FSD100 MbP?h㈵> d c
2 d fffffr@ м@ Harry Kooijman and Ross TaylorButanol_Water_ef22p4249o8ChemSepAdapted from Luyben et al., Ind. Energy Fuels (2008) 22 pp. 4249-4258
Separation of Butanol and Water by making use of the liquid-liquid-equilibria providing a means to break the vapor-liquid azeotrope
Restoring flowsheet from file
$Loaded Butanol_Water_ef22p4249.fsd
Restoring flowsheet from file
$Loaded Butanol_Water_ef22p4249.fsd
W x temperaturepressure compositionflow
Butanol-WaterAUwNA\t & &
B u t a n o l - W a t e r ư>MbP?MbP?MbP?K - C:\Program Files (x86)\COCO\data\ChemSep1.pcd Butanol CH3(CH2)3OH C4H10O 71-36-3 CCCCOQ `f@ VPA ? ף? nx@ @3f@ Qg@ 4? @߇R@ ? x? z)= @ T9 @,Ԫ? @A @^ A ,aA 8 wL @33,@ [C> 8 8 8 Qg@ Q@h@ @a? /? `f@ #? 8 Qg@ @i %@ @ g@ Ծ @ Qg@ @e WA C? w @
@ `9 Qg@ @j ̪@
5qw l? 4@ Gg@d @ @ @ `6? Qg@ lx@ @ @,)@ $? p b@ p@ ? @T "K h@ q@ p@h `XF @3@ р@ `ؾ @ g@ lx@e `> .? R@ @3h@ 8 Qg@ @@f ߓ? 3 `ff QX Qg@ lx@ J-? `? @ p 8 @3+w@ G@f n "Q@ 1
]? I*Ѿ `fq@ `fy@ "@ =
a@ `S? sfJ ``> I@ @@d 8 8 8 8 8 8 8 `x5@ @ z4[ 8 8 @3/u@ s@
(@ ? 8 8 g@ lx@
eX@@ffffg I-LN]m{?#\> @ h @ j@ (? ? L@ ? ? ? 7? .? ِ? 7 ? `? 3W@ ?k
p@ q@]Jz? `B>? X? Z Water HOH H2O 7732-18-5 OT 9@
uA z? @O? `fRw@ `fq@ `q@ @ 2@ ? ? = ^@ I9 @qU? A Ӭ `@ A VA 8 {J@ ` 8 8 8 $m@ `fq@ J{? x? `f:@ ? Qa @3o@ Q:@i X@ Y % @ó> @ `frp@ Q:@e FpA O? | :? : `fq@ =:@j )hp ࣐a@ Mо I = @33 @ `fq@d 0q@ @ a@ eп f'? q@ @3@ @/@ `0;@ @ `3c? I@ @@ 4? `6 l2 v G)@ `fq@ @@h `f` @@ Qx2@ `T @ q@ @
9@e @r> ? `f f@ 8 `q@ Đ@f } @ K ? R? s q@ @3Ƀ@ `1> P? /M@ > 8 `q@ Đ@f J @d@ l
v? ϧ p@ 8@ @ fA `? k ! @6l> I@ @@d 8 8 8 8 8 8 8 f7@ &@ B 8 8 tx@ @3@
Z Wt l> 8 8 q@ @
9@
:#J{#Q@\ yf8TBfm?w-! b= @ p? `ff? ? ? `X@ B? `i? 8? A N? έ? `? ? Q8*@ ?@1(@ 8@y ? (? B? a c t i v i t y a c t i v i t y D a c t i v i t y C o e f f i c i e n t a c t i v i t y C o e f f i c i e n t D d e n s i t y d e n s i t y
e n t h a l p y e n t h a l p y e n t h a l p y F e n t h a l p y F e n t r o p y e n t r o p y ! e n t r o p y F e n t r o p y F e x c e s s E n t h a l p y e x c e s s E n t h a l p y f u g a c i t y f u g a c i t y ; f u g a c i t y C o e f f i c i e n t f u g a c i t y C o e f f i c i e n t ; g i b b s F r e e E n e r g y g i b b s E n e r g y G G h e a t C a p a c i t y h e a t C a p a c i t y C p K K
h e a t O f V a p o r i z a t i o n h e a t O f V a p o r i z a t i o n O i d e a l G a s E n t h a l p y i d e a l G a s E n t h a l p y l o g F u g a c i t y C o e f f i c i e n t l o g F u g a c i t y C o e f f i c i e n t ; m o l e c u l a r W e i g h t m o l e c u l a r W e i g h t H H H s u r f a c e T e n s i o n s u r f a c e T e n s i o n s u r f a c e T e n s i o n ( p u r e ) s u r f a c e T e n s i o n ( p u r e ) t h e r m a l C o n d u c t i v i t y t h e r m a l C o n d u c t i v i t y 0 4 t h e r m a l C o n d u c t i v i t y ( p u r e ) t h e r m a l C o n d u c t i v i t y ( p u r e ) R S
v a p o r P r e s s u r e
v a p o r P r e s s u r e N v i s c o s i t y v i s c o s i t y & v i s c o s i t y ( p u r e ) v i s c o s i t y ( p u r e ) " v o l u m e v o l u m e V a p o r V a p o r p h a s e L i q u i d L i q u i d p h a s e .!u? Water/n-Butanol p336 1/1a imported from NRTL.IPD.!u? Water/n-Butanol p336 1/1a imported from NRTL.IPD @ n-butanol/n-butanol imported from HAYDENO.IPD? Water/n-butanol imported from HAYDENO.IPD? Water/n-butanol imported from HAYDENO.IPD333333? Water/water imported from HAYDENO.IPD p_@ Water/n-butanol p329 1/1a imported from VANLAAR.IPDea? Water/n-butanol p329 1/1a imported from VANLAAR.IPD 镲 @ Water/n-butanol p329 1/1 imported from MARGULES.IPDˡE? Water/n-butanol p329 1/1 imported from MARGULES.IPD <z@ Water/n-butanol p336 1/1a imported from WILSON.IPD(
@ Water/n-butanol p336 1/1a imported from WILSON.IPD jo@ Water/n-Butanol p336 1/1a imported from NRTL.IPD"%ظ@ Water/n-Butanol p336 1/1a imported from NRTL.IPD
]kF@ Water/n-butanol p336 1/1a imported from UNIQUAC.IPD&Aq@ Water/n-butanol p336 1/1a imported from UNIQUAC.IPD QXC@ Water/n-Butanol imported from UNIQUACP.IPD(\&@ Water/n-Butanol imported from UNIQUACP.IPD CH2 OH H2O CH3 ͪ?A`"? rh.@ CH2 N
O?HzG?Zd;O
,@ OH ?333333?5^I 1@ H2O q=
ףp?ffffff?kt2@ Ԏ@ @̌c@ v@ r@33333l CH2 OH H2O CH3 ͪ?A`"? rh.@ CH2 N
O?HzG?Zd;O
,@ OH ?333333?5^I 1@ H2O q=
ףp?ffffff?kt2@ $@ P@33333t@ {G<@ffffffu@^ V瞯<
Butanol-Water 71-36-3Butanol @߇R@ nx@C4H10O
Butanol-WaterButanol 7732-18-5Water 2@ `fRw@H2O
Butanol-WaterWater
? ? ? ? ? ? ? ? ? ? ? ? excessEnthalpy.Dpressure ? ? thermalConductivity.Dmoles ? ? / molenthalpyF.DmolFraction ? ? gibbsFreeEnergy.Dpressure ? ? viscosity.Dtemperature ? ? ? ? activityCoefficient enthalpyF.Dpressure ? ? thermalConductivity.Dpressure ? ? thermalConductivity.Dtemperature ? ? heatCapacity.DmolFraction ? ? entropyF.Dmoles ? ? heatOfVaporization ? ? density.Dpressure ? @ ? @ enthalpy.Dmoles ? ? molecularWeight #logFugacityCoefficient.DmolFraction entropy.Dtemperature ? ? viscosity.Dmoles ? ? ? ? / mol
volume.Dmoles @@ @@ vaporPressure.Dtemperature ? ? enthalpy ? ? enthalpyF ? ? activity.DmolFraction fugacity.Dtemperature ? ? excessEnthalpy.Dtemperature ? ? volume.Dpressure @@ @@ surfaceTension.DmolFraction ? ? activityCoefficient.Dtemperature fugacityCoefficient.Dmoles / molgibbsFreeEnergy ? ? activity.Dmoles / molactivityCoefficient.Dmoles / mol gibbsFreeEnergy.DmolFraction ? ? enthalpy.DmolFraction ? ? enthalpy.Dpressure ? ? logFugacityCoefficient activity molecularWeight.Dtemperature fugacity.Dpressure fugacityCoefficient.DmolFraction density ? @ ? @ volume.DmolFraction @@ @@ activity.Dtemperature enthalpyF.Dtemperature ? ? entropyF.DmolFraction ? ? thermalConductivity ? ? surfaceTension.Dtemperature ? ? density.DmolFraction ? @ ? @ surfaceTension ? ? heatCapacity.Dtemperature ? ? #logFugacityCoefficient.Dtemperature excessEnthalpy ? ? fugacityCoefficient.Dpressure viscosity.DmolFraction ? ? ? ? enthalpy.Dtemperature ? ? entropy.Dpressure ? ? surfaceTension.Dmoles ? ? / molgibbsFreeEnergy.Dmoles ? ? density.Dmoles ? @ ? @ / mol thermalConductivity.DmolFraction ? ? idealGasEnthalpy.Dtemperature ? ? logFugacityCoefficient.Dmoles / mol heatOfVaporization.Dtemperature ? ? enthalpyF.Dmoles ? ? surfaceTension.Dpressure ? ? entropy.DmolFraction ? ? entropyF.Dtemperature ? ? entropy ? ? entropyF ? ? volume @@ @@ heatCapacity.Dpressure ? ? molecularWeight.Dpressure gibbsFreeEnergy.Dtemperature ? ? fugacityCoefficient idealGasEnthalpy ? ? logFugacityCoefficient.Dpressure viscosity.Dpressure ? ? entropy.Dmoles ? ? entropyF.Dpressure ? ? fugacityCoefficient.Dtemperature heatCapacity ? ? activityCoefficient.Dpressure activityCoefficient.DmolFraction viscosity ? ? ? ? excessEnthalpy.Dmoles ? ? volume.Dtemperature @@ @@ density.Dtemperature ? @ ? @ fugacity.Dmoles ? ? / molheatCapacity.Dmoles ? ? activity.Dpressure molecularWeight.DmolFraction excessEnthalpy.DmolFraction ? ? molecularWeight.Dmoles / mol @ &{71F5AC07-65A1-4357-8F1B-A8CD58148763} RelativePerturbationTemperature ? RelativePerturbationPressure ? PerturbationComposition ? Temperature profile ? ? Pressure profile ? ? Vapour Flow profile ? ? Liquid Flow profile ? ? Duties profile ? ? Vapour Density profile @ ? @ ? Vapour Viscosity profile ? ? ? ? Vapour Heat capacity profile ? ? #Vapour Thermal conductivity profile ? ? Liquid Density profile @ ? @ ? Liquid Viscosity profile ? ? ? ? Liquid Heat capacity profile ? ? Liquid Thermal cond. profile ? ? Surface tension profile ? ? Reboiler duty ? ?
Top pressure ? ? TotalMassBalanceProperties Fraction ?
TotalFlowMass ? ? &{779B2C7A-F54B-4A1D-B345-7FA14B889642} Outlet temperature ? ? Heat duty ? ?
