BLKID = \142
M0-1 143 M0-1 139 M0-1 ) OUT = ( 120 M0-1 121 M2-3 ) \\ \\ BLOCK BLKID = \
BLKTYPE = HEATER IN = ( 126 M0-1 ) OUT = ( 140 M0-1 ) \\ \\ BLOCK BLKID
=
\BLKTYPE = HEATER IN = ( 120 M0-1 ) OUT = ( 138 M0-1 ) \\ \\ BLOCK BLKID = \130
M3-4 131 M1-2 ) \\ \\ BLOCK BLKID = \BLKTYPE = DECANTER IN = ( 138 M0-1
130 M0-1 129 M0-1 ) OUT = ( \BLKID
= M1 BLKTYPE = FSPLIT IN = ( 45 M0-1 ) OUT = ( 45A M0-1 45B M0-1 ) \\ \\ BLOCK
BLKID = M2 BLKTYPE = FSPLIT IN = ( \143 M0-1
) \\ \\ BLOCK BLKID = M3 BLKTYPE = FSPLIT IN = ( \= ( 126
M0-1 139 M0-1 ) \\ \\ \SCLASS = CONVEN \\ ? PROPERTIES MAIN ? \\
GPROPERTIES GBASEOPSET = \-2 \\ ?
PROPERTIES COMPARE ? ? PROPERTIES \= NRTL \\
? PROPERTIES \PROPERTIES
\\\\PARNAME =
\COMPI = \COMPJ = \VALUE = ( \\\
\\\\\\\\
\DIRECTOR
ALLONLY = NONE UNCHOICE = NO TCHOICE = NO GRPCHOICE = NO \\ ? PROPERTIES PARAMETERS BINARY SCALAR \PARAMNAME = HOCETA SETNO = 1 UNITROW = 0 BDBANK = ( \BPVAL
PARAMNAME2 = HOCETA CID1 = H2O CID2 = H2O VALUE = EOS-LIT \\ \\ BPVAL PARAMNAME2 = HOCETA CID1 = H2O CID2 = NBA VALUE = EOS-LIT \\ \\ BPVAL PARAMNAME2 = HOCETA CID1 = H2O CID2 = HAC VALUE = EOS-LIT \\ \\ BPVAL PARAMNAME2 = HOCETA CID1 = H2O CID2 = MA VALUE = EOS-LIT \\ \\ BPVAL PARAMNAME2
= HOCETA CID1 = NBA CID2 = H2O VALUE = EOS-LIT \\ \\ BPVAL PARAMNAME2 = HOCETA
CID1 = NBA CID2 = NBA VALUE = EOS-LIT \\ \\ BPVAL PARAMNAME2 = HOCETA CID1 =
NBA CID2 = HAC VALUE = EOS-LIT \\ \\ BPVAL PARAMNAME2 = HOCETA CID1 = NBA CID2
= MA VALUE = EOS-LIT \\ \\ BPVAL PARAMNAME2 = HOCETA CID1 = NBA CID2 = PX
VALUE = EOS-LIT \\ \\ BPVAL PARAMNAME2 = HOCETA CID1 = HAC CID2 = H2O VALUE =
EOS-LIT \\ \\ BPVAL PARAMNAME2 = HOCETA CID1 = HAC CID2 = NBA VALUE = EOS-LIT \\
\\ BPVAL PARAMNAME2 = HOCETA CID1 = HAC CID2 = HAC VALUE = EOS-LIT \\ \\ BPVAL
PARAMNAME2 = HOCETA CID1 = HAC CID2 = MA VALUE = EOS-LIT \\ \\ BPVAL PARAMNAME2
= HOCETA CID1 = HAC CID2 = PX VALUE = EOS-LIT \\ \\ BPVAL PARAMNAME2 = HOCETA
CID1 = MA CID2 = H2O VALUE = EOS-LIT \\ \\ BPVAL PARAMNAME2 = HOCETA CID1 = MA
CID2 = NBA VALUE = EOS-LIT \\ \\ BPVAL PARAMNAME2 = HOCETA CID1 = MA CID2 = HAC
VALUE = EOS-LIT \\ \\ BPVAL PARAMNAME2 = HOCETA CID1 = MA CID2 = MA VALUE =
EOS-LIT \\ \\ BPVAL PARAMNAME2 = HOCETA CID1 = MA CID2 = PX VALUE = EOS-LIT \\ \\ BPVAL PARAMNAME2 = HOCETA CID1 = PX CID2 = NBA VALUE = EOS-LIT \\ \\ BPVAL PARAMNAME2 = HOCETA CID1 = PX CID2 = HAC VALUE = EOS-LIT \\ \\ BPVAL PARAMNAME2
= HOCETA CID1 = PX CID2 = MA VALUE = EOS-LIT \\ ? PROPERTIES PARAMETERS BINARY SCALAR \? ; \; \\ PROP-LIST PARAMNAME = RKTKIJ SETNO = 1 UNITROW = 0 \\ ? PROPERTIES PARAMETERS BINARY \\
? ; \0
TUNITROW = 22 TUNITLABEL = F NEL = 2 \\ ? PROPERTIES PARAMETERS BINARY \\? ; \; \\ PROP-LIST PARAMNAME = ANDMIJ SETNO = 1 UNITROW = 0 TUNITROW = 22 TUNITLABEL = F NEL = 2 \\ ? PROPERTIES PARAMETERS BINARY \\? ; \; \\ PROP-LIST
PARAMNAME = HENRY SETNO = 1 UNITROW = 20 UNITLABEL = bar TUNITROW = 22
TUNITLABEL = C BDBANK = ( BINARY HENRY ) NEL = 6 \\ ? PROPERTIES PARAMETERS BINARY \\? ; \; \\ PROP-LIST PARAMNAME = NRTL SETNO = 1 UNITROW = 0 TUNITROW = 22 TUNITLABEL = C BDBANK = ( \