Pressure drop ? ? d heatOfVaporization heatOfVaporization.Dtemperature idealGasEnthalpy idealGasEnthalpy.Dtemperature
vaporPressure vaporPressure.Dtemperature activity activity.Dmoles activity.DmolFraction activity.Dpressure activity.Dtemperature activityCoefficient activityCoefficient.Dmoles activityCoefficient.DmolFraction activityCoefficient.Dpressure activityCoefficient.Dtemperature density density.Dmoles density.DmolFraction density.Dpressure density.Dtemperature enthalpy enthalpy.Dmoles enthalpy.DmolFraction enthalpy.Dpressure enthalpy.Dtemperature enthalpyF enthalpyF.Dmoles enthalpyF.DmolFraction enthalpyF.Dpressure enthalpyF.Dtemperature entropy entropy.Dmoles entropy.DmolFraction entropy.Dpressure entropy.Dtemperature entropyF entropyF.Dmoles entropyF.DmolFraction entropyF.Dpressure entropyF.Dtemperature excessEnthalpy excessEnthalpy.Dmoles excessEnthalpy.DmolFraction excessEnthalpy.Dpressure excessEnthalpy.Dtemperature fugacity fugacity.Dmoles fugacity.DmolFraction fugacity.Dpressure fugacity.Dtemperature fugacityCoefficient fugacityCoefficient.Dmoles fugacityCoefficient.DmolFraction fugacityCoefficient.Dpressure fugacityCoefficient.Dtemperature gibbsFreeEnergy gibbsFreeEnergy.Dmoles gibbsFreeEnergy.DmolFraction gibbsFreeEnergy.Dpressure gibbsFreeEnergy.Dtemperature heatCapacity heatCapacity.Dmoles heatCapacity.DmolFraction heatCapacity.Dpressure heatCapacity.Dtemperature logFugacityCoefficient logFugacityCoefficient.Dmoles #logFugacityCoefficient.DmolFraction logFugacityCoefficient.Dpressure #logFugacityCoefficient.Dtemperature molecularWeight molecularWeight.Dmoles molecularWeight.DmolFraction molecularWeight.Dpressure molecularWeight.Dtemperature thermalConductivity thermalConductivity.Dmoles thermalConductivity.DmolFraction thermalConductivity.Dpressure thermalConductivity.Dtemperature viscosity viscosity.Dmoles viscosity.DmolFraction viscosity.Dpressure viscosity.Dtemperature volume
volume.Dmoles volume.DmolFraction volume.Dpressure volume.Dtemperature surfaceTension surfaceTension.Dmoles surfaceTension.DmolFraction surfaceTension.Dpressure surfaceTension.Dtemperature bubblePointTemperature bubblePointPressure dewPointTemperature dewPointPressure Vapor Vapor phase
Butanol-WaterVapor Liquid Liquid phase
Butanol-WaterLiquid VaporLiquid defaultdefault material template
Butanol-Water Feed 2 2 2 2 2 2 2
PEN .Net default м@ v@q q\q@kluC@ |Gz?`9Գ?\(\?ϸ h? D? 1?Rn?B3?H? |n? 2: M?
?:?/?`? |Gz?`9Գ?\(\?ϸ h? v@ м@q q\q@kluC@ 2 8 8 8 8
default м@Iv@4CCD@
Ё? t0?!?bٳ9? o? ? t0? !?bٳ9? o? `y(?:d-?^?TI.? 2 Water ( F = F ; F ( F = F ( F = F
' = default м@?`8v@^4
q@|#^@ MbP?hp?+?.f? JU{??{<~u?U%B?p8P)? ? MbP?hp?+?.f? \ Aqueous : ! " $ ' $ " ! : $ : ! : $ " $
default м@ pu@=]EB@&вD? 3WAZښ?rv3<{[? ? +?\?MbP?!&4
P/? d 10 :
: : :
: :
:
default м@}Gu@ui#?K@^? E`!?~ Ʃ?g?A ? Vv? ʳi?'h?M
?1ˤ? jb
? "q%?'S`L ?wu9j?ͪ9? 2 11 : : : : : : :
default м@ pu@ui#?K@^? E`!?~ Ʃ?g?A ? ? E`!?~ Ʃ?g?A ? ?H? ?n?fffffs@ м@r q ;@8y? 2 C1ChemSep Unit Operation qeWCXc y CSUOe [ChemSep]
Version=6.90
Compiled=2012-1-31 20:40 41769b34bc6e
Name=C:\windows\profiles\harry\Temp\CS_A~TRF.sep
Title=ChemSep CO Unit Operation "Column" in COFE Flowsheet
User=harry
Date=2012-02-01
Time=10:22:22
[Cape-Open]
unitname=Column
CO_ID=CS_10_172C_1CD8AF9_6B9948F0
2 components
Butanol
71-36-3
74.1230010986 Mw
Water
7732-18-5
18.0149993896 Mw
1 thermo
exe=C:\Program Files\ChemSepL6v92\bin\co-col2.exe
mode=COFE
NoWarnings=FALSE
WilsonEstimate=TRUE
Status=Unit is valid
0 only K-values and ethalpies
0 use only perturbed derivative
0 use only perturbed mole derivative
0.001 relative T perturbation
0.001 relative P perturbation
0.001 X perturbation
0 write all values to log
1 use initial guess
0 inlet reflash
0 outlet reflash
0 expose energy ports
0 clear log
0 update icon
CO Thermo Version=Auto
2 number of run levels
normal
simplified
1 current run level
[Paths]
Device drivers path=c:\program files\chemsepl\bin\
Help and Info path=c:\program files\chemsepl\help\
Component data path=c:\program files\chemsepl\pcd\
Property data path=c:\program files\chemsepl\ipd\
Section data path=c:\program files\chemsepl\ild\
Executables path=C:\Program Files\ChemSepL\bin\
Temporary path=C:\windows\profiles\harry\Temp\
Scripts path=c:\program files\chemsepl\bin\
[Units]
Temperature=C
Flow=mol/s
Mass flow=kg/s
Pressure=atm
Heat=MW
Enthalpy=kJ/kmol
Entropy=J/kmol/K
Fraction=_
Length=m
1/Length=1/m
Area=m2
Volume=m3
Mass=kg
Angle=deg
Velocity=m/s
Surface tension=dyn/cm
Density=kg/m3
Molar density=kmol/m3
Viscosity=Pa.s
Molecular weight=kg/kmol
Heat capacity=J/kmol/K
Thermal conductivity=J/s/m/K
Diffusivity=1e-8 m2/s
Interaction parameter=J/mol
Time=s
[Components]
2
94 1105 Library Offset, Index DT=2012-01-31,09:17:24 CHK=53304 CAS=71-36-3 CID=1-butanol
Name=1-butanol
Lib=c:\program files\chemsepl\pcd\chemsep1.pcd
14 1921 Library Offset, Index DT=2012-01-31,09:17:24 CHK=26350 CAS=7732-18-5 CID=Water
Name=Water
Lib=c:\program files\chemsepl\pcd\chemsep1.pcd
[Operation]
2 Operation Column
1 Operation kind Simple Distillation
5 Condenser None
1 Reboiler Partial (Liquid product)
10 Stages
2 Feed stages
0 Sidestream stages
F=1,6
S=
0 Pumparound stages
P=
[Properties]
350 BIP estimation temperature
[Thermodynamics]
4 K model DECHEMA
8 * Activity coefficient UNIFAC
* Wilson model *
* UNIQUAC model *
* Equation of State *
* Cubic EOS *
* Virial EOS *
1 Vapour pressure Antoine
0 Henry's law
* Henry's default *
[Enthalpy]
3 Enthalpy Excess
1 Enthalpy reference state Vapour
298.15 Enthalpy reference temperature
1 Formation enthalpies Excluded
298.15 Exergy surroundings temperature
[Physical property models]
1 No Check T range
* Cubic EOS *
* Virial EOS *
* Vapour model *
* Liquid mixture density *
* Liquid component density *
* Vapour mixture viscosity *
* Vapour mixture viscosity pressure correction *
* Vapour component viscosity *
* Liquid mixture viscosity *
* Liquid component viscosity
* Vapour mixture Cp
* Vapour component Cp
* Liquid mixture Cp
* Liquid component Cp
* Vapour mixture conductivity *
* Vapour component conductivity *
* Liquid mixture conductivity *
* Liquid component conductivity
* Mixture surface tension *
* Component surface tension *
* Vignes MS D-model *
* D mixture model *
* Vapour Diffusion Coefficients *
[Reaction data]
0 Number of reactions
[Specifications]
Top
Bottom
[Heaters/Coolers]
0 Number
0 Column duty Qcolumn
1 First stage
9 Last stage
0 Qcolumn lost to surroundings
[Efficiencies]
1 Default efficiency
0 Number
[Pressures]
1 Column pressure Constant pressure
* Condenser pressure
50662.5 Top pressure
* Pressure Drop
* Bottom pressure
[Feeds]
2 Number
1 Feed state T & p
1 Stage Reflux{split}
343 Temperature
101325 Pressure
0 Vapour fraction
2 componentflows
0.000958260018995 Component 1 flow
0.0355836706201 Component 2 flow
1 Feed state T & p
6 Stage Feed1{split}
352 Temperature
50662.5 Pressure
0.0635459414034 Vapour fraction
2 componentflows
0.00555555555556 Component 1 flow
0.272222222222 Component 2 flow
[Reboiler]
7 Type Mole fraction of a component
0.001 Value Qreboiler
1 1st comp.
* Type *
* Initialization guess
[Monitored Variables]
*
[Solve options]
3 Initialization Old Results
1 Method Newton's method
0.5 Flow Step limit
10 Temperature Step limit
1 Composition Step limit
1 Flux Step limit
0.000001 Accuracy
30 Maximum iterations
1 Iteration count & function vector
0 T/V/L profiles
0 X/Y profiles
0 Variable and function vectors
0 Jacobian
1 History Screen
History file=
1 Feeds type Stage below
1 Interactive
0 Log thermodynamics
0 Log enthalpy/entropy
0 Log physical properties
0 Log timing
0 CO numeric differencing
0 Log from iteration
0 CS K-value
0 CS enthalpy
0 CS entropy
0 CS flash
0 CS activity coefficient
0 CS vapor pressuure
0 CS density
0 CS viscosity
0 CS thermal conductivity
0 CS heat capacity
0 CS surface tension
0 CS diffusivity
[Programs]
Temporary file=SCRATCH.TMP
User program=
8 DOS extender NT
1 Show windows Hidden
[User-Data]
Water distillation column
[End User-Data]
[FlowSheet]
[CoCo]
# Coco column icon generated by ChemSep
# Sizes
WIDTH 14
HEIGHT 16
DEFHEIGHT 24
XGROW 4
YGROW 6
# column + Internals
BODY 0 0 8 12 -1 4
LINE DASHED 0 4 8 4
LINE DASHED 0 8 8 8
# No Condenser
CONNECTION 4 0
# Partial Reboiler
BODY 10 12 14 16 -1 -1
LINE 4 12 4 14
LINE ARROW 4 14 10 14
LINE 12 12 12 8
LINE ARROW 12 8 8 8
LINE THINLINE OARROW 10 16 14 12
CONNECTION 10 16
CONNECTION 12 16
CONNECTION 14 14
# Connections and free space for feeds and sidestreams
VCONNECTION 0 4 8
VCONNECTION 8 5 7
FREESPACE 9 5 12 7
FREESPACE 13 5 14 7
[Settings]
ComboBox=ComboBox14
-1
ComboBox=ComboBox20
-1
ComboBox=ComboBox21
-1
CheckBox=CheckBox3
0 Show settings
CheckBox=CheckBox1
1 Auto colors
CheckBox=CheckBox2
1 Auto points
Edit=Edit9
0.2
StringGrid=StringGrid5
2
8
Title
Labels
Stages
Axis color
Commands
Box
Labels box
Import data
StringGrid=StringGrid4
5
9
Title
Start
End
Tic interval
Small tics
Grid
Logarithmic
Scientific notation
x1
y1
x2
y2
StringGrid=StringGrid3
1
14
Label
Plot X
Plot Y
X axis
Y axis
Units X
Units Y
Color
Points
Thickness
Style
1st stage
Last stage
CheckBox=CheckBox10
0 Show settings
ComboBox=ComboBox22
0
ComboBox=ComboBox23
1
StringGrid=StringGrid7
16
2
Title
McCabe-Thiele diagram 1-butanol - Water
Xlabel
X 1-butanol/(1-butanol+Water)
Ylabel
Y 1-butanol/(1-butanol+Water)
X interval
0.2
Y interval
0.2
X min
0
X max
1
Y min
0
Y max
1
X tics
0
Y tics
0
Axis color
Black
Grid
Off
y Fractions
Vertical
Commands
set label "ChemSep" at 1,0.02 right
Stage numbers
On
StringGrid=StringGrid11
5
3
CheckBox=CheckBox45
0 Lumped
ComboBox=ComboBox75
-1
ComboBox=ComboBox76
-1
ComboBox=ComboBox77
-1
Edit=Edit55
0.95
Edit=Edit56
0.95
Edit=Edit57
1.2
Edit=Edit1
1
CheckBox=CheckBox2
0 Use old results
CheckBox=CheckBox3
1 Automatic
CheckBox=CheckBox1
0 Keep sep-files
CheckBox=CheckBox4
1 Restore original
StringGrid=StringGrid1
1
6
Name
Variable
Units
Value
Start/Valuelist
End
StringGrid=StringGrid2
4
1
Name
Variable
Units
Current Value
StringGrid=StringGrid3
1
1
None
ComboBox=ComboBox1
-1
ComboBox=ComboBox2
-1
ComboBox=ComboBox3
0
Edit=Edit1
50662.5
Edit=Edit2
21
Edit=Edit3
1-butanol + Water @ p=50662.5 (N/m2)
ComboBox=ComboBox4
0
ComboBox=ComboBox15
0
Edit=Edit17
Plot font
CheckBox=CheckBox2
1
Color=Edit18
3404024
SpinEdit=SpinEdit1
1
CheckBox=CheckBox2
1
Color=Edit19
3404024
Edit=Edit5
StringGrid=StringGrid2
7
2
StringGrid=StringGrid3
7
2
StringGrid=StringGrid4
7
2
Color=BVLEbplineColor
3404024
SpinEdit=SpinEdit2
1
ComboBox=ComboBox13
0
Color=BVLEdplineColor
3404024
SpinEdit=SpinEdit3
1
ComboBox=ComboBox14
0
RadioButton=RadioButton3
TRUE
DrawSetColors=BVLEcolors
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
ComboBox=ComboBox7
-1
ComboBox=ComboBox11
-1
ComboBox=ComboBox6
-1
Memo=Memo1
Memo1,
ComboBox=ComboBox1
-1
ComboBox=ComboBox2
-1
ComboBox=ComboBox2
-1
ComboBox=ComboBox4
0
Edit=Edit1
Edit=Edit2
21
Edit=Edit3
Ternary Phase Diagram
Edit=Edit4
1,6
Edit=Edit6
Edit=Edit7
chemsep1.pcd
Edit=Edit8
Edit=Edit5
StringGrid=StringGrid1
3
7
Identifier
L#
File
Loc.
CAS
SMILES
Name
1-butanol
1105
c:\program files\chemsepl\pcd\chemsep1.pcd
94
71-36-3
CCCCO
1-butanol
Water
1921
c:\program files\chemsepl\pcd\chemsep1.pcd
14
7732-18-5
O
Water
0
0
ComboBox=ComboBox1
-1
ComboBox=ComboBox2
-1
ComboBox=ComboBox3
-1
Edit=Edit1
Edit=Edit2
Edit=Edit3
21
Edit=Edit4
Binary Property Diagram
Memo=Memo1
StringGrid=StringGrid1
13
4
Axis
Left
Right
X/Y
Property
-click to select-
-click to select-
x
Title
x
Units
-
Minimum
0
Maximum
1
Interval
0.2
Grid
Off
Off
Off
Log
Off
Off
Off
Color
Blue
Red
Black
Line
Normal
Normal
Style
Solid
Solid
Point
None
None
Edit=Edit5
ComboBox=ComboBox7
-1
ComboBox=ComboBox6
-1
[End Settings]
[End of Input]
[Results]
1 Converged
1 Iterations
[Profiles]
Stage Temperature Pressure Vapour Flow Liquid Flow Duties
1 350.6516354 5.066250000E+04 4.183019636E-02 3.710361218E-02 0.000000000E+00
2 351.0132396 5.066250000E+04 4.239187790E-02 3.713114233E-02 0.000000000E+00
3 351.0564476 5.066250000E+04 4.241940805E-02 3.713440136E-02 0.000000000E+00
4 351.0612931 5.066250000E+04 4.242266709E-02 3.713476648E-02 0.000000000E+00
5 351.0618326 5.066250000E+04 4.242303220E-02 3.713498688E-02 0.000000000E+00
6 351.2407227 5.066250000E+04 2.477160571E-02 2.975039499E-01 0.000000000E+00
7 351.8417002 5.066250000E+04 2.501443787E-02 2.978646035E-01 0.000000000E+00
8 352.5951303 5.066250000E+04 2.537509142E-02 2.983109109E-01 0.000000000E+00
9 353.3554918 5.066250000E+04 2.582139881E-02 2.987563984E-01 0.000000000E+00
10 353.9735475 5.066250000E+04 2.626688631E-02 2.724895121E-01 1.108479256E+06
[Enthalpies/Entropies]
Stage Vap.Enthalpy Liq.Enthalpy Vap.Entropy Liq.Entropy
1 0.2413151E+07 -0.3996678E+08 0.1671558E+05 -0.1054705E+06
2 0.2370689E+07 -0.3994129E+08 0.1637642E+05 -0.1054338E+06
3 0.2365523E+07 -0.3993825E+08 0.1633463E+05 -0.1054294E+06
4 0.2364943E+07 -0.3993790E+08 0.1632993E+05 -0.1054289E+06
5 0.2364878E+07 -0.3993786E+08 0.1632940E+05 -0.1054289E+06
6 0.2343264E+07 -0.3992523E+08 0.1615322E+05 -0.1054105E+06
7 0.2268058E+07 -0.3988267E+08 0.1552298E+05 -0.1053486E+06
8 0.2167895E+07 -0.3982911E+08 0.1463482E+05 -0.1052712E+06
9 0.2059856E+07 -0.3977484E+08 0.1359141E+05 -0.1051956E+06
10 0.1966668E+07 -0.3973059E+08 0.1257163E+05 -0.1051388E+06
[Vapour Properties]
Stage Moleweight Density Viscosity Heat capacity Thermal conductivity
1 0.2638666E+02 0.4585484E+00 0.1116838E-04 0.4725021E+05 0.2199319E-01
2 0.2561855E+02 0.4447415E+00 0.1121660E-04 0.4604086E+05 0.2206097E-01
3 0.2552634E+02 0.4430861E+00 0.1122226E-04 0.4589548E+05 0.2206908E-01
4 0.2551599E+02 0.4429004E+00 0.1122290E-04 0.4587916E+05 0.2206999E-01
5 0.2551484E+02 0.4428797E+00 0.1122297E-04 0.4587734E+05 0.2207010E-01
6 0.2513197E+02 0.4360119E+00 0.1124620E-04 0.4527328E+05 0.2210376E-01
7 0.2383308E+02 0.4127713E+00 0.1132125E-04 0.4321872E+05 0.2221741E-01
8 0.2217517E+02 0.3832368E+00 0.1140729E-04 0.4058472E+05 0.2236125E-01
9 0.2046626E+02 0.3529420E+00 0.1148208E-04 0.3785652E+05 0.2250804E-01
10 0.1904926E+02 0.3279321E+00 0.1153111E-04 0.3558450E+05 0.2262862E-01
[Liquid Properties]
Stage Moleweight Density Viscosity Heat capacity Thermal cond. Surface tension
1 0.1871322E+02 0.9560404E+03 0.3635893E-03 0.7748597E+05 0.6614774E+00 0.6271281E-01
2 0.1861299E+02 0.9571513E+03 0.3613635E-03 0.7723543E+05 0.6626740E+00 0.6272541E-01
3 0.1860178E+02 0.9572742E+03 0.3611031E-03 0.7720738E+05 0.6628099E+00 0.6272632E-01
4 0.1860053E+02 0.9572879E+03 0.3610740E-03 0.7720425E+05 0.6628250E+00 0.6272641E-01
5 0.1860039E+02 0.9572894E+03 0.3610707E-03 0.7720391E+05 0.6628267E+00 0.6272642E-01
6 0.1855558E+02 0.9577773E+03 0.3600047E-03 0.7709177E+05 0.6633737E+00 0.6272890E-01
7 0.1842073E+02 0.9592116E+03 0.3565434E-03 0.7675384E+05 0.6650627E+00 0.6272483E-01
8 0.1827843E+02 0.9606565E+03 0.3524200E-03 0.7639620E+05 0.6669256E+00 0.6269854E-01
9 0.1815711E+02 0.9618164E+03 0.3484532E-03 0.7609020E+05 0.6685915E+00 0.6265424E-01
10 0.1807111E+02 0.9625881E+03 0.3453484E-03 0.7587249E+05 0.6698232E+00 0.6260812E-01
[Vapour phase compositions]
Component Mole fractions on stages: 1 to 5
1 0.149206234E+00 0.135516366E+00 0.133872840E+00 0.133688425E+00 0.133667891E+00
2 0.850793766E+00 0.864483634E+00 0.866127160E+00 0.866311575E+00 0.866332109E+00
Component Mole fractions on stages: 6 to 10
1 0.126844210E+00 0.103694381E+00 0.741457646E-01 0.436883306E-01 0.184334639E-01
2 0.873155790E+00 0.896305619E+00 0.925854235E+00 0.956311669E+00 0.981566536E+00
[Liquid phase compositions]
Component Mole fractions on stages: 1 to 5
1 0.124442652E-01 0.106579152E-01 0.104580519E-01 0.104358052E-01 0.104333303E-01
2 0.987555735E+00 0.989342085E+00 0.989541948E+00 0.989564195E+00 0.989566670E+00
Component Mole fractions on stages: 6 to 10
1 0.963464908E-02 0.723128912E-02 0.469504557E-02 0.253276321E-02 0.100000000E-02
2 0.990365351E+00 0.992768711E+00 0.995304954E+00 0.997467237E+00 0.999000000E+00
[Reaction rates]
Component reaction rates on stages: 1 to 5
1 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00
2 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00
Component reaction rates on stages: 6 to 10
1 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00
2 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00
[Reboiler Heat Duty]
1.108479256E+06
[UA Column]
0.000000000E+00
[K-values]
Component K-values on stages: 1 to 5
1 0.119899594E+02 0.127150914E+02 0.128009347E+02 0.128105520E+02 0.128116226E+02
2 0.861514685E+00 0.873796484E+00 0.875280893E+00 0.875447575E+00 0.875466137E+00
Component K-values on stages: 6 to 10
1 0.131654208E+02 0.143396812E+02 0.157923419E+02 0.172492756E+02 0.184334640E+02
2 0.881650181E+00 0.902834275E+00 0.930221669E+00 0.958739931E+00 0.982549086E+00
[Molecular weights]
1 74.123
2 18.015
[Feed stream 1]
1 Stage Number
3.6541930639095E-02 Flow rate
3.4300000000000E+02 Temperature [K]
1.0132500000000E+05 Pressure [Pa]
-4.0568941216335E+07 Enthalpy [J/kmol]
-1.0678897012126E+05 Entropy [J/kmol/K]
0.0000000000000E+00 Vapour fraction [-]
1.0000000000000E+00 Liquid phase split ratio [-]
2.6223573911823E-02 Mole fraction of component 1
9.7377642608818E-01 Mole fraction of component 2
3.6541930639095E-02 Flow rate
2.6223573911823E-02 Mole fraction of component 1
9.7377642608818E-01 Mole fraction of component 2
1.9486351719509E+01 Molar mass
9.5200570767553E+02 Density
4.0783316569542E-04 Viscosity
6.4848379095506E-01 Thermal conductivity
7.9239899623034E+04 Heat capacity
6.3458745831308E-02 Surface tension
[Feed stream 2]
6 Stage Number
2.7777777777756E-01 Flow rate
3.5080966185860E+02 Temperature [K]
5.0662500000000E+04 Pressure [Pa]
-3.7264454971416E+07 Enthalpy [J/kmol]
-8.8884916540079E+04 Entropy [J/kmol/K]
6.3545941403400E-02 Vapour fraction [-]
1.0000000000000E+00 Liquid phase split ratio [-]
2.0000000000032E-02 Mole fraction of component 1
9.7999999999997E-01 Mole fraction of component 2
1.7651650389819E-02 Flow rate
1.4323749966328E-01 Mole fraction of component 1
8.5676250033672E-01 Mole fraction of component 2
2.6012612738774E-01 Flow rate
1.1637344218533E-02 Mole fraction of component 1
9.8836265578147E-01 Mole fraction of component 2
2.6051769265546E+01 Molar mass
4.5252468384564E-01 Density
1.1189617527120E-05 Viscosity
2.2022773009712E-02 Thermal conductivity
4.6723289870281E+04 Heat capacity
1.8667947518950E+01 Molar mass
9.5654486430023E+02 Density
3.6260591318232E-04 Viscosity
6.6201422242088E-01 Thermal conductivity
7.7372831006745E+04 Heat capacity
6.2719473639256E-02 Surface tension
[Reflashed Feed stream 1]
1 Stage Number
3.6541930639095E-02 Flow rate
3.4300000000000E+02 Temperature [K]
5.0662500000000E+04 Pressure [Pa]
-4.0568941216335E+07 Enthalpy [J/kmol]
-1.0678897012126E+05 Entropy [J/kmol/K]
0.0000000000000E+00 Vapour fraction [-]
1.0000000000000E+00 Liquid phase split ratio [-]
2.6223573911823E-02 Mole fraction of component 1
9.7377642608818E-01 Mole fraction of component 2
3.6541930639095E-02 Flow rate
2.6223573911823E-02 Mole fraction of component 1
9.7377642608818E-01 Mole fraction of component 2
1.9486351719509E+01 Molar mass
9.5200218851120E+02 Density
4.0783316569542E-04 Viscosity
6.4848379095506E-01 Thermal conductivity
7.9239899623034E+04 Heat capacity
6.3458745831308E-02 Surface tension
[Reflashed Feed stream 2]
6 Stage Number
2.7777777777756E-01 Flow rate
3.5080966917805E+02 Temperature [K]
5.0662500000000E+04 Pressure [Pa]
-3.7264454971416E+07 Enthalpy [J/kmol]
-8.8884921708674E+04 Entropy [J/kmol/K]
6.3545928822970E-02 Vapour fraction [-]
1.0000000000000E+00 Liquid phase split ratio [-]
2.0000000000032E-02 Mole fraction of component 1
9.7999999999997E-01 Mole fraction of component 2
1.7651646895255E-02 Flow rate
1.4323722272420E-01 Mole fraction of component 1
8.5676277727580E-01 Mole fraction of component 2
2.6012613088230E-01 Flow rate
1.1637364794893E-02 Mole fraction of component 1
9.8836263520511E-01 Mole fraction of component 2
2.6051753727048E+01 Molar mass
4.5252440449700E-01 Density
1.1189618504812E-05 Viscosity
2.2022774381177E-02 Thermal conductivity
4.6723265409377E+04 Heat capacity
1.8667948673448E+01 Molar mass
9.5654484199927E+02 Density
3.6260588517435E-04 Viscosity
6.6201421681248E-01 Thermal conductivity
7.7372834104776E+04 Heat capacity
6.2719471440410E-02 Surface tension
[Top product]
1 Stage Number
4.1830196363508E-02 Flow rate
3.5065163541505E+02 Temperature [K]
5.0662500000000E+04 Pressure [Pa]
2.4131505212409E+06 Enthalpy [J/kmol]
1.6715579815925E+04 Entropy [J/kmol/K]
1.0000000000000E+00 Vapour fraction [-]
1.0000000000000E+00 Liquid phase split ratio [-]
1.4920623398658E-01 Mole fraction of component 1
8.5079376601342E-01 Mole fraction of component 2
4.1830196363408E-02 Flow rate
1.4920623398658E-01 Mole fraction of component 1
8.5079376601342E-01 Mole fraction of component 2
2.6386663021159E+01 Molar mass
4.5854841712728E-01 Density
1.1168384359936E-05 Viscosity
2.1993189610923E-02 Thermal conductivity
4.7250210440270E+04 Heat capacity
* Surface tension
[Bottom product]
10 Stage Number
2.7248951205325E-01 Flow rate
3.5397354754307E+02 Temperature [K]
5.0662500000000E+04 Pressure [Pa]
-3.9730586885568E+07 Enthalpy [J/kmol]
-1.0513881651238E+05 Entropy [J/kmol/K]
0.0000000000000E+00 Vapour fraction [-]
1.0000000000000E+00 Liquid phase split ratio [-]
9.9999999999963E-04 Mole fraction of component 1
9.9899999999963E-01 Mole fraction of component 2
2.7248951205325E-01 Flow rate
9.9999999999963E-04 Mole fraction of component 1
9.9899999999963E-01 Mole fraction of component 2
1.8071107391351E+01 Molar mass
9.6258807069794E+02 Density
3.4534840356673E-04 Viscosity
6.6982315995806E-01 Thermal conductivity
7.5872494453892E+04 Heat capacity
6.2608120721597E-02 Surface tension
[Equilibrium Data at 5.06625E+04 Pa]
Temperature X(1) Y(1)
354.418 0.0000000 0.0000000
349.014 0.0250000 0.2100717
347.987 0.0500000 0.2484301
347.908 0.0750000 0.2515435
348.043 0.1000000 0.2449305
348.191 0.1250000 0.2360622
348.299 0.1500000 0.2274875
348.361 0.1750000 0.2200801
348.386 0.2000000 0.2140829
348.386 0.2250000 0.2094964
348.373 0.2500000 0.2062345
348.357 0.2750000 0.2041892
348.346 0.3000000 0.2032566
348.348 0.3250000 0.2033477
348.367 0.3500000 0.2043909
348.410 0.3750000 0.2063326
348.480 0.4000000 0.2091356
348.580 0.4250000 0.2127790
348.713 0.4500000 0.2172560
348.882 0.4750000 0.2225745
349.090 0.5000000 0.2287559
349.338 0.5250000 0.2358364
349.630 0.5500000 0.2438672
349.968 0.5750000 0.2529168
350.356 0.6000000 0.2630733
350.797 0.6250000 0.2744476
351.294 0.6500000 0.2871795
351.854 0.6750000 0.3014436
352.482 0.7000000 0.3174601
353.185 0.7250000 0.3355085
353.971 0.7500000 0.3559474
354.853 0.7750000 0.3792439
355.844 0.8000000 0.4060169
356.964 0.8250000 0.4371029
358.237 0.8500000 0.4736605
359.698 0.8750000 0.5173380
361.392 0.9000000 0.5705596
363.387 0.9250000 0.6370296
365.780 0.9500000 0.7226783
368.722 0.9750000 0.8375606
372.451 1.0000000 1.0000000
[End of Results]
G U I A r g u m e n t s / k p l d U s e C O S E T h e r m o : U s e C O S E D i f f u s i o n C o e f f i c i e n t s 8 U s e P e r t u r b e d D e r i v a t i v e s O n l y " U s e P e r t u r b e d _ d d X " S u p p r e s s W a r n i n g s @ R e l a t i v e P e r t u r b a t i o n T e m p e r a t u r e MbP?: R e l a t i v e P e r t u r b a t i o n P r e s s u r e MbP?0 P e r t u r b a t i o n C o m p o s i t i o n MbP? I n l e t R e f l a s h < n o n e > O u t l e t F l a s h
A u t o D U s e O n l y K V a l u e s A n d E n t h a l p y F r o m C O S E * R e s t a r t D a t a A v a i l a b l e , O m i t S t a g e F r o m P o r t N a m e W i l s o n E s t i m a t e " L o g P r o p e r t y C a l l s E n e r g y P o r t s U s e I n i t i a l G u e s s ( T e m p e r a t u r e p r o f i l e 4 T e m p e r a t u r e a t e a c h s t a g e
=mu@2:6u@?5u@?yu@:-.Du@z u@ wu@uY v@o+v@ v@" P r e s s u r e p r o f i l e . P r e s s u r e a t e a c h s t a g e
м@ м@ м@ м@ м@ м@ м@ м@ м@ м@( V a p o u r F l o w p r o f i l e 4 V a p o u r F l o w a t e a c h s t a g e
CD@8C)2E@6)5E@R6E@L%6E@[۩8@QyC39@`9@_A1G9@;3ERD:@( L i q u i d F l o w p r o f i l e 4 L i q u i d F l o w a t e a c h s t a g e
H)CB@Q V a p o u r V i s c o s i t y a t e a c h s t a g e
uk>R݅>x>^?>k@I> b> >G=>_e> Vְ.>: V a p o u r H e a t c a p a c i t y p r o f i l e F V a p o u r H e a t c a p a c i t y a t e a c h s t a g e
됛G@wۅ:G@n F@PF@WLF@PSF@}WE@JD@Y/rB@A`A@H V a p o u r T h e r m a l c o n d u c t i v i t y p r o f i l e T V a p o u r T h e r m a l c o n d u c t i v i t y a t e a c h s t a g e
!#a?&?kFiF??eV?GF9^?bDh%)?l?X ?#j+?4 L i q u i d M o l e w e i g h t p r o f i l e @ L i q u i d M o l e w e i g h t a t e a c h s t a g e
f2@iƢ2@ c A2@RDU2@oض(2@O}:2@2rk2@9@0GG2@g\8(2@'kC42@. L i q u i d D e n s i t y p r o f i l e : L i q u i d D e n s i t y a t e a c h s t a g e
6W[@n@@#@9m@2 L i q u i d V i s c o s i t y p r o f i l e > L i q u i d V i s c o s i t y a t e a c h s t a g e
d'7?Ɣj7?LFN7?|ѩ7?wf©7? :i7?V>]7?^_7?"6?o6?: L i q u i d H e a t c a p a c i t y p r o f i l e F L i q u i d H e a t c a p a c i t y a t e a c h s t a g e
5!_S@ӟHOS@ vöEMS@PnMS@T MS@A0GES@ >0S@6>W[S@Y8S@LR@: L i q u i d T h e r m a l c o n d . p r o f i l e F L i q u i d T h e r m a l c o n d . a t e a c h s t a g e
)a*?4?~5??5?LV5?6P{[:?@CI1H?[tW?RF\ e?"DC1o?0 S u r f a c e t e n s i o n p r o f i l e < S u r f a c e t e n s i o n a t e a c h s t a g e
ˁ[
?Y?(??~?N ?E?"
?w
?1? Number of stages NSi Feed2 stage F1Ni Reboiler duty QRo ? @ @ J/s
Top pressure PPTi ? N/m2
U n i t i s v a l i d C h e m S e p ( T M ) - C O L 2 6 . 9 0
C o p y r i g h t ( c ) 1 9 8 8 - 2 0 1 2 H a r r y K o o i j m a n a n d R o s s T a y l o r
L i c e n s e : 2 1 0 0 - 6 L I T E f r e e l i c e n s e
B u i l d : 6 4 9 4 e 2 b 6 9 d 2 3
C h e c k i n g d a t a f i l e C : \ w i n d o w s \ p r o f i l e s \ h a r r y \ T e m p \ C S _ A ~ T R F . S E P
C a p e O p e n u n i t n a m e : C 1
C a p e - O p e n u n i t i d : C S _ A _ 4 5 _ 1 C C E 0 C 2 _ A 4 5 C E 3 9 0
C a p e - O p e n r u n l e v e l : n o r m a l
C a p e o p e n I n i t i a l i z e d
C a p e O p e n T h e r m o d y n a m i c - p r o p e r t i e s d i s a b l e d
R e a d i n g c o n f i g u r a t i o n
R e a d i n g c o m p o n e n t p r o p e r t y l i b r a r i e s
R e a d i n g t h e r m o d y n a m i c p r o p e r t y o p t i o n s
R e a d i n g p h y s i c a l p r o p e r t y o p t i o n s
R e a d i n g t h e r m o d y n a m i c p r o p e r t y d a t a
R e a d i n g s p e c i f i c a t i o n s
R e a d i n g r e a c t i o n d a t a
C h e c k i n g C o m p o n e n t D a t a
7 1 - 3 6 - 3 1 - b u t a n o l
7 7 3 2 - 1 8 - 5 W a t e r
* N o c l a s s
D e t e r m i n i n g f e e d c o n d i t i o n s
S o l v i n g T P f l a s h
P o s s i b l e t r i v i a l s o l u t i o n
S o l v i n g P V f l a s h
R u n l e v e l : I n i t i a l i z a t i o n
R e a d i n g i n i t i a l t e m p e r a t u r e p r o f i l e s
R e a d i n g i n i t i a l c o m p o s i t i o n p r o f i l e s
I n i t 1 2 2 m i l l i s e c o n d s
R u n l e v e l : C o m p l e t e m o d e l
I t e r a t i o n l o g ( E r r / T o l )
0 1 . 2 7 5 9
1 - 2 . 7 2 0 9
R u n l e v e l : R e p o r t
C o n v e r g e n c e o b t a i n e d i n 1 i t e r a t i o n s
G e n e r a t i n g e q u i l i b r i u m d a t a
T i m e 4 7 m i l l i s e c o n d s
F i x M e m d r i v e r d o n e
r u n t i m e : 0 . 5 3 s e c o n d s
U s i n g : C : \ P r o g r a m F i l e s \ C h e m S e p L \ b i n \ c o - c o l 2 . e x e
C A P E - O P E N t h e r m o - p r o p e r t i e s w e r e d i s a b l e d .
A l l c a l c u l a t i o n m e t h o d s h a v e b e e n d e t e r m i n e d b y C h e m S e p .
S e e o u t p u t r e p o r t o r g r a p h i c a l u s e r i n t e r f a c e f o r m o r e i n f o r m a t i o n .
( H
not all ports are connected Feed1{split}_stage6 Reflux{split}_stage1
TopProduct
BottomProduct @ (@ @ @ @ @ @ @ @ @ @ @ $@ (@ ,@ 0@ @ (@ @ ,@ @ ,@ $@ ,@ (@ (@ (@ @ (@ @ @ @ $@ 0@ ,@ (@ @
0@ ,@ (@ 0@ ,@ (@ 0@ ,@ (@ 0@ ,@ (@ 0@ ,@ (@ ,@ (@
,@ (@ @*%@ DecanterChemSep Unit Operation qeWCXc : CSUO) [ChemSep]
Version=6.90
Compiled=2012-1-31 20:40 41769b34bc6e
Name=C:\windows\profiles\harry\Temp\CS_B~E2Z.sep
Title=ChemSep CO Unit Operation "Decanter" in COFE Flowsheet
User=harry
Date=2012-02-01
Time=10:19:53
[Cape-Open]
unitname=Decanter
CO_ID=CS_B_45_1CCE0C2_A5C1CAC0
2 components
Butanol
71-36-3
74.1230010986 Mw
Water
7732-18-5
18.0149993896 Mw
1 thermo
exe=C:\Program Files\ChemSepL\bin\co-col2.exe
mode=COFE
NoWarnings=FALSE
WilsonEstimate=TRUE
Status=
0 only K-values and ethalpies
0 use only perturbed derivative
0 use only perturbed mole derivative
0.001 relative T perturbation
0.001 relative P perturbation
0.001 X perturbation
0 write all values to log
1 use initial guess
0 inlet reflash
0 outlet reflash
0 expose energy ports
0 clear log
0 update icon
CO Thermo Version=Auto
2 number of run levels
normal
simplified
1 current run level
[Paths]
Device drivers path=c:\program files\chemsepl\bin\
Help and Info path=c:\program files\chemsepl\help\
Component data path=c:\program files\chemsepl\pcd\
Property data path=c:\program files\chemsepl\ipd\
Section data path=c:\program files\chemsepl\ild\
Executables path=C:\Program Files\ChemSepL\bin\
Temporary path=C:\windows\profiles\harry\Temp\
Scripts path=c:\program files\chemsepl\bin\
[Units]
Temperature=K
Flow=kmol/s
Mass flow=kg/s
Pressure=N/m2
Heat=J/s
Enthalpy=J/kmol
Entropy=J/kmol/K
Fraction=_
Length=m
1/Length=1/m
Area=m2
Volume=m3
Mass=kg
Angle=rad
Velocity=m/s
Surface tension=N/m
Density=kg/m3
Molar density=kmol/m3
Viscosity=N/m2.s
Molecular weight=kg/kmol
Heat capacity=J/kmol/K
Thermal conductivity=J/s/m/K
Diffusivity=m2/s
Interaction parameter=J/mol
Time=s
[Components]
2
94 1105 Library Offset, Index DT=2012-01-31,09:17:24 CHK=53304 CAS=71-36-3 CID=1-butanol
Name=1-butanol
Lib=c:\program files\chemsepl\pcd\chemsep1.pcd
14 1921 Library Offset, Index DT=2012-01-31,09:17:24 CHK=26350 CAS=7732-18-5 CID=Water
Name=Water
Lib=c:\program files\chemsepl\pcd\chemsep1.pcd
[Operation]
1 Operation Flash
1 Operation kind Simple Distillation
1 Condenser Total (Liquid product)
1 Reboiler Partial (Liquid product)
1 Stages
1 Feed stages
0 Sidestream stages
F=10
S=
0 Pumparound stages
P=
[Properties]
350 BIP estimation temperature
[Thermodynamics]
7 K model Liquid-Liquid
8 * Activity coefficient UNIFAC
* Wilson model *
* UNIQUAC model *
* Equation of State *
* Cubic EOS *
* Virial EOS *
* Vapour pressure *
0 Henry's law
* Henry's default *
[Enthalpy]
3 Enthalpy Excess
1 Enthalpy reference state Vapour
298.15 Enthalpy reference temperature
1 Formation enthalpies Excluded
298.15 Exergy surroundings temperature
[Physical property models]
0 No Check T range
* Cubic EOS *
* Virial EOS *
* Vapour model *
* Liquid mixture density *
* Liquid component density *
* Vapour mixture viscosity *
* Vapour mixture viscosity pressure correction *
* Vapour component viscosity *
* Liquid mixture viscosity *
* Liquid component viscosity
* Vapour mixture Cp
* Vapour component Cp
* Liquid mixture Cp
* Liquid component Cp
* Vapour mixture conductivity *
* Vapour component conductivity *
* Liquid mixture conductivity *
* Liquid component conductivity
* Mixture surface tension *
* Component surface tension *
* Vignes MS D-model *
* D mixture model *
* Vapour Diffusion Coefficients *
[Reaction data]
0 Number of reactions
[Specifications]
Top
Bottom
[Feeds]
1 Number
1 Feed state T & p
10 Stage Feed1{split}
343 Temperature
50662.5 Pressure
0 Vapour fraction
2 componentflows
0.00897384097974 Component 1 flow
0.0455195757573 Component 2 flow
[Flash]
10 Flash type LL flash temperature
* Pressure
343 Temperature
* Vapour flow
* Liquid flow
* Heat duty Qcolumn
[Solve options]
3 Initialization Old Results
1 Method Newton's method
0.5 Flow Step limit
10 Temperature Step limit
1 Composition Step limit
1 Flux Step limit
0.000001 Accuracy
30 Maximum iterations
1 Iteration count & function vector
0 T/V/L profiles
0 X/Y profiles
0 Variable and function vectors
0 Jacobian
1 History Screen
History file=
1 Feeds type Stage below
1 Interactive
0 Log thermodynamics
0 Log enthalpy/entropy
0 Log physical properties
0 Log timing
0 CO numeric differencing
0 Log from iteration
0 CS K-value
0 CS enthalpy
0 CS entropy
0 CS flash
0 CS activity coefficient
0 CS vapor pressuure
0 CS density
0 CS viscosity
0 CS thermal conductivity
0 CS heat capacity
0 CS surface tension
0 CS diffusivity
[Programs]
Temporary file=SCRATCH.TMP
User program=
8 DOS extender NT
1 Show windows Hidden
[FlowSheet]
[CoCo]
[Settings]
ComboBox=ComboBox14
-1
ComboBox=ComboBox20
-1
ComboBox=ComboBox21
-1
CheckBox=CheckBox3
0 Show settings
CheckBox=CheckBox1
1 Auto colors
CheckBox=CheckBox2
1 Auto points
Edit=Edit9
0.2
StringGrid=StringGrid5
2
8
Title
Labels
Stages
Axis color
Commands
Box
Labels box
Import data
StringGrid=StringGrid4
5
9
Title
Start
End
Tic interval
Small tics
Grid
Logarithmic
Scientific notation
x1
y1
x2
y2
StringGrid=StringGrid3
1
14
Label
Plot X
Plot Y
X axis
Y axis
Units X
Units Y
Color
Points
Thickness
Style
1st stage
Last stage
Edit=Edit1
1
CheckBox=CheckBox2
0 Use old results
CheckBox=CheckBox3
1 Automatic
CheckBox=CheckBox1
0 Keep sep-files
CheckBox=CheckBox4
1 Restore original
StringGrid=StringGrid1
1
6
Name
Variable
Units
Value
Start/Valuelist
End
StringGrid=StringGrid2
4
1
Name
Variable
Units
Current Value
StringGrid=StringGrid3
1
1
None
ComboBox=ComboBox1
-1
ComboBox=ComboBox2
-1
ComboBox=ComboBox3
-1
Edit=Edit1
Edit=Edit2
21
Edit=Edit3
Title
ComboBox=ComboBox4
0
ComboBox=ComboBox15
0
Edit=Edit17
Plot font
CheckBox=CheckBox2
1
Color=Edit18
3404024
SpinEdit=SpinEdit1
1
CheckBox=CheckBox2
1
Color=Edit19
3404024
Edit=Edit5
StringGrid=StringGrid2
7
2
StringGrid=StringGrid3
7
2
StringGrid=StringGrid4
7
2
Color=BVLEbplineColor
3404024
SpinEdit=SpinEdit2
1
ComboBox=ComboBox13
0
Color=BVLEdplineColor
3404024
SpinEdit=SpinEdit3
1
ComboBox=ComboBox14
0
RadioButton=RadioButton3
TRUE
DrawSetColors=BVLEcolors
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
ComboBox=ComboBox7
-1
ComboBox=ComboBox11
-1
ComboBox=ComboBox6
-1
Memo=Memo1
Memo1,
ComboBox=ComboBox1
-1
ComboBox=ComboBox2
-1
ComboBox=ComboBox2
-1
ComboBox=ComboBox4
0
Edit=Edit1
Edit=Edit2
21
Edit=Edit3
Ternary Phase Diagram
Edit=Edit4
10
Edit=Edit6
Edit=Edit7
chemsep1.pcd
Edit=Edit8
Edit=Edit5
StringGrid=StringGrid1
3
7
Identifier
L#
File
Loc.
CAS
SMILES
Name
1-butanol
1105
c:\program files\chemsepl\pcd\chemsep1.pcd
94
71-36-3
CCCCO
1-butanol
Water
1921
c:\program files\chemsepl\pcd\chemsep1.pcd
14
7732-18-5
O
Water
0
0
ComboBox=ComboBox1
-1
ComboBox=ComboBox2
-1
ComboBox=ComboBox3
-1
Edit=Edit1
Edit=Edit2
Edit=Edit3
21
Edit=Edit4
Binary Property Diagram
Memo=Memo1
StringGrid=StringGrid1
13
4
Axis
Left
Right
X/Y
Property
-click to select-
-click to select-
x
Title
x
Units
-
Minimum
0
Maximum
1
Interval
0.2
Grid
Off
Off
Off
Log
Off
Off
Off
Color
Blue
Red
Black
Line
Normal
Normal
Style
Solid
Solid
Point
None
None
Edit=Edit5
ComboBox=ComboBox7
-1
ComboBox=ComboBox6
-1
[End Settings]
[End of Input]
[Results]
1 Converged
1 Iterations
[Feed stream 1]
0 Stage Number
5.4493416737040E-02 Flow rate
3.4300000000000E+02 Temperature [K]
1.0132500000000E+05 Pressure [Pa]
-4.1014731817158E+07 Enthalpy [J/kmol]
1.0306225671085E+04 Entropy [J/kmol/K]
0.0000000000000E+00 Vapour fraction [-]
1.0000000000000E+00 Liquid phase split ratio [-]
1.6467752468236E-01 Mole fraction of component 1
8.3532247531764E-01 Mole fraction of component 2
5.4493416737040E-02 Flow rate
1.6467752468236E-01 Mole fraction of component 1
8.3532247531764E-01 Mole fraction of component 2
2.7254726225958E+01 Molar mass
8.7738791804576E+02 Density
4.5990833798233E-04 Viscosity
5.7674476409132E-01 Thermal conductivity
9.8239178134454E+04 Heat capacity
* Surface tension
[Top product]
0 Stage Number
1.7951486097969E-02 Flow rate
3.4300000000000E+02 Temperature [K]
1.0132500000000E+05 Pressure [Pa]
-4.1748356270777E+07 Enthalpy [J/kmol]
1.5502235335870E+04 Entropy [J/kmol/K]
1.0000000000000E+00 Vapour fraction [-]
1.0000000000000E+00 Liquid phase split ratio [-]
4.4651350406313E-01 Mole fraction of component 1
5.5348649593687E-01 Mole fraction of component 2
1.7951486097969E-02 Flow rate
4.4651350406313E-01 Mole fraction of component 1
5.5348649593687E-01 Mole fraction of component 2
4.3067979838707E+01 Molar mass
8.0650189470010E+02 Density
5.8736268891790E-04 Viscosity
4.3071325842867E-01 Thermal conductivity
1.3691398832942E+05 Heat capacity
* Surface tension
[Bottom product]
0 Stage Number
3.6541930639071E-02 Flow rate
3.4300000000000E+02 Temperature [K]
1.0132500000000E+05 Pressure [Pa]
-4.0654333530862E+07 Enthalpy [J/kmol]
6.0238534750430E+03 Entropy [J/kmol/K]
0.0000000000000E+00 Vapour fraction [-]
1.0000000000000E+00 Liquid phase split ratio [-]
2.6223573911846E-02 Mole fraction of component 1
9.7377642608815E-01 Mole fraction of component 2
3.6541930639071E-02 Flow rate
2.6223573911846E-02 Mole fraction of component 1
9.7377642608815E-01 Mole fraction of component 2
1.9486351719510E+01 Molar mass
9.5200570767552E+02 Density
4.0783316569542E-04 Viscosity
6.4848379095504E-01 Thermal conductivity
7.9239899623037E+04 Heat capacity
1.6422065777191E-03 Surface tension
[Flash Heat Duty]
0.000000000E+00
[K-values]
Component K-values:
1 1.702717965E+01
2 5.683917592E-01
[End of Results]
G U I A r g u m e n t s / k p l d U s e C O S E T h e r m o : U s e C O S E D i f f u s i o n C o e f f i c i e n t s 8 U s e P e r t u r b e d D e r i v a t i v e s O n l y " U s e P e r t u r b e d _ d d X " S u p p r e s s W a r n i n g s @ R e l a t i v e P e r t u r b a t i o n T e m p e r a t u r e MbP?: R e l a t i v e P e r t u r b a t i o n P r e s s u r e MbP?0 P e r t u r b a t i o n C o m p o s i t i o n MbP? I n l e t R e f l a s h < n o n e > O u t l e t F l a s h
A u t o D U s e O n l y K V a l u e s A n d E n t h a l p y F r o m C O S E * R e s t a r t D a t a A v a i l a b l e , O m i t S t a g e F r o m P o r t N a m e W i l s o n E s t i m a t e " L o g P r o p e r t y C a l l s E n e r g y P o r t s U s e I n i t i a l G u e s s
U n i t i s v a l i d i C h e m S e p ( T M ) - C O L 2 6 . 9 0
C o p y r i g h t ( c ) 1 9 8 8 - 2 0 1 2 H a r r y K o o i j m a n a n d R o s s T a y l o r
L i c e n s e : 2 1 0 0 - 6 L I T E f r e e l i c e n s e
B u i l d : 6 4 9 4 e 2 b 6 9 d 2 3
C h e c k i n g d a t a f i l e C : \ w i n d o w s \ p r o f i l e s \ h a r r y \ T e m p \ C S _ B ~ E 2 Z . S E P
C a p e O p e n u n i t n a m e : D e c a n t e r
C a p e - O p e n u n i t i d : C S _ B _ 4 5 _ 1 C C E 0 C 2 _ A 5 C 1 C A C 0
C a p e - O p e n r u n l e v e l : n o r m a l
C a p e o p e n I n i t i a l i z e d
C a p e O p e n T h e r m o d y n a m i c - p r o p e r t i e s d i s a b l e d
R e a d i n g c o n f i g u r a t i o n
R e a d i n g c o m p o n e n t p r o p e r t y l i b r a r i e s
R e a d i n g t h e r m o d y n a m i c p r o p e r t y o p t i o n s
R e a d i n g p h y s i c a l p r o p e r t y o p t i o n s
R e a d i n g t h e r m o d y n a m i c p r o p e r t y d a t a
R e a d i n g s p e c i f i c a t i o n s
C h e c k i n g C o m p o n e n t D a t a
7 1 - 3 6 - 3 1 - b u t a n o l
7 7 3 2 - 1 8 - 5 W a t e r
* N o c l a s s
D e t e r m i n i n g f e e d c o n d i t i o n s
R e a d i n g f l a s h s p e c i f i c a t i o n s
R e a d i n g o l d r e s u l t s
A t t e m p t i n g L i q u i d - L i q u i d f l a s h
P e r f o r m i n g s t a b i l i t y c h e c k
U s i n g N e w t o n m e t h o d
C o n v e r g e n c e o b t a i n e d
T i m e 1 6 m i l l i s e c o n d s
F i x M e m d r i v e r d o n e
r u n t i m e : 0 . 4 9 s e c o n d s
U s i n g : C : \ P r o g r a m F i l e s \ C h e m S e p L \ b i n \ c o - c o l 2 . e x e
C A P E - O P E N t h e r m o - p r o p e r t i e s w e r e d i s a b l e d .
A l l c a l c u l a t i o n m e t h o d s h a v e b e e n d e t e r m i n e d b y C h e m S e p .
S e e o u t p u t r e p o r t o r g r a p h i c a l u s e r i n t e r f a c e f o r m o r e i n f o r m a t i o n .
6 ? !
not all ports are connected Feed1{split}_stage10
TopProduct
BottomProduct @ @ ? @ @ @ @ @ @ @ @ @ @ @ @ @ @ @ @
@ C2ChemSep Unit Operation qeWCXc J} CSUOZ [ChemSep]
Version=6.90
Compiled=2012-1-31 20:40 41769b34bc6e
Name=C:\windows\profiles\harry\Temp\CS_C~WUC.sep
Title=ChemSep CO Unit Operation "Column" in COFE Flowsheet
User=harry
Date=2012-02-01
Time=10:22:17
[Cape-Open]
unitname=Column
CO_ID=CS_12_172C_1CD8AF9_6CCA75F0
2 components
Butanol
71-36-3
74.1230010986 Mw
Water
7732-18-5
18.0149993896 Mw
1 thermo
exe=C:\Program Files\ChemSepL6v92\bin\co-col2.exe
mode=COFE
NoWarnings=FALSE
WilsonEstimate=TRUE
Status=Unit is valid
0 only K-values and ethalpies
0 use only perturbed derivative
0 use only perturbed mole derivative
0.001 relative T perturbation
0.001 relative P perturbation
0.001 X perturbation
0 write all values to log
1 use initial guess
0 inlet reflash
0 outlet reflash
0 expose energy ports
0 clear log
0 update icon
CO Thermo Version=Auto
2 number of run levels
normal
simplified
1 current run level
[Paths]
Device drivers path=c:\program files\chemsepl\bin\
Help and Info path=c:\program files\chemsepl\help\
Component data path=c:\program files\chemsepl\pcd\
Property data path=c:\program files\chemsepl\ipd\
Section data path=c:\program files\chemsepl\ild\
Executables path=C:\Program Files\ChemSepL\bin\
Temporary path=C:\windows\profiles\harry\Temp\
Scripts path=c:\program files\chemsepl\bin\
[Units]
Temperature=K
Flow=kmol/s
Mass flow=kg/s
Pressure=N/m2
Heat=J/s
Enthalpy=J/kmol
Entropy=J/kmol/K
Fraction=_
Length=m
1/Length=1/m
Area=m2
Volume=m3
Mass=kg
Angle=rad
Velocity=m/s
Surface tension=N/m
Density=kg/m3
Molar density=kmol/m3
Viscosity=N/m2.s
Molecular weight=kg/kmol
Heat capacity=J/kmol/K
Thermal conductivity=J/s/m/K
Diffusivity=m2/s
Interaction parameter=J/mol
Time=s
[Components]
2
94 1105 Library Offset, Index DT=2012-01-31,09:17:24 CHK=53304 CAS=71-36-3 CID=1-butanol
Name=1-butanol
Lib=c:\program files\chemsepl\pcd\chemsep1.pcd
14 1921 Library Offset, Index DT=2012-01-31,09:17:24 CHK=26350 CAS=7732-18-5 CID=Water
Name=Water
Lib=c:\program files\chemsepl\pcd\chemsep1.pcd
[Operation]
2 Operation Column
1 Operation kind Simple Distillation
5 Condenser None
1 Reboiler Partial (Liquid product)
10 Stages
1 Feed stages
0 Sidestream stages
F=1
S=
0 Pumparound stages
P=
[Properties]
350 BIP estimation temperature
[Thermodynamics]
4 K model DECHEMA
8 * Activity coefficient UNIFAC
* Wilson model *
* UNIQUAC model *
* Equation of State *
* Cubic EOS *
* Virial EOS *
1 Vapour pressure Antoine
0 Henry's law
* Henry's default *
[Enthalpy]
3 Enthalpy Excess
1 Enthalpy reference state Vapour
298.15 Enthalpy reference temperature
1 Formation enthalpies Excluded
298.15 Exergy surroundings temperature
[Physical property models]
0 No Check T range
* Cubic EOS *
* Virial EOS *
* Vapour model *
* Liquid mixture density *
* Liquid component density *
* Vapour mixture viscosity *
* Vapour mixture viscosity pressure correction *
* Vapour component viscosity *
* Liquid mixture viscosity *
* Liquid component viscosity
* Vapour mixture Cp
* Vapour component Cp
* Liquid mixture Cp
* Liquid component Cp
* Vapour mixture conductivity *
* Vapour component conductivity *
* Liquid mixture conductivity *
* Liquid component conductivity
* Mixture surface tension *
* Component surface tension *
* Vignes MS D-model *
* D mixture model *
* Vapour Diffusion Coefficients *
[Reaction data]
0 Number of reactions
[Specifications]
Top
Bottom
[Heaters/Coolers]
0 Number
0 Column duty Qcolumn
1 First stage
9 Last stage
0 Qcolumn lost to surroundings
[Efficiencies]
1 Default efficiency
0 Number
[Pressures]
1 Column pressure Constant pressure
* Condenser pressure
50662.5 Top pressure
* Pressure Drop
* Bottom pressure
[Feeds]
1 Number
1 Feed state T & p
1 Stage Feed1{split}
343 Temperature
101325 Pressure
0 Vapour fraction
2 componentflows
0.00801558096074 Component 1 flow
0.00993590513722 Component 2 flow
[Reboiler]
7 Type Mole fraction of a component
0.001 Value Qreboiler
2 1st comp.
* Type *
* Initialization guess
[Monitored Variables]
*
[Solve options]
3 Initialization Old Results
1 Method Newton's method
0.5 Flow Step limit
10 Temperature Step limit
1 Composition Step limit
1 Flux Step limit
0.000001 Accuracy
30 Maximum iterations
1 Iteration count & function vector
0 T/V/L profiles
0 X/Y profiles
0 Variable and function vectors
0 Jacobian
1 History Screen
History file=
1 Feeds type Stage below
1 Interactive
0 Log thermodynamics
0 Log enthalpy/entropy
0 Log physical properties
0 Log timing
0 CO numeric differencing
0 Log from iteration
0 CS K-value
0 CS enthalpy
0 CS entropy
0 CS flash
0 CS activity coefficient
0 CS vapor pressuure
0 CS density
0 CS viscosity
0 CS thermal conductivity
0 CS heat capacity
0 CS surface tension
0 CS diffusivity
[Programs]
Temporary file=SCRATCH.TMP
User program=
8 DOS extender NT
1 Show windows Hidden
[User-Data]
n-Butanol distillation column
[End User-Data]
[FlowSheet]
[CoCo]
# Coco column icon generated by ChemSep
# Sizes
WIDTH 14
HEIGHT 16
DEFHEIGHT 24
XGROW 4
YGROW 6
# column + Internals
BODY 0 0 8 12 -1 4
LINE DASHED 0 4 8 4
LINE DASHED 0 8 8 8
# No Condenser
CONNECTION 4 0
# Partial Reboiler
BODY 10 12 14 16 -1 -1
LINE 4 12 4 14
LINE ARROW 4 14 10 14
LINE 12 12 12 8
LINE ARROW 12 8 8 8
LINE THINLINE OARROW 10 16 14 12
CONNECTION 10 16
CONNECTION 12 16
CONNECTION 14 14
# Connections and free space for feeds and sidestreams
VCONNECTION 0 4 8
VCONNECTION 8 5 7
FREESPACE 9 5 12 7
FREESPACE 13 5 14 7
[Settings]
ComboBox=ComboBox14
-1
ComboBox=ComboBox20
-1
ComboBox=ComboBox21
-1
CheckBox=CheckBox3
0 Show settings
CheckBox=CheckBox1
1 Auto colors
CheckBox=CheckBox2
1 Auto points
Edit=Edit9
0.2
StringGrid=StringGrid5
2
8
Title
Labels
Stages
Axis color
Commands
Box
Labels box
Import data
StringGrid=StringGrid4
5
9
Title
Start
End
Tic interval
Small tics
Grid
Logarithmic
Scientific notation
x1
y1
x2
y2
StringGrid=StringGrid3
1
14
Label
Plot X
Plot Y
X axis
Y axis
Units X
Units Y
Color
Points
Thickness
Style
1st stage
Last stage
CheckBox=CheckBox10
0 Show settings
ComboBox=ComboBox22
1
ComboBox=ComboBox23
0
StringGrid=StringGrid7
16
2
Title
McCabe-Thiele diagram Water - 1-butanol
Xlabel
X Water/(Water+1-butanol)
Ylabel
Y Water/(Water+1-butanol)
X interval
0.2
Y interval
0.2
X min
0
X max
1
Y min
0
Y max
1
X tics
0
Y tics
0
Axis color
Black
Grid
Off
y Fractions
Vertical
Commands
set label "ChemSep" at 1,0.02 right
Stage numbers
On
StringGrid=StringGrid11
5
3
CheckBox=CheckBox45
0 Lumped
ComboBox=ComboBox75
-1
ComboBox=ComboBox76
-1
ComboBox=ComboBox77
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Edit=Edit55
0.95
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0.95
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1.2
Edit=Edit1
1
CheckBox=CheckBox2
0 Use old results
CheckBox=CheckBox3
1 Automatic
CheckBox=CheckBox1
0 Keep sep-files
CheckBox=CheckBox4
1 Restore original
StringGrid=StringGrid1
1
6
Name
Variable
Units
Value
Start/Valuelist
End
StringGrid=StringGrid2
4
1
Name
Variable
Units
Current Value
StringGrid=StringGrid3
1
1
None
ComboBox=ComboBox1
-1
ComboBox=ComboBox2
-1
ComboBox=ComboBox3
-1
Edit=Edit1
Edit=Edit2
21
Edit=Edit3
Title
ComboBox=ComboBox4
0
ComboBox=ComboBox15
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Edit=Edit17
Plot font
CheckBox=CheckBox2
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3404024
SpinEdit=SpinEdit1
1
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Color=Edit19
3404024
Edit=Edit5
StringGrid=StringGrid2
7
2
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3404024
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1
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Color=BVLEdplineColor
3404024
SpinEdit=SpinEdit3
1
ComboBox=ComboBox14
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RadioButton=RadioButton3
TRUE
DrawSetColors=BVLEcolors
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ComboBox=ComboBox7
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Memo=Memo1
Memo1,
ComboBox=ComboBox1
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ComboBox=ComboBox4
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Ternary Phase Diagram
Edit=Edit4
1
Edit=Edit6
Edit=Edit7
chemsep1.pcd
Edit=Edit8
Edit=Edit5
StringGrid=StringGrid1
3
7
Identifier
L#
File
Loc.
CAS
SMILES
Name
1-butanol
1105
c:\program files\chemsepl\pcd\chemsep1.pcd
94
71-36-3
CCCCO
1-butanol
Water
1921
c:\program files\chemsepl\pcd\chemsep1.pcd
14
7732-18-5
O
Water
0
0
ComboBox=ComboBox1
-1
ComboBox=ComboBox2
-1
ComboBox=ComboBox3
-1
Edit=Edit1
Edit=Edit2
Edit=Edit3
21
Edit=Edit4
Binary Property Diagram
Memo=Memo1
StringGrid=StringGrid1
13
4
Axis
Left
Right
X/Y
Property
-click to select-
-click to select-
x
Title
x
Units
-
Minimum
0
Maximum
1
Interval
0.2
Grid
Off
Off
Off
Log
Off
Off
Off
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Blue
Red
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Normal
Normal
Style
Solid
Solid
Point
None
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Edit=Edit5
ComboBox=ComboBox7
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ComboBox=ComboBox6
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[End Settings]
[End of Input]
[Results]
1 Converged
1 Iterations
[Profiles]
Stage Temperature Pressure Vapour Flow Liquid Flow Duties
1 348.6682657 5.066250000E+04 1.266307182E-02 1.828982103E-02 0.000000000E+00
2 348.6690570 5.066250000E+04 1.300140675E-02 1.828938840E-02 0.000000000E+00
3 348.6748398 5.066250000E+04 1.300097413E-02 1.828623941E-02 0.000000000E+00
4 348.7173363 5.066250000E+04 1.299782514E-02 1.826379546E-02 0.000000000E+00
5 349.0368464 5.066250000E+04 1.297538118E-02 1.812759783E-02 0.000000000E+00
6 351.2525063 5.066250000E+04 1.283918356E-02 1.770699542E-02 0.000000000E+00
7 359.0769092 5.066250000E+04 1.241858115E-02 1.753177482E-02 0.000000000E+00
8 367.9627734 5.066250000E+04 1.224336054E-02 1.794543824E-02 0.000000000E+00
9 371.4973376 5.066250000E+04 1.265702396E-02 1.819301240E-02 0.000000000E+00
10 372.2828557 5.066250000E+04 1.290459813E-02 5.288414275E-03 5.885094059E+05
[Enthalpies/Entropies]
Stage Vap.Enthalpy Liq.Enthalpy Vap.Entropy Liq.Entropy
1 0.2595187E+07 -0.4090266E+08 0.1813298E+05 -0.1053013E+06
2 0.2595338E+07 -0.4090290E+08 0.1813372E+05 -0.1053011E+06
3 0.2596438E+07 -0.4090469E+08 0.1813911E+05 -0.1052994E+06
4 0.2604465E+07 -0.4091695E+08 0.1817829E+05 -0.1052868E+06
5 0.2662463E+07 -0.4097697E+08 0.1845596E+05 -0.1051815E+06
6 0.3040009E+07 -0.4093672E+08 0.2011332E+05 -0.1042290E+06
7 0.4588207E+07 -0.3962052E+08 0.2550289E+05 -0.1000045E+06
8 0.7124452E+07 -0.3760813E+08 0.3125371E+05 -0.9499712E+05
9 0.8449923E+07 -0.3675166E+08 0.3250700E+05 -0.9314310E+05
10 0.8773760E+07 -0.3655838E+08 0.3233606E+05 -0.9278376E+05
[Vapour Properties]
Stage Moleweight Density Viscosity Heat capacity Thermal conductivity
1 0.3012206E+02 0.5264400E+00 0.1090644E-04 0.5307718E+05 0.2163205E-01
2 0.3012354E+02 0.5264645E+00 0.1090639E-04 0.5307957E+05 0.2163205E-01
3 0.3013429E+02 0.5266437E+00 0.1090602E-04 0.5309702E+05 0.2163201E-01
4 0.3021240E+02 0.5279445E+00 0.1090335E-04 0.5322382E+05 0.2163178E-01
5 0.3076348E+02 0.5370822E+00 0.1088488E-04 0.5412075E+05 0.2163189E-01
6 0.3406801E+02 0.5910225E+00 0.1077386E-04 0.5956169E+05 0.2165983E-01
7 0.4598670E+02 0.7804075E+00 0.1027769E-04 0.7975924E+05 0.2176708E-01
8 0.6328522E+02 0.1048033E+01 0.9441694E-05 0.1101262E+06 0.2174642E-01
9 0.7168517E+02 0.1175845E+01 0.9042762E-05 0.1251996E+06 0.2167800E-01
10 0.7368666E+02 0.1206125E+01 0.8950177E-05 0.1288177E+06 0.2165758E-01
[Liquid Properties]
Stage Moleweight Density Viscosity Heat capacity Thermal cond. Surface tension
1 0.4282955E+02 0.8012145E+03 0.5354716E-03 0.1385322E+06 0.4349013E+00 0.4438706E-01
2 0.4283749E+02 0.8011920E+03 0.5355288E-03 0.1385527E+06 0.4348275E+00 0.4438080E-01
3 0.4289520E+02 0.8010291E+03 0.5359445E-03 0.1387011E+06 0.4342906E+00 0.4433531E-01
4 0.4330230E+02 0.7998934E+03 0.5388712E-03 0.1397492E+06 0.4305038E+00 0.4401418E-01
5 0.4573700E+02 0.7935617E+03 0.5561142E-03 0.1460571E+06 0.4078617E+00 0.4208612E-01
6 0.5437320E+02 0.7759814E+03 0.6105085E-03 0.1692450E+06 0.3274623E+00 0.3513869E-01
7 0.6653748E+02 0.7577009E+03 0.6411156E-03 0.2065069E+06 0.2127000E+00 0.2498997E-01
8 0.7238705E+02 0.7467193E+03 0.6016537E-03 0.2298349E+06 0.1555354E+00 0.1975563E-01
9 0.7379718E+02 0.7427323E+03 0.5793419E-03 0.2368869E+06 0.1412703E+00 0.1839550E-01
10 0.7406689E+02 0.7418512E+03 0.5741860E-03 0.2383448E+06 0.1385065E+00 0.1812750E-01
[Vapour phase compositions]
Component Mole fractions on stages: 1 to 5
1 0.215781379E+00 0.215807646E+00 0.215999274E+00 0.217391403E+00 0.227213217E+00
2 0.784218621E+00 0.784192354E+00 0.784000726E+00 0.782608597E+00 0.772786783E+00
Component Mole fractions on stages: 6 to 10
1 0.286109186E+00 0.498533262E+00 0.806840659E+00 0.956551111E+00 0.992223125E+00
2 0.713890814E+00 0.501466738E+00 0.193159341E+00 0.434488889E-01 0.777687533E-02
[Liquid phase compositions]
Component Mole fractions on stages: 1 to 5
1 0.442263969E+00 0.442405545E+00 0.443434055E+00 0.450689671E+00 0.494082796E+00
2 0.557736031E+00 0.557594455E+00 0.556565945E+00 0.549310329E+00 0.505917204E+00
Component Mole fractions on stages: 6 to 10
1 0.648003874E+00 0.864805025E+00 0.969060547E+00 0.994193053E+00 0.999000000E+00
2 0.351996126E+00 0.135194975E+00 0.309394530E-01 0.580694735E-02 0.100000000E-02
[Reaction rates]
Component reaction rates on stages: 1 to 5
1 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00
2 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00
Component reaction rates on stages: 6 to 10
1 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00
2 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00
[Reboiler Heat Duty]
5.885094059E+05
[UA Column]
0.000000000E+00
[K-values]
Component K-values on stages: 1 to 5
1 0.487901782E+00 0.487805021E+00 0.487105742E+00 0.482352752E+00 0.459868709E+00
2 0.140607488E+01 0.140638478E+01 0.140863941E+01 0.142471124E+01 0.152749655E+01
Component K-values on stages: 6 to 10
1 0.441523882E+00 0.576468970E+00 0.832600875E+00 0.962138197E+00 0.993216340E+00
2 0.202812122E+01 0.370921136E+01 0.624314013E+01 0.748222540E+01 0.777687533E+01
[Molecular weights]
1 74.123
2 18.015
[Feed stream 1]
1 Stage Number
1.7951486097960E-02 Flow rate
3.4300000000000E+02 Temperature [K]
1.0132500000000E+05 Pressure [Pa]
-4.1722576032674E+07 Enthalpy [J/kmol]
-1.0776602551315E+05 Entropy [J/kmol/K]
0.0000000000000E+00 Vapour fraction [-]
1.0000000000000E+00 Liquid phase split ratio [-]
4.4651350406309E-01 Mole fraction of component 1
5.5348649593691E-01 Mole fraction of component 2
1.7951486097960E-02 Flow rate
4.4651350406309E-01 Mole fraction of component 1
5.5348649593691E-01 Mole fraction of component 2
4.3067979838705E+01 Molar mass
8.0650189470011E+02 Density
5.8736268891788E-04 Viscosity
4.3071325842869E-01 Thermal conductivity
1.3691398832942E+05 Heat capacity
4.4975262301988E-02 Surface tension
[Reflashed Feed stream 1]
1 Stage Number
1.7951486097960E-02 Flow rate
3.4300000000000E+02 Temperature [K]
5.0662500000000E+04 Pressure [Pa]
-4.1722576032674E+07 Enthalpy [J/kmol]
-1.0776602551315E+05 Entropy [J/kmol/K]
0.0000000000000E+00 Vapour fraction [-]
1.0000000000000E+00 Liquid phase split ratio [-]
4.4651350406309E-01 Mole fraction of component 1
5.5348649593691E-01 Mole fraction of component 2
1.7951486097960E-02 Flow rate
4.4651350406309E-01 Mole fraction of component 1
5.5348649593691E-01 Mole fraction of component 2
4.3067979838705E+01 Molar mass
8.0645268685580E+02 Density
5.8736268891788E-04 Viscosity
4.3071325842869E-01 Thermal conductivity
1.3691398832942E+05 Heat capacity
4.4975262301988E-02 Surface tension
[Top product]
1 Stage Number
1.2663071823435E-02 Flow rate
3.4866826566299E+02 Temperature [K]
5.0662500000000E+04 Pressure [Pa]
2.5951867491930E+06 Enthalpy [J/kmol]
1.8132981890715E+04 Entropy [J/kmol/K]
1.0000000000000E+00 Vapour fraction [-]
1.0000000000000E+00 Liquid phase split ratio [-]
2.1578137902725E-01 Mole fraction of component 1
7.8421862097275E-01 Mole fraction of component 2
1.2663071823447E-02 Flow rate
2.1578137902725E-01 Mole fraction of component 1
7.8421862097275E-01 Mole fraction of component 2
3.0122061372876E+01 Molar mass
5.2643998021986E-01 Density
1.0906437035283E-05 Viscosity
2.1632053508278E-02 Thermal conductivity
5.3077183246365E+04 Heat capacity
* Surface tension
[Bottom product]
10 Stage Number
5.2884142745127E-03 Flow rate
3.7228285574669E+02 Temperature [K]
5.0662500000000E+04 Pressure [Pa]
-3.6558382873532E+07 Enthalpy [J/kmol]
-9.2783756232535E+04 Entropy [J/kmol/K]
0.0000000000000E+00 Vapour fraction [-]
1.0000000000000E+00 Liquid phase split ratio [-]
9.9900000000236E-01 Mole fraction of component 1
1.0000000000024E-03 Mole fraction of component 2
5.2884142745127E-03 Flow rate
9.9900000000236E-01 Mole fraction of component 1
1.0000000000024E-03 Mole fraction of component 2
7.4066893097099E+01 Molar mass
7.4185117620389E+02 Density
5.7418600518839E-04 Viscosity
1.3850645641876E-01 Thermal conductivity
2.3834482125534E+05 Heat capacity
1.8127503198804E-02 Surface tension
[Equilibrium Data at 5.06625E+04 Pa]
Temperature X(1) Y(1)
354.418 0.0000000 0.0000000
349.014 0.0250000 0.2100717
347.987 0.0500000 0.2484301
347.908 0.0750000 0.2515435
348.043 0.1000000 0.2449305
348.191 0.1250000 0.2360622
348.299 0.1500000 0.2274875
348.361 0.1750000 0.2200801
348.386 0.2000000 0.2140829
348.386 0.2250000 0.2094964
348.373 0.2500000 0.2062345
348.357 0.2750000 0.2041892
348.346 0.3000000 0.2032566
348.348 0.3250000 0.2033477
348.367 0.3500000 0.2043909
348.410 0.3750000 0.2063326
348.480 0.4000000 0.2091356
348.580 0.4250000 0.2127790
348.713 0.4500000 0.2172560
348.882 0.4750000 0.2225745
349.090 0.5000000 0.2287559
349.338 0.5250000 0.2358364
349.630 0.5500000 0.2438672
349.968 0.5750000 0.2529168
350.356 0.6000000 0.2630733
350.797 0.6250000 0.2744476
351.294 0.6500000 0.2871795
351.854 0.6750000 0.3014436
352.482 0.7000000 0.3174601
353.185 0.7250000 0.3355085
353.971 0.7500000 0.3559474
354.853 0.7750000 0.3792439
355.844 0.8000000 0.4060169
356.964 0.8250000 0.4371029
358.237 0.8500000 0.4736605
359.698 0.8750000 0.5173380
361.392 0.9000000 0.5705596
363.387 0.9250000 0.6370296
365.780 0.9500000 0.7226783
368.722 0.9750000 0.8375606
372.451 1.0000000 1.0000000
[End of Results]
G U I A r g u m e n t s / k p l d U s e C O S E T h e r m o : U s e C O S E D i f f u s i o n C o e f f i c i e n t s 8 U s e P e r t u r b e d D e r i v a t i v e s O n l y " U s e P e r t u r b e d _ d d X " S u p p r e s s W a r n i n g s @ R e l a t i v e P e r t u r b a t i o n T e m p e r a t u r e MbP?: R e l a t i v e P e r t u r b a t i o n P r e s s u r e MbP?0 P e r t u r b a t i o n C o m p o s i t i o n MbP? I n l e t R e f l a s h < n o n e > O u t l e t F l a s h
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!湦? $?n% ?>
R?O?졿Ȳ??Y) :?}E֒? ? Number of stages NSi Reboiler duty QRo ? @ @ J/s Number of stages NSi Feed1 stage F1Ni
Top pressure PPTi ? N/m2
U n i t i s v a l i d C h e m S e p ( T M ) - C O L 2 6 . 9 0
C o p y r i g h t ( c ) 1 9 8 8 - 2 0 1 2 H a r r y K o o i j m a n a n d R o s s T a y l o r
L i c e n s e : 2 1 0 0 - 6 L I T E f r e e l i c e n s e
B u i l d : 6 4 9 4 e 2 b 6 9 d 2 3
C h e c k i n g d a t a f i l e C : \ w i n d o w s \ p r o f i l e s \ h a r r y \ T e m p \ C S _ C ~ W U C . S E P
C a p e O p e n u n i t n a m e : C 2
C a p e - O p e n u n i t i d : C S _ C _ 4 5 _ 1 C C E 0 C 2 _ A 5 C 3 2 A 5 0
C a p e - O p e n r u n l e v e l : n o r m a l
C a p e o p e n I n i t i a l i z e d
C a p e O p e n T h e r m o d y n a m i c - p r o p e r t i e s d i s a b l e d
R e a d i n g c o n f i g u r a t i o n
R e a d i n g c o m p o n e n t p r o p e r t y l i b r a r i e s
R e a d i n g t h e r m o d y n a m i c p r o p e r t y o p t i o n s
R e a d i n g p h y s i c a l p r o p e r t y o p t i o n s
R e a d i n g t h e r m o d y n a m i c p r o p e r t y d a t a
R e a d i n g s p e c i f i c a t i o n s
R e a d i n g r e a c t i o n d a t a
C h e c k i n g C o m p o n e n t D a t a
7 1 - 3 6 - 3 1 - b u t a n o l
7 7 3 2 - 1 8 - 5 W a t e r
* N o c l a s s
D e t e r m i n i n g f e e d c o n d i t i o n s
S o l v i n g T P f l a s h
P o s s i b l e t r i v i a l s o l u t i o n
R u n l e v e l : I n i t i a l i z a t i o n
R e a d i n g i n i t i a l t e m p e r a t u r e p r o f i l e s
R e a d i n g i n i t i a l c o m p o s i t i o n p r o f i l e s
I n i t 1 1 7 m i l l i s e c o n d s
R u n l e v e l : C o m p l e t e m o d e l
I t e r a t i o n l o g ( E r r / T o l )
0 0 . 6 6 9 2
1 - 2 . 8 5 8 8
R u n l e v e l : R e p o r t
C o n v e r g e n c e o b t a i n e d i n 1 i t e r a t i o n s
G e n e r a t i n g e q u i l i b r i u m d a t a
T i m e 2 5 m i l l i s e c o n d s
F i x M e m d r i v e r d o n e
r u n t i m e : 0 . 5 4 s e c o n d s
U s i n g : C : \ P r o g r a m F i l e s \ C h e m S e p L \ b i n \ c o - c o l 2 . e x e
C A P E - O P E N t h e r m o - p r o p e r t i e s w e r e d i s a b l e d .
A l l c a l c u l a t i o n m e t h o d s h a v e b e e n d e t e r m i n e d b y C h e m S e p .
S e e o u t p u t r e p o r t o r g r a p h i c a l u s e r i n t e r f a c e f o r m o r e i n f o r m a t i o n .
T b >
not all ports are connected Feed1{split}_stage1
TopProduct
BottomProduct @ (@ @ @ @ @ @ @ @ @ @ @ $@ (@ ,@ 0@ @ (@ @ ,@ @ ,@ $@ ,@ (@ (@ (@ @ (@ @ @ @ $@ 0@ ,@ (@ @
0@ ,@ (@ 0@ ,@ (@ 0@ ,@ (@ 0@ ,@ (@ 0@ ,@ (@ ,@ (@
,@ (@ @ /@ Mixer_46Mixer - mix 2 or more inlet streams to a single outlet k!^/E a- COUSCOUS0002 N u m b e r o f i n l e t s N u m b e r o f i n l e t p o r t s
P r e s s u r e d r o p P r e s s u r e d r o p a l o n g t h e m i x e r ? ? _B T h e r m o V e r s i o n * T h e r m o d y n a m i c s C A P E - O P E N I n t e r f a c e v e r s i o n 1 . 1 1 . 0 1 . 0 1 . 1 L a s t r u n D + + + s p e c i f i c a t i o n s + + +
N u m b e r o f i n l e t s : 2
P r e s s u r e d r o p : 0 P a
7 =
$not all material ports are connected Inlet 1 Inlet 2 Outlet 0 @ @ @ @ @ @ @ HeaterCooler_5MHeaterCooler - heat or cool stream specifying heat duty or outlet temperature z,wK JEKB COUSCOUS0002 T y p e T y p e o f h e a t d u t y s p e c i f i c a t i o n T e m p e r a t u r e H e a t d u t y H e a t d u t y T e m p e r a t u r e E n e r g y i n l e t O u t l e t t e m p e r a t u r e ! T e m p e r a t u r e o f t h e p r o d u c t s t r e a m ? pu@ r@ _B H e a t d u t y H e a t d u t y @ ? @ 3ˋB @x @x D
P r e s s u r e d r o p P r e s s u r e d r o p a l o n g t h e u n i t ? ? _B T h e r m o V e r s i o n * T h e r m o d y n a m i c s C A P E - O P E N I n t e r f a c e v e r s i o n 1 . 1 1 . 0 1 . 0 1 . 1 L a s t r u n + + + s p e c i f i c a t i o n s + + +
H e a t d u t y : - 2 3 6 2 1 3 7 . 2 4 4 8 7 2 0 7 W
P r e s s u r e d r o p : 0 P a
+ + + o p t i o n a l p a r a m e t e r s + + +
O u t l e t t e m p e r a t u r e : 3 4 3 K
